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Sample records for water treatment process

  1. Water treatment processes for oilfield steam injection

    Energy Technology Data Exchange (ETDEWEB)

    Shannon, A.; Pauley, J.C. [Chevron Canada Ltd., Vancouver, BC (Canada)

    2009-07-01

    Various water treatment processes are used within the oilfield industry. Processes tend to be common within one region of the world, but different between regions due to untreated water characteristics and treated water quality requirements. This paper summarized Chevron's view of water treatment requirements and processes for oilfield steam injection. It identified water treatment systems that have been used at thermal projects, where they are most commonly utilized, their purpose, and the limits of each process. The advantages and disadvantages of different water treatment systems were also reviewed. The paper focused on the treatment of fresh waters, low-TDS produced waters, high-hardness waters, and high-silica produced waters. Challenges and opportunities were also identified. It was concluded that the challenges created by high-silica, or by high-hardness produced waters lead to more costly processes. 25 refs., 5 tabs., 4 figs.

  2. Hybrid Sludge Modeling in Water Treatment Processes

    OpenAIRE

    Brenda, Marian

    2015-01-01

    Sludge occurs in many waste water and drinking water treatment processes. The numeric modeling of sludge is therefore crucial for developing and optimizing water treatment processes. Numeric single-phase sludge models mainly include settling and viscoplastic behavior. Even though many investigators emphasize the importance of modeling the rheology of sludge for good simulation results, it is difficult to measure, because of settling and the viscoplastic behavior. In this thesis, a new method ...

  3. Thermophilic aerobic post treatment of anaerobically pretreated paper process water

    OpenAIRE

    Vogelaar, J.C.T.

    2002-01-01

    Thermophilic waste- or process water treatment increases in importance as industries shift from end-of-pipe treatment towards integrated process water treatment. The need for process water treatment becomes evident as the levels of pollutants in industrial water circuits need to be controlled whereas the intake of fresh water generally diminishes. In the paper and board industry, high process water temperatures prevail and thus water treatment needs to take place under thermophilic conditions...

  4. Thermophilic aerobic post treatment of anaerobically pretreated paper process water

    NARCIS (Netherlands)

    Vogelaar, J.C.T.

    2002-01-01

    Thermophilic waste- or process water treatment increases in importance as industries shift from end-of-pipe treatment towards integrated process water treatment. The need for process water treatment becomes evident as the levels of pollutants in industrial water circuits need to be co

  5. Thermophilic aerobic post treatment of anaerobically pretreated paper process water

    NARCIS (Netherlands)

    Vogelaar, J.C.T.

    2002-01-01

    Thermophilic waste- or process water treatment increases in importance as industries shift from end-of-pipe treatment towards integrated process water treatment. The need for process water treatment becomes evident as the levels of pollutants in industrial water

  6. TECHNOLOGICAL PROCESS ASSESSMENT OF THE DRINKING WATER TREATMENT AT TARGU-MURES WATER TREATMENT PLANT

    OpenAIRE

    CORNELIA DIANA HERTIA; ANCA ELENA GURZAU; MARIA ILONA SZASZ

    2011-01-01

    This paper intends to assess the technological process of obtaining drinking water at Targu-Mures water treatment plant. The assessment was performed before changing the technological process and four months were chosen to be analized during 2008: January, April, July and October for its efficiency analysis on treatment steps. Mures River is the water source for the water treatment plant, being characterized by unsteady flow and quality parameters with possible important variability in a very...

  7. Urea Synthesis Plant - Process Water Treatment

    Directory of Open Access Journals (Sweden)

    Matijašević, Lj.

    2007-09-01

    Full Text Available After the years of operation of Petrokemija d. d. from Kutina it has been recognized that the technology of urea production can be improved at several points, including wastewater treatment.The wastewater treatment area is a part of the urea plant, Urea 2 of Petrokemija d. d., Kutina. The plant has been in operation since 1983 based on the licensed Stamicarbon CO2 stripping process. So far there have been no major process improvements in terms of utility savings. This part of the plant releases into the environment almost 800 t per day of superfluous wastewater polluted with small, however significant, amounts of urea and ammonium. As such, this wastewater cannot be used in any other segment of urea production. The aim of this paper is to improve the current process from the economical and ecological point of view with ultimate goal of implementing the results obtained.

  8. TECHNOLOGICAL PROCESS ASSESSMENT OF THE DRINKING WATER TREATMENT AT TARGU-MURES WATER TREATMENT PLANT

    Directory of Open Access Journals (Sweden)

    CORNELIA DIANA HERTIA

    2011-03-01

    Full Text Available This paper intends to assess the technological process of obtaining drinking water at Targu-Mures water treatment plant. The assessment was performed before changing the technological process and four months were chosen to be analized during 2008: January, April, July and October for its efficiency analysis on treatment steps. Mures River is the water source for the water treatment plant, being characterized by unsteady flow and quality parameters with possible important variability in a very short period of time. The treatment technological process is the classic one, represented by coagulation, sedimentation, filtration and disinfection, but also prechlorination was constantly applied as additional treatment during 2008. Results showed that for the measured parameters, raw water at the water treatment plant fits into class A3 for surface waters, framing dictated by the bacterial load. The treatment processes efficiency is based on the performance calculation for sedimentation, filtration, global and for disinfection, a better conformation degree of technological steps standing out in January in comparison to the other three analyzed months. A variable non-compliance of turbidity and residual chlorine levels in the disinfected water was observed constantly. Previous treatment steps managed to maintain a low level of oxidisability, chlorine consumption and residual chlorine levels being also low. 12% samples were found inconsistent with the national legislation in terms of bacteriological quality. Measures for the water treatment plant retechnologization are taken primarily for hyperchlorination elimination, which currently constitutes a discomfort factor (taste, smell, and a generating factor of chlorination by-products.

  9. Treatment Process Requirements for Waters Containing Hydraulic Fracturing Chemicals

    Science.gov (United States)

    Stringfellow, W. T.; Camarillo, M. K.; Domen, J. K.; Sandelin, W.; Varadharajan, C.; Cooley, H.; Jordan, P. D.; Heberger, M. G.; Reagan, M. T.; Houseworth, J. E.; Birkholzer, J. T.

    2015-12-01

    A wide variety of chemical additives are used as part of the hydraulic fracturing (HyF) process. There is concern that HyF chemicals will be released into the environment and contaminate drinking water, agricultural water, or other water used for beneficial purposes. There is also interest in using produced water (water extracted from the subsurface during oil and gas production) for irrigation and other beneficial purposes, especially in the arid Southwest US. Reuse of produced water is not speculative: produced water can be low in salts and is being used in California for irrigation after minimal treatment. In this study, we identified chemicals that are used for hydraulic fracturing in California and conducted an analysis to determine if those chemicals would be removed by a variety of technically available treatment processes, including oil/water separation, air stripping, a variety of sorption media, advanced oxidation, biological treatment, and a variety of membrane treatment systems. The approach taken was to establish major physiochemical properties for individual chemicals (log Koc, Henry's constant, biodegradability, etc.), group chemicals by function (e.g corrosion inhibition, biocides), and use those properties to predict the fate of chemical additives in a treatment process. Results from this analysis is interpreted in the context of what is known about existing systems for the treatment of produced water before beneficial reuse, which includes a range of treatment systems from oil/water separators (the most common treatment) to sophisticated treatment trains used for purifying produced water for groundwater recharge. The results show that most HyF chemical additives will not be removed in existing treatment systems, but that more sophisticated treatment trains can be designed to remove additives before beneficial reuse.

  10. Predicting the residual aluminum level in water treatment process

    OpenAIRE

    J. Tomperi; M. Pelo; K. Leiviskä

    2012-01-01

    In water treatment processes, aluminum salts are widely used as coagulation chemical. High dose of aluminum has been proved to be at least a minor health risk and some evidence points out that aluminum could increase the risk of Alzheimer's disease thus it is important to minimize the amount of residual aluminum in drinking water and water used at food industry. In this study, the data of a water treatment plant (WTP) was analyzed and the residual aluminum in drinking water was predicted usin...

  11. Predicting the residual aluminum level in water treatment process

    OpenAIRE

    J. Tomperi; M. Pelo; K. Leiviskä

    2013-01-01

    In water treatment processes, aluminum salts are widely used as coagulation chemical. High dose of aluminum has been proved to be at least a minor health risk and some evidence points out that aluminum could increase the risk of Alzheimer's disease. Thus it is important to minimize the amount of residual aluminum in drinking water and water used at food industry. In this study, the data of a water treatment plant (WTP) was analyzed and the residual aluminum in drinking water was predicted usi...

  12. COST ESTIMATION MODELS FOR DRINKING WATER TREATMENT UNIT PROCESSES

    Science.gov (United States)

    Cost models for unit processes typically utilized in a conventional water treatment plant and in package treatment plant technology are compiled in this paper. The cost curves are represented as a function of specified design parameters and are categorized into four major catego...

  13. Fate of antibiotics during municipal water recycling treatment processes.

    Science.gov (United States)

    Le-Minh, N; Khan, S J; Drewes, J E; Stuetz, R M

    2010-08-01

    Municipal water recycling processes are potential human and environmental exposure routes for low concentrations of persistent antibiotics. While the implications of such exposure scenarios are unknown, concerns have been raised regarding the possibility that continuous discharge of antibiotics to the environment may facilitate the development or proliferation of resistant strains of bacteria. As potable and non-potable water recycling schemes are continuously developed, it is imperative to improve our understanding of the fate of antibiotics during conventional and advanced wastewater treatment processes leading to high-quality water reclamation. This review collates existing knowledge with the aim of providing new insight to the influence of a wide range of treatment processes to the ultimate fate of antibiotics during conventional and advanced wastewater treatment. Although conventional biological wastewater treatment processes are effective for the removal of some antibiotics, many have been reported to occur at 10-1000 ng L(-1) concentrations in secondary treated effluents. These include beta-lactams, sulfonamides, trimethoprim, macrolides, fluoroquinolones, and tetracyclines. Tertiary and advanced treatment processes may be required to fully manage environmental and human exposure to these contaminants in water recycling schemes. The effectiveness of a range of processes including tertiary media filtration, ozonation, chlorination, UV irradiation, activated carbon adsorption, and NF/RO filtration has been reviewed and, where possible, semi-quantitative estimations of antibiotics removals have been provided.

  14. Treatment of gasoline-contaminated waters by advanced oxidation processes

    Energy Technology Data Exchange (ETDEWEB)

    Tiburtius, Elaine Regina Lopes [Departamento de Quimica, Universidade Federal do Parana, CP 19081, 81531-990 Curitiba, PR (Brazil); Peralta-Zamora, Patricio [Departamento de Quimica, Universidade Federal do Parana, CP 19081, 81531-990 Curitiba, PR (Brazil)]. E-mail: zamora@quimica.ufpr.br; Emmel, Alexandre [Centro Integrado de Tecnologia e Educacao Profissional, 81310-010 Curitiba, PR (Brazil)

    2005-11-11

    In this study, the efficiency of advanced oxidative processes (AOPs) was investigated toward the degradation of aqueous solutions containing benzene, toluene and xylenes (BTX) and gasoline-contaminated waters. The results indicated that BTX can be effectively oxidized by near UV-assisted photo-Fenton process. The treatment permits almost total degradation of BTX and removal of more than 80% of the phenolic intermediates at reaction times of about 30 min. Preliminary investigations using water contaminated by gasoline suggest a good potentiality of the process for the treatment of large volumes of aqueous samples containing these polluting species. Heterogeneous photocatalysis and H{sub 2}O{sub 2}/UV system show lower degradation efficiency, probably due to the heterogeneous character of the TiO{sub 2}-mediated system and lost of photonic efficiency of the H{sub 2}O{sub 2}/UV system in the presence of highly colored intermediated.

  15. Water recycle treatment system for use in metal processing

    Energy Technology Data Exchange (ETDEWEB)

    Hewitt, D.E.; Dando, T.J.

    1976-08-10

    A water recycle treatment system is described comprising two main treatment sub-systems for treatment of contaminated water from a plurality of concentrated solutions and rinse baths to separate out the impurities therein. A first sub-system treats less concentrated solutions used for the rinse baths by channeling the flow therefrom to a first neutralizing tank which provides for pH control to produce a mixed output solution having a substantially constant pH factor, which is filtered to remove gross particles, the filtered solution being cooled in a holding tank and passed through a reverse osmosis process and carbon bed to produce clean water. The second sub-system treats highly concentrated solutions obtained from a plurality of chemical processes, mixes them in a second neutralizing tank which is utilized to produce a substantially constant pH output, which is fed to an evaporator to precipitate the metals and salts in sludge and also forms a water vapor output. The reverse osmosis waste is fed back into the second neutralizing tank and processed as noted above.

  16. Oil sand process-affected water treatment using coke adsorption

    Energy Technology Data Exchange (ETDEWEB)

    Gamal El-Din, M.; Pourrezaei, P.; Chelme-Ayala, P.; Zubot, W. [Alberta Univ., Edmonton, AB (Canada). Dept. of Civil and Environmental Engineering

    2010-07-01

    Oil sands operations generate an array of oil sands process-affected water (OSPW) that will eventually be released to the environment. This water must be evaluated within conventional and advanced water treatment technologies. Water management strategies propose options for increased reuse and recycling of water from settling ponds, as well as safe discharge. This presentation outlined the typical composition of OSPW. Constituents of concern in OSPW include suspended solids, hydrocarbons, salts, ammonia, trace metals, and dissolved organics such as naphthenic acids (NAs). Petroleum coke is one of the by-products generated from bitumen extraction in the oil sands industry and can be used as one of the possible treatment processes for the removal of organic compounds found in OSPW. Activated carbon adsorption is an effective process, able to adsorb organic substances such as oils, radioactive compounds, petroleum hydrocarbons, poly aromatic hydrocarbons and various halogenated compounds. The objectives of this study were to evaluate the production of activated carbon from petroleum coke using steam as the activation media; to determine the factors affecting the absorption of NAs; and to evaluate the activated coke adsorption capacity for the reduction of NAs and dissolved organic carbons present in OSPW. It was concluded that petroleum non-activated coke has the ability to decrease COD, alkalinity, and NA concentration. tabs., figs.

  17. Predicting the residual aluminum level in water treatment process

    Directory of Open Access Journals (Sweden)

    J. Tomperi

    2012-06-01

    Full Text Available In water treatment processes, aluminum salts are widely used as coagulation chemical. High dose of aluminum has been proved to be at least a minor health risk and some evidence points out that aluminum could increase the risk of Alzheimer's disease thus it is important to minimize the amount of residual aluminum in drinking water and water used at food industry. In this study, the data of a water treatment plant (WTP was analyzed and the residual aluminum in drinking water was predicted using Multiple Linear Regression (MLR and Artificial Neural Network (ANN models. The purpose was to find out which variables affect the amount of residual aluminum and create simple and reliable prediction models which can be used in an early warning system (EWS. Accuracy of ANN and MLR models were compared. The new nonlinear scaling method based on generalized norms and skewness was used to scale all measurement variables to range [−2...+2] before data-analysis and modeling. The effect of data pre-processing was studied by comparing prediction results to ones achieved in an earlier study. Results showed that it is possible to predict the baseline level of residual aluminum in drinking water with a simple model. Variables that affected the most the amount of residual aluminum were among others: raw water temperature, raw water KMnO4 and PAC / KMnO4-ratio. The accuracies of MLR and ANN models were found to be almost equal. Study also showed that data pre-processing affects to the final prediction result.

  18. Predicting the residual aluminum level in water treatment process

    Directory of Open Access Journals (Sweden)

    J. Tomperi

    2013-06-01

    Full Text Available In water treatment processes, aluminum salts are widely used as coagulation chemical. High dose of aluminum has been proved to be at least a minor health risk and some evidence points out that aluminum could increase the risk of Alzheimer's disease. Thus it is important to minimize the amount of residual aluminum in drinking water and water used at food industry. In this study, the data of a water treatment plant (WTP was analyzed and the residual aluminum in drinking water was predicted using Multiple Linear Regression (MLR and Artificial Neural Network (ANN models. The purpose was to find out which variables affect the amount of residual aluminum and create simple and reliable prediction models which can be used in an early warning system (EWS. Accuracy of ANN and MLR models were compared. The new nonlinear scaling method based on generalized norms and skewness was used to scale all measurement variables to range [−2...+2] before data-analysis and modeling. The effect of data pre-processing was studied by comparing prediction results to ones achieved in an earlier study. Results showed that it is possible to predict the baseline level of residual aluminum in drinking water with a simple model. Variables that affected the most the amount of residual aluminum were among others: raw water temperature, raw water KMnO4 and PAC/KMnO4 (Poly-Aluminum Chloride/Potassium permanganate-ratio. The accuracies of MLR and ANN models were found to be almost the same. Study also showed that data pre-processing affects to the final prediction result.

  19. INTEC CPP-603 Basin Water Treatment System Closure: Process Design

    Energy Technology Data Exchange (ETDEWEB)

    Kimmitt, Raymond Rodney; Faultersack, Wendell Gale; Foster, Jonathan Kay; Berry, Stephen Michael

    2002-09-01

    This document describes the engineering activities that have been completed in support of the closure plan for the Idaho Nuclear Technology and Engineering Center (INTEC) CPP-603 Basin Water Treatment System. This effort includes detailed assessments of methods and equipment for performing work in four areas: 1. A cold (nonradioactive) mockup system for testing equipment and procedures for vessel cleanout and vessel demolition. 2. Cleanout of process vessels to meet standards identified in the closure plan. 3. Dismantlement and removal of vessels, should it not be possible to clean them to required standards in the closure plan. 4. Cleanout or removal of pipelines and pumps associated with the CPP-603 basin water treatment system. Cleanout standards for the pipes will be the same as those used for the process vessels.

  20. The function of advanced treatment process in a drinking water treatment plant with organic matter-polluted source water.

    Science.gov (United States)

    Lin, Huirong; Zhang, Shuting; Zhang, Shenghua; Lin, Wenfang; Yu, Xin

    2017-04-01

    To understand the relationship between chemical and microbial treatment at each treatment step, as well as the relationship between microbial community structure in biofilms in biofilters and their ecological functions, a drinking water plant with severe organic matter-polluted source water was investigated. The bacterial community dynamics of two drinking water supply systems (traditional and advanced treatment processes) in this plant were studied from the source to the product water. Analysis by 454 pyrosequencing was conducted to characterize the bacterial diversity in each step of the treatment processes. The bacterial communities in these two treatment processes were highly diverse. Proteobacteria, which mainly consisted of beta-proteobacteria, was the dominant phylum. The two treatment processes used in the plant could effectively remove organic pollutants and microbial polution, especially the advanced treatment process. Significant differences in the detection of the major groups were observed in the product water samples in the treatment processes. The treatment processes, particularly the biological pretreatment and O3-biological activated carbon in the advanced treatment process, highly influenced the microbial community composition and the water quality. Some opportunistic pathogens were found in the water. Nitrogen-relative microorganisms found in the biofilm of filters may perform an important function on the microbial community composition and water quality improvement.

  1. Estrogen-related receptor γ disruption of source water and drinking water treatment processes extracts

    Institute of Scientific and Technical Information of China (English)

    Na Li; Weiwei Jiang; Kaifeng Rao; Mei Ma; Zijian Wang; Satyanarayanan Senthik Kumaran

    2011-01-01

    Environmental chemicals in drinking water can impact human health through nuclear receptors.Additionally, estrogen-related receptors (ERRs) are vulnerable to endocrine-disrupting effects.To date, however, ERR disruption of drinking water potency has not been reported.We used ERRγtwo-hybrid yeast assay to screen ERRγ disrupting activities in a drinking water treatment plant (DWTP) located in north China and in source water from a reservoir, focusing on agonistic, antagonistic, and inverse agonisfic activity to 4-hydroxytamoxifen (4-OHT).Water treatment processes in the DWTP consisted of pre-chlorination, coagulation, coal and sand filtration, activated carbon filtration, and secondary chlorination processes.Samples were extracted by solid phase extraction.Results showed that ERRγ antagonistic activities were found in all sample extracts, but agonistic and inverse agonistic activity to 4-OHT was not found.When calibrated with the toxic equivalent of 4-OHT, antagonistic effluent effects ranged from 3.4 to 33.1 μg/L.In the treatment processes, secondary chlorination was effective in removing ERRγ antagonists, but the coagulation process led to significantly increased ERRγ antagonistic activity.The drinking water treatment processes removed 73.5% of ERRγ antagonists.To our knowledge,the occurrence of ERRγ disruption activities on source and drinking water in vitro had not been reported previously.It is vital, therefore,to increase our understanding of ERRγdisrupting activities in drinking water.

  2. Removal of antibiotics from surface and distilled water in conventional water treatment processes

    Science.gov (United States)

    Adams, C.; Wang, Y.; Loftin, K.; Meyer, M.

    2002-01-01

    Conventional drinking water treatment processes were evaluated under typical water treatment plant conditions to determine their effectiveness in the removal of seven common antibiotics: carbadox, sulfachlorpyridazine, sulfadimethoxine, sulfamerazine, sulfamethazine, sulfathiazole, and trimethoprim. Experiments were conducted using synthetic solutions prepared by spiking both distilled/ deionized water and Missouri River water with the studied compounds. Sorption on Calgon WPH powdered activated carbon, reverse osmosis, and oxidation with chlorine and ozone under typical plant conditions were all shown to be effective in removing the studied antibiotics. Conversely, coagulation/flocculation/sedimentation with alum and iron salts, excess lime/soda ash softening, ultraviolet irradiation at disinfection dosages, and ion exchange were all relatively ineffective methods of antibiotic removal. This study shows that the studied antibiotics could be effectively removed using processes already in use many water treatment plants. Additional work is needed on by-product formation and the removal of other classes of antibiotics.

  3. Advanced treatment and reuse system developed for oilfield process water

    Energy Technology Data Exchange (ETDEWEB)

    Conroy, Kevin

    2011-01-15

    An innovative plant to treat oilfield produced wastewater is being constructed in Trinidad and Tobago following recent regulations and industrial water supply challenges. The 4,100m3/day treatment system, developed by Golder Associates, will produce water for industrial reuse and effluent that meets new regulations. The treatment stages include: oil-water separation by gravity, equalization with a two-day capacity basin, dissolved air flotation, cooling, biotreatment/settling with immobilized cell bioreactors (ICB) technology, prefiltration/reverse osmosis and effluent storage/transfer. This advanced system will provide several important benefits including the elimination of inland discharge of minimally-treated water and the reduction of environmental and public health concerns. In addition, it will provide a new source of industrial water, resulting in a decrease in demand for fresh water. The success of this plant could lead to additional facilities in other oil field locations, expanding economic and environmental benefits of water reuse.

  4. Water chemistry and antimicrobial treatment in poultry processing

    Science.gov (United States)

    This study examined the influence of calcium and magnesium ions in process water on the solubility of trisodium phosphate. Water used in poultry processing operations may be treated with sanitizers such as trisodium phosphate to reduce microbial activity and the risk of contamination. This occurs wh...

  5. A comparative life cycle assessment of process water treatment ...

    African Journals Online (AJOL)

    2011-07-29

    Jul 29, 2011 ... Two different raw water desalination technologies, an existing ion exchange plant .... tect membranes from attack by residual free chlorine. The ecoInvent ..... SON F (1999) Treatment of industrial wastewater for reuse. Desali.

  6. Integration of drinking water treatment plant process models and emulated process automation software

    NARCIS (Netherlands)

    Worm, G.I.M.

    2012-01-01

    The objective of this research is to limit the risks of fully automated operation of drinking water treatment plants and to improve their operation by using an integrated system of process models and emulated process automation software. This thesis contains the design of such an integrated system.

  7. Integration of drinking water treatment plant process models and emulated process automation software

    NARCIS (Netherlands)

    Worm, G.I.M.

    2012-01-01

    The objective of this research is to limit the risks of fully automated operation of drinking water treatment plants and to improve their operation by using an integrated system of process models and emulated process automation software. This thesis contains the design of such an integrated system.

  8. WASTE WATER TREATMENT IN VISCOUS CRUDE PROCESSING IN SHENGLI OILFIELDS

    Institute of Scientific and Technical Information of China (English)

    Yang Huaijie; Xu Hui

    1997-01-01

    @@ Apart from sewage pretreatment and stepped control, the Viscous Crude Processing Plant of Shengli Petrochemical General Works has established a new process of sewage treatment featuring with flexible and advanced technology and strong impact strength, with the crude sewage treatment yield reaching more than 95%.

  9. Air flotation treatment of salmon processing waste water

    Data.gov (United States)

    US Fish and Wildlife Service, Department of the Interior — This paper discusses methods for the reduction of the pollution strength of salmon processing waste water. Past research has indicated the success of air pressure...

  10. Evaluation of Effectiveness Technological Process of Water Purification Exemplified on Modernized Water Treatment Plant at Otoczna

    Directory of Open Access Journals (Sweden)

    Jordanowska Joanna

    2014-12-01

    Full Text Available The article presents the work of the Water Treatment Plant in the town of Otoczna, located in the Wielkopolska province, before and after the modernization of the technological line. It includes the quality characteristics of the raw water and treated water with particular emphasis on changes in the quality indicators in the period 2002 -2012 in relation to the physicochemical parameters: the content of total iron and total manganese, the ammonium ion as well as organoleptic parameters(colour and turbidity. The efficiency of technological processes was analysed, including the processes of bed start up with chalcedonic sand to remove total iron and manganese and ammonium ion. Based on the survey, it was found that the applied modernization helped solve the problem of water quality, especially the removal of excessive concentrations of iron, manganese and ammonium nitrogen from groundwater.

  11. Cooling water treatment - Processes and regulations; Kuehlwasserbehandlung - Verfahren und Vorschriften

    Energy Technology Data Exchange (ETDEWEB)

    Kirsten, J. [Aquatech GmbH, Nieder-Olm (Germany)

    1998-09-01

    Determination of optimal water treatment methods is to be based on requirements set by technical specifications, economic efficiency aspects, and legal regulations. It is an important task and should be done by experts in cooperation with the responsible supervisory bodies. (orig./CB) [Deutsch] Zusammenfassend kann gesagt werden, dass bei der Auswahl des optimalen Verfahrens einer Kuehlwasserbehandlung technische Anforderungen, wirtschaftliche Vorgaben und behoerdliche Auflagen gleichermassen beruecksichtigt werden muessen. Diese Aufgabe sollte von Fachleuten wahrgenommen und mit den zustaendigen Behoerden abgestimmt werden. (orig.)

  12. Microbial fuel cell treatment of ethanol fermentation process water

    Science.gov (United States)

    Borole, Abhijeet P [Knoxville, TN

    2012-06-05

    The present invention relates to a method for removing inhibitor compounds from a cellulosic biomass-to-ethanol process which includes a pretreatment step of raw cellulosic biomass material and the production of fermentation process water after production and removal of ethanol from a fermentation step, the method comprising contacting said fermentation process water with an anode of a microbial fuel cell, said anode containing microbes thereon which oxidatively degrade one or more of said inhibitor compounds while producing electrical energy or hydrogen from said oxidative degradation, and wherein said anode is in electrical communication with a cathode, and a porous material (such as a porous or cation-permeable membrane) separates said anode and cathode.

  13. Radiation processing applications in the Czechoslovak water treatment technologies

    Science.gov (United States)

    Vacek, K.; Pastuszek, F.; Sedláček, M.

    The regeneration of biologically clogged water wells by radiation proved to be a successful and economically beneficial process among other promising applications of ionizing radiation in the water supply technology. The application conditions and experience are mentioned. The potential pathogenic Mycobacteria occuring in the warm washing and bathing water are resistant against usual chlorine and ozone concentrations. The radiation sensitivity of Mycobacteria allowed to suggest a device for their destroying by radiation. Some toxic substances in the underground water can be efficiently degraded by gamma radiation directly in the wells drilled as a hydraulic barrier surrounding the contaminated land area. Substantial decrease of CN - concentration and C.O.D. value was observed in water pumped from such well equipped with cobalt sources and charcoal. The removing of pathogenic contamination remains to be the main goal of radiation processing in the water purification technologies. The decrease of liquid sludge specific filter resistance and sedimentation acceleration by irradiation have a minor technological importance. The hygienization of sludge cake from the mechanical belt filter press by electron beam appears to be the optimum application in the Czechoslovak conditions. The potatoes and barley crop yields from experimental plots treated with sludge were higher in comparison with using the manure. Biological sludge from the municipal and food industry water purification plants contains nutritive components. The proper hygienization is a necessary condition for using them as a livestock feed supplement. Feeding experiments with broilers and pigs confirmed the possibility of partial (e.g. 50%) replacement of soya-, bone- or fish flour in feed mixtures by dried sludge hygienized either by heat or by the irradiation.

  14. Thermophilic anaerobic waste water treatment, temperature aspects and process stability.

    NARCIS (Netherlands)

    Lier, van J.B.

    1995-01-01

    The main objective of this thesis was to assess the thermostability of thermophilic anaerobic wastewater treatment processes and the possibility to optimize the performance of thermophilic high-rate systems.Experiments were conducted to study the suitability of two types of seed material to start a

  15. Mesophilic and thermophilic activated sludge post-treatment of paper mill process water

    NARCIS (Netherlands)

    Vogelaar, J.C.T.; Bouwhuis, E.; Klapwijk, A.; Spanjers, H.; Lier, van J.B.

    2002-01-01

    Increasing system closure in paper mills and higher process water temperatures make the applicability of thermophilic treatment systems increasingly important. The use of activated sludge as a suitable thermophilic post-treatment system for anaerobically pre-treated paper process water from a paper

  16. The role of advanced oxidation processes in drinking water treatment

    OpenAIRE

    Philippe, Karine K.

    2010-01-01

    Removal of natural organic matter (NOM) is an ever growing challenge for water utilities as many surface waters used for drinking water in the UK exhibit increasing organics levels and it is well known that these organics can lead to problems such as water colouration, unpleasant odour and taste, bacterial growth and disinfection by-products (DBPs) formation. NOM is traditionally removed by coagulation, however in the case of hydrophilic organic matter rich waters the performances of these pr...

  17. Intended process water management concept for the mechanical biological treatment of municipal solid waste

    Institute of Scientific and Technical Information of China (English)

    D. Weichgrebe; S. Maerker; T. Boning; H. Stegemann

    2008-01-01

    Accumulating operational experience in both aerobic and anaerobic mechanical biological waste treatment (MBT) makes it increasingly obvious that controlled water management would substantially reduce the cost of MBT and also enhance resource recovery of the organic and inorganic fraction. The MBT plant at Gescher, Germany, is used as an example in order to determine the quantity and composition of process water and leachates from intensive and subsequent rotting, pressing water from anaerobic digestion and scrubber water from acid exhaust air treatment, and hence prepare an MBT water balance. The potential of, requirements for and limits to internal process water reuse as well as the possibilities of resource recovery from scrubber water are also examined. Finally, an assimilated process water management concept with the purpose of an extensive reduction of wastewater quantity and freshwater demand is presented.

  18. Novel Electrochemical Process for Treatment of Perchlorate in Waste Water

    Science.gov (United States)

    2011-03-06

    technology combines ion exchange and electrochemistry to provide a selective and reversible method for removing target species from wastewater. In...nanotube nanocomposite for removing perchlorate from drinking water and wastewater. The ESIX technology combines ion exchange and electrochemistry to...potential for perchlorate occurrence in drinking water and food supplies is a human health concern because it can interfere with iodide uptake by the

  19. Advanced primary treatment of waste water using a bio-flocculation-adsorption sedimentation process

    Energy Technology Data Exchange (ETDEWEB)

    Zhao, W.; Ting, Y.P.; Chen, J.P.; Xing, C.H. [National Univ., Singapore (Singapore). Dept. of Chemical and Environmental Engineering; Shi, S.Q. [Tsinghua Univ., Beijing (China). Dept. of Environmental Science and Engineering

    2000-07-01

    An advanced primary treatment process for a municipal waste water was systematically studied, using a bio-flocculation-adsorption, sedimentation and stabilization process (BSS). It was shown that the organic removal efficiency was higher than that of the traditional primary treatment processes but lower than that of the traditional secondary treatment processes. Both adsorption and bio-flocculation played an important role in the removal of pollutants. The activated sludge within the bio-flocculation-adsorption tank could be considered a bio-flocculent which improved the quality of the effluent from the primary treatment process. As the effluent of the BSS process did not meet the requirements for a typical secondary effluent, the process may be regarded as an advanced (or enhanced) primary treatment process, suitable for waste water containing a high concentration of suspended solids and colloidal particles. (orig.)

  20. A new water treatment scheme for thermal development : the SIBE process

    Energy Technology Data Exchange (ETDEWEB)

    Pedenaud, P.; Dang, F. [Total, Paris (France)

    2008-10-15

    The production of extra heavy oil or bitumen through thermal methods such as steam assisted gravity drainage (SAGD) involves the generation and injection into the reservoir of large quantities of steam which is recirculated with the produced bitumen. It is expected that maximizing the recycling of the produced water into steam will be mandatory, because of the need to minimize fresh water consumption and the possibility of increasingly stringent environmental regulations. The SAGD water treatment scheme is complex. It depends on the water characteristics, the steam generator type selected, and the decision to completely eliminate waste water disposal or use other waste handling and disposal methods. Other challenges such as the high silica content in the produced water, are encountered with SAGD water treatment. This paper presented an overview of the current water treatment process options for SAGD, as well as a new patented process called silica inhibition and blowdown evaporation (SIBE). The paper also presented an estimate of the economic benefit of the new SIBE process relative to conventional process schemes. Treatment objectives and water characteristics and the steps involved in conventional water treatment were first outlined. It was concluded that the silica and hardness removal scheme combined with the boiler blowdown evaporator were less economical because of higher investment cost due to the evaporation unit. 1 ref., 3 tabs., 4 figs.

  1. Reducing the public health risk of cryptosporidiosis by optimizing treatment processes at a military water system.

    Science.gov (United States)

    Clarke, Steven H

    2011-01-01

    Safe drinking water supplies are critical to public health and mission success. One of the primary goals of water treatment is to effectively reduce the acute health risks posed by pathogenic microorganisms present in our raw, untreated water supplies. As a result of recent drinking water regulations, a military water system identified significant levels of Cryptosporidium in their raw water supply requiring additional or improved treatment to remove. Cryptosporidium, the pathogenic microorganism that causes Cryptosporidiosis, has been indicated in numerous waterborne outbreaks worldwide, including the United States. The US Army Public Health Command conducted a year-long study evaluating the ability of the water system to provide improved treatment by optimizing the existing treatment processes. Study results show that optimizing existing treatment processes and switching to an alternative coagulant chemical will achieve the Cryptosporidium removal required to comply with drinking water regulations, with subsequent reduction in the risk of Cryptosporidiosis. These improvements will also ensure effective treatment in all raw water quality conditions and reduce overall chemical costs without increasing operational and maintenance burdens. The optimization evaluation and techniques used for this water system can be applied to all military-owned water systems to help ensure the protection of public health and mission success.

  2. Efficacy of conventional drinking water treatment processes in ...

    African Journals Online (AJOL)

    2013-10-07

    Oct 7, 2013 ... chlorine residual varied between 1 and 2.5 mg/ℓ after 20 min of contact time. .... waters supplied to DWTP in Quebec, Canada (Zamyadi et al.,. 2012b), Bahia ..... late Ceratium in Albert Falls Dam (KZN): History, causes, spatial features and ... HEISLER J, GILBERT PM, BURKHOLDER JM, ANDERSON DM,.

  3. Microbial community structures and dynamics in the O3/BAC drinking water treatment process.

    Science.gov (United States)

    Tian, Jian; Lu, Jun; Zhang, Yu; Li, Jian-Cheng; Sun, Li-Chen; Hu, Zhang-Li

    2014-06-16

    Effectiveness of drinking water treatment, in particular pathogen control during the water treatment process, is always a major public health concern. In this investigation, the application of PCR-DGGE technology to the analysis of microbial community structures and dynamics in the drinking water treatment process revealed several dominant microbial populations including: α-Proteobacteria, β-Proteobacteria, γ-Proteobacteria, Bacteroidetes, Actinobacteria Firmicutes and Cyanobacteria. α-Proteobacteria and β-Proteobacteria were the dominant bacteria during the whole process. Bacteroidetes and Firmicutes were the dominant bacteria before and after treatment, respectively. Firmicutes showed season-dependent changes in population dynamics. Importantly, γ-Proteobacteria, which is a class of medically important bacteria, was well controlled by the O3/biological activated carbon (BAC) treatment, resulting in improved effluent water bio-safety.

  4. Microbial Community Structures and Dynamics in the O3/BAC Drinking Water Treatment Process

    Directory of Open Access Journals (Sweden)

    Jian Tian

    2014-06-01

    Full Text Available Effectiveness of drinking water treatment, in particular pathogen control during the water treatment process, is always a major public health concern. In this investigation, the application of PCR-DGGE technology to the analysis of microbial community structures and dynamics in the drinking water treatment process revealed several dominant microbial populations including: α-Proteobacteria, β-Proteobacteria, γ-Proteobacteria, Bacteroidetes, Actinobacteria Firmicutes and Cyanobacteria. α-Proteobacteria and β-Proteobacteria were the dominant bacteria during the whole process. Bacteroidetes and Firmicutes were the dominant bacteria before and after treatment, respectively. Firmicutes showed season-dependent changes in population dynamics. Importantly, γ-Proteobacteria, which is a class of medically important bacteria, was well controlled by the O3/biological activated carbon (BAC treatment, resulting in improved effluent water bio-safety.

  5. IMPROVEMENT OF COAGULATION PROCESS FOR THE PRUT RIVER WATER TREATMENT USING ALUMINUM SULPHATE

    Directory of Open Access Journals (Sweden)

    Larisa Postolachi

    2015-06-01

    Full Text Available The aim of presented research was to optimize the treatment process of the Prut River water. In order to realize the proposed goal, there were studied the following factors which can improve the process of coagulation: (i the influence of stirring speed during coagulation and (ii the influence of the concentration of the coagulant solution added in the process of coagulation. The optimal conditions of coagulation were established using the Jar-test method. Application of the recommended procedure contribute to the reduction of the coagulant dose, the contact time, the aluminum concentration in water and the expenses for water treatment.

  6. Plant-wide (BSM2) evaluation of reject water treatment with a SHARON-Anammox process

    DEFF Research Database (Denmark)

    Volcke, Eveline; Gernaey, Krist; Vrecko, Darko;

    2006-01-01

    In wastewater treatment plants (WWTPs) equipped with sludge digestion and dewatering systems, the reject water originating from these facilities contributes significantly to the nitrogen load of the activated sludge tanks, to which it is typically recycled. In this paper, the impact of reject water...... streams on the performance of a WWTP is assessed in a simulation study, using the Benchmark Simulation Model no. 2 (BSM2), that includes the processes describing sludge treatment and in this way allows for plant-wide evaluation. Comparison of performance of a WWTP without reject water with a WWTP where...... treatment plant, reject water treatment with a combined SHARON-Anammox process seems a promising option. The simulation results indicate that significant improvements of the effluent quality of the main wastewater treatment plant can be realized. An economic evaluation of the different scenarios...

  7. Multicausal analysis on water deterioration processes present in a drinking water treatment system.

    Science.gov (United States)

    Wang, Li; Ma, Fang; Pang, Changlong; Firdoz, Shaik

    2013-03-01

    The fluctuation of water turbidity has been studied during summer in the settling tanks of a drinking water treatment plant. Results from the multiple cause-effect model indicated that five main pathways interactively influenced thequalityof tank water. During rain, turbidity levels increased mainly as a result of decreasing pH and anaerobic reactions (partial effect = 68%). Increasing water temperature combined with dissolved oxygen concentration (partial effect = 64%) was the key parameterforcontrolling decreases in water turbidity during nighttime periods after a rainy day. The dominant factor influencing increases in turbidity during sunny daytime periods was algal blooms (partial effect = 86%). However, short-circuiting waves (partial effect = 77%) was the main cause for increased nighttime water turbidity after a sunny day. The trade offbetween regulatory pathways was responsible for environmental changes, and the outcome was determined by the comparative strengths of each pathway.

  8. Characterizing natural organic matter in drinking water treatment processes and trains

    NARCIS (Netherlands)

    Baghoth, S.A.

    2012-01-01

    Natural organic matter (NOM) generally influences water treatment processes such as coagulation, oxidation, adsorption, and membrane filtration. NOM contributes colour, taste and odour in drinking water, fouls membranes, serves as a precursor for disinfection by-products, increases the exhaustion a

  9. Development and Validation of an Acid Mine Drainage Treatment Process for Source Water

    Energy Technology Data Exchange (ETDEWEB)

    Lane, Ann [Battelle Memorial Institute, Columbus, OH (United States)

    2016-03-01

    Throughout Northern Appalachia and surrounding regions, hundreds of abandoned mine sites exist which frequently are the source of Acid Mine Drainage (AMD). AMD typically contains metal ions in solution with sulfate ions which have been leached from the mine. These large volumes of water, if treated to a minimum standard, may be of use in Hydraulic Fracturing (HF) or other industrial processes. This project’s focus is to evaluate an AMD water treatment technology for the purpose of providing treated AMD as an alternative source of water for HF operations. The HydroFlex™ technology allows the conversion of a previous environmental liability into an asset while reducing stress on potable water sources. The technology achieves greater than 95% water recovery, while removing sulfate to concentrations below 100 mg/L and common metals (e.g., iron and aluminum) below 1 mg/L. The project is intended to demonstrate the capability of the process to provide AMD as alternative source water for HF operations. The second budget period of the project has been completed during which Battelle conducted two individual test campaigns in the field. The first test campaign demonstrated the ability of the HydroFlex system to remove sulfate to levels below 100 mg/L, meeting the requirements indicated by industry stakeholders for use of the treated AMD as source water. The second test campaign consisted of a series of focused confirmatory tests aimed at gathering additional data to refine the economic projections for the process. Throughout the project, regular communications were held with a group of project stakeholders to ensure alignment of the project objectives with industry requirements. Finally, the process byproduct generated by the HydroFlex process was evaluated for the treatment of produced water against commercial treatment chemicals. It was found that the process byproduct achieved similar results for produced water treatment as the chemicals currently in use. Further

  10. Enzymatic treatment of paper mill process waters; Entsyymit paperitehtaan kiertoveden kaesittelyssae - EKT 06

    Energy Technology Data Exchange (ETDEWEB)

    Mustranta, A.; Buchert, J. [VTT Biotechnology and Food Research, Espoo (Finland); Ekman, R.; Spetz, P. [Aabo Akademi, Turku (Finland). Lab. of Forest Products Chemistry; Luukko, K. [Helsinki Univ. of Technology, Otaniemi (Finland). Paper Technology

    1998-12-31

    Dissolved and colloidal substances (DCS) are dispersed into the process waters during different stages of pulp and paper production. These are lipophilic extractives (pitch), hydrophilic extractives (lignan) and carbohydrates, mainly hemicelluloses. These dissolved and colloidal substances accumulate during water circulation and results in impaired paper machine runnability. DCS can also interfere with wet-end process chemicals. In this project the chemical composition of the process waters of spruce TMP pulping have been characterized. Simultaneously, potential enzymes for modification of DCS has been produced and purified. The enzymatic treatments have been started with lipase acting on triglycerides present in extractives. The effect of enzymatic treatment on the properties of process waters and technical properties of the pulp have been evaluated. (orig.)

  11. The use of process simulation models in virtual commissioning of process automation software in drinking water treatment plants

    NARCIS (Netherlands)

    Worm, G.I.M.; Kelderman, J.P.; Lapikas, T.; Van der Helm, A.W.C.; Van Schagen, K.M.; Rietveld, L.C.

    2012-01-01

    This research deals with the contribution of process simulation models to the factory acceptance test (FAT) of process automation (PA) software of drinking water treatment plants. Two test teams tested the same piece of modified PA-software. One team used an advanced virtual commissioning (AVC) syst

  12. Removal of cyclops in pre-oxidizing cooperation water treatment process

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    Zooplankton cyclops propagates profusely in waterbody, cannot be effectively inactivated by conventional disinfection process, and becomes a troublesome drinking water treatment problem. In this work, the qualitative and quantitative experimental studies were carried out on inactivation of zooplankton cyclops using oxidants, such as chlorine (Cl2), chlorine dioxide (ClO2), ozone (O3), hydrogen peroxide (H2O2), ozone/hydrogen peroxide (O3/H2O2), chloramines (Cl2-NH3) and potassium permanganate (KMnO4). The influences of various factors include different oxidant dosages, organic substance contents and pH values. The results showed that currently available oxidants used all might inactivate cyclops in some extent. According to the experimental results, chlorine dioxide, ozone, ozone/hydrogen peroxide and chloramines can be selected as effective oxidants for inactivating cyclops because of their strong inactivation abilities. Then the synergic removal effects on cyclops with ozone,ozone/hydrogen peroxide pre-oxidation followed by conventional water treatment processes were investigated. The results showed that ozone and ozone/hydrogen peroxide pre-oxidation can inactivate cyclops effectively, which then can be removed thoroughly by conventional water treatment processes. Cyclops cannot appear in water after filtration with 1.65 mg/L of ozone and 6 mg/L of hydrogen peroxide, with the inactivation rate being 62% before conventional water treatment processes. Cyclops cannot appear in water after filtration with 1.8 mg/L of ozone, with the inactivation rate being 50% before conventional water treatment processes. For different oxidants, when removal rate was the best, the inactivation rate was not the same. These results may provide reference and model for actual waterworks.

  13. Effect of drinking water treatment process parameters on biological removal of manganese from surface water.

    Science.gov (United States)

    Hoyland, Victoria W; Knocke, William R; Falkinham, Joseph O; Pruden, Amy; Singh, Gargi

    2014-12-01

    Soluble manganese (Mn) presents a significant treatment challenge to many water utilities, causing aesthetic and operational concerns. While application of free chlorine to oxidize Mn prior to filtration can be effective, this is not feasible for surface water treatment plants using ozonation followed by biofiltration because it inhibits biological removal of organics. Manganese-oxidizing bacteria (MOB) readily oxidize Mn in groundwater treatment applications, which normally involve pH > 7.0. The purpose of this study was to evaluate the potential for biological Mn removal at the lower pH conditions (6.2-6.3) often employed in enhanced coagulation to optimize organics removal. Four laboratory-scale biofilters were operated over a pH range of 6.3-7.3. The biofilters were able to oxidize Mn at a pH as low as pH 6.3 with greater than 98% Mn removal. Removal of simulated organic ozonation by-products was also greater than 90% in all columns. Stress studies indicated that well-acclimated MOB can withstand variations in Mn concentration (e.g., 0.1-0.2 mg/L), hydraulic loading rate (e.g., 2-4 gpm/ft(2); 1.36 × 10(-3)-2.72 × 10(-3) m/s), and temperature (e.g., 7-22 °C) typically found at surface water treatment plants at least for relatively short (1-2 days) periods of time. Copyright © 2014 Elsevier Ltd. All rights reserved.

  14. THE SEQUENTIAL WATER TREATMENT CONTAINING MYCOESTROGENS IN PHOTOCATALYSIS AND NANOFILTRATION PROCESSES

    Directory of Open Access Journals (Sweden)

    Mariusz Dudziak

    2014-10-01

    Full Text Available The results of the study focused on the impact of membrane on the performance of the integrated system photocatalysis/nanofiltration applied to remove mycoestrogens from water are discussed in the paper. The results were compared with ones obtained during single step photocatalysis and nanofiltration processes. The subject of the study were simulated waters containing difference concentration of humic acids to which mycoestrogens were added to the concentration level 500 μg/dm3. It was shown, that the application of integrated system improved the efficiency of mycoestrogens removal in comparison with single step photocatalysis process. In case of nanofiltration, the efficiency of the treatment was comparable in both, integrated and single nanofiltration processes regardless of the membrane type applied. However, it was found that investigated membranes differ in the affinity to fouling and removal rate of inorganic compounds, what should be considered during water treatment technology development.

  15. [Occurrence and distribution of volatile organic compounds in conventional and advanced drinking water treatment processes].

    Science.gov (United States)

    Chen, Xi-Chao; Luo, Qian; Chen, Hu; Wei, Zi; Wang, Zi-Jian; Xu, Ke-Wen

    2013-12-01

    A series of experiments were conducted to study the occurrence and distribution of volatile organic compounds (VOCs) in conventional and advanced drinking water treatment processes of 3 water treatment plants in Lianyungang City. Results showed that 30 compounds of 3 classes were detected from 67 kinds of VOCs in all the samples collected. The concentrations of carbonyl compounds, halogenated hydrocarbons and benzenes detected were in the ranges of 0.04-61.27, 0.02-35.61 and 0.07-2.33 microg x L(-1) respectively. Comparing the changes of different VOCs in three drinking water treatment plants, conventional chlorination process could effectively remove benzenes but meanwhile produced trihalomethanes (THMs). Additional advanced treatment ozonation-biological activated carbon process could decrease the formation of THMs during pre-chlorination but produced new risky contaminants like carbonyl compounds. The changes of VOCs in tap water were also investigated. It was found that carbonyl compounds produced by ozonation could be further transformed to THMs with residual chlorine. However, the health risks of all detected compounds in tap water were at a low level, except that the carcinogenic risk of crotonaldehydes (9.3 x 10(-5)-2.2 x 10(-4)) was slightly higher than the US EPA threshold (10(-6)-10(-4)).

  16. Swimming Pool Water Treatment Chemicals and/or Processes. Standard No. 22.

    Science.gov (United States)

    National Sanitation Foundation, Ann Arbor, MI.

    Chemicals or processes used or intended for use, in the treatment of swimming pool water are covered. Minimum public health limits or acceptability in regard to toxicity, biocidal effectiveness, and chemical behavior and analysis are presented. The appendices give guidelines to the scientific and statistically sound evaluations to determine the…

  17. Removal of diclofenac by conventional drinking water treatment processes and granular activated carbon filtration.

    Science.gov (United States)

    Rigobello, Eliane Sloboda; Dantas, Angela Di Bernardo; Di Bernardo, Luiz; Vieira, Eny Maria

    2013-06-01

    This study was carried out to evaluate the efficiency of conventional drinking water treatment processes with and without pre-oxidation with chlorine and chlorine dioxide and the use of granular activated carbon (GAC) filtration for the removal of diclofenac (DCF). Water treatment was performed using the Jar test with filters on a lab scale, employing nonchlorinated artesian well water prepared with aquatic humic substances to yield 20HU true color, kaolin turbidity of 70 NTU and 1mgL(-1) DCF. For the quantification of DCF in water samples, solid phase extraction and HPLC-DAD methods were developed and validated. There was no removal of DCF in coagulation with aluminum sulfate (3.47mgAlL(-1) and pH=6.5), flocculation, sedimentation and sand filtration. In the treatment with pre-oxidation and disinfection, DCF was partially removed, but the concentration of dissolved organic carbon (DOC) was unchanged and byproducts of DCF were observed. Chlorine dioxide was more effective than chorine in oxidizing DCF. In conclusion, the identification of DCF and DOC in finished water indicated the incomplete elimination of DCF through conventional treatments. Nevertheless, conventional drinking water treatment followed by GAC filtration was effective in removing DCF (⩾99.7%). In the oxidation with chlorine, three byproducts were tentatively identified, corresponding to a hydroxylation, aromatic substitution of one hydrogen by chlorine and a decarboxylation/hydroxylation. Oxidation with chlorine dioxide resulted in only one byproduct (hydroxylation).

  18. Filtration treatment of processing kapuas river's water by coral sands/kaolinite/activated carbon

    Science.gov (United States)

    Sasri, Risya; Wahyuni, Nelly; Utomo, Kiki Prio

    2017-03-01

    Filtration treatment of processing Kapuas river's water in the Sepuk Keladi village, West Kalimantan has been conducted. The aims of the treatments to process kapuas river's water with the characteristics of peat into clean water. Processing method using flow-up-flow filtration system with filter media coral sands / kaolinite / activated carbon. Coral sands was obtained from Kijing beach and characterized using X-Ray Diffraction (XRD) and BET method. The XRD spectrum showed strongest peak at 33.09°, 52.40°, 29.34° and it can be concluded that mineral was verified corresponding to calcium consisting of calcite phase. While the result of BET plot point that surface area of coral sands was 4.954 m2/g. The effectiveness of the filtration media was determined by testing parameters such as pH, total suspended solid (TSS), total dissolved solid (TDS), chloride as Cl, and iron as Fe, before and after filtration of Kapuas river's water. The result show that kapuas river's water after filtration treatment was increased pH from 6,53 to 7,2. Filtration using this systems resulted in an average 43,53% reduction in TSS, 91,63% reduction in TDS, 83,63% reduction in content of chloride as Cl and 33,56 % reduction in content iron as Fe, respectively.

  19. Transformation of pharmaceuticals during oxidation/disinfection processes in drinking water treatment.

    Science.gov (United States)

    Postigo, Cristina; Richardson, Susan D

    2014-08-30

    Pharmaceuticals are emerging contaminants of concern and are widespread in the environment. While the levels of these substances in finished drinking waters are generally considered too low for human health concern, there are now concerns about their disinfection by-products (DBPs) that can form during drinking water treatment, which in some cases have been proven to be more toxic than the parent compounds. The present manuscript reviews the transformation products of pharmaceuticals generated in water during different disinfection processes, i.e. chlorination, ozonation, chloramination, chlorine dioxide, UV, and UV/hydrogen peroxide, and the main reaction pathways taking place. Most of the findings considered for this review come from controlled laboratory studies involving reactions of pharmaceuticals with these oxidants used in drinking water treatment. Copyright © 2014 Elsevier B.V. All rights reserved.

  20. Removal of the cyanotoxin anatoxin-a by drinking water treatment processes: a review.

    Science.gov (United States)

    Vlad, Silvia; Anderson, William B; Peldszus, Sigrid; Huck, Peter M

    2014-12-01

    Anatoxin-a (ANTX-a) is a potent alkaloid neurotoxin, produced by several species of cyanobacteria and detected throughout the world. The presence of cyanotoxins, including ANTX-a, in drinking water sources is a potential risk to public health. This article presents a thorough examination of the cumulative body of research on the use of drinking water treatment technologies for extracellular ANTX-a removal, focusing on providing an analysis of the specific operating parameters required for effective treatment and on compiling a series of best-practice recommendations for owners and operators of systems impacted by this cyanotoxin. Of the oxidants used in drinking water treatment, chlorine-based processes (chlorine, chloramines and chlorine dioxide) have been shown to be ineffective for ANTX-a treatment, while ozone, advanced oxidation processes and permanganate can be successful. High-pressure membrane filtration (nanofiltration and reverse osmosis) is likely effective, while adsorption and biofiltration may be effective but further investigation into the implementation of these processes is necessary. Given the lack of full-scale verification, a multiple-barrier approach is recommended, employing a combination of chemical and non-chemical processes.

  1. Study of the combining adsorption-micro filtration process for the treatment of coloured waters

    Energy Technology Data Exchange (ETDEWEB)

    Addaou, A.; Laajeb, A.; Lahsini, A.; Bentama, J.; Rodriguez, M. A.

    2012-11-01

    Generally textile effluents are highly coloured, contain non-biodegradable compounds and they have high content of solid wastes, comprising fibres and paper wastes. The discharge of such effluents in the environment is worrying for both toxicological and esthetical reasons. The aim of the present work is to study the performances of the combining micro filtration-adsorption process for the treatment of coloured waters. Methylene Blue (MB) was used as model compound. The effects of significant operating parameters such as transmembrane pressure (TMP) and bentonite concentration on the process performance characterized by flux and rejection factor were investigated. Experiments carried out with Methylene Blue solutions confirmed the potential of this combined process for the treatment of dyed waters. (Author) 13 refs.

  2. Adsorption onto activated carbons in environmental engineering: some trends in water and air treatment processes

    Energy Technology Data Exchange (ETDEWEB)

    Le Cloirec, P. [Ecole des Mines de Nantes, UMR CNRS 6144 GEPEA, 44 (France)

    2005-07-01

    Full text of publication follows: Adsorption is commonly used in environmental protection processes and particularly in water and air treatment systems. Organic pollutants in aqueous or gaseous phases are transferred and adsorbed onto porous materials. Activated carbon (powder, grains) treatment is usually carried out and filters are used to eliminate volatile organic compounds (VOC), odors or micropollutants. The main objectives of this paper are to present examples of classical or new activated carbon processes used in drinking water production, wastewater purification or in air treatment in terms of processes, performances and modeling. - Water treatment: Micropollutants such as pesticides, herbicides... are classically removed by activated carbon granular systems in drinking water treatment plants. In order to get a good water quality and to safe money, the breakthrough time has to be accurately determined. Models with mass balance and transfer equations are proposed. However, some difficulties are found especially for complex solutions to get good agreement between experimental data and calculated values. A statistical approach using neural networks is proposed to simulate breakthrough curves. Examples are presented and compared to deterministic models. In order to intensify processes, a combination of ultrafiltration and activated carbon fiber cloth (ACFC) is presented to remove the large spectra of particles and organic molecules present in water. Systems (UF/ACFC) for surface water and industrial colored wastewater are applied and performances are determined as a function of operating conditions. - Air treatment: Activated carbon grain filters are used to control VOC emissions. Due to an exothermic reaction, an increase of local temperature in the reactor is noted and some fire accidents have been reported. For safety technologies, this temperature has to be previously determined. A model is proposed to simulate the breakthrough curves and temperatures

  3. Transformations of particles, metal elements and natural organic matter in different water treatment processes

    Institute of Scientific and Technical Information of China (English)

    YAN Ming-quan; WANG Dong-sheng; SHI Bao-you; WEI Qun-shan; QU Jiu-hui; TANG Hong-xiao

    2007-01-01

    Characterizing namral organic matter(NOM),particles and elements in different water treatment processes Can give a useful information to optimize water treatment operations.In this article,transformations of particles,metal elements and NOM in a pilot-scale water treatment plant were investigated by laser light granularity system,particle counter,glass-fiber membrane filtration,inductively coupled plasma-optical emission spectroscopy,ultra filtration and resin absorbents fractionation.The results showed that particles,NOM and trihalomethane formation precursors were removed synergistically by sequential treamaent of different processes. Preozonation markedly changed the polarity and molecular weight of NOM.and it could be conducive to the following coagulation processthrough destabilizing particles and colloids;mid-ozonation enhanced the subsequent granular activated carbon(GAC)filtration process by decreasing molecular weight of organic matters.Coagulation-flotation and GAC were more efficient in removing fixed suspended solids and larger particles;while sand-filtration was more effcient in removing volatile suspended solids and smaller particles.Flotation performed better than sedimentation in terms of particle and NOM removal.The type of coagulant could greatly affect the performance of coagulation-flotation.Pre-hydrolyzed composite coagulant(HPAC)was superior to FeCl3 concerning the removals of hydrophobic dissolved organic carbon and volatile suspended solids.The leakages of flocs from sand-filtration and microorganisms from GAC should be mitigated to ensure the reliability of the whole treatment system.

  4. Integration of biopolymer production with process water treatment at a sugar factory.

    Science.gov (United States)

    Anterrieu, Simon; Quadri, Luca; Geurkink, Bert; Dinkla, Inez; Bengtsson, Simon; Arcos-Hernandez, Monica; Alexandersson, Tomas; Morgan-Sagastume, Fernando; Karlsson, Anton; Hjort, Markus; Karabegovic, Lamija; Magnusson, Per; Johansson, Peter; Christensson, Magnus; Werker, Alan

    2014-06-25

    The present investigation has focused on generating a surplus denitrifying biomass with high polyhydroxyalkanoate (PHA) producing potential while maintaining water treatment performance in biological nitrogen removal. The motivation for the study was to examine integration of PHA production into the water treatment and residuals management needs at the Suiker Unie sugar beet factory in Groningen, the Netherlands. At the factory, process waters are treated in nitrifying-denitrifying sequencing batch reactors (SBRs) to remove nitrogen found in condensate. Organic slippage (COD) in waters coming from beet washing is the substrate used for denitrification. The full-scale SBR was mimicked at laboratory scale. In two parallel laboratory scale SBRs, a mixed-culture biomass selection strategy of anoxic-feast and aerobic-famine was investigated using the condensate and wash water from Suiker Unie. One laboratory SBR was operated as conventional activated sludge with long solids retention time similar to the full-scale (SRT >16 days) while the other SBR was a hybrid biofilm-activated sludge (IFAS) process with short SRT (4-6 days) for the suspended solids. Both SBRs were found to produce biomass with augmented PHA production potential while sustaining process water treatment for carbon, nitrogen and phosphorus for the factory process waters. PHA producing potential in excess of 60 percent g-PHA/g-VSS was achieved with the lab scale surplus biomass. Surplus biomass of low (4-6 days) and high (>16 days) solids retention time yielded similar results in PHA accumulation potential. However, nitrification performance was found to be more robust for the IFAS SBR. Assessment of the SBR microbial ecology based on 16sDNA and selected PHA synthase genes at full-scale in comparison to biomass from the laboratory scale SBRs suggested that the full-scale process was enriched with a PHA storing microbial community. However, structure-function relationships based on RNA levels for the

  5. Solar-Enhanced Advanced Oxidation Processes for Water Treatment: Simultaneous Removal of Pathogens and Chemical Pollutants.

    Science.gov (United States)

    Tsydenova, Oyuna; Batoev, Valeriy; Batoeva, Agniya

    2015-08-14

    The review explores the feasibility of simultaneous removal of pathogens and chemical pollutants by solar-enhanced advanced oxidation processes (AOPs). The AOPs are based on in-situ generation of reactive oxygen species (ROS), most notably hydroxyl radicals •OH, that are capable of destroying both pollutant molecules and pathogen cells. The review presents evidence of simultaneous removal of pathogens and chemical pollutants by photocatalytic processes, namely TiO2 photocatalysis and photo-Fenton. Complex water matrices with high loads of pathogens and chemical pollutants negatively affect the efficiency of disinfection and pollutant removal. This is due to competition between chemical substances and pathogens for generated ROS. Other possible negative effects include light screening, competitive photon absorption, adsorption on the catalyst surface (thereby inhibiting its photocatalytic activity), etc. Besides, some matrix components may serve as nutrients for pathogens, thus hindering the disinfection process. Each type of water/wastewater would require a tailor-made approach and the variables that were shown to influence the processes-catalyst/oxidant concentrations, incident radiation flux, and pH-need to be adjusted in order to achieve the required degree of pollutant and pathogen removal. Overall, the solar-enhanced AOPs hold promise as an environmentally-friendly way to substitute or supplement conventional water/wastewater treatment, particularly in areas without access to centralized drinking water or sewage/wastewater treatment facilities.

  6. Online total organic carbon (TOC) monitoring for water and wastewater treatment plants processes and operations optimization

    Science.gov (United States)

    Assmann, Céline; Scott, Amanda; Biller, Dondra

    2017-08-01

    Organic measurements, such as biological oxygen demand (BOD) and chemical oxygen demand (COD) were developed decades ago in order to measure organics in water. Today, these time-consuming measurements are still used as parameters to check the water treatment quality; however, the time required to generate a result, ranging from hours to days, does not allow COD or BOD to be useful process control parameters - see (1) Standard Method 5210 B; 5-day BOD Test, 1997, and (2) ASTM D1252; COD Test, 2012. Online organic carbon monitoring allows for effective process control because results are generated every few minutes. Though it does not replace BOD or COD measurements still required for compliance reporting, it allows for smart, data-driven and rapid decision-making to improve process control and optimization or meet compliances. Thanks to the smart interpretation of generated data and the capability to now take real-time actions, municipal drinking water and wastewater treatment facility operators can positively impact their OPEX (operational expenditure) efficiencies and their capabilities to meet regulatory requirements. This paper describes how three municipal wastewater and drinking water plants gained process insights, and determined optimization opportunities thanks to the implementation of online total organic carbon (TOC) monitoring.

  7. Ceramics Vitreous China Produced by Utilizing Sediment Soil from Water Supply Treatment Process

    OpenAIRE

    Wangrakdiskul Ubolrat; Wanasbodee Jindakarn; Sansroi Pornnapa

    2017-01-01

    Due to generating the abundant of sediment soil, it makes the high burden of disposal cost to the metropolitan waterworks authority. Enhancing the value of sediment soil has been explored. This research aims to utilize the sediment soil, wastes of water supply treatment process for producing ceramics vitreous china. In this experiment, five types of raw materials are exploited, namely, sediment soil, ball clay, kaolin, feldspar and silica sand. The formulas have been divided into two groups. ...

  8. Solar-Enhanced Advanced Oxidation Processes for Water Treatment: Simultaneous Removal of Pathogens and Chemical Pollutants

    Directory of Open Access Journals (Sweden)

    Oyuna Tsydenova

    2015-08-01

    Full Text Available The review explores the feasibility of simultaneous removal of pathogens and chemical pollutants by solar-enhanced advanced oxidation processes (AOPs. The AOPs are based on in-situ generation of reactive oxygen species (ROS, most notably hydroxyl radicals •OH, that are capable of destroying both pollutant molecules and pathogen cells. The review presents evidence of simultaneous removal of pathogens and chemical pollutants by photocatalytic processes, namely TiO2 photocatalysis and photo-Fenton. Complex water matrices with high loads of pathogens and chemical pollutants negatively affect the efficiency of disinfection and pollutant removal. This is due to competition between chemical substances and pathogens for generated ROS. Other possible negative effects include light screening, competitive photon absorption, adsorption on the catalyst surface (thereby inhibiting its photocatalytic activity, etc. Besides, some matrix components may serve as nutrients for pathogens, thus hindering the disinfection process. Each type of water/wastewater would require a tailor-made approach and the variables that were shown to influence the processes—catalyst/oxidant concentrations, incident radiation flux, and pH—need to be adjusted in order to achieve the required degree of pollutant and pathogen removal. Overall, the solar-enhanced AOPs hold promise as an environmentally-friendly way to substitute or supplement conventional water/wastewater treatment, particularly in areas without access to centralized drinking water or sewage/wastewater treatment facilities.

  9. Solar-Enhanced Advanced Oxidation Processes for Water Treatment: Simultaneous Removal of Pathogens and Chemical Pollutants

    Science.gov (United States)

    Tsydenova, Oyuna; Batoev, Valeriy; Batoeva, Agniya

    2015-01-01

    The review explores the feasibility of simultaneous removal of pathogens and chemical pollutants by solar-enhanced advanced oxidation processes (AOPs). The AOPs are based on in-situ generation of reactive oxygen species (ROS), most notably hydroxyl radicals •OH, that are capable of destroying both pollutant molecules and pathogen cells. The review presents evidence of simultaneous removal of pathogens and chemical pollutants by photocatalytic processes, namely TiO2 photocatalysis and photo-Fenton. Complex water matrices with high loads of pathogens and chemical pollutants negatively affect the efficiency of disinfection and pollutant removal. This is due to competition between chemical substances and pathogens for generated ROS. Other possible negative effects include light screening, competitive photon absorption, adsorption on the catalyst surface (thereby inhibiting its photocatalytic activity), etc. Besides, some matrix components may serve as nutrients for pathogens, thus hindering the disinfection process. Each type of water/wastewater would require a tailor-made approach and the variables that were shown to influence the processes—catalyst/oxidant concentrations, incident radiation flux, and pH—need to be adjusted in order to achieve the required degree of pollutant and pathogen removal. Overall, the solar-enhanced AOPs hold promise as an environmentally-friendly way to substitute or supplement conventional water/wastewater treatment, particularly in areas without access to centralized drinking water or sewage/wastewater treatment facilities. PMID:26287222

  10. Control policies for a water-treatment system using the Markov Decision Process.

    Science.gov (United States)

    Chiam, Tze; Mitchell, Cary; Yih, Yuehwern

    the system's current state but not the "path" that it has taken. Due to this "memoryless" property and the stochastic properties of the system, the state transition can be modeled by the Markov process. A reward system was constructed to assign reward values to every state visited. A water system is considered to be in a "good" state when it has sufficient clean water to meet the demands of crewmembers. Such states will receive a much higher reward value than states in which crewmembers suffer from water deficiencies. Transition probabilities are obtained through simulation using the Markovian model. Nine policies based on different values of treatment efficiencies for both subsystems were defined. One policy is applied to the system at every hour. The choice of policy to apply affects the system behavior (and state). Hence, it is important to apply a policy that is "best" for the system every hour. The Policy Iteration algorithm is used for this purpose. This algorithm provides the best policy under steady-state conditions. The transition probabilities and reward values are formulated into appropriate mathematical representation and are solved by applying the Policy Iteration algorithm. A system that uses the best policy is compared against one that uses a fixed policy by the use of a paired-t test. Results show that a system applying best policies has statistically better performance than a system operating on a fixed policy. This methodology is also applicable to various other scenarios with different system design, magnitude of "stochastic-ness", including system modules such as the crop system. Research sponsored in part by NASA grant NAG5-12686.

  11. Chemical and ecotoxicological assessments of water samples before and after being processed by a Water Treatment Plant

    Directory of Open Access Journals (Sweden)

    Regina Teresa Rosim Monteiro

    2014-01-01

    Full Text Available Physicochemical and ecotoxicological measurements were employed to appraise the water quality of the Corumbataí River raw water (RW intake, and that of its filtered (FW and treated (TW waters, processed by the Water Treatment Plant (WTP of Piracicaba (SP, Brazil during 2010. Some herbicides: ametrine, atrazine, simazine and tebuthiuron, were measured, with levels ranging from 0.01 to 10.3 µg L-1 . These were lower than those required to produce ecotoxicological effects to aquatic life based on published literature. Similarly, trihalomethanes, such as chloroform and bromodichloromethane produced as a result of the WTP process were also shown to be present in concentrations that would neither harm environmental nor human health. Elevated free chlorine concentrations found in FW and TW were credibly responsible for toxicity effects observed in algae and daphnids. (Pseudokirchneriella subcapitata and Daphnia magna. In contrast, results of toxicity testing conducted with Hydra attenuata suggested that this organism is resistant to free chorine and could be used for drinking water evaluations. Coupling bioassays with chemical analyses proved valuable to uncover putative cause-effect relationships existing between physical, chemical and toxic results, as well as in optimizing data interpretation of water quality.

  12. Synergy of sewage water treatment plants and processing of manure; Synergie RWZI en mestverwerking

    Energy Technology Data Exchange (ETDEWEB)

    Bisschops, I.; Weijma, J.; Van Eekert, M.; Spanjers, H. [Lettinga Associates Foundation LeAF, Wageningen (Netherlands); Timmerman, M.; Fe Buisonje, F. [Wageningen UR Livestock Research WLR, Wageningen (Netherlands)

    2011-05-15

    The goal of this study is to explore profitable ways of processing manure in sewage water treatment plants. Technological options are explored for processing manure, the availability of manure in the surroundings, the space taken up by manure digestion and annual costs and benefits [Dutch] Het doel van deze studie is te verkennen hoe mest op rendabele wijze in rwzi's (rioolwaterzuiveringsinstallaties) verwerkt kunnen worden. Er is gekeken naar de technologische mogelijkheden om mest te kunnen verwerken, de beschikbaarheid van mest in de omgeving, ruimtebeslag van mestvergisting, en jaarlijkse kosten en opbrengsten.

  13. Characterization of titanium dioxide nanoparticle removal in simulated drinking water treatment processes.

    Science.gov (United States)

    Chang, Hui-Hsien; Cheng, Tsun-Jen; Huang, Chin-Pao; Wang, Gen-Shuh

    2017-12-01

    This study characterized the fate of nano-TiO2 in both powder (TiO2(P)) and suspension (TiO2(S)) forms in simulated drinking water treatments. Nano-TiO2 solutions of 0.1, 1.0, and 10mg/L were prepared with deionized water and raw waters from the Changxing and Fengshan Water Treatment Plants in Taiwan to assess the effects of water matrices on nano-TiO2 behavior during water treatment. After the laboratory simulated water treatment, including pre-chlorination, coagulation, sedimentation, filtration and post-chlorination, the residual Ti concentration ranged from 2.7 to 47.4% in different treatment units and overall removal efficiency was between 52.6% and 97.3% in all cases except for nano-TiO2 at concentration of 0.1mg/L. Overall removal efficiency for the TiO2 at 10mg/L concentration ranged from 9.3 to 53.5%. Sedimentation (after coagulation) and filtration were the most important processes for removing nano-TiO2 due in part to particle agglomeration, which was confirmed by size distribution and zeta potential measurements. The size of nano-TiO2 increased from 21-36nm to 4490nm in the supernatant after sedimentation, and subsequent filtration treatment further removed all agglomerates at size >1μm. Zeta potential revealed interactions between nano-TiO2 particles and anionic functional groups or negatively-charged natural organic matters, leading to a decrease in surface charge. After sedimentation and filtration, the zeta potential of supernatants and filtrates were close to zero, meaning the absence of nanoparticles. The highest Ti removal after sedimentation occurred in Fengshan raw water due to higher ionic strength and coagulant dosage applied. On the other hand, the surfactant additives in TiO2(S) promoted dispersion of nano-TiO2 particles, which in turn led to lower particle removal. SEM images of nanoparticles after chlorination or coagulation revealed the coverage of nano-TiO2 particles by viscous substances and formation of colloidal structures

  14. Transformation of pharmaceuticals during oxidation/disinfection processes in drinking water treatment

    Energy Technology Data Exchange (ETDEWEB)

    Postigo, Cristina [Institute for Environmental Assessment and Water Research (IDAEA)—Spanish National Research Council (CID-CSIC), Barcelona (Spain); Richardson, Susan D., E-mail: richardson.susan@sc.edu [Department of Chemistry and Biochemistry, University of South Carolina, Columbia, SC (United States)

    2014-08-30

    Graphical abstract: - Highlights: • Review of transformation pathways of pharmaceuticals during disinfection processes. • DBPs are formed with chlorine, chloramine, ozone, chlorine dioxide, UV, or UV/H{sub 2}O{sub 2}. • Chlorine reacts with amine and reduced sulfur groups and activated aromatic systems. • Chlorine dioxide and ozone react with electron-rich functional groups. • Potential health effects are noted for some pharmacuetical DBPs when available. - Abstract: Pharmaceuticals are emerging contaminants of concern and are widespread in the environment. While the levels of these substances in finished drinking waters are generally considered too low for human health concern, there are now concerns about their disinfection by-products (DBPs) that can form during drinking water treatment, which in some cases have been proven to be more toxic than the parent compounds. The present manuscript reviews the transformation products of pharmaceuticals generated in water during different disinfection processes, i.e. chlorination, ozonation, chloramination, chlorine dioxide, UV, and UV/hydrogen peroxide, and the main reaction pathways taking place. Most of the findings considered for this review come from controlled laboratory studies involving reactions of pharmaceuticals with these oxidants used in drinking water treatment.

  15. Removal of Stabilized Silver Nanoparticles from Ohio River Water by Potable Water Treatment Processes

    Science.gov (United States)

    Due to their extensive use, silver nanoparticles (Ag NPs) are likely to occur in drinking water sources. Once released into the environment they are considered an emerging contaminant in water and wastewater. The main objective of this research is to investigate the removal of di...

  16. Characterization of aquatic humic substances to DBPs formation in advanced treatment processes for conventionally treated water.

    Science.gov (United States)

    Kim, Hyun-Chul; Yu, Myong-Jin

    2007-05-01

    An advanced water treatment demonstration plant consisted of ozone/granular activated carbon processes was operated to study feasibility of the processes. Natural organic matter (NOM) from raw and process waters at the demonstration plant was isolated into humic and non-humic fractions by physicochemical fractionation method to investigate characteristics of humic fraction (i.e., humic substances, HS) as a predominant haloform reactant. Ozone did not significantly oxidize the carboxylic fraction (from 39.1 to 35.9%), while GAC removed some of the carboxylic fraction (from 35.9 to 29.1%). Formation potential of trihalomethanes (THMs) as compared to haloacetic acids formation potential (HAAFP) was highly influenced by HS. Higher yields of THMs resulted from chlorination of HS with a higher phenolic content and phenolic fraction in the HS gradually decreased from 60.5% to 15.8% through the water treatment. The structural and functional changes of HS were identified by elemental, Fourier-transform infrared (FT-IR) and proton nuclear magnetic resonance ((1)H NMR) analyses, and these results were mutually consistent. The functional distribution data obtained by using A-21 resin could be used to support the interpretation of data obtained from the spectroscopic analyses. Decreases in ratio of UV absorbance at 253 nm and 203 nm (A(253)/A(203)) and DBPFPs/DOC showed consistent trends, therefore, A(253)/A(203) ratio may be a good indicator for the disinfection by-product formation potentials (DBPFPs).

  17. Comparison of methods for assessing reverse osmosis membrane treatment of shrimp process water.

    Science.gov (United States)

    Casani, Sandra; Hansen, Tina B; Christensen, Jakob; Knøchel, Susanne

    2005-04-01

    Interest in reuse of process water from the food industry has reinforced the importance of controlling and monitoring the effectiveness and reliability of treatment systems regarding removal of organic matter and microorganisms. The ability of adenosine triphosphate bioluminescence, conductivity, turbidometry, absorbance, and multichannel fluorescence spectroscopy for indirectly monitoring the integrity of a reverse osmosis membrane when treating process water recovered from peeling in a shrimp processing line was evaluated. This study demonstrated that reverse osmosis was capable of removing bacteria (ca. 7 log CFU ml(-1)) to the levels required by the regulatory authorities for water recycling within the same food unit operation. Adenosine triphosphate and turbidometry showed a higher sensitivity for detecting compromising conditions at the treatment system (0.1% concentration of feed in permeate) and a better correlation with the aerobic count at lower levels than the other methods investigated. The sensitivity for assessing membrane integrity of conductivity and multichannel fluorescence was 1% of feed in permeate. Impact of feed variations was best leveled out in the permeates for turbidity measurements. Multichannel fluorescence spectroscopy may require laborious calibration procedures and expertise regarding data analysis and interpretation of results, which are not always available in food industries. Absorbance did not respond to changes in membrane integrity and was not well correlated to the aerobic count because of the poor sensitivity of this method for these purposes.

  18. Treatment of sewage sludge in supercritical water and evaluation of the combined process of supercritical water gasification and oxidation.

    Science.gov (United States)

    Qian, Lili; Wang, Shuzhong; Xu, Donghai; Guo, Yang; Tang, Xingying; Wang, Longfei

    2015-01-01

    Influences of temperature and oxidation coefficient (n) on sewage sludge treatment in supercritical water and its corresponding reaction mechanism were studied. Moreover, the combined process of supercritical water gasification (SCWG) and supercritical water oxidation (SCWO) was also investigated. The results show that ammonia nitrogen, phenols and pyridines are main refractory intermediates. The weight of solid products at 873K and n=4 is only 3.5wt.% of the initial weight, which is lower than that after combustion. Volatile organics in solid phase have almost released at 723K and n=0. Highest yield of combustible gases was obtained at n=0, and H2 yield can reach 11.81mol/kg at 873K. Furthermore, the combination of SCWG at 723K and SCWO at 873K with a total n=1 is feasible for its good effluent quality and low operation costs.

  19. Special wettable nanostructured copper mesh achieved by a facile hot water treatment process

    Science.gov (United States)

    Saadi, Nawzat S.; Hassan, Laylan B.; Brozak, Matt; Karabacak, Tansel

    2017-09-01

    In this research, a special wettable copper mesh with superhydrophobicity and superoleophilicity properties is reported using a low-cost, eco-friendly, rapid, and scalable synthesis method. Hot water treatment (HWT) method is used to integrate the micro-textured copper mesh surface with a nanoscale roughness to achieve a hierarchical micro-nano structured surface. The surface energy of the nanoscale roughened copper mesh reduced by coating the hot water treated mesh with polymer ligands containing thiol or fluorine functional groups of low energy. Surface morphology characterization showed the formation of copper oxide nanostructures on the mesh surface by hot water process performed at 95 °C and under a low dissolved oxygen condition. X-ray diffraction patterns reveal the development of stable, uniformly distributed, and compactly arranged, cubic and plate-like nanostructures of cuprous oxide (Cu2O) on the copper mesh surface. The surface wettability of the as-prepared copper mesh was assessed by contact angle (CA) measurement for water and several oils and organic solvents. CA values showed the formation of special wettable copper mesh surface with superhydrophobic property with water contact angle of about 157° and superoleophilic property with oil contact angle as low as 0°. In addition, the effect of the mesh’s geometry on the wetting property was examined through correlations between wire diameter, pore size, and optimal values for the highest water CA.

  20. Characterization of suspended bacteria from processing units in an advanced drinking water treatment plant of China.

    Science.gov (United States)

    Wang, Feng; Li, Weiying; Zhang, Junpeng; Qi, Wanqi; Zhou, Yanyan; Xiang, Yuan; Shi, Nuo

    2017-05-01

    For the drinking water treatment plant (DWTP), the organic pollutant removal was the primary focus, while the suspended bacterial was always neglected. In this study, the suspended bacteria from each processing unit in a DWTP employing an ozone-biological activated carbon process was mainly characterized by using heterotrophic plate counts (HPCs), a flow cytometer, and 454-pyrosequencing methods. The results showed that an adverse changing tendency of HPC and total cell counts was observed in the sand filtration tank (SFT), where the cultivability of suspended bacteria increased to 34%. However, the cultivability level of other units stayed below 3% except for ozone contact tank (OCT, 13.5%) and activated carbon filtration tank (ACFT, 34.39%). It meant that filtration processes promoted the increase in cultivability of suspended bacteria remarkably, which indicated biodegrading capability. In the unit of OCT, microbial diversity indexes declined drastically, and the dominant bacteria were affiliated to Proteobacteria phylum (99.9%) and Betaproteobacteria class (86.3%), which were also the dominant bacteria in the effluent of other units. Besides, the primary genus was Limnohabitans in the effluents of SFT (17.4%) as well as ACFT (25.6%), which was inferred to be the crucial contributors for the biodegradable function in the filtration units. Overall, this paper provided an overview of community composition of each processing units in a DWTP as well as reference for better developing microbial function for drinking water treatment in the future.

  1. Pilot plant study on ozonation and biological activated carbon process for drinking water treatment

    Institute of Scientific and Technical Information of China (English)

    2006-01-01

    A study on advanced drinking water treatment was conducted in a pilot scale plant taking water from conventional treatment process. Ozonation-biological activated carbon process (O3-BAC) and granular activated carbon process (GAC) were evaluated based on the following parameters: CODMn, UV254, total organic carbon (TOC), assimilable organic carbon (AOC) and biodegradable dissolved organic carbon (BDOC). In this test, the average removal rates of CODMn , UV254 and TOC in O3-BAC were18.2%, 9.0% and 10.2% higher on (AOC) than in GAC, respectively. Ozonation increased 19.3-57.6 μg Acetate-C/L in AOC-P17,45.6-130.6 μg Acetate-C/L in AOC-NOX and 0.1-0.5 mg/L in BDOC with ozone doses of 2-8 mg/L. The optimum ozone dose for maximum AOC formation was 3 mgO3/L. BAC filtration was effective process to improve biostability.

  2. Replacement of chemical intensive water treatment processes with energy saving membrane. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Mickley, M.C.; Goering, S.W.

    1983-11-01

    The project investigated the use of charged ultrafiltration membranes to treat hard water. More specifically, the work was undertaken to (1) make charged ultrafiltration membranes to demonstrate the technical feasibility of the chemical grafting approach; (2) evaluate the market potential for charged ultrafiltration membranes; and (3) evaluate the cost and energy savings for using charged ultrafiltration as compared to lime-based clarification and other treatment methods. The results suggest that chemical grafting is a relatively simple, reproducible and low-cost way to modify existing substrate materials to give them enhanced transport performance. Process studies lead to the identification of good market potential for membrane processes using charged ultrafiltration membranes. Capital and operating costs relative to lime-based clarification are favorable for low- and medium-sized treatment plants. Finally, substantial energy savings are apparent as compared to lime-based precipitation systems which incur substantial energy consumption in the lime production and transportation steps.

  3. Separation, Characterization and Fouling Potential of Sludge Waters from Different Biological Wastewater Treatment Processes

    KAUST Repository

    Xue, Jinkai

    2011-07-01

    The major limitation, which hinders the wider application of membrane technology and increases the operating costs of membranes involved in wastewater treatment plants, is membrane fouling induced by organic matter. Extracellular polymeric products (EPS) and soluble microbial products (SMP) are the two most mentioned major foulants in publications, for which the debate on precise definitions seems to be endless. Therefore, a concept of sludge water, which conceptually covers both EPS and SMP, has been developed in this research. A standard procedure of sludge water separation, which is centrifugation at 4000g for 15 min followed by 1.2μm glass fiber filter filtration, was established based on separation experiments with membrane tank sludge from the KAUST MBR wastewater treatment plant. Afterwards, sludge waters from the KAUST MBR WWTP anoxic tank, aerobic tank and membrane tank as well as sludge waters from the Jeddah WWTP anoxic tank, aerobic tank and secondary effluent were produced through the previously developed standard procedure. The obtained sludge water samples were thereafter characterized with TOC/COD, LC-­‐OCD and F-­‐EEM, which showed that KAUST anoxic/ aerobic /membrane tank sludge waters had similar characteristics for all investigated parameters, yet the influent naturally had a higher DOC and biopolymer concentration. Moreover, lower TOC/COD, negligible biopolymers and low levels of humics were found in KAUST effluent. Compared with the KAUST MBR WWTP, the Jeddah WWTP’s sludge waters generally had higher DOC and biopolymer concentrations. To investigate sludge water fouling potential, the KAUST membrane tank sludge water as well as the Jeddah secondary effluent were filtrated through a membrane array consisting of an ultrafiltration (UF) Millipore RC10kDa at the first step followed by a nanofiltration (NF) KOCH Acid/Base stable NF200 at the second step. It was found that cake layer and standard blocking occurred simultaneously during both

  4. Recent Developments in Homogeneous Advanced Oxidation Processes for Water and Wastewater Treatment

    Directory of Open Access Journals (Sweden)

    M. Muruganandham

    2014-01-01

    Full Text Available This paper reports on recent developments in homogeneous Advanced Oxidation Processes (AOPs for the treatment of water and wastewater. It has already been established that AOPs are very efficient compared to conventional treatment methods for degradation and mineralization of recalcitrant pollutants present in water and wastewater. AOPs generate a powerful oxidizing agent, hydroxyl radical, which can react with most of the pollutants present in wastewater. Therefore, it is important to discuss recent developments in AOPs. The homogeneous AOPs such as O3, UV/O3, UV/O3/H2O2, and UV/H2O2, Fe2+/H2O2, UV/Fe2+/H2O2 on the degradation of pollutants are discussed in this paper. The influence on the process efficiency of various experimental parameters such as solution pH, temperature, oxidant concentration, and the dosage of the light source is discussed. A list of contaminants used for degradation by various AOPs and the experimental conditions used for the treatment are discussed in detail.

  5. Improving AOC degradation rate by intensified biological process in advanced water treatment

    Institute of Scientific and Technical Information of China (English)

    AN Dong; LI Wei-guang; SONG Jia-xiu; CUI Fu-yi

    2007-01-01

    The object of is to evaluate assimilable organic carbon(AOC) degradation rate by intensified biological technique in advanced water treatment. By artificially acclimating and cultivating strains attached onto carbon surface, the selected strains can be intensified for their degradation to organic matters. The research indicates that ozonation process increases AOC concentration considerably, however, it is beneficial to microdegradation. Temperature and empty bed contact time ( TEBC ) are two important factors affecting microbiology. From 14 to 27 ℃, intensified biological carbon can remove AOC better compared with granular activated carbon (GAC). Under identical TEBC, intensified technique increases more than 10% AOC reduction.

  6. Produced Water Treatment Using the Switchable Polarity Solvent Forward Osmosis (SPS FO) Desalination Process: Preliminary Engineering Design Basis

    Energy Technology Data Exchange (ETDEWEB)

    Wendt, Daniel; Adhikari, Birendra; Orme, Christopher; Wilson, Aaron

    2016-05-01

    Switchable Polarity Solvent Forward Osmosis (SPS FO) is a semi-permeable membrane-based water treatment technology. INL is currently advancing SPS FO technology such that a prototype unit can be designed and demonstrated for the purification of produced water from oil and gas production operations. The SPS FO prototype unit will used the thermal energy in the produced water as a source of process heat, thereby reducing the external process energy demands. Treatment of the produced water stream will reduce the volume of saline wastewater requiring disposal via injection, an activity that is correlated with undesirable seismic events, as well as generate a purified product water stream with potential beneficial uses. This paper summarizes experimental data that has been collected in support of the SPS FO scale-up effort, and describes how this data will be used in the sizing of SPS FO process equipment. An estimate of produced water treatment costs using the SPS FO process is also provided.

  7. Microbiological contamination and resistance genes in biofilms occurring during the drinking water treatment process.

    Science.gov (United States)

    Farkas, Anca; Butiuc-Keul, Anca; Ciatarâş, Dorin; Neamţu, Călin; Crăciunaş, Cornelia; Podar, Dorina; Drăgan-Bularda, Mihail

    2013-01-15

    Biofilms are the predominant mode of microbial growth in drinking water systems. A dynamic exchange of individuals occurs between the attached and planktonic populations, while lateral gene transfer mediates genetic exchange in these bacterial communities. Integrons are important vectors for the spread of antimicrobial resistance. The presence of class 1 integrons (intI1, qac and sul genes) was assessed in biofilms occurring throughout the drinking water treatment process. Isolates from general and specific culture media, covering a wide range of environmental bacteria, fecal indicators and opportunistic pathogens were tested. From 96 isolates tested, 9.37% were found to possess genetic determinants of putative antimicrobial resistance, and these occurred in both Gram-positive and Gram-negative bacteria. Class 1 integron integrase gene was present in 8.33% of bacteria, all positive for the qacEΔ1 gene. The sul1 gene was present in 3.12% of total isolates, representing 37.5% of the class 1 integron positive cells. The present study shows that biofilm communities in a drinking water treatment plant are a reservoir of class 1 integrons, mainly in bacteria that may be associated with microbiological contamination. Eight out of nine integron bearing strains (88.8%) were identified based on 16S rRNA gene sequencing as either enteric bacteria or species that may be connected to animal and anthropogenic disturbance. Copyright © 2012 Elsevier B.V. All rights reserved.

  8. Fate of cyanobacteria and their metabolites during water treatment sludge management processes

    Energy Technology Data Exchange (ETDEWEB)

    Ho, Lionel, E-mail: lionel.ho@sawater.com.au [Australian Water Quality Centre, SA Water Corporation, 250 Victoria Square, Adelaide, SA 5000 (Australia); Centre for Water Management and Reuse, University of South Australia, Mawson Lakes, SA 5095 (Australia); Dreyfus, Jennifer; Boyer, Justine; Lowe, Todd [Australian Water Quality Centre, SA Water Corporation, 250 Victoria Square, Adelaide, SA 5000 (Australia); Bustamante, Heriberto; Duker, Phil [Sydney Water, PO Box 399, Parramatta, NSW 2124 (Australia); Meli, Tass [TRILITY Pty Ltd, PO Box 86, Appin, NSW 2560 (Australia); Newcombe, Gayle [Australian Water Quality Centre, SA Water Corporation, 250 Victoria Square, Adelaide, SA 5000 (Australia); Centre for Water Management and Reuse, University of South Australia, Mawson Lakes, SA 5095 (Australia)

    2012-05-01

    Cyanobacteria and their metabolites are an issue for water authorities; however, little is known as to the fate of coagulated cyanobacterial-laden sludge during waste management processes in water treatment plants (WTPs). This paper provides information on the cell integrity of Anabaena circinalis and Cylindrospermopsis raciborskii during: laboratory-scale coagulation/sedimentation processes; direct filtration and backwashing procedures; and cyanobacterial-laden sludge management practices. In addition, the metabolites produced by A. circinalis (geosmin and saxitoxins) and C. raciborskii (cylindrospermopsin) were investigated with respect to their release (and possible degradation) during each of the studied processes. Where sedimentation was used, coagulation effectively removed cyanobacteria (and intracellular metabolites) without any considerable exertion on coagulant demand. During direct filtration experiments, cyanobacteria released intracellular metabolites through a stagnation period, suggesting that more frequent backwashing of filters may be required to prevent floc build-up and metabolite release. Cyanobacteria appeared to be protected within the flocs, with minimal damage during backwashing of the filters. Within coagulant sludge, cyanobacteria released intracellular metabolites into the supernatant after 3 d, even though cells remained viable up to 7 d. This work has improved the understanding of cyanobacterial metabolite risks associated with management of backwash water and sludge and is likely to facilitate improvements at WTPs, including increased monitoring and the application of treatment strategies and operational practices, with respect to cyanobacterial-laden sludge and/or supernatant recycle management. - Highlights: Black-Right-Pointing-Pointer Coagulation removed cyanobacteria without an additional exertion on coagulant demand. Black-Right-Pointing-Pointer During a stagnation period in direct filtration intracellular metabolites were

  9. Hydrogen production by supercritical water gasification of wastewater from food waste treatment processes

    Energy Technology Data Exchange (ETDEWEB)

    Lee, In-Gu [Korea Institute of Energy Research (Korea, Republic of)

    2010-07-01

    Korean food wastes have high moisture content (more than 85 wt%) and their major treatment processes such as drying or biological fermentations generate concentrated organic wastewater (CODs of about 100,000 mgO{sub 2}/L). For obtaining both wastewater treatment and hydrogen production from renewable resources, supercritical water gasification (SCWG) of the organic wastewater was carried out in this work. The effect of catalyst, reaction temperature, and reactor residence time on COD destruction and composition of gas products was examined. As a result, a SCWG of the wastewater over Ni- Y/activated charcoal at 700 C, 28 MPa yielded 99 % COD destruction and hydrogen-rich gas production (45 vol% H{sub 2}). A liquid-phase thermal pretreatment to destroy solid particles from the wastewater was proposed for more effective operation of the SCWG system. (orig.)

  10. Impact of treatment processes on the removal of perfluoroalkyl acids from the drinking water production chain

    NARCIS (Netherlands)

    C. Eschauzier; E. Beerendonk; P. Scholte-Veenendaal; P. de Voogt

    2012-01-01

    The behavior of polyfluoralkyl acids (PFAAs) from intake (raw source water) to finished drinking water was assessed by taking samples from influent and effluent of the several treatment steps used in a drinking water production chain. These consisted of intake, coagulation, rapid sand filtration, du

  11. Radiological assessment of water treatment processes in a water treatment plant in Saudi Arabia: Water and sludge radium content, radon air concentrations and dose rates

    Energy Technology Data Exchange (ETDEWEB)

    Al-Jaseem, Q.Kh., E-mail: qjassem@kacst.edu.sa [Nuclear Science Research Institute (NSRI), King Abdulaziz City for Science and Technology (KACST), P.O. Box 6086, Riyadh 11442 (Saudi Arabia); Almasoud, Fahad I. [Nuclear Science Research Institute (NSRI), King Abdulaziz City for Science and Technology (KACST), P.O. Box 6086, Riyadh 11442 (Saudi Arabia); Ababneh, Anas M. [Physics Dept., Faculty of Science, Islamic University in Madinah, Al-Madinah, P.O. Box 170 (Saudi Arabia); Al-Hobaib, A.S. [Nuclear Science Research Institute (NSRI), King Abdulaziz City for Science and Technology (KACST), P.O. Box 6086, Riyadh 11442 (Saudi Arabia)

    2016-09-01

    There is an increase demand for clean water sources in Saudi Arabia and, yet, renewable water resources are very limited. This has forced the authorities to explore deep groundwater which is known to contain large concentrations of radionuclides, mainly radium isotopes. Lately, there has been an increase in the number of water treatment plants (WTPs) around the country. In this study, a radiological assessment of a WTP in Saudi Arabia was performed. Raw water was found to have total radium activity of 0.23 Bq/L, which exceeds the international limit of 0.185 Bq/L (5 pCi/L). The WTP investigated uses three stages of treatment: flocculation/sedimentation, sand filtration and reverse osmosis. The radium removal efficiency was evaluated for each stage and the respective values were 33%, 22% and 98%. Moreover, the activity of radium in the solid waste generated from the WTP in the sedimentation and sand filtrations stages were measured and found to be 4490 and 6750 Bq/kg, respectively, which exceed the national limit of 1000 Bq/kg for radioactive waste. A radiological assessment of the air inside the WTP was also performed by measuring the radon concentrations and dose rates and were found in the ranges of 2–18 Bq/m{sup 3} and 70–1000 nSv/h, respectively. The annual effective dose was calculated and the average values was found to be 0.3 mSv which is below the 1 mSv limit. - Highlights: • Radiological assessment of groundwater treatment plant was performed. • Radium Removal efficiency was calculated for different stages during water treatment. • Radium concentrations in sludge were measured and found to exceed the national limit for radioactive waste. • Air radon concentrations and dose rates were monitored in the water treatment plant. • The Reverse Osmosis (RO) unit was found to record the highest air radon concentrations and dose rates.

  12. Water Treatment Technology - Flouridation.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on flouridation provides instructional materials for three competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: purpose and process of flouridation, correct…

  13. Water Treatment Technology - Chlorination.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on chlorination provides instructional materials for nine competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: purpose and process of chlorination, chlorine…

  14. Study of the combining adsorption-microfiltration process for the treatment of coloured waters

    Directory of Open Access Journals (Sweden)

    Addaou, Abdelah

    2012-06-01

    Full Text Available Generally textile effluents are highly coloured, contain non-biodegradable compounds and they have high content of solid wastes, comprising fibres and paper wastes. The discharge of such effluents in the environment is worrying for both toxicological and esthetical reasons. The aim of the present work is to study the performances of the combining microfiltration-adsorption process for the treatment of coloured waters. Methylene Blue (MB was used as model compound. The effects of significant operating parameters such as transmembrane pressure (TMP and bentonite concentration on the process performance characterized by flux and rejection factor were investigated. Experiments carried out with Methylene Blue solutions confirmed the potential of this combined process for the treatment of dyed waters.

    Normalmente los efluentes de la industria textil están coloreados y contienen compuestos no biodegradables además de residuos sólidos, fibras y residuos de papel. La liberación de tales efluentes al ambiente es preocupante tanto por razones estéticas como toxicológicas. El propósito del presente trabajo es realizar el estudio de las prestaciones del proceso combinado de adsorción-microfiltración para el tratamiento de aguas coloreadas. Se utilizó Azul de Metileno como compuesto tipo. La influencia de parámetros de operación tales como Presión transmembrana y la concentración de bentonita en el comportamiento del proceso, caracterizado por el flujo del permeado y el factor de retorno que fueron los parámetros estudiados. Los experimentos realizados con las soluciones de Azul de Metileno han confirmado el potencial del proceso combinado para el tratamiento de las aguas teñidas.

  15. Critical review of electrochemical advanced oxidation processes for water treatment applications.

    Science.gov (United States)

    Chaplin, Brian P

    2014-05-01

    Electrochemical advanced oxidation processes (EAOPs) have emerged as novel water treatment technologies for the elimination of a broad-range of organic contaminants. Considerable validation of this technology has been performed at both the bench-scale and pilot-scale, which has been facilitated by the development of stable electrode materials that efficiently generate high yields of hydroxyl radicals (OH˙) (e.g., boron-doped diamond (BDD), doped-SnO2, PbO2, and substoichiometic- and doped-TiO2). Although a promising new technology, the mechanisms involved in the oxidation of organic compounds during EAOPs and the corresponding environmental impacts of their use have not been fully addressed. In order to unify the state of knowledge, identify research gaps, and stimulate new research in these areas, this review critically analyses published research pertaining to EAOPs. Specific topics covered in this review include (1) EAOP electrode types, (2) oxidation pathways of select classes of contaminants, (3) rate limitations in applied settings, and (4) long-term sustainability. Key challenges facing EAOP technologies are related to toxic byproduct formation (e.g., ClO4(-) and halogenated organic compounds) and low electro-active surface areas. These challenges must be addressed in future research in order for EAOPs to realize their full potential for water treatment.

  16. Treatment and Recycling of the Process Water in Iron Ore Flotation of Yuanjiacun Iron Mine

    Directory of Open Access Journals (Sweden)

    Wen-li Jiang

    2017-01-01

    Full Text Available Coagulating sedimentation and oxidation treatment of process water in iron ore flotation of Yuanjiacun iron mine had been studied. The process water of this mine carried residual polyacrylamide (PAM, poly(diallyldimethylammonium chloride (PDADMAC, and Ca2+ from the flotation and caused decrease of the iron flotation recovery or grade of the concentrate. The studies on high-intensity magnetic separation (HIMS tailings for coagulating sedimentation showed that the settling performance of coagulant (named CYH was better than that of PDADMAC. The analyses of FTIR spectra and zeta potential demonstrated that CYH is adsorbed mainly through electrostatic attraction onto HIMS tailings. Sodium hypochlorite was adopted to oxidize the residual organics in tailings wastewater. When sodium hypochlorite is at the dosage of 1.0 g/L, reaction temperature is of 20°C, and reaction time is of 30 minutes, the removal rates of PAM, COD, and Ca2+ were 90.48%, 83.97%, and 85.00%, respectively. Bench-scale flotation studies on the treated tailings wastewater indicated that the iron recovery and grade of concentrate were close to those of freshwater.

  17. Contaminants retention in soils as a complementary water treatment method: application in soil-aquifer treatment processes

    OpenAIRE

    Martins, Tiago André Nunes

    2016-01-01

    Tese de mestrado, Geologia Aplicada (Hidrogeologia), Universidade de Lisboa, Faculdade de Ciências, 2016 Soil-Aquifer Treatment (SAT) is a well-established Managed Aquifer Recharge (MAR) complementary method which main purpose is to increase water availability in aquifers by enhancing the quality of the injected water. SAT-MAR methods are an important way of addressing water scarcity challenges by reusing water of impaired quality, such as wastewater, converting it into a reliable resource...

  18. Occurrence and removal of phenolic endocrine disrupting chemicals in the water treatment processes

    Science.gov (United States)

    Lv, Xuemin; Xiao, Sanhua; Zhang, Gang; Jiang, Pu; Tang, Fei

    2016-03-01

    This paper evaluated the occurrence and removal efficiency of four selected phenolic endocrine disrupting chemicals (bisphenol A (BPA), octylphenol (OP), nonylphenol (NP) and diethylstilbestrol (DES)) in two drinking waterworks in Jiangsu province which take source water from Taihu Lake. The recombined yeast estrogen screen (YES) and liquid chromatography tandem mass spectrometry (LC-MS/MS) were applied to assess the estrogenicity and detect the estrogens in the samples. The estrogen equivalents (EEQs) ranged from nd (not detected) to 2.96 ng/L, and the estrogenic activities decreased along the processes. Among the 32 samples, DES prevailed in all samples, with concentrations ranging 1.46-12.0 ng/L, BPA, OP and NP were partially detected, with concentrations ranging from nd to 17.73 ng/L, nd to 0.49 ng/L and nd to 3.27 ng/L, respectively. DES was found to be the main contributor to the estrogenicity (99.06%), followed by NP (0.62%), OP (0.23%) and BPA (0.09%). From the observation of treatment efficiency, the advanced treatment processes presented much higher removal ratio in reducing DES, the biodegradation played an important role in removing BPA, ozonation and pre-oxidation showed an effective removal on all the four estrogens; while the conventional ones can also reduce all the four estrogens.

  19. Microbicidal efficacy of an advanced oxidation process using ozone/hydrogen peroxide in water treatment.

    Science.gov (United States)

    Sommer, R; Pribil, W; Pfleger, S; Haider, T; Werderitsch, M; Gehringer, P

    2004-01-01

    The combined application of ozone and hydrogen peroxide represents a kind of advanced oxidation for water treatment. The radicals that are generated during the process are used for the degradation of organic pollutants from groundwater and industrial effluents. The aim of our study was to evaluate the possible microbicidal, and particularly virucidal, efficacy of such a process, since no substantial data were available. The investigations were performed at a pilot plant installed for the elimination of perchloroethylene from polluted groundwater (reduction efficacy for perchloroethylene from 26 microg/L to 5 microg/L). To enable a reliable evaluation of the microbicidal effect, a set of alternate test organisms was used. As model viruses we chose bacteriophages MS2 (F+ specific, single-stranded RNA), phiX174 (single-stranded DNA) and PRD-1 (coated, double-stranded DNA). Furthermore, spores of Bacillus subtilis were included as possible surrogates for protozoa and Escherichia coli as representative for traditional indicator bacteria used in water analysis. The microbicidal efficiency was compared to the inactivation by means of ozone under two standard conditions (20 degrees C): (a) 0.4 mg/L residual after 4 min and (b) 0.1 mg/L residual after 10 min. Surprisingly, a good microbicidal effect of the ozone/hydrogen peroxide process was found. This was somewhat unexpected, because we had assumed that the disinfection potential of ozone would have been interfered with by the presence of hydrogen peroxide. Escherichia coli and the three test viruses revealed a reduction of about 6-log. In contrast, spores of Bacillus subtilis showed after the total process a reduction of 0.4-log. These results matched the effect of the ozone treatment (a) with a residual of 0.4 mg/L after 4 min contact time (20 degrees C). The test condition (b) with a residual of 0.1 mg/L ozone after a contact time of 10 min at 20 degrees C gave a higher reduction of the B. subtilis spores (1.5-log

  20. Seasonal and spatial evolution of trihalomethanes in a drinking water distribution system according to the treatment process.

    Science.gov (United States)

    Domínguez-Tello, A; Arias-Borrego, A; García-Barrera, Tamara; Gómez-Ariza, J L

    2015-11-01

    This paper comparatively shows the influence of four water treatment processes on the formation of trihalomethanes (THMs) in a water distribution system. The study was performed from February 2005 to January 2012 with analytical data of 600 samples taken in Aljaraque water treatment plant (WTP) and 16 locations along the water distribution system (WDS) in the region of Andévalo and the coast of Huelva (southwest Spain), a region with significant seasonal and population changes. The comparison of results in the four different processes studied indicated a clear link of the treatment process with the formation of THM along the WDS. The most effective treatment process is preozonation and activated carbon filtration (P3), which is also the most stable under summer temperatures. Experiments also show low levels of THMs with the conventional process of preoxidation with potassium permanganate (P4), delaying the chlorination to the end of the WTP; however, this simple and economical treatment process is less effective and less stable than P3. In this study, strong seasonal variations were obtained (increase of THM from winter to summer of 1.17 to 1.85 times) and a strong spatial variation (1.1 to 1.7 times from WTP to end points of WDS) which largely depends on the treatment process applied. There was also a strong correlation between THM levels and water temperature, contact time and pH. On the other hand, it was found that THM formation is not proportional to the applied chlorine dose in the treatment process, but there is a direct relationship with the accumulated dose of chlorine. Finally, predictive models based on multiple linear regressions are proposed for each treatment process.

  1. Characterisation and treatment of VOCs in process water from upgrading facilities for compressed biogas (CBG).

    Science.gov (United States)

    Nilsson Påledal, S; Arrhenius, K; Moestedt, J; Engelbrektsson, J; Stensen, K

    2016-02-01

    Compression and upgrading of biogas to vehicle fuel generates process water, which to varying degrees contains volatile organic compounds (VOCs) originating from the biogas. The compostion of this process water has not yet been studied and scientifically published and there is currently an uncertainty regarding content of VOCs and how the process water should be managed to minimise the impact on health and the environment. The aim of the study was to give an overview about general levels of VOCs in the process water. Characterisation of process water from amine and water scrubbers at plants digesting waste, sewage sludge or agricultural residues showed that both the average concentration and composition of particular VOCs varied depending on the substrate used at the biogas plant, but the divergence was high and the differences for total concentrations from the different substrate groups were only significant for samples from plants using waste compared to residues from agriculture. The characterisation also showed that the content of VOCs varied greatly between different sampling points for same main substrate and between sampling occasions at the same sampling point, indicating that site-specific conditions are important for the results which also indicates that a number of analyses at different times are required in order to make an more exact characterisation with low uncertainty. Inhibition of VOCs in the anaerobic digestion (AD) process was studied in biomethane potential tests, but no inhibition was observed during addition of synthetic process water at concentrations of 11.6 mg and 238 mg VOC/L.

  2. Ceramics Vitreous China Produced by Utilizing Sediment Soil from Water Supply Treatment Process

    Directory of Open Access Journals (Sweden)

    Wangrakdiskul Ubolrat

    2017-01-01

    Full Text Available Due to generating the abundant of sediment soil, it makes the high burden of disposal cost to the metropolitan waterworks authority. Enhancing the value of sediment soil has been explored. This research aims to utilize the sediment soil, wastes of water supply treatment process for producing ceramics vitreous china. In this experiment, five types of raw materials are exploited, namely, sediment soil, ball clay, kaolin, feldspar and silica sand. The formulas have been divided into two groups. Sediment soil has been used as substituted material in ball clay for the first group, and substituted in kaolin for the second group. The specimens of each formula are formed by uniaxial pressing at 100 bar of size 50×100×7 mm. Then they have been sintered at two different temperatures, 1200°C and 1250°C, with heating rate 400° C/ hr and soaking for 30 minutes. The result reveals that the suitable formula for ceramics vitreous china is No. 2_4 of Group 2 with sintering temperature 1250°C. Its mixture consists of 0% kaolin, 35% ball clay, 30% feldspar, 20% silica sand and 15% sediment soil. The properties of this formula are 9.4% shrinkage, 9.39 MPa of bending strength, 6.34×10−6/K coefficient of thermal expansion, and 0.66% water absorption.

  3. Concentrations of disinfection by-products in swimming pool following modifications of the water treatment process: An exploratory study.

    Science.gov (United States)

    Tardif, Robert; Rodriguez, Manuel; Catto, Cyril; Charest-Tardif, Ginette; Simard, Sabrina

    2017-08-01

    The formation and concentration of disinfection by-products (DBPs) in pool water and the ambient air vary according to the type of water treatment process used. This exploratory study was aimed at investigating the short-term impact of modifications of the water treatment process on traditional DBP levels (e.g., trihalomethanes (THMs), chloramines) and emerging DBPs (e.g., Halonitromethanes, Haloketones, NDMA) in swimming pool water and/or air. A sampling program was carried to understand the impact of the following changes made successively to the standard water treatment process: activation of ultraviolet (UV) photoreactor, halt of air stripping with continuation of air extraction from the buffer tank, halt of air stripping and suppression of air extraction from the buffer tank, suppression of the polyaluminium silicate sulfate (PASS) coagulant. UV caused a high increase of Halonitromethanes (8.4 fold), Haloketones (2.1 fold), and THMs in the water (1.7 fold) and, of THMs in the air (1.6 fold) and contributed to reducing the level of chloramines in the air (1.6 fold) and NDMA in the water (2.1 fold). The results highlight the positive impact of air stripping in reducing volatile contaminants. The PASS did not change the presence of DBPs, except for the THMs, which decrease slightly with the use of this coagulant. This study shows that modifications affecting the water treatment process can rapidly produce important and variable impacts on DBP levels in water and air and suggests that implementation of any water treatment process to reduce DBP levels should take into account the specific context of each swimming pool. Copyright © 2017. Published by Elsevier B.V.

  4. Post-treatment of reclaimed waste water based on an electrochemical advanced oxidation process

    Science.gov (United States)

    Verostko, Charles E.; Murphy, Oliver J.; Hitchens, G. D.; Salinas, Carlos E.; Rogers, Tom D.

    1992-01-01

    The purification of reclaimed water is essential to water reclamation technology life-support systems in lunar/Mars habitats. An electrochemical UV reactor is being developed which generates oxidants, operates at low temperatures, and requires no chemical expendables. The reactor is the basis for an advanced oxidation process in which electrochemically generated ozone and hydrogen peroxide are used in combination with ultraviolet light irradiation to produce hydroxyl radicals. Results from this process are presented which demonstrate concept feasibility for removal of organic impurities and disinfection of water for potable and hygiene reuse. Power, size requirements, Faradaic efficiency, and process reaction kinetics are discussed. At the completion of this development effort the reactor system will be installed in JSC's regenerative water recovery test facility for evaluation to compare this technique with other candidate processes.

  5. Post-treatment of reclaimed waste water based on an electrochemical advanced oxidation process

    Science.gov (United States)

    Verostko, Charles E.; Murphy, Oliver J.; Hitchens, G. D.; Salinas, Carlos E.; Rogers, Tom D.

    1992-01-01

    The purification of reclaimed water is essential to water reclamation technology life-support systems in lunar/Mars habitats. An electrochemical UV reactor is being developed which generates oxidants, operates at low temperatures, and requires no chemical expendables. The reactor is the basis for an advanced oxidation process in which electrochemically generated ozone and hydrogen peroxide are used in combination with ultraviolet light irradiation to produce hydroxyl radicals. Results from this process are presented which demonstrate concept feasibility for removal of organic impurities and disinfection of water for potable and hygiene reuse. Power, size requirements, Faradaic efficiency, and process reaction kinetics are discussed. At the completion of this development effort the reactor system will be installed in JSC's regenerative water recovery test facility for evaluation to compare this technique with other candidate processes.

  6. Laboratory Scale Study of Activated Sludge Process in Jet Loop Reactor for Waste WaterTreatment

    Directory of Open Access Journals (Sweden)

    M. S. Patil

    2014-03-01

    Full Text Available The present study was undertaken to evaluate the feasibility of Activated Sludge Process (ASP for the treatment of synthetic wastewater and to develop a simple design criteria under local conditions.A laboratory scale Compact jet loop reactor model comprising of an aeration tank and final clarifier was used for this purpose.Settled synthetic wastewater was used as influent to the aeration tank. The Chemical Oxygen Demand (COD of the influent and effluent was measured to find process efficiency at various mixed liquorvolatile suspended solids (MLVSS and hydraulic retention time (θ. The results of the studydemonstrated that an efficiency of above 95% could be obtained for COD if the ASP is operated atan MLVSS concentration of 3000 mg/L keeping an aeration time of 1 hour.In the present investigation the preliminary studies were carried out in a lab scale Jet loop reactor made of glass. Synthetic waste water having a composition of 1000 mg/L mixed with other nutrients such as Urea, Primary and secondary Potassium phosphates, Magnesium sulfate, Iron chloriderequired for the bacteria was prepared in the laboratory and reduction in COD and the increase inSuspended Solids (SSand the Sludge Volume Index (SVI were determined.

  7. Radiological assessment of water treatment processes in a water treatment plant in Saudi Arabia: Water and sludge radium content, radon air concentrations and dose rates.

    Science.gov (United States)

    Al-Jaseem, Q Kh; Almasoud, Fahad I; Ababneh, Anas M; Al-Hobaib, A S

    2016-09-01

    There is an increase demand for clean water sources in Saudi Arabia and, yet, renewable water resources are very limited. This has forced the authorities to explore deep groundwater which is known to contain large concentrations of radionuclides, mainly radium isotopes. Lately, there has been an increase in the number of water treatment plants (WTPs) around the country. In this study, a radiological assessment of a WTP in Saudi Arabia was performed. Raw water was found to have total radium activity of 0.23Bq/L, which exceeds the international limit of 0.185Bq/L (5pCi/L). The WTP investigated uses three stages of treatment: flocculation/sedimentation, sand filtration and reverse osmosis. The radium removal efficiency was evaluated for each stage and the respective values were 33%, 22% and 98%. Moreover, the activity of radium in the solid waste generated from the WTP in the sedimentation and sand filtrations stages were measured and found to be 4490 and 6750Bq/kg, respectively, which exceed the national limit of 1000Bq/kg for radioactive waste. A radiological assessment of the air inside the WTP was also performed by measuring the radon concentrations and dose rates and were found in the ranges of 2-18Bq/m(3) and 70-1000nSv/h, respectively. The annual effective dose was calculated and the average values was found to be 0.3mSv which is below the 1mSv limit.

  8. Recovery of metals from waste printed circuit boards by supercritical water pre-treatment combined with acid leaching process.

    Science.gov (United States)

    Xiu, Fu-Rong; Qi, Yingying; Zhang, Fu-Shen

    2013-05-01

    Waste printed circuit boards (PCBs) contain a large number of metals such as Cu, Sn, Pb, Cd, Cr, Zn, and Mn. In this work, an efficient and environmentally friendly process for metals recovery from waste PCBs by supercritical water (SCW) pre-treatment combined with acid leaching was developed. In the proposed process, waste PCBs were pre-treated by SCW, then the separated solid phase product with concentrated metals was subjected to an acid leaching process for metals recovery. The effect of SCW pre-treatment on the recovery of different metals from waste PCBs was investigated. Two methods of SCW pre-treatment were studied: supercritical water oxidation (SCWO) and supercritical water depolymerization (SCWD). Experimental results indicated that SCWO and SCWD pre-treatment had significant effect on the recovery of different metals. SCWO pre-treatment was highly efficient for enhancing the recovery of Cu and Pb, and the recovery efficiency increased significantly with increasing pre-treatment temperature. The recovery efficiency of Cu and Pb for SCWO pre-treatment at 420°C was 99.8% and 80%, respectively, whereas most of the Sn and Cr were immobilized in the residue. The recovery of all studied metals was enhanced by SCWD pre-treatment and increased along with pre-treatment temperature. Up to 90% of Sn, Zn, Cr, Cd, and Mn could be recovered for SCWD pre-treatment at 440°C. Copyright © 2013 Elsevier Ltd. All rights reserved.

  9. Water Treatment Group

    Data.gov (United States)

    Federal Laboratory Consortium — This team researches and designs desalination, water treatment, and wastewater treatment systems. These systems remediate water containing hazardous c hemicals and...

  10. A process for the treatment of olive mill waste waters by immobilized cells.

    Directory of Open Access Journals (Sweden)

    ElYachioui, M.

    2005-06-01

    Full Text Available Mould strains were immobilized on sawdust from woods as a solid material for the treatment of Olive Mill Waste (OMW waters. Assays were carried out in flasks. The treatment process was monitored by physico-chemical determinations including pH, polyphenols and COD, which were followed up during the incubation time. In parallel the chemical inhibitory activity of OMW was confirmed biologically by the determination of some microorganisms in the medium including the plate count, yeasts and lactic acid bacteria. Results indicated that the polyphenol degradation level was 87 %. The COD was also reduced by 60 %. The pH of the effluent increased from 4.5 to 6.6. The microbial profiles showed their best growth during the treatment period indicating a removal of the inhibitory activities from the OMW waters. The growth patterns of all microorganism groups were similar and could reach high levels in the effluent.Cepas de moho fueron inmovilizadas sobre serrín de madera como material sólido para el tratamiento de aguas residuales de un molino de aceituna (OMW. Los ensayos se realizaron en matraces. El proceso de tratamiento se monitorizó mediante determinaciones físico-químicas incluyendo pH, polifenoles y DQO, que también se analizaron durante el tiempo de incubación. En paralelo, la actividad inhibidora química de las OMW se confirma biológicamente mediante su efecto sobre algunos microorganismos incluyendo levaduras y bactérias ácido lácticas. Los resultados indicaron que los polifenoles se degradan hasta un nivel del 87 %. La DQO se redujo también al 60 %. El pH del efluente aumentó de 4.5 a 6.6. Los perfiles microbiológicos mostraron un mejor crecimiento a medida que avanzaba el tratamiento indicando una supresión de las actividades inhibidoras de las aguas (OMW. El comportamiento del crecimiento de todos los grupos de microorganismos fue similar y puede alcanzar altos niveles en el efluente

  11. A review on bisphenol A occurrences, health effects and treatment process via membrane technology for drinking water.

    Science.gov (United States)

    Muhamad, Mimi Suliza; Salim, Mohd Razman; Lau, Woei Jye; Yusop, Zulkifli

    2016-06-01

    Massive utilization of bisphenol A (BPA) in the industrial production of polycarbonate plastics has led to the occurrence of this compound (at μg/L to ng/L level) in the water treatment plant. Nowadays, the presence of BPA in drinking water sources is a major concern among society because BPA is one of the endocrine disruption compounds (EDCs) that can cause hazard to human health even at extremely low concentration level. Parallel to these issues, membrane technology has emerged as the most feasible treatment process to eliminate this recalcitrant contaminant via physical separation mechanism. This paper reviews the occurrences and effects of BPA toward living organisms as well as the application of membrane technology for their removal in water treatment plant. The potential applications of using polymeric membranes for BPA removal are also discussed. Literature revealed that modifying membrane surface using blending approach is the simple yet effective method to improve membrane properties with respect to BPA removal without compromising water permeability. The regeneration process helps in maintaining the performances of membrane at desired level. The application of large-scale membrane process in treatment plant shows the feasibility of the technology for removing BPA and possible future prospect in water treatment process.

  12. Spectroscopic characterization of changes of DOM deprotonation-protonation properties in water treatment processes.

    Science.gov (United States)

    Yan, Mingquan; Dryer, Deborah; Korshin, Gregory V

    2016-04-01

    The deprotonation-protonation properties of dissolved organic matter (DOM) in drinking water produced at critical treatment points were quantified using absorbance spectra in combination with DOM fractionation data. Analysis of differential spectra of DOM present in inlet, settled and filtered waters from two large treatment plants and their fractions were obtained. The data demonstrated the presence of six Gaussian bands largely associated with carboxylic and phenolic DOM functionalities. Properties of the protonation-active groups of DOM in raw and treated waters were further examined based on data of potentiometric titrations at pH from 2.5 to 10. Interpretation of the differential log-transformed absorbance at wavelength 350 nm (DlnA350) based on the NICA-Donnan model showed that the normalized concentrations of low- and high-affinity protonation-active groups in residual DOMs increases as a result of water treatment. This was consistent with the results of DOM fractionation. This study demonstrates that changes of the composition and reactivity of DOM found in drinking water treatment sequences can be quantified based on the examination of their optical properties.

  13. The drinking water treatment process as a potential source of affecting the bacterial antibiotic resistance.

    Science.gov (United States)

    Bai, Xiaohui; Ma, Xiaolin; Xu, Fengming; Li, Jing; Zhang, Hang; Xiao, Xiang

    2015-11-15

    Two waterworks, with source water derived from the Huangpu or Yangtze River in Shanghai, were investigated, and the effluents were plate-screened for antibiotic-resistant bacteria (ARB) using five antibiotics: ampicillin (AMP), kanamycin (KAN), rifampicin (RFP), chloramphenicol (CM) and streptomycin (STR). The influence of water treatment procedures on the bacterial antibiotic resistance rate and the changes that bacteria underwent when exposed to the five antibiotics at concentration levels ranging from 1 to 100 μg/mL were studied. Multi-drug resistance was also analyzed using drug sensitivity tests. The results indicated that bacteria derived from water treatment plant effluent that used the Huangpu River rather than the Yangtze River as source water exhibited higher antibiotic resistance rates against AMP, STR, RFP and CM but lower antibiotic resistance rates against KAN. When the antibiotic concentration levels ranged from 1 to 10 μg/mL, the antibiotic resistance rates of the bacteria in the water increased as water treatment progressed. Biological activated carbon (BAC) filtration played a key role in increasing the antibiotic resistance rate of bacteria. Chloramine disinfection can enhance antibiotic resistance. Among the isolated ARB, 75% were resistant to multiple antibiotics. Ozone oxidation, BAC filtration and chloramine disinfection can greatly affect the relative abundance of bacteria in the community.

  14. Processes of microbial pesticide degradation in rapid sand filters for treatment of drinking water

    DEFF Research Database (Denmark)

    Hedegaard, Mathilde Jørgensen; Albrechtsen, Hans-Jørgen

    concentrations of 0.04-2.4 μg/L. The pesticides were removed from the water in microcosms with filter sand from all three investigated sand filters. Within the experimental periode of six to 13 days, 65-85% of the bentazone, 86-93% of the glyphosate, 97-99% of the p-nitrophenol was removed from the water phase......Aerobic rapid sand filters for treatment of groundwater at waterworks were investigated for the ability to remove pesticides. The potential, kinetics and mechanisms of microbial pesticide removal was investigated in microcosms consisting of filter sand, treated water and pesticides in initial...

  15. Treatment of Zn-Containing Acidic Waste Water by Emulsion Liquid Membrane Process

    Institute of Scientific and Technical Information of China (English)

    王士柱; 何培炯; 郝东萍; 朱永贝睿

    2002-01-01

    Zn-containing waste water from a viscose staple fiber plant has been treated using the emulsion liquid membrane (ELM) process since 1995. The flow sheet and operating parameters of the ELM process are introduced. After adjusting the membrane composition, changing the emulsion phase ratio, and adding a scrubbing step, the ELM process operated normally without trouble for emulsion splitting and mass transport throughput. The splitter voltage was decreased to 3.55 kV. The zinc concentration of treated waste water was lowered to less than 10 mgL-1. More than 95% of the zinc was recovered and reused.

  16. The Optimization-Based Design and Synthesis of Water Network for Water Management in an Industrial Process: Refinery Effluent Treatment Plant

    DEFF Research Database (Denmark)

    Sueviriyapan, Natthapong; Siemanond, Kitipat; Quaglia, Alberto

    2014-01-01

    The increasing awareness of the sustainability of water resources has become an important issue. Many process industries contribute to high water consumption and wastewater generation. Problems in industrial water management include the processing of complex contaminants in wastewater, selection......-based synthesis process for a water/wastewater treatment network design problem utilizing the framework of Quaglia et al. (2013) in order to effectively design, synthesize, and optimize an industrial water management problem using different scenarios (both existing and retrofit system design). The model...... criteria. In addition, the effluent options (for different retrofit scenarios) in the modified superstructure could be set as discharge only, zero liquid discharge (total recycling), or a combination of recycling and discharge with the aim of minimizing the amount of fresh process water consumption through...

  17. Industrial process water treatment and reuse: A framework for synthesis and design

    DEFF Research Database (Denmark)

    Quaglia, Alberto; Pennati, Alessandra; Bogataj, Milos;

    2014-01-01

    Mathematical optimization has shown the potential to contribute to industrial water management, through the development of the solution methods needed for optimization-based design of wastewater treatment and reuse networks (also called water networks). Nevertheless, the application...... and solution of the design problems with fair complexity representative of industrial applications. The framework is demonstrated through the solution of a case study dealing with the treatment and reuse of water effluent produced by an oil refinery. The problem is solved, and a win−win solution is identified...... of this approach is still limited to motivating examples lacking the ability to handle problems with complexity of industrial relevance. To address this challenge, in this contribution, we focus on the integration of wastewater engineering concepts and models, together with optimization methods and solution...

  18. Polyhydroxyalkanoate Production on Waste Water Treatment Plants: Process Scheme, Operating Conditions and Potential Analysis for German and European Municipal Waste Water Treatment Plants

    Directory of Open Access Journals (Sweden)

    Timo Pittmann

    2017-06-01

    Full Text Available This work describes the production of polyhydroxyalkanoates (PHA as a side stream process on a municipal waste water treatment plant (WWTP and a subsequent analysis of the production potential in Germany and the European Union (EU. Therefore, tests with different types of sludge from a WWTP were investigated regarding their volatile fatty acids (VFA production-potential. Afterwards, primary sludge was used as substrate to test a series of operating conditions (temperature, pH, retention time (RT and withdrawal (WD in order to find suitable settings for a high and stable VFA production. In a second step, various tests regarding a high PHA production and stable PHA composition to determine the influence of substrate concentration, temperature, pH and cycle time of an installed feast/famine-regime were conducted. Experiments with a semi-continuous reactor operation showed that a short RT of 4 days and a small WD of 25% at pH = 6 and around 30 °C is preferable for a high VFA production rate (PR of 1913 mgVFA/(L×d and a stable VFA composition. A high PHA production up to 28.4% of cell dry weight (CDW was reached at lower substrate concentration, 20 °C, neutral pH-value and a 24 h cycle time. A final step a potential analysis, based on the results and detailed data from German waste water treatment plants, showed that the theoretically possible production of biopolymers in Germany amounts to more than 19% of the 2016 worldwide biopolymer production. In addition, a profound estimation regarding the EU showed that in theory about 120% of the worldwide biopolymer production (in 2016 could be produced on European waste water treatment plants.

  19. Grey water treatment by a continuous process of an electrocoagulation unit and a submerged membrane bioreactor system

    KAUST Repository

    Bani-Melhem, Khalid

    2012-08-01

    This paper presents the performance of an integrated process consisting of an electro-coagulation (EC) unit and a submerged membrane bioreactor (SMBR) technology for grey water treatment. For comparison purposes, another SMBR process without electrocoagulation (EC) was operated in parallel with both processes operated under constant transmembrane pressure for 24. days in continuous operation mode. It was found that integrating EC process with SMBR (EC-SMBR) was not only an effective method for grey water treatment but also for improving the overall performance of the membrane filtration process. EC-SMBR process achieved up to 13% reduction in membrane fouling compared to SMBR without electrocoagulation. High average percent removals were attained by both processes for most wastewater parameters studied. The results demonstrated that EC-SMBR performance slightly exceeded that of SMBR for COD, turbidity, and colour. Both processes produced effluent free of suspended solids, and faecal coliforms were nearly (100%) removed in both processes. A substantial improvement was achieved in removal of phosphate in the EC-SMBR process. However, ammonia nitrogen was removed more effectively by the SMBR only. Accordingly, the electrolysis condition in the EC-SMBR process should be optimized so as not to impede biological treatment. © 2012 Elsevier B.V.

  20. Development of Ultrafiltration Membrane-Separation Technology for Energy-Efficient Water Treatment and Desalination Process

    Energy Technology Data Exchange (ETDEWEB)

    Yim, Woosoon [Univ. of Nevada, Las Vegas, NV (United States); Bae, Chulsung [Rensselaer Polytechnic Inst., Troy, NY (United States)

    2016-10-28

    The growing scarcity of fresh water is a major political and economic challenge in the 21st century. Compared to thermal-based distillation technique of water production, pressure driven membrane-based water purification process, such as ultrafiltration (UF), nanofiltration (NF) and reverse osmosis (RO), can offer more energy-efficient and environmentally friendly solution to clean water production. Potential applications also include removal of hazardous chemicals (i.e., arsenic, pesticides, organics) from water. Although those membrane-separation technologies have been used to produce drinking water from seawater (desalination) and non-traditional water (i.e., municipal wastewater and brackish groundwater) over the last decades, they still have problems in order to be applied in large-scale operations. Currently, a major huddle of membrane-based water purification technology for large-scale commercialization is membrane fouling and its resulting increases in pressure and energy cost of filtration process. Membrane cleaning methods, which can restore the membrane properties to some degree, usually cause irreversible damage to the membranes. Considering that electricity for creating of pressure constitutes a majority of cost (~50%) in membrane-based water purification process, the development of new nano-porous membranes that are more resistant to degradation and less subject to fouling is highly desired. Styrene-ethylene/butylene-styrene (SEBS) block copolymer is one of the best known block copolymers that induces well defined morphologies. Due to the polarity difference of aromatic styrene unit and saturated ethylene/butylene unit, these two polymer chains self-assemble each other and form different phase-separated morphologies depending on the ratios of two polymer chain lengths. Because the surface of SEBS is hydrophobic which easily causes fouling of membrane, incorporation of ionic group (e,g, sulfonate) to the polymer is necessary to reduces fouling

  1. Improvement of the flocculation process in water treatment by using moringa oleifera seeds extract

    Directory of Open Access Journals (Sweden)

    J. Sánchez-Martín

    2012-09-01

    Full Text Available Water scarcity encourages researchers to keep working on natural coagulant agents such as Moringa oleifera seed extract, that could be used even in developing countries. With this scope, this investigation is focused on the optimization of certain parameters affecting the use of this coagulant product in the clarification of real surface water. Acidic pH levels seem to enhance the coagulation performance and the turbidity removal increases as the stirring period becomes longer (up to 95% with 40 min. The optimum stirring rate is identified as 80 rpm. Water clarified with this optimum coagulation and flocculation process is turbidity-competitive with other well known coagulants and flocculants and its quality is inside standard ranges for clarified water. No microbial growth is observed within the first 72 hours after the coagulant trials.

  2. Increased insight in microbial processes in rapid sandfilters in drinking water treatment (DW BIOFILTERS)

    DEFF Research Database (Denmark)

    Albrechtsen, Hans-Jørgen; Gülay, Arda; Lee, Carson

    2012-01-01

    been established at Islevbro Water Works (operated by Copenhagen Energy) with material from the full-scale afterfilter. After validation that the pilot plant is mimicking the full scale filter, it will be used to investigate processes at larger scales such as backwashing procedures and effect...

  3. Evaluation of the freeze-thaw/evaporation process for the treatment of produced waters. Final report, August 1992--August 1996

    Energy Technology Data Exchange (ETDEWEB)

    Boysen, J.E.; Walker, K.L.; Mefford, J.L.; Kirsch, J.R. [Resource Technology Corp., Laramie, WY (United States); Harju, J.A. [North Dakota Univ., Grand Forks, ND (United States). Energy and Environmental Research Center

    1996-06-01

    The use of freeze-crystallization is becoming increasingly acknowledged as a low-cost, energy-efficient method for purifying contaminated water. The natural freezing process can be coupled with natural evaporative processes to treat oil and gas produced waters year round in regions where subfreezing temperatures seasonally occur. The climates typical of Colorado`s San Juan Basin and eastern slope, as well as the oil and gas producing regions of Wyoming, are well suited for application of these processes in combination. Specifically, the objectives of this research are related to the development of a commercially-economic FTE (freeze-thaw/evaporation) process for the treatment and purification of water produced in conjunction with oil and natural gas. The research required for development of this process consists of three tasks: (1) a literature survey and process modeling and economic analysis; (2) laboratory-scale process evaluation; and (3) field demonstration of the process. Results of research conducted for the completion of these three tasks indicate that produced water treatment and disposal costs for commercial application of the process, would be in the range of $0.20 to $0.30/bbl in the Rocky Mountain region. FTE field demonstration results from northwestern New Mexico during the winter of 1995--96 indicate significant and simultaneous removal of salts, metals, and organics from produced water. Despite the unusually warm winter, process yields demonstrate disposal volume reductions on the order of 80% and confirm the potential for economic production of water suitable for various beneficial uses. The total dissolved solids concentrations of the FTE demonstration streams were 11,600 mg/L (feed), 56,900 mg/L (brine), and 940 mg/L (ice melt).

  4. A hybrid approach for treating fluorided water and biogeophysical monitoring of treatment processes

    Science.gov (United States)

    Singh, K. P.

    2016-12-01

    A laboratory experiment has been conducted for investigating the possibility of development of novel techniques for treating fluoride contamination and monitoring of physico-chemical alterations caused by biogeochemical processes in the media. In the present study, high adsorption capacity and ion-exchange property of natural zeolites have been utilized in treating fluoride contamination. The preset goals are achieved by designing and constructing experimental setup consisting of three columns, first one is filled with 450 ppm fluorided water prepared by dissolving sodium fluoride in deionized water, the second is filled with zeolite and fluorided water, and the third is filled with zeolite, fluorided water, sodium lactate and the bacterial seed. The first and the second columns were poisoned with sodium azide for preventing the growth of microorganisms. The self-potential (SP) signals associated with physico-chemical alterations in natural zeolite induced by biogeochemical processes are measured by using Cu-CuSO4 gel electrodes. Liquid-phase analysis of samples from column two and three show the reduced concentrations of fluoride and aluminum and it indicates the possibility of precipitation of insoluble aluminum fluoride. This is further confirmed by the presence of fluoride and aluminum in the solid samples as detected by energy dispersive X-ray analysis. The distinct SP of the order of -50 mV and 200 mV have been associated with biostimulated fluoride remediation and geochemical fluoride remediation processes respectively. Thus, there is a possibility of non-invasive monitoring of fluoride remediation processes driven by both microbes and chemical processes. It is found that after thirty-day nitrate and sulfate is introduced in column two due chemical interaction between water and natural zeolite. Furthermore, this study demonstrates that a hybrid approach, a combination of ion exchange and adsorption properties of natural zeolite and the bioremediation is more

  5. Biological treatment process for removing petroleum hydrocarbons from oil field produced waters

    Energy Technology Data Exchange (ETDEWEB)

    Tellez, G.; Khandan, N.

    1995-12-31

    The feasibility of removing petroleum hydrocarbons from oil fields produced waters using biological treatment was evaluated under laboratory and field conditions. Based on previous laboratory studies, a field-scale prototype system was designed and operated over a period of four months. Two different sources of produced waters were tested in this field study under various continuous flow rates ranging from 375 1/D to 1,800 1/D. One source of produced water was an open storage pit; the other, a closed storage tank. The TDS concentrations of these sources exceeded 50,000 mg/l; total n-alkanes exceeded 100 mg/l; total petroleum hydrocarbons exceeded 125 mg/l; and total BTEX exceeded 3 mg/l. Removals of total n-alkanes, total petroleum hydrocarbons, and BTEX remained consistently high over 99%. During these tests, the energy costs averaged $0.20/bbl at 12 bbl/D.

  6. The Optimization-Based Design and Synthesis of Water Network for Water Management in an Industrial Process: Refinery Effluent Treatment Plant

    DEFF Research Database (Denmark)

    Sueviriyapan, Natthapong; Siemanond, Kitipat; Quaglia, Alberto;

    2014-01-01

    -based mathematical problem was formulated as mixed integer linear (MILP) and mixed integer non-linear programming (MINLP) and strived to identify the best wastewater treatment processes among a set of predefined alternatives that produce a minimum total annualized cost, while meeting all wastewater specification...... of wastewater treatment technologies, as well as water allocation, limited reuse, and recycling strategies. Therefore, a water and wastewater treatment network design requires the integration of both economic and environmental perspectives. The aim of this work was to modify and develop a generic model...

  7. Characterization and calibration of a novel detection system for real time monitoring of radioactive contamination in water processed at water treatment facilities.

    Science.gov (United States)

    Carconi, P; De Felice, P; Fazio, A; Petrucci, A; Lunardon, M; Moretto, S; Stevanato, L; Cester, D; Pastore, P

    2017-08-01

    Characterization and calibration measurements were carried out at the National Institute of Ionizing Radiation Metrology of ENEA on the TAp WAter RAdioactivity (TAWARA) Real Time Monitor system recently developed for real time monitoring of radioactive contamination in water processed at water treatment facilities. Reference radiations and radionuclides were chosen in order to reflect energy ranges and radiation types of the major water radioactive contaminants possibly arising from environmental, industrial or terroristic origin. The following instrument parameters were tested: sensitivity, selectivity, background, short/long term stability, linearity with respect to activity. Copyright © 2017 Elsevier Ltd. All rights reserved.

  8. The study of potable water treatment process in Algeria (boudouaou station) -by the application of life cycle assessment (LCA).

    Science.gov (United States)

    Mohamed-Zine, Messaoud-Boureghda; Hamouche, Aksas; Krim, Louhab

    2013-12-19

    Environmental impact assessment will soon become a compulsory phase in future potable water production projects, in algeria, especially, when alternative treatment processes such sedimentation ,coagulation sand filtration and Desinfection are considered. An impact assessment tool is therefore developed for the environmental evaluation of potable water production. in our study The evaluation method used is the life cycle assessment (LCA) for the determination and evaluation of potential impact of a drink water station ,near algiers (SEAL-Boudouaoua).LCA requires both the identification and quantification of materials and energy used in all stages of the product's life, when the inventory information is acquired, it will then be interpreted into the form of potential impact " eco-indicators 99" towards study areas covered by LCA, using the simapro6 soft ware for water treatment process is necessary to discover the weaknesses in the water treatment process in order for it to be further improved ensuring quality life. The main source shown that for the studied water treatment process, the highest environmental burdens are coagulant preparation (30% for all impacts), mineral resource and ozone layer depletion the repartition of the impacts among the different processes varies in comparison with the other impacts. Mineral resources are mainly consumed during alumine sulfate solution preparation; Ozone layer depletion originates mostly from tetrachloromethane emissions during alumine sulfate production. It should also be noted that, despite the small doses needed, ozone and active Carbone treatment generate significant impacts with a contribution of 10% for most of the impacts.Moreover impacts of energy are used in producing pumps (20-25 GHC) for plant operation and the unitary processes (coagulation, sand filtration decantation) and the most important impacts are localized in the same equipment (40-75 GHC) and we can conclude that:- Pre-treatment, pumping and EDR (EDR: 0

  9. Integrated treatment process using a natural Wyoming clinoptilolite for remediating produced waters from coalbed natural gas operations

    Science.gov (United States)

    Zhao, H.; Vance, G.F.; Urynowicz, M.A.; Gregory, R.W.

    2009-01-01

    Coalbed natural gas (CBNG) development in western U.S. states has resulted in an increase in an essential energy resource, but has also resulted in environmental impacts and additional regulatory needs. A concern associated with CBNG development relates to the production of the copious quantities of potentially saline-sodic groundwater required to recover the natural gas, hereafter referred to as CBNG water. Management of CBNG water is a major environmental challenge because of its quantity and quality. In this study, a locally available Na-rich natural zeolite (clinoptilolite) from Wyoming (WY) was examined for its potential to treat CBNG water to remove Na+ and lower the sodium adsorption ratio (SAR, mmol1/2 L- 1/2). The zeolite material was Ca-modified before being used in column experiments. Column breakthrough studies indicated that a metric tonne (1000??kg) of Ca-WY-zeolite could be used to treat 60,000??L of CBNG water in order to lower SAR of the CBNG water from 30 to an acceptable level of 10??mmol1/2 L- 1/2. An integrated treatment process using Na-WY-zeolite for alternately treating hard water and CBNG water was also examined for its potential to treat problematic waters in the region. Based on the results of this study, use of WY-zeolite appears to be a cost-effective water treatment technology for maximizing the beneficial use of poor-quality CBNG water. Ongoing studies are evaluating water treatment techniques involving infiltration ponds lined with zeolite. ?? 2008 Elsevier B.V. All rights reserved.

  10. Electrocoagulation in Water Treatment

    Science.gov (United States)

    Liu, Huijuan; Zhao, Xu; Qu, Jiuhui

    Electrocoagulation (EC) is an electrochemical method of treating polluted water where sacrificial anodes corrode to release active coagulant precursors (usually aluminum or iron cations) into solution. At the cathode, gas evolves (usually as hydrogen bubbles) accompanying electrolytic reactions. EC needs simple equipments and is designable for virtually any size. It is cost effective and easily operable. Specially, the recent technical improvements combined with a growing need for small-scale water treatment facilities have led to a revaluation of EC. In this chapter, the basic principle of EC was introduced first. Following that, reactions at the electrodes and electrode assignment were reviewed; electrode passivation process and activation method were presented; comparison between electrocoagulation and chemical coagulation was performed; typical design of the EC reactors was also described; and factors affecting electrocoagulation including current density, effect of conductivity, temperature, and pH were introduced in details. Finally, application of EC in water treatment was given in details.

  11. A comparison of additional treatment processes to limit particle accumulation and microbial growth during drinking water distribution.

    Science.gov (United States)

    Liu, G; Lut, M C; Verberk, J Q J C; Van Dijk, J C

    2013-05-15

    Water quality changes, particle accumulation and microbial growth occurring in pilot-scale water distribution systems fed with normally treated and additional treated groundwater were monitored over a period of almost one year. The treatment processes were ranked in the following order: nanofiltration (NF) > (better than) ultrafiltration (UF) > ion exchange (IEX) for limiting particle accumulation. A different order was found for limiting overall microbial growth: NF > IEX > UF. There were strong correlations between particle load and particle accumulation, and between nutrient load and microbial growth. It was concluded that particle accumulation can be controlled by reducing the particle load in water treatment plants; and the microbial growth can be better controlled by limiting organic nutrients rather than removing biomass in water treatment plants. The major focus of this study was on microbial growth. The results demonstrated that growth occurred in all types of treated water, including the phases of bulk water, biofilm and loose deposits. Considering the growth in different phases, similar growth in bulk water was observed for all treatments; NF strongly reduced growth both in loose deposits and in biofilm; UF promoted growth in biofilm, while strongly limiting growth in loose deposits. IEX had good efficiency in between UF and NF, limiting both growths in loose deposits and in biofilm. Significant growth was found in loose deposits, suggesting that loose deposit biomass should be taken into account for growth evaluation and/or prediction. Strong correlations were found between microbial growth and pressure drop in a membrane fouling simulator which proved that a membrane fouling simulator can be a fast growth predictor (within a week). Different results obtained by adenosine triphosphate and flow cytometry cell counts revealed that ATP can accurately describe both suspended and particle-associated biomass, and flow cytometry files of TCC measurements needs

  12. Treatment of produced water: is a flotation viable process?; Tratamento da agua produzida: a flotacao e um processo viavel?

    Energy Technology Data Exchange (ETDEWEB)

    Santana, Claudia Ramos; Freitas, Andrea Goncalves Bueno de; Silva, Gabriel Francisco da; Paixao, Ana Eleonora Almeida [Universidade Federal de Sergipe (UFS), Aracaju, SE (Brazil); Oliveira, Rosivania da Paixao Silva [Fundacao de Apoio a Pesquisa e Extensao de Sergipe (FAPESE), Aracaju, SE (Brazil)

    2008-07-01

    In petroleum oil wells there comes a situation when most of the oil drilled accompanies a large amount of water. This may be due to the proper conditions of the reservoir or as a consequence of the water injection in the secondary recovery processes from the well. The amount of produced water together with oil can vary to a great extent and it frequently attains to about 50% of the drilled oil. One technique employed for the treatment of industrial effluents, mainly the oily ones which is of great interest is that of flotation. This phenomenon is being extensively used for oil removal from emulsified oils in various areas, such as that of dissolved air flotation (DAF) and the induced air flotation (IAF). The conventional flotation processes consist of the following stages: bubble gas generation (normally air) from the interior of the effluent; collision between the gas bubbles and the suspended oil drops in the water; adhesion of the gas bubbles in the oil drops and ascension of aggregate oil drops/bubbles until the surface, where the oil is removed. This work seeks to contribute for the understanding of the factors which contribute for the selection of the flotation process as one of the methods most viable for the treatment of the produced water. (author)

  13. Combined photochemical and biological processes for the treatment of linear alkylbenzene sulfonate in water.

    Science.gov (United States)

    Mehrvar, Mehrab; Tabrizi, Gelareh Bankian

    2006-01-01

    In this study, the effects of photochemical pre-treatment (pilot-plant UV/H2O2 process) of linear alkylbenzene sulfonate (LAS) on its subsequent biological treatment were examined. It was observed that the photochemical pre-treatment of the LAS solution did not increase its biodegradability. Moreover, the effects of acclimated microorganisms on the biodegradability of the LAS solution were also studied. It was observed that the acclimated activated sludge increased the biodegradation of the LAS solution. However, due to the presence of some intermediates in the effluent of the photoreactor, the biodegradability of this effluent was less than the biodegradability of the untreated LAS solution with the same concentration of the LAS in the effluent of the photoreactor.

  14. Comparative Study of Ozonation and Catalyzed Ozonation Processes for Drinking Water Treatment by Pilot Test

    Institute of Scientific and Technical Information of China (English)

    GUAN Chun-yu; MA Jun; SHI Feng-hua; ZHANG Xiao-lan

    2009-01-01

    The ozone consumption effect and organic removal ability of metal coated cordierite ceramic honeycombs catalytic ozonation (catazone) process and ozonation process were comparatively studied by pilot-scale experiments. By Scan Electron Microscope (SEM), Atomic Force Microscope (AFM), BET, and X-ray photoelectron spectroscopy (XPS) analysis, metal oxides attached to ceramic surface were found to be in the form of crystal cluster, and the pore structure of ceramics was less developed. The air flow statuses of vacant catazone and ozone contactors were inclined to be plug-flow and mixed flow, respectively. Comparing with ozonation process, the ozone mass transfer efficiency of catazone process is lower, and the ozone decomposition efficiency of catazone is higher. The former effect is more obvious in semi-batch experiment, and the latter effect is more obvious in continuous-flow experiment. Unsaturated organics removal efficiencies of the two oxidation processes are similar, and are less affected by dissolved ozone concentration when it is higher than 1 mg/L. More dissolved organics were detected in catazone process in continuous-flow reaction, and more CH3Cl3formation potential (CH3Cl3FP) was removed by catazone in semi-batch mode, especially in the water with lower UV254.

  15. Advanced treatment of benzothiazole contaminated waters: comparison of O3, AC, and O3/AC processes.

    Science.gov (United States)

    Valdés, H; Zaror, C A

    2005-01-01

    Benzothiazole (BT) is a toxic and poorly biodegradable contaminant, usually found in wastewater from rubber related applications. This compound could be effectively eliminated using advanced treatment processes. This paper compares experimental results on detoxification systems based on ozone oxidation, activated carbon adsorption, and simultaneous adsorption-oxidation using ozone in the presence of activated carbon. The effect of pH (2-11), and the presence of radical scavengers (tert-butyl alcohol and sodium carbonate) on process rates and removal efficiencies are assessed at laboratory scale. The experimental system consisted of a 1 L differential circular flow reactor and an ozone generator rated at 5 g O3/h. Results show that ozone oxidation combined with activated carbon adsorption increases the overall BT oxidation rate with respect to the ozonation process and activated carbon adsorption. In the presence of free radical scavenger, only a 44% reduction in BT removal rate is observed in the simultaneous treatment, as compared with 72% when ozonation treatment is used, suggesting that BT oxidation reactions mainly take place on the activated carbon surface.

  16. Chemical surface modification of glass beads for the treatment of paper machine process waters

    Energy Technology Data Exchange (ETDEWEB)

    Jradi, Khalil, E-mail: khalil.jradi@uqtr.c [Centre de Recherche en Pates et Papiers, Universite du Quebec a Trois Rivieres, 3351 boul. des forges, C.P. 500, Trois Rivieres, QC, G9A-5H7 (Canada); Daneault, Claude [Canada Research Chair in Value-Added Paper Manufacturing (Canada); Chabot, Bruno [Centre de Recherche en Pates et Papiers, Universite du Quebec a Trois Rivieres, 3351 boul. des forges, C.P. 500, Trois Rivieres, QC, G9A-5H7 (Canada)

    2011-04-29

    Adsorption of detrimental contaminants on a solid sorbent is proposed to remove these contaminants from process waters to increase water recycling and reduce effluent loads in the papermaking industry. A self-assembly process of attaching (covalent grafting) cationic aminosilane molecules to glass beads was investigated. The existence and the hydrolytic stability of self-assembled monolayers and multilayers were confirmed by X-Ray Photoelectron Spectroscopy and contact angle measurements. Effects of reaction time and curing on aminosilane layer structures are also discussed. The curing step after silanization seems to be crucial in the hydrophobization of the quaternary ammonium silane coated onto glass beads, and curing could affect the final chemical structure of the ammonium groups of grafted organosilane. Results indicated that modified glass beads have a strong hydrophobicity, which is attributed to the hydrophobic property of the longest carbon chain grafted onto the glass surface. Adsorption of a model contaminant (stearic acid) onto chemically modified glass beads was determined using colloidal titration. Hydrophobic interactions could be the main driving force involved between the long carbon chains of stearic acid and the carbon chains of the aminosilane layers on glass bead surfaces. Finally, self-assembly processes applied onto glass beads may have two promising applications for papermaking and self-cleaning systems.

  17. Application of Water Treatment Process for Cold-rolling Waste Water to Be Drained into Natural Water%排至自然水体的冷轧废水处理工艺应用

    Institute of Scientific and Technical Information of China (English)

    尹军喜

    2014-01-01

    The water treatment process for cold rolling waste water to be drained into natural water is introduced. Treatment methods for cold rolling waste water containing chrome, acid, oil, temper mill fluid and thin alkali are summarized. The main problems and functions of the process are also analyzed. This water treatment process has reached the advanced level in the field of domestic cold rolling waste water treatment.%介绍了排至自然水体的冷轧废水处理工艺,综述了冷轧废水中含铬废水、含酸废水、含油废水、平整液废水、稀碱废水的处理方法,对主要问题和功能进行了分析,其处理工艺达到了国内冷轧废水的先进水平。

  18. Use of solar energy in the treatment of water contaminated with phenol by photochemical processes

    Directory of Open Access Journals (Sweden)

    K. R. B. Nogueira

    2008-12-01

    Full Text Available The solar driven photo-Fenton process for treating water containing phenol as a contaminant has been evaluated by means of pilot-scale experiments with a parabolic trough solar reactor (PTR. The effects of Fe(II (0.04-1.0 mmol L-1, H2O2 (7-270 mmol L-1, initial phenol concentration (100 and 500 mg C L-1, solar radiation, and operation mode (batch and fed-batch on the process efficiency were investigated. More than 90% of the dissolved organic carbon (DOC was removed within 3 hours of irradiation or less, a performance equivalent to that of artificially-irradiated reactors, indicating that solar light can be used either as an effective complementary or as an alternative source of photons for the photo-Fenton degradation process. A non-linear multivariable model based on a neural network was fit to the experimental results of batch-mode experiments in order to evaluate the relative importance of the process variables considered on the DOC removal over the reaction time. This included solar radiation, which is not a controlled variable. The observed behavior of the system in batch-mode was compared with fed-batch experiments carried out under similar conditions. The main contribution of the study consists of the results from experiments under different conditions and the discussion of the system behavior. Both constitute important information for the design and scale-up of solar radiation-based photodegradation processes.

  19. Increased insight in microbial processes in rapid sandfilters in drinking water treatment (DW BIOFILTERS)

    DEFF Research Database (Denmark)

    Albrechtsen, Hans-Jørgen; Gülay, Arda; Lee, Carson

    2012-01-01

    . The sustainability and climate friendliness are evaluated by life cycle assessment (LCA). Molecular methods based on qPCR are being developed and implemented to quantify bacteria in different functional groups, such as those responsible for nitrification. This allows for development of diagnostic tools to detect......The aim of this research project is to improve our knowledge on biological rapid sand filters as they are present in thousands groundwater based water works. This includes molecular investigations of the microorganisms responsible for the individual processes (e.g. nitrification); and detailed...... monitoring and experiments in the filters and laboratory to provide insight in the process mechanisms, kinetics and effect of environmental factors. Management of the filters (e.g. backwashing, flow rate, carrier type) will be investigated at pilot and full scale, supported by mathematical models...

  20. Reuse & Recirculation of Filter Backwash Water of Water Treatment Water

    Directory of Open Access Journals (Sweden)

    Mangesh L. Jibhakate

    2017-04-01

    Full Text Available Most of the water treatment plant, filtration is done by means of sand filtration process. Due to continuous filtration process, sand pores get clogged and decreases the efficiency. For mitigating such problem, reverse flow of water & air i.e. backwashing process is carried out. To carry out backwashing operation, 4% of treated water has been utilized and will result in muddy water known as backwash water. This backwash water is then discharged into a natural stream or storage tank near the plant for recirculation. The present study includes a trial for the reuse & recirculation of backwash water.

  1. Cyclic process of simazine removal from waters by adsorption on zeolite H-Y and its regeneration by thermal treatment.

    Science.gov (United States)

    Sannino, Filomena; Ruocco, Silvia; Marocco, Antonello; Esposito, Serena; Pansini, Michele

    2012-08-30

    Removal of the agrochemical simazine from polluted waters through adsorption by zeolite Y in its protonic form was studied. The investigated parameters were: pH, time, initial simazine concentration and solid/liquid ratio. An iterative process of simazine removal from waters is proposed, featuring: (i) final agrochemical concentration well below 0.05 mg/dm(3), the maximum concentration allowed by Italian laws in wastewaters; (ii) regeneration of the adsorbent by a few minutes thermal treatment in air at about 500°C, which results in the combustion of simazine without damage of the adsorbent; (iii) destruction of the agrochemical compound by combustion.

  2. Integration of processes induced air flotation and photo-Fenton for treatment of residual waters contaminated with xylene

    Energy Technology Data Exchange (ETDEWEB)

    Silva, Syllos S. da [Departamento Engenharia Quimica, NUPEG, Universidade Federal do Rio Grande do Norte, Campus Universitario, Lagoa Nova, Natal 59066-800, RN (Brazil); Chiavone-Filho, Osvaldo, E-mail: osvaldo@eq.ufrn.br [Departamento Engenharia Quimica, NUPEG, Universidade Federal do Rio Grande do Norte, Campus Universitario, Lagoa Nova, Natal 59066-800, RN (Brazil); Barros Neto, Eduardo L. de [Departamento Engenharia Quimica, NUPEG, Universidade Federal do Rio Grande do Norte, Campus Universitario, Lagoa Nova, Natal 59066-800, RN (Brazil); Nascimento, Claudio A.O. [Departamento de Engenharia Quimica, Escola Politecnica, Universidade de Sao Paulo, Cidade Universitaria, Sao Paulo 05508-900, SP (Brazil)

    2012-01-15

    Highlights: Black-Right-Pointing-Pointer We have studied the treatment of wastewater contaminated with hydrocarbons represented by the xylene, using these processes in an integrated mode: induced air flotation and photo-Fenton. Black-Right-Pointing-Pointer We have selected xylene as representative contaminant due to properties of toxicity, solubility in water and vapor pressure. Black-Right-Pointing-Pointer The manuscript presents a series of accurate experimental data that can be useful for material and energy optimization purposes in the xylene removal aiming the treatment of oil field produced water. - Abstract: Produced water in oil fields is one of the main sources of wastewater generated in the industry. It contains several organic compounds, such as benzene, toluene, ethyl benzene and xylene (BTEX), whose disposal is regulated by law. The aim of this study is to investigate a treatment of produced water integrating two processes, i.e., induced air flotation (IAF) and photo-Fenton. The experiments were conducted in a column flotation and annular lamp reactor for flotation and photodegradation steps, respectively. The first order kinetic constant of IAF for the wastewater studied was determined to be 0.1765 min{sup -1} for the surfactant EO 7. Degradation efficiencies of organic loading were assessed using factorial planning. Statistical data analysis shows that H{sub 2}O{sub 2} concentration is a determining factor in process efficiency. Degradations above 90% were reached in all cases after 90 min of reaction, attaining 100% mineralization in the optimized concentrations of Fenton reagents. Process integration was adequate with 100% organic load removal in 20 min. The results of the integration of the IAF with the photo-Fenton allowed to meet the effluent limits established by Brazilian legislation for disposal.

  3. Pathway fraction of bromate formation during O₃ and O₃/H₂O₂ processes in drinking water treatment.

    Science.gov (United States)

    Qi, Shengqi; Mao, Yuqin; Lv, Miao; Sun, Lili; Wang, Xiaomao; Yang, Hongwei; Xie, Yuefeng F

    2016-02-01

    Ozone process has been widely used for drinking water treatment recently. In the oxidation process, bromate is formed by three pathways, i.e., the direct pathway, the direct-indirect pathway and the indirect-direct pathway. This study developed a method to calculate the percentage of these three pathways for bromate formation during O3 process and O3/H2O2 process. Two kinds of water, distilled water containing bromide (DW) and surface water from the Yellow River (SW) were selected as raw rater. The result showed that in natural water systems, the direct-indirect pathway was dominant for bromate formation during the oxidation process. When 3 mg L(-1) O3 was used as the only oxidant, nearly 26% of bromide ion was transferred into bromate in two kinds of water after 80 min. The dominant pathway in DW was the direct pathway (48.5%) and the direct-indirect pathway (46.5%), while that was the direct-indirect pathway (68.9%) in SW. When O3/H2O2 were used as oxidants, as the H2O2 dosage increased, the fractions of bromate formation by direct pathway and direct-indirect pathway decreased, while that by indirect-direct pathway increased. The conversion ratio from bromide to bromate first kept stable or increased, then decreased and reached its minimum when [H2O2]/[O3] ratio was 1.0 in DW and 1.5 in SW. Under this condition the indirect-direct pathway took the largest fraction of 70.7% in DW and 64.0% in SW, respectively. Copyright © 2015. Published by Elsevier Ltd.

  4. Treatment of a waste oil-in-water emulsion from a copper-rolling process by ultrafiltration and vacuum evaporation.

    Science.gov (United States)

    Gutiérrez, Gemma; Lobo, Alberto; Benito, José M; Coca, José; Pazos, Carmen

    2011-01-30

    A process is proposed for the treatment of a waste oil-in-water (O/W) emulsion generated in an industrial copper-rolling operation. The use of demulsifier agents improves the subsequent treatment by techniques such as ultrafiltration (UF) or evaporation. The effluent COD is reduced up to 50% when the O/W emulsion is treated by UF using a flat 30 nm TiO(2) ceramic membrane (ΔP = 0.1 MPa) and up to 70% when it is treated by vacuum evaporation, after an emulsion destabilization pretreatment in both cases. Increases in the UF permeate flux and in the evaporation rate are observed when a chemical demulsifier is used in the pretreatment step. A combined process consisting of destabilization/settling, UF, and vacuum evaporation can yield a very high-quality aqueous effluent that could be used for process cooling or emulsion reformulation.

  5. Sunlight inactivation of viruses in open-water unit process treatment wetlands: modeling endogenous and exogenous inactivation rates.

    Science.gov (United States)

    Silverman, Andrea I; Nguyen, Mi T; Schilling, Iris E; Wenk, Jannis; Nelson, Kara L

    2015-03-03

    Sunlight inactivation is an important mode of disinfection for viruses in surface waters. In constructed wetlands, for example, open-water cells can be used to promote sunlight disinfection and remove pathogenic viruses from wastewater. To aid in the design of these systems, we developed predictive models of virus attenuation that account for endogenous and exogenous sunlight-mediated inactivation mechanisms. Inactivation rate models were developed for two viruses, MS2 and poliovirus type 3; laboratory- and field-scale experiments were conducted to evaluate the models' ability to estimate inactivation rates in a pilot-scale, open-water, unit-process wetland cell. Endogenous inactivation rates were modeled using either photoaction spectra or total, incident UVB irradiance. Exogenous inactivation rates were modeled on the basis of virus susceptibilities to singlet oxygen. Results from both laboratory- and field-scale experiments showed good agreement between measured and modeled inactivation rates. The modeling approach presented here can be applied to any sunlit surface water and utilizes easily measured inputs such as depth, solar irradiance, water matrix absorbance, singlet oxygen concentration, and the virus-specific apparent second-order rate constant with singlet oxygen (k2). Interestingly, the MS2 k2 in the open-water wetland was found to be significantly larger than k2 observed in other waters in previous studies. Examples of how the model can be used to design and optimize natural treatment systems for virus inactivation are provided.

  6. Comprehensive reuse of drinking water treatment residuals in coagulation and adsorption processes.

    Science.gov (United States)

    Jung, Kyung-Won; Hwang, Min-Jin; Park, Dae-Seon; Ahn, Kyu-Hong

    2016-10-01

    While drinking water treatment residuals (DWTRs) inevitably lead to serious problems due to their huge amount of generation and limitation of landfill sites, their unique properties of containing Al or Fe contents make it possible to reuse them as a beneficial material for coagulant recovery and adsorbent. Hence, in the present study, to comprehensively handle and recycle DWTRs, coagulant recovery from DWTRs and reuse of coagulant recovered residuals (CRs) were investigated. In the first step, coagulant recovery from DWTRs was conducted using response surface methodology (RSM) for statistical optimization of independent variables (pH, solid content, and reaction time) on response variable (Al recovery). As a result, a highly acceptable Al recovery of 97.5 ± 0.4% was recorded, which corresponds to 99.5% of the predicted Al recovery. Comparison study of recovered and commercial coagulant from textile wastewater treatment indicated that recovered coagulant has reasonable potential for use in wastewater treatment, in which the performance efficiencies were 68.5 ± 2.1% COD, 97.2 ± 1.9% turbidity, and 64.3 ± 1.0% color removals at 50 mg Al/L. Subsequently, in a similar manner, RSM was also applied to optimize coagulation conditions (Al dosage, initial pH, and reaction time) for the maximization of real cotton textile wastewater treatment in terms of COD, turbidity, and color removal. Overall performance revealed that the initial pH had a remarkable effect on the removal performance compared to the effects of other independent variables. This is mainly due to the transformation of metal species form with increasing or decreasing pH conditions. Finally, a feasibility test of CRs as adsorbent for phosphate adsorption from aqueous solution was conducted. Adsorption equilibrium of phosphate at different temperatures (10-30 °C) and initial levels of pH (3-11) indicated that the main mechanisms of phosphate adsorption onto CRs are endothermic and chemical

  7. Estimation and filtering of nonlinear systems application to a waste-water treatment process

    Energy Technology Data Exchange (ETDEWEB)

    Ben Youssef, C.; Dahhou, B. [Centre National de la Recherche Scientifique (CNRS), 31 - Toulouse (France). Lab. d`Automatique et d`Analyse des Systemes]|[Institut National des Sciences Appliquees (INSA), 31 - Toulouse (France); Zeng, F.Y.; Rols, J.L. [Institut National des Sciences Appliquees (INSA), 31 - Toulouse (France)

    1994-04-01

    A fundamental task in design and control of biotechnological processes is system modelling. This task is made difficult by the scarceness of on-line direct sensors for some key variables and by the fact that identifiability of models including Michaelis-Menten type of nonlinearities is not straightforward. The use of adaptive estimation approaches constitutes an interesting alternative to circumvent these kind of problems. This paper discusses an identification technique derived to solve the problem of estimating simultaneously inaccessible state variables and time-varying parameters of a nonlinear wastewater treatment process. An extended linearization technique using Kronecker`s calculation provides the error model of the joint observer-estimator procedure which convergence is proved via Lyapunov`s method. Sufficient conditions for stability of this joint identification scheme are given and discussed according to the persistence excitation conditions of the signals. A simulation study with measurement noises and abrupt jumps of the process parameters shows the feasibility and significant robustness of the proposed adaptive estimation methodologies. (author). (author). 10 refs., 3 figs.

  8. The impact of sea water flushing on biological nitrification-denitrification activated sludge sewage treatment process.

    Science.gov (United States)

    Yu, S M; Leung, W Y; Ho, K M; Greenfield, P F; Eckenfelder, W W

    2002-01-01

    The process performance of the two largest activated sludge processes in Hong Kong, the Sha Tin and the Tai Po Sewage Treatment Works (STW), deteriorated in the initial period after the introduction of seawater flushing in 1995 and 1996, respectively. High effluent ammonia nitrogen (NH4-N) and total suspended solids (TSS) in excess of the discharge standards resulted from incomplete nitrification and changes in floc characteristics. A desktop study on the inhibitory effects of salinity, particularly on nitrification, was subsequently conducted using the Tai Po STW operating data. To assist the upgrade of the Sha Tin STW a five-month extensive bench-scale investigation on a simple but flexible modified Ludzack-Ettinger configuration with bio-selector was conducted to quantify the inhibitory effects due to the saline concentration. The Sha Tin STW upgrade consists of restoration of its original design capacity (conventional process) of 205,000 m3/day from its currently much reduced capacity as a Bardenpho process. Only the volume of the existing biological process and clarifier is to be utilized. The saline concentration ranges from 3,500 up to 6,500 mg Cl-/L, both daily and seasonally. High and greatly fluctuating saline concentrations have been known to inhibit nitrification. Design consideration should also be given to the peak daily and seasonal TKN loading of up to three times the average. Although the nitrifiers maximum specific growth rate was significantly reduced to a low 0.25 day(-1), the inhibition was considered to be tolerable with effluent NH4-N and NO3-N consistently at < 1 and < 6 mg/L. The bio-selector was demonstrated to be efficient in control of sludge foaming and bulking with SVI consistently < or = 125 mL/g. Results from the IAWO Model No. 1 and the hydraulic model of the secondary clarifiers allowed overall process capacity maximization. With an anoxic mass fraction of 25-30%, operating sludge age of 9-14 days and SVI < or = 125 mL/g, both the

  9. Alternative disinfectant water treatments

    Science.gov (United States)

    Alternative disinfestant water treatments are disinfestants not as commonly used by the horticultural industry. Chlorine products that produce hypochlorous acid are the main disinfestants used for treating irrigation water. Chlorine dioxide will be the primary disinfestant discussed as an alternativ...

  10. Control-oriented modeling and real-time control for the ozone dosing process of drinking water treatment.

    Science.gov (United States)

    Wang, Dongsheng; Li, Shihua; Zhou, Xingpeng

    2013-03-01

    Ozonation is one of the most important steps during drinking water treatment. To improve the efficiency of ozonation and to stabilize the quality of the treated water, control-oriented modeling and a real-time control method for the ozone dosing process are developed in this study. Compared with existing ozonation models developed by bench-scale and pilot-scale batch experiments, the model reported herein is control-oriented and based on plant-scale batch experiments. A real-time control strategy for maintaining a constant ozone exposure is attempted to meet primary disinfection requirements. An internal model control scheme is proposed to maintain a constant ozone exposure by adjusting the ozone dosage. The proposed real-time control method can cope with changing water quality, water flow rate, and process operational conditions. Both simulations and experimental studies have been carried out and implemented for the ozone dosing process control system, and the results demonstrate the effectiveness and practicality of this real-time control method.

  11. Cyclic process of simazine removal from waters by adsorption on zeolite H-Y and its regeneration by thermal treatment

    Energy Technology Data Exchange (ETDEWEB)

    Sannino, Filomena, E-mail: fsannino@unina.it [Dipartimento di Scienze del Suolo, della Pianta, dell' Ambiente e delle Produzioni Animali, Universita di Napoli ' Federico II' , Via Universita 100, 80055 Portici (Italy); Ruocco, Silvia [Dipartimento di Scienze del Suolo, della Pianta, dell' Ambiente e delle Produzioni Animali, Universita di Napoli ' Federico II' , Via Universita 100, 80055 Portici (Italy); Marocco, Antonello; Esposito, Serena; Pansini, Michele [Laboratorio Materiali - Dipartimento di Meccanica, Strutture, Ambiente e Territorio - Universita di Cassino - Via Di Biasio 43 - 03043 Cassino (Italy)

    2012-08-30

    Highlights: Black-Right-Pointing-Pointer Bringing agrochemical concentration below the law limit allowed in wastewaters. Black-Right-Pointing-Pointer Regenerating the adsorbent which can be used again in the cyclic process. Black-Right-Pointing-Pointer Destroying the agrochemical molecules by combustion. - Abstract: Removal of the agrochemical simazine from polluted waters through adsorption by zeolite Y in its protonic form was studied. The investigated parameters were: pH, time, initial simazine concentration and solid/liquid ratio. An iterative process of simazine removal from waters is proposed, featuring: (i) final agrochemical concentration well below 0.05 mg/dm{sup 3}, the maximum concentration allowed by Italian laws in wastewaters; (ii) regeneration of the adsorbent by a few minutes thermal treatment in air at about 500 Degree-Sign C, which results in the combustion of simazine without damage of the adsorbent; (iii) destruction of the agrochemical compound by combustion.

  12. Autotrophic nitrogen removal process in a potable water treatment biofilter that simultaneously removes Mn and NH4(+)-N.

    Science.gov (United States)

    Cai, Yan'an; Li, Dong; Liang, Yuhai; Zeng, Huiping; Zhang, Jie

    2014-11-01

    Ammonia (NH4(+)-N) removal pathways were investigated in a potable water treatment biofilter that simultaneously removes manganese (Mn) and NH4(+)-N. The results indicated a significant loss of nitrogen in the biofilter. Both the completely autotrophic nitrogen removal over nitrite (CANON) process and nitrification were more likely to contribute to NH4(+)-N removal. Moreover, the model calculation results demonstrated that the CANON process contributed significantly to the removal of NH4(+)-N. For influent NH4(+)-N levels of 1.030 and 1.749mg/L, the CANON process contribution was about 48.5% and 46.6%, respectively. The most important finding was that anaerobic ammonia oxidation (ANAMMOX) bacteria were detectable in the biofilter. It is interesting that the CANON process was effective even for such low NH4(+)-N concentrations. Copyright © 2014 Elsevier Ltd. All rights reserved.

  13. Mechanism of combination membrane and electro-winning process on treatment and remediation of Cu2+ polluted water body.

    Science.gov (United States)

    Zhang, Linnan; Wu, Yanjun; Qu, Xiaoyan; Li, Zhenshan; Ni, Jinren

    2009-01-01

    Mechanism of treatment and remediation of synthetic Cu2+ polluted water body by membrane and electro-winning combination process was investigated. The influences of electrolysis voltage, pH, and electrolysis time on the metal recovery efficiencies were studied. Relationship between trans-membrane pressure drop (DeltaP), additions ratio, initial Cu2+ concentration on operating efficiency, stability of membrane and the possibility of water reuse were also investigated. The morphology of membrane and electrodes were observed using scanning electron microscopy (SEM), the composition of surface deposits was ascertained using combined energy dispersive X-ray spectroscopy (EDX) and atomic absorption spectrophotometer. The results showed that using low pressure reverse osmosis (LPRO), Cu2+ concentration could increase from 20 to 100 mg/L or even higher in concentrated solutions and permeate water conductivity could be less than 20 microS/cm. The addition of sodium dodecy/sulfate sodium dodecyl sulfate improved Cu2+ removal efficiency, while EDTA had little side influence. In electro-reduction process, using plante electrode cell, Cu2+ concentration could be further reduced to 5 mg/L, and the average current efficiency ranged from 9% to 40%. Using 3D electrolysis treatment, Cu2+ concentration could be reduced to 0.5 mg/L with a current efficiency range 60%-70%.

  14. Mechnism of combination membrane and electro-winning process on treatment and remediation of Cu2+ polluted water body

    Institute of Scientific and Technical Information of China (English)

    ZHANG Linnan; WU Yanjun; QU Xiaoyan; LI Zhenshan; NI Jinren

    2009-01-01

    Mechnism of treatment and remediation of synthetic Cu2+ polluted water body by membrane and electro-winning combination process was investigated.The influnce of electrolysis voltage,pH,and electrolysis time on the metal recovery efficiencies were studied.Relationship between trans-membrane pressure drop (ΔP),additions ratio,initial Cu2+ concentration on operating efficency,stability of membrane and the possibility of water reuse were also investigated.The morphology of membrane and electrodes were observed using scanning electron microscopy (SEM),the composition of suface deposits was ascertained using combined energy dispersive X-ray spectroscopy (EDX) and atomic absorption spectrophotometer.The results showed that using low presure reverse osmosis (LPRO),the Cu2+ concentration could increase from 20 mg/L to 100 mg/L or even higher in the concentrate solutions and permeate water conductivity could be less than 20 μS/cm.The addition of SDS can improve the Cu2+ removal efficiency,while EDTA had little side influence.In electro-reduction process,using plante electrode cell,Cu2+ concentration can be further reduced to 5 mg/L,and the average current efficiency ranged from 9% to 40%.Using 3D electrolysis treatment,Cu2+ concentration could be reduced to 0.5 mg/L with a current efficiency range 60%-70%.

  15. The removal process of 2,2-dichloroacetamide (DCAcAm), a new disinfection by-product, in drinking water treatment process and its toxicity on zebrafish.

    Science.gov (United States)

    Lin, Tao; Zhou, Dongju; Yu, Shilin; Chen, Wei

    2016-09-01

    The removal process of 2,2-dichloroacetamide (DCAcAm), a new disinfection by-product (DBP) in conventional drinking water treatment plant (C-DWTP) and advanced DWTP (ADWTP) was studied with newly maximum formation potential (MFP) process. It was demonstrated that the advanced treatment displayed greater removal efficiency towards DCAcAm formation potential (MFP) than the conventional treatment. The hydrophilic natural organic matter and natural organic matter with molecular weight 10 kDa leaded to more DCAcAm formation, and the aromatic protein was inferred as one part of DCAcAm precursor. DCAcAm was found to cause delayed development and malformation to zebrafish embryos at embryonic growth stage. Compared with heart toxicity, it caused a significant neuron toxicity. It also could cause the acute DNA damage to adult zebrafish, which should be extremely cautioned.

  16. Removal of sulphite-reducing clostridia spores by full-scale water treatment processes as a surrogate for protozoan (oo)cysts removal

    NARCIS (Netherlands)

    Hijnen, W.A.M.; Willemsen-Zwaagstra, J.; Hiemstra, P.; Medema, Gerriet Jan; Kooij, D. van der

    2000-01-01

    At eight full-scale water treatment plants in the Netherlands the removal of spores of sulphite-reducing clostridia (SSRC) was determined. By sampling and processing large volumes of water (1 up to 500 litres) SSRC were detected after each stage of the treatment. This enabled the assessment of the

  17. Understanding the impacts of allocation approaches during process-based life cycle assessment of water treatment chemicals.

    Science.gov (United States)

    Alvarez-Gaitan, Juan P; Peters, Gregory M; Short, Michael D; Schulz, Matthias; Moore, Stephen

    2014-01-01

    Chemicals are an important component of advanced water treatment operations not only in terms of economics but also from an environmental standpoint. Tools such as life cycle assessment (LCA) are useful for estimating the environmental impacts of water treatment operations. At the same time, LCA analysts must manage several fundamental and as yet unresolved methodological challenges, one of which is the question of how best to "allocate" environmental burdens in multifunctional processes. Using water treatment chemicals as a case study example, this article aims to quantify the variability in greenhouse gas emissions estimates stemming from methodological choices made in respect of allocation during LCA. The chemicals investigated and reported here are those most important to coagulation and disinfection processes, and the outcomes are illustrated on the basis of treating 1000 ML of noncoagulated and nondisinfected water. Recent process and economic data for the production of these chemicals is used and methodological alternatives for solving the multifunctionality problem, including system expansion and mass, exergy, and economic allocation, are applied to data from chlor-alkali plants. In addition, Monte Carlo simulation is included to provide a comprehensive picture of the robustness of economic allocation results to changes in the market price of these industrial commodities. For disinfection, results demonstrate that chlorine gas has a lower global warming potential (GWP) than sodium hypochlorite regardless of the technique used to solve allocation issues. For coagulation, when mass or economic allocation is used to solve the multifunctionality problem in the chlor-alkali facility, ferric chloride was found to have a higher GWP than aluminum sulfate and a slightly lower burden where system expansion or exergy allocation are applied instead. Monte Carlo results demonstrate that when economic allocation is used, GWP results were relatively robust and resilient

  18. Applying the polarity rapid assessment method to characterize nitrosamine precursors and to understand their removal by drinking water treatment processes.

    Science.gov (United States)

    Liao, Xiaobin; Bei, Er; Li, Shixiang; Ouyang, Yueying; Wang, Jun; Chen, Chao; Zhang, Xiaojian; Krasner, Stuart W; Suffet, I H Mel

    2015-12-15

    Some N-nitrosamines (NAs) have been identified as emerging disinfection by-products during water treatment. Thus, it is essential to understand the characteristics of the NA precursors. In this study, the polarity rapid assessment method (PRAM) and the classical resin fractionation method were studied as methods to fractionate the NA precursors during drinking water treatment. The results showed that PRAM has much higher selectivity for NA precursors than the resin approach. The normalized N-nitrosodimethylamine formation potential (NDMA FP) and N-nitrosodiethylamine (NDEA) FP of four resin fractions was at the same level as the average yield of the bulk organic matter whereas that of the cationic fraction by PRAM showed 50 times the average. Thus, the cationic fraction was shown to be the most important NDMA precursor contributor. The PRAM method also helped understand which portions of the NA precursor were removed by different water treatment processes. Activated carbon (AC) adsorption removed over 90% of the non-polar PRAM fraction (that sorbs onto the C18 solid phase extraction [SPE] cartridge) of NDMA and NDEA precursors. Bio-treatment removed 80-90% of the cationic fraction of PRAM (that is retained on the cation exchange SPE cartridge) and 40-60% of the non-cationic fractions. Ozonation removed 50-60% of the non-polar PRAM fraction of NA precursors and transformed part of them into the polar fraction. Coagulation and sedimentation had very limited removal of various PRAM fractions of NA precursors. Copyright © 2015 Elsevier Ltd. All rights reserved.

  19. Endogenous System Microbes as Treatment Process Indicators for Decentralized Non-potable Water Reuse

    Science.gov (United States)

    Monitoring the efficacy of treatment strategies to remove pathogens in decentralized systems remains a challenge. Evaluating log reduction targets by measuring pathogen levels is hampered by their sporadic and low occurrence rates. Fecal indicator bacteria are used in centraliz...

  20. Performance of BAC process for treatment of micro-polluted water

    Institute of Scientific and Technical Information of China (English)

    WANG Chen; MA Fang; SHAN Dan; YANG Ji-xian; Chang Chein-chi

    2008-01-01

    Biological activated carbon (BAC) has been developed on the granular activated carbon by immobi-lization of selected and acclimated species of bacteria to treat the micro-polluted water. The BAC removal effi-ciencies for nitrobenzene, permanganate index, turbidity and ammonia were investigated. Effects of shock load-ing and SEM (Scanning Electron Microscope) observation on BAC were studied. Baekwashing and its intensity of BAC were also discussed. The results showed that BAC took short time to start up and recover to the normal condition after shock loading. The shock loading studies showed that the removal efficiency of BAC was not completely inhibited even at high concentration of nitrobenzene. Backwashing performed once every 10- 20 d,or an average of 15 d. Backwashing intensity was 12-14 L/( s·m2) with air and 3-4 L/( s·m2) with water.

  1. Efficient operation of photo-Fenton process for the treatment of emerging contaminants in water solutions

    OpenAIRE

    Yamal Turbay, Evelyn

    2013-01-01

    The growth of population density in some areas of the planet and the increasing fast advances in technology and energy issues, have resulted in a remarkable increment in the necessity for goods and services, with a subsequent over-exploitation and pollution of the environmental resources. Water, a non-renewable resource, does not escape from the harmful effects of human activity and its increasing pollution levels threaten the normal development of ecosystems and life as well. In the last ...

  2. Water Treatment Technology - Filtration.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on filtration provides instructional materials for six competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: purposes of sedimentation basins and flocculation…

  3. Water Treatment Technology - Springs.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on springs provides instructional materials for two competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on spring basin construction and spring protection. For each competency, student…

  4. Water Treatment Technology - Wells.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on wells provides instructional materials for five competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: dug, driven, and chilled wells, aquifer types, deep well…

  5. Water Treatment Technology - Pumps.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on pumps provides instructional materials for three competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: types of pumps in plant and distribution systems, pump…

  6. Water Treatment Technology - Hydraulics.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on hydraulics provides instructional materials for three competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: head loss in pipes in series, function loss in…

  7. Cellulose based cationic adsorbent fabricated via radiation grafting process for treatment of dyes waste water.

    Science.gov (United States)

    Goel, Narender Kumar; Kumar, Virendra; Misra, Nilanjal; Varshney, Lalit

    2015-11-05

    A cationized adsorbent was prepared from cellulosic cotton fabric waste via a single step-green-radiation grafting process using gamma radiation source, wherein poly[2-(methacryloyloxy) ethyl]trimethylammonium chloride (PMAETC) was covalently attached to cotton cellulose substrate. Radiation grafted (PMAETC-g-cellulose) adsorbent was investigated for removal of acid dyes from aqueous solutions using two model dyes: Acid Blue 25 (AB25) and Acid Blue 74 (AB74). The equilibrium adsorption data was analyzed by Langmuir and Freundlich isotherms, whereas kinetic data was analyzed by pseudo first order, pseudo second order, intra particle diffusion and Boyd's models. The PMAETC-g-cellulose adsorbent with 25% grafting yield exhibited equilibrium adsorption capacities of ∼ 540.0mg/g and ∼ 340.0mg/g for AB25 and AB74, respectively. Linear and nonlinear fitting of adsorption data suggested that the equilibrium adsorption process followed Langmuir adsorption isotherm model, whereas, the kinetic adsorption process followed pseudo-second order model. The multi-linearities observed in the intra-particle kinetic plots suggested that the intraparticle diffusion was not the only rate-controlling process in the adsorption of acid dyes on the adsorbent, which was further supported by Boyd's model. The adsorbent could be regenerated by eluting the adsorbed dye from the adsorbent and could be repeatedly used.

  8. Influence of Brij58 on the Characteristic and Performance of PES Membrane for Water Treatment Process

    Science.gov (United States)

    Mukramah; Syawaliah; Mulyati, S.; Arahman, N.

    2017-03-01

    This study proposes a modification of polyether sulfone (PES) membrane by blending the polymer with a hydrophilic additive of Brij-58. Flat-sheet PES membrane was prepared through a non-solvent induced phase separation (NIPS) method using dimethylformamide (DMF) as a solvent. PES membrane was modified by adding Brij-58 into dope solution at a different concentration, i.e 1, 3, 5, 7, and 10 wt %. The fabricated membranes were characterized by means of Scanning Electron Microscopy (SEM) and Fourier Transform Infra-Red (FTIR) spectroscopy. Filtration performance of membrane was analyzed by using a dead-end module. It is found that the addition of a small amount of Brij into polymer solution brought about the increase of water flux. FT-IR investigation showed that the additive exist on the surface of a blended membrane.

  9. Photocatalytic Oxidation and Reduction Chemistry and a New Process for Treatment of Pink Water and Related Contaminated Water

    Science.gov (United States)

    1996-10-01

    passed to the near UV region. Actinometry measurements showed that about 5.2 watts of incident light that is available for TiO2 photocatalysis (300-400...studies. The combined processes of TiO2 assisted photocatalysis and follow-on biological mineralization have the potential for being an effective...onto the TiO2 particles or glass of the holding vials or spontaneous reaction and conversion to other chemical forms. II. PHOTOCATALYSIS OF TNT AND

  10. Water chemistry and poultry processing water quality

    Science.gov (United States)

    This study examined the influences of water chemistry on the quality of process water used in immersion chillers. During commercial poultry processing the bird carcasses come in direct contact with process water during washing and chilling operations. Contamination of the process water with bacteria...

  11. High Throughput Plasma Water Treatment

    Science.gov (United States)

    Mujovic, Selman; Foster, John

    2016-10-01

    The troublesome emergence of new classes of micro-pollutants, such as pharmaceuticals and endocrine disruptors, poses challenges for conventional water treatment systems. In an effort to address these contaminants and to support water reuse in drought stricken regions, new technologies must be introduced. The interaction of water with plasma rapidly mineralizes organics by inducing advanced oxidation in addition to other chemical, physical and radiative processes. The primary barrier to the implementation of plasma-based water treatment is process volume scale up. In this work, we investigate a potentially scalable, high throughput plasma water reactor that utilizes a packed bed dielectric barrier-like geometry to maximize the plasma-water interface. Here, the water serves as the dielectric medium. High-speed imaging and emission spectroscopy are used to characterize the reactor discharges. Changes in methylene blue concentration and basic water parameters are mapped as a function of plasma treatment time. Experimental results are compared to electrostatic and plasma chemistry computations, which will provide insight into the reactor's operation so that efficiency can be assessed. Supported by NSF (CBET 1336375).

  12. Development of a Novel Process Integrating the Treatment of Sludge Reject Water and the Production of Polyhydroxyalkanoates (PHAs).

    Science.gov (United States)

    Frison, Nicola; Katsou, Evina; Malamis, Simos; Oehmen, Adrian; Fatone, Francesco

    2015-09-15

    Polyhydroxyalkanoates (PHAs) from activated sludge and renewable organic material can become an alternative product to traditional plastics since they are biodegradable and are produced from renewable sources. In this work, the selection of PHA storing bacteria was integrated with the side stream treatment of nitrogen removal via nitrite from sewage sludge reject water. A novel process was developed and applied where the alternation of aerobic-feast and anoxic-famine conditions accomplished the selection of PHA storing biomass and nitrogen removal via nitrite. Two configurations were examined: in configuration 1 the ammonium conversion to nitrite occurred in the same reactor in which the PHA selection process occurred, while in configuration 2 two separate reactors were used. The results showed that the selection of PHA storing biomass was successful in both configurations, while the nitrogen removal efficiency was much higher (almost 90%) in configuration 2. The PHA selection degree was evaluated by the volatile fatty acid (VFA) uptake rate (-qVFAs) and the PHA production rate (qPHA), which were 239 ± 74 and 89 ± 7 mg of COD per gram of active biomass (Xa) per hour, respectively. The characterization of the biopolymer recovered after the accumulation step, showed that it was composed of 3-hydroxybutyrate (3HB) (60%) and 3-hydroxyvalerate (3HV) (40%). The properties associated with the produced PHA suggest that they are suitable for thermoplastic processing.

  13. [Investigation of the microbial diversity and structure of biological activated carbon from different sources in drinking water treatment process].

    Science.gov (United States)

    Du, Er-Deng; Zheng, Lu; Feng, Xin-Xin; Gao, Nai-Yun

    2014-11-01

    Restriction fragment length polymorphism (RFLP) technology was used to investigate the microbial diversity and structure of biological activated carbon (BAC) from different sources in drinking water advanced treatment process. Diversity indices of samples A, B and C, with relatively high tannic acid and humic acid adsorption capacity, were close to each other, which meant higher microbial diversity. However, samples D and E had relatively lower diversity indices with the low tannic acid and humic acid adsorption capacity. There were five species including β-Proteobacteria, α-Proteobacteria, Planctomycetes, γ-Proteobacteria, Bacteroidetes in the phylogenetic tree of BAC samples. Among them, β-Proteobacteria and α-Proteobacteria were the dominant microbial species in these BAC samples, which played an important role in organic matter removal. Planctomycetes, γ-Proteobacteria, and Bacteroidetes were the non-dominant microbial species. Bacteroidetes only existed in samples A, B, C and D, while did not occur in sample E. The BAC samples with the higher tannic acid and humic acid adsorption capacity had higher microbial diversity. This research should deepen the understanding of microbial community in BAC, and provide a theoretical basis for the safety of drinking water.

  14. Forward osmosis for the treatment of reverse osmosis concentrate from water reclamation: process performance and fouling control.

    Science.gov (United States)

    Kazner, C; Jamil, S; Phuntsho, S; Shon, H K; Wintgens, T; Vigneswaran, S

    2014-01-01

    While high quality water reuse based on dual membrane filtration (membrane filtration or ultrafiltration, followed by reverse osmosis) is expected to be progressively applied, treatment and sustainable management of the produced reverse osmosis concentrate (ROC) are still important issues. Forward osmosis (FO) is a promising technology for maximising water recovery and further dewatering ROC so that zero liquid discharge is produced. Elevated concentrations of organic and inorganic compounds may act as potential foulants of the concentrate desalting system, in that they consist of, for example, FO and a subsequent crystallizer. The present study investigated conditions under which the FO system can serve as concentration phase with the focus on its fouling propensity using model foulants and real ROC. Bulk organics from ROC consisted mainly of humic acids (HA) and building blocks since wastewater-derived biopolymers were retained by membrane filtration or ultrafiltration. Organic fouling of the FO system by ROC-derived bulk organics was low. HA was only adsorbed moderately at about 7% of the initial concentration, causing a minor flux decline of about 2-4%. However, scaling was a major impediment to this process if not properly controlled, for instance by pH adjustment or softening.

  15. Characteristics of meso-particles formed in coagulation process causing irreversible membrane fouling in the coagulation-microfiltration water treatment.

    Science.gov (United States)

    Ding, Q; Yamamura, H; Murata, N; Aoki, N; Yonekawa, H; Hafuka, A; Watanabe, Y

    2016-09-15

    In coagulation-membrane filtration water treatment processes, it is still difficult to determine the optimal coagulation condition to minimize irreversible membrane fouling. In microfiltration (MF), meso-particles (i.e., 20 nm-0.5 μm) are thought to play an important role in irreversible membrane fouling, especially their characteristics of particle number (PN) and zeta potential (ZP). In this study, a new nanoparticle tracker combined a high-output violet laser with a microscope was developed to identify the physicochemical characteristics of these microscopic and widely dispersed meso-particles. The effects of pH and coagulant dose on ZP and PN of micro-particles (i.e., >0.5 μm) and meso-particles were investigated, and then coagulation-MF tests were conducted. As the result, irreversible membrane fouling was best controlled for both types of membranes, while meso-particle ZP approached zero at around pH 5.5 for both types of natural water. Since PN was greatest under these conditions, ZP is more important in determining the extent of irreversible membrane fouling than PN. However, the acidic condition to neutralize meso-particles is not suitable for actual operation, as considering residual aluminum concentration, pipe corrosion, and chlorination efficiency. It is therefore necessary to investigate coagulants or other methods for the appropriate modification of meso-particle characteristics.

  16. Bacteriophages as microorganisms shape in the processes of treatment of drinkable waters; Bacteriofagos como microorganismos modelo en los procesos de tratamiento de aguas potables

    Energy Technology Data Exchange (ETDEWEB)

    Arza, I.; Mendez, X.; Valero, F.; Jofre, J.; Lucena, F.

    2002-07-01

    The removal of bacteriophages and bacterial indicators at the different stages of treatment in a drinking treatment plant were determined in order to investigate the usefulness of phages as model organisms to evaluate the effectiveness of the processes of the plant. Pre chlorination-flocculation-sedimentation was by far the most efficient step in removing phages, faecal coliforms and faecal streptococci during the periods. Sulphite reducing clostridia were the most resistant to this first stage of treatment. Entero viruses were never detected in finished water, and consequently their removal could not be quantified. The phages infecting Bact, fragilis and somatic coli phages are significantly more abundant then entero viruses in raw waters, heir numbers more elevated and their greater resistance during the process, allows their isolation throughout the processing. Consequently, somatic coliphages and phages infectingBact. fragilis deserve durther attention as model organisms for the evaluation of removal of human enteric viruses in water treatment plants. (Author) 21 refs.

  17. CFD in drinking water treatment

    NARCIS (Netherlands)

    Wols, B.A.

    2010-01-01

    Hydrodynamic processes largely determine the efficacy of drinking water treatment systems, in particular disinfection systems. A lack of understanding of the hydrodynamics has resulted in suboptimal designs of these systems. The formation of unwanted disinfection-by-products and the energy consumpti

  18. CFD in drinking water treatment

    NARCIS (Netherlands)

    Wols, B.A.

    2010-01-01

    Hydrodynamic processes largely determine the efficacy of drinking water treatment systems, in particular disinfection systems. A lack of understanding of the hydrodynamics has resulted in suboptimal designs of these systems. The formation of unwanted disinfection-by-products and the energy consumpti

  19. CFD in drinking water treatment

    NARCIS (Netherlands)

    Wols, B.A.

    2010-01-01

    Hydrodynamic processes largely determine the efficacy of drinking water treatment systems, in particular disinfection systems. A lack of understanding of the hydrodynamics has resulted in suboptimal designs of these systems. The formation of unwanted disinfection-by-products and the energy

  20. Effect of two-stage coagulant addition on coagulation-ultrafiltration process for treatment of humic-rich water.

    Science.gov (United States)

    Liu, Ting; Chen, Zhong-lin; Yu, Wen-zheng; Shen, Ji-min; Gregory, John

    2011-08-01

    A novel two-stage coagulant addition strategy applied in a coagulation-ultrafiltration (UF) process for treatment of humic-rich water at neutral pH was investigated in this study. When aluminum sulfate (alum) doses were set at a ratio of 3:1 added during rapid mix stage and half way through flocculation stage, the integrated process of two-stage alum addition achieved almost the same organic matter removal as that of conventional one-stage alum addition at the same overall dose. Whereas membrane fouling could be effectively mitigated by the two-stage addition exhibited by trans-membrane pressure (TMP) developments. The TMP developments were found to be primarily attributed to external fouling on membrane surface, which was closely associated with floc characteristics. The results of jar tests indicated that the average size of flocs formed in two-stage addition mode roughly reached one half larger than that in one-stage addition mode, which implied a beneficial effect on membrane fouling reduction. Moreover, the flocs with more irregular structure and lower effective density resulted from the two-stage alum addition, which caused higher porosity of cake layer formed by such flocs on membrane surface. Microscopic observations of membrane surface demonstrated that internal fouling in membrane pores could be also remarkably limited by two-stage alum addition. It is likely that the freshly formed hydroxide precipitates were distinct in surface characteristics from the aged precipitates due to formation of more active groups or adsorption of more labile aluminum species. Consequently, the flocs could further connect and aggregate to contribute to preferable properties for filtration performance of the coagulation-UF process. As a simple and efficient approach, two-stage coagulant addition strategy could have great practical significance in coagulation-membrane processes.

  1. DRINKING WATER TREATMENT

    Science.gov (United States)

    The purpose of water treatment is threefold: 1. To improve the aethetic quality ofwater, 2. to remove toxic or health-hazardous chemicals, 3. to remove and/or inactivate any disease causing microorganisms. These objectives should be accomplished using a reasonable safety factor...

  2. Basic Water Treatment Operation.

    Science.gov (United States)

    Ontario Ministry of the Environment, Toronto.

    This manual was developed for use at workshops designed to introduce the fundamentals of water treatment plant operations. The course consists of lecture-discussions and hands-on activities. Each of the fourteen lessons in this document has clearly stated behavioral objectives to tell the trainee what he should know or do after completing that…

  3. Process water usage and water quality in poultry processing equipment

    Science.gov (United States)

    The operation of poultry processing equipment was analyzed to determine the impact of water reduction strategies on process water quality. Mandates to reduce the consumption of process water in poultry processing facilities have created the need to critically examine water usage patterns and develop...

  4. Research of possibilities for the use of multienzyme complex of algae Mycrocystis aeruginosa for treatment of drinkable and process water

    Directory of Open Access Journals (Sweden)

    V. I. Karpenko

    2010-01-01

    Full Text Available The methods and a laboratory bench have been developed for research of the multienzyme systems of cyanobacteriae Mycrocystis aeruginosa. The bench allows regulating the luminous intensity and suspension agitation, studying the cells reproduction and conducting the chemical analysis of water. It has been established that algae can be used in a biofilter for reducing low concentrations of total iron in water to the levels which meet state standard (GOST 2874-82 requirements. Algae cells reproduction during water treatment from iron in a biofilter indicates that the number of enzyme systems and their activity increase. The advantage of the algae multienzyme systems use for the water treatment is the fact that they maintain their activity for a long time and do not need any carbonaceous energy substrata.

  5. Contaminated water treatment

    Science.gov (United States)

    Gormly, Sherwin J. (Inventor); Flynn, Michael T. (Inventor)

    2010-01-01

    Method and system for processing of a liquid ("contaminant liquid") containing water and containing urine and/or other contaminants in a two step process. Urine, or a contaminated liquid similar to and/or containing urine and thus having a relatively high salt and urea content is passed through an activated carbon filter to provide a resulting liquid, to remove most of the organic molecules. The resulting liquid is passed through a semipermeable membrane from a membrane first side to a membrane second side, where a fortified drink having a lower water concentration (higher osmotic potential) than the resulting liquid is positioned. Osmotic pressure differential causes the water, but not most of the remaining inorganic (salts) contaminant(s) to pass through the membrane to the fortified drink. Optionally, the resulting liquid is allowed to precipitate additional organic molecules before passage through the membrane.

  6. Variation in water density related to pollutants removal in wastewater treatment processes and its use in explaining the working principles of the Unifed SBR.

    Science.gov (United States)

    Xiang, Liancheng; Wu, Junqi; Song, Yonghui; Liu, Ruixia; Yu, Huibin; Gao, Qiong; Yang, Yingjie; Dai, Yunrong

    2016-11-01

    The wastewater quality of several municipal wastewater treatment plants (MWTPs) in Beijing was studied, and the water densities of different processing units were also measured during the wastewater treatment process. The results clearly showed that the water density declined from influent to effluent of the wastewater treatment process. Meanwhile, the variation in water density had good statistical correlation with the concentrations of total organic carbon, total phosphorus, suspended solids and total solids. Furthermore, the variation in water density could be used to explain the working principles of the Unifed sequencing batch reactor (SBR). Tracer tests were conducted in the Unifed SBR to investigate the hydraulic characteristics of the reactor. The experimental results showed that the variable values of water density from influent to effluent in the Fangzhuang MWTPs were greater than those caused by the temperature difference of >3 °C between the influent and the liquid in the reactor at 13 °C. Moreover, the flow regime of wastewater in the Unifed SBR was affected by the variation in water density, which may lead to stratification or a density current. Ascribed to the appearance of stratification in the Unifed SBR reactor, the water quality of the effluent could not be affected by that of the influent.

  7. Pilot scale hybrid processes for olive mill wastewater treatment, energy production and water reuse: comparison between fungal and electro-coagulation pre-treatments

    Energy Technology Data Exchange (ETDEWEB)

    Sayadi, S.

    2009-07-01

    Olive oil mill wastewaters (OMW) cause disposal problems because they contain powerful pollutants such as phenolic compounds. Complete biodegradation or removal of these compounds is hardly achieved by a single treatment method. In this work, we investigated 2 integrated technologies for the treatment of the recalcitrant contaminants of OMW, allowing water recovery and reuse for agricultural purposes. (Author)

  8. Analysis and Comparison of Water Purification Processes and Finished Water Quality for 3 Water Treatment Plants%关于三个水厂净水工艺与供水水质的比较和分析

    Institute of Scientific and Technical Information of China (English)

    岳宇明; 陆茸; 毛丽娜; 沈元静; 何小清

    2014-01-01

    该文介绍了国内一自来水公司三个水厂的两个原水水质、净水工艺及出厂水水质。结果显示第一水厂的出厂水质较为理想,第二水厂次之,第三水厂为第三。第三水厂由于水源的问题导致出厂氨氮季节性超标,建议采取有效措施改进水源水质,以提高出厂水质。第二水厂需进行工艺改造,实施臭氧活性炭深度处理以进一步提高供水水质。第三水厂一期系统臭氧生物活性炭池置于砂滤池后较二期活性炭滤池置于砂滤池前出水有机物CODMn及TOC略低,但两者基本相近。建议第三水厂采取必要的措施改进水源水质,或再增加一道臭氧生物活性炭工序。%Water plants with two different raw water qualities,purification processes and their effluent water qualities were introduced in this paper. The finished water quality of NO. 1 plant is the best,and the NO. 2 is better. Due to raw water quality problem No. 3 water plant’s finished water ammonia nitrogen hardly meets the standard of GB 5749-2006 seasonally. Effective measures should be taken to improve the effluent water quality of No. 3 water plant No. 2 water plant need technological transformation to implement advanced treatment of O3 actived carbon to improve finished water quality. The organic indexes of effluent water of first-stage system in No. 3 water plant,of which O3 actived carbon filter is located behind the sand filter,is a little better than that of second-stage system, of which O3 actived carbon filter is located before the sand filter. But their finished water qualities are approximately same. Necessary measures to improve raw water quality for No. 3 water plant or to apply an additional ozone BAC process are recommended.

  9. Industrial Water Treatment Primer

    Science.gov (United States)

    1992-03-01

    2040) Gallic Acid Powder (item 2063) METHOD: It is necessary to follow the instructions furnished with the conductivity meter that is being used . The...reduces CO. Caustic soda raises pH to desired level. (Courtesy of Power: McGraw-Hill Publications) (2) A hydrogen zeolite softener (Figure 9) uses acid ...a) The acid used in the regeneration process makes the effluent water more corrosive (lower pH on effluent). (b) The hazards that exist in handling

  10. Abundance and diversity of ammonia-oxidizing archaea and bacteria on biological activated carbon in a pilot-scale drinking water treatment plant with different treatment processes.

    Science.gov (United States)

    Kasuga, Ikuro; Nakagaki, Hirotaka; Kurisu, Futoshi; Furumai, Hiroaki

    2010-01-01

    The effects of different placements of rapid sand filtration on nitrification performance of BAC treatment in a pilot-scale plant were evaluated. In this plant, rapid sand filtration was placed after ozonation-BAC treatment in Process (A), while it preceded ozonation-BAC treatment in Process (B). Analysis of amoA genes of ammonia-oxidizing archaea (AOA) and bacteria (AOB) combined with nitrification potential test was conducted. BAC from Process (A) demonstrated slightly higher nitrification potential at every sampling occasion. This might be due to higher abundances of AOB on BAC from Process (A) than those on BAC from Process (B). However, AOA rather than AOB could be predominant ammonia-oxidizers in BAC treatment regardless of the position of rapid sand filtration. The highest nitrification potential was observed for BAC from both processes in February when the highest abundances of AOA-amoA and AOB-amoA genes were detected. Since rapid sand filtration was placed after BAC treatment in Process (A), residual aluminum concentration in BAC influent was higher in Process (A). However, adverse effects of aluminum on nitrification activity were not observed. These results suggest that factors other than aluminum concentration in different treatment processes could possibly have some influence on abundances of ammonia-oxidizing microorganisms on BAC.

  11. The effects of various control and water treatment processes on the membrane integrity and toxin fate of cyanobacteria.

    Science.gov (United States)

    Fan, Jiajia; Hobson, Peter; Ho, Lionel; Daly, Robert; Brookes, Justin

    2014-01-15

    Cyanobacterial blooms are one of the main contaminants that can degrade drinking water quality with the associated taste, odour and toxic compounds. Although a wide range of techniques have shown promise for cyanobacterial bloom control and cyanobacterial cell/metabolite removal in reservoirs and water treatment plants (WTPs), these treatments may have negative consequences through release of intracellular metabolites into the surrounding water. This study assessed the impact of copper sulphate (CuSO4), chlorine, potassium permanganate (KMnO4), hydrogen peroxide (H2O2) and ozone on Microcystis aeruginosa culture and the toxins it produced. All of these agents induced the loss of cyanobacterial membrane integrity. However, no associated increase in dissolved toxins was detected during chlorine and H2O2 treatments which may be due to faster toxin oxidation rates than release rates. KMnO4 doses of 1 and 3mgL(-1) degraded dissolved toxins while having no impact on cyanobacterial membrane integrity. In contrast, ozone induced a significant increase in extracellular toxins but it was unable to degrade these toxins to the same degree as the other oxidants which may due to the lack of residual. All chemicals, except CuSO4, were able to reduce cyanotoxins and chlorine was the most effective with a rate up to 2161M(-1)s(-1).

  12. Advanced oxidation processes for treatment of petroleum refinery sour waters; Processos oxidativos avancados para tratamento de aguas acidas de refinaria de petroleo

    Energy Technology Data Exchange (ETDEWEB)

    Castro, Antonio V.; Coelho, Alessandra D.; Sant' Anna Junior, Geraldo L.; Dezotti, Marcia [Universidade Federal do Rio de Janeiro (UFRJ), RJ (Brazil). Coordenacao dos Programas de Pos-graduacao de Engenharia (COPPE). Programa de Engenharia Quimica

    2004-07-01

    The characteristics of the waste water generated by the petroleum refineries are related to the type and amount of processed oil, to the nature and the efficiency of the refining operation. The effluents are composed basically of oily waters, originating from of the contact with the oil. Among them, the current of sour water is one of the most preoccupying due to its composition: sulfide, ammonia, mercaptans, phenol, dissolved oil, basic pH, dissolved organic carbon (DOC) and chemical oxygen demand (COD) high. The aim of this work was to evaluate the advanced oxidation processes to degrade sour water (UV radiation, H{sub 2}O{sub 2} and H{sub 2}O{sub 2}/UV, photocatalysis, Fenton and photo-Fenton). All process, except Fenton and photo-Fenton, did not supply satisfactory results, reducing 25% of initial DOC, which it is of 450 mg/L. The results using the Fenton process reached removal of 50% of the initial COD, and when photo- Fenton process obtaining removal of 90%. The processes Fenton and photo-Fenton were shown capable to degrade this kind of waste water, minimizing the environmental problems and corrosion, operating as a pre-treatment for the biological system, or acting alone to degrade the organic matter contained, seeking the water reuse. The effluent used in this work came from Duque de Caxias Refinery (Reduc)/PETROBRAS. (author)

  13. Study of nematodes as indicators of efficiency of the waste water treatment process; Los nematodos como indicadores en el proceso de depuracion de las aguas residuales

    Energy Technology Data Exchange (ETDEWEB)

    Santos Lobaton, M. C.; Trujillo Mena, E.M.; Casaus Alvarez, M.; Oliva Rodriguez, J.

    2004-07-01

    In this paper we present the first results of a study about the role of nematodes as indicators of efficiency of the waste-water treatment process. These organisms, besides being considered as indicators of quality of the purification processes and contemplated in normative and guidelines, corroborate the importance of the bio indication in a mans that present special conditions as they are purifying of residual waters. Also, the character bacteriofagous of some species contributes to reduce the concentrations of bacterial populations and to reduce the DBO. The study was carried out on Andalusia (Spain) and they were nematode belonging to forty-three genera. (Author) 10 refs.

  14. Inactivation characteristics of ozone and electrolysis process for ballast water treatment using B. subtilis spores as a probe.

    Science.gov (United States)

    Jung, Youmi; Yoon, Yeojoon; Hong, Eunkyung; Kwon, Minhwan; Kang, Joon-Wun

    2013-07-15

    Since ballast water affects the ocean ecosystem, the International Maritime Organization (IMO) sets a standard for ballast water management and might impose much tighter regulations in the future. The aim of this study is to evaluate the inactivation efficiency of ozonation, electrolysis, and an ozonation-electrolysis combined process, using B. subtilis spores. In seawater ozonation, HOBr is the key active substance for inactivation, because of rapid reactivity of ozone with Br(-) in seawater. In seawater electrolysis, it is also HOBr, but not HOCl, because of the rapid reaction of HOCl with Br(-), which has not been recognized carefully, even though many electrolysis technologies have been approved by the IMO. Inactivation pattern was different in ozonation and electrolysis, which has some limitations with the tailing or lag-phase, respectively. However, each deficiency can be overcome with a combined process, which is most effective as a sequential application of ozonation followed by electrolysis.

  15. Numerical Simulation and Experimental Studies of Air Treatment Process with Water Spray of One Row Parallel Flow

    Institute of Scientific and Technical Information of China (English)

    倪波

    2001-01-01

    The main purpose of the present work is to make a further insight into the procedure of heat and mass transfer between water droplets sprayed and air stream in a direct evaporative air cooler used in air-conditioning system in textile mills. The thermodynamic models of the two-phase flow in such a air treatment system have been developed for one row parallel flow spray.The fields of temperature and relative humidity in spraylchamber, as well as the trajectories of sprayed drops have been obtained by calculation. A series of experiment aiming at quantifying the system performance and its influence factors have been conducted. It indicates that the increases of air velocity and water/air ratio while the decrease of nozzle density are favorable. Finally, the comparison between numerical simulation and experimental results have been carried out. Good agreements have been found for outlet air temperaturewhile a maximum error of 10% has been observed for air relative humidity.

  16. 火力发电厂膜法水处理技术应用%THE APPLICATION OF IMT WATER TREATMENT PROCESSING IN THE POWER PLANT

    Institute of Scientific and Technical Information of China (English)

    张铭; 禾志强; 刘永江; 韦强

    2011-01-01

    全膜法( IMT)处理工艺,用两级反渗透(RO)+电去离子(EDI)处理工艺,代替传统的RO+混床处理工艺,在初始投资相近的情况下,由于系统无酸碱消耗,无废水排放,无需再生用水,运行费用显著降低,同时系统占地面积大大下降.IMT水处理系统出水水质优良,运行稳定,出水电导率小于0.2 μS·cm-1,含硅量小于20μg·L-1,符合电厂锅炉补给水水质要求,综合性能优于RO+混床处理工艺.%IMT watertreatment technology, which instead of the RO+osmosis-mixed bed treatment process, with two step RO+EDI processing, had a lower operating costs than the traditional watertreatment technology with the similar initial investment, since no acid-base system consumption, no waste water discharge, no regeneration of water, and small footprint. IMT water treatment system was stable, the effluent water conductivity was less than 0.2 u,S · cm-1, silicon content was less than 20 u,g · L-1, which was consistent with requirements of the power plant boiler make-up water quality. The overall performance of the IMT water treatment technology was superior than the RO+osmosis-mixed bed treatment process.

  17. Evaluation of virus removal efficiency of coagulation-sedimentation and rapid sand filtration processes in a drinking water treatment plant in Bangkok, Thailand.

    Science.gov (United States)

    Asami, Tatsuya; Katayama, Hiroyuki; Torrey, Jason Robert; Visvanathan, Chettiyappan; Furumai, Hiroaki

    2016-09-15

    In order to properly assess and manage the risk of infection by enteric viruses in tap water, virus removal efficiency should be evaluated quantitatively for individual processes in actual drinking water treatment plants (DWTPs); however, there have been only a few studies due to technical difficulties in quantifying low virus concentration in water samples. In this study, the removal efficiency of indigenous viruses was evaluated for coagulation-sedimentation (CS) and rapid sand filtration (RSF) processes in a DWTP in Bangkok, Thailand by measuring the concentration of viruses before and after treatment processes using real-time polymerase chain reaction (qPCR). Water samples were collected and concentrated from raw source water, after CS, and after RSF, and inhibitory substances in water samples were reduced by use of a hydrophobic resin (DAX-8). Pepper mild mottle virus (PMMoV) and JC polyomavirus (JC PyV) were found to be highly prevalent in raw waters, with concentrations of 10(2.88 ± 0.35) and 10(3.06 ± 0.42) copies/L (geometric mean ± S.D.), respectively. Step-wise removal efficiencies were calculated for individual processes, with some variation observed between wet and dry seasons. During the wet season, PMMoV was removed less by CS and more by RSF on average (0.40 log10 vs 1.26 log10, respectively), while the reverse was true for JC PyV (1.91 log10 vs 0.49 log10, respectively). Both viruses were removed similarly during the dry season, with CS removing the most virus (PMMoV, 1.61 log10 and 0.78 log10; JC PyV, 1.70 log10, and 0.59 log10; CS and RSF, respectively). These differences between seasons were potentially due to variations in raw water quality and the characteristics of the viruses themselves. These results suggest that PMMoV and JC PyV, which are more prevalent in environmental waters than the other enteric viruses evaluated in this study, could be useful in determining viral fate for the risk management of viruses in water treatment

  18. Effects of ultrasound pretreatment on the characteristic evolutions of drinking water treatment sludge and its impact on coagulation property of sludge recycling process.

    Science.gov (United States)

    Zhou, Zhiwei; Yang, Yanling; Li, Xing

    2015-11-01

    Large amounts of drinking water treatment sludge (DWTS) are produced during the flocculation or flotation process. The recycling of DWTS is important for reducing and reclaiming the waste residues from drinking water treatment. To improve the coagulation step of the DWTS recycling process, power ultrasound was used as a pretreatment to disintegrate the DWTS and degrade or inactivate the constituents that are difficult to remove by coagulation. The effects of ultrasound pretreatment on the characteristics of DWTS, including the extent of disintegration, variation in DWTS floc characteristics, and DWTS dewaterability, were investigated. The capacity of the recycling process to remove particulates and organic matter from low-turbidity surface water compared to a control treatment process without DWTS was subsequently evaluated. The coagulation mechanism was further investigated by analyzing the formation, breakage, and re-growth of re-coagulated flocs. Our results indicated that under the low energy density applied (0.03-0.033 W/mL) for less than 15 min at a frequency of 160 kHz, the level of organic solubilization was less elevated, which was evidenced by the lower release of proteins and polysaccharides and lower fluorescence intensities of humic- and protein-like substances. The applied ultrasound conditions had an adverse effect on the dewaterability of the DWTS. Ultrasound pretreatment had no significant impact on the pH or surface charge of the DWTS flocs, whereas particle size decreased slightly and the specific surface area was moderately increased. The pollution removal capacity decreased somewhat for the recycled sonicated DWTS treatment, which was primarily ascribed to organic solubilization rather than variability in the floc characteristics of sonicated DWTS. The main coagulation mechanism was floc sweeping and physical adsorption. The breakage process of the flocs formed by the recycling process displayed distinct irreversibility, and the flocs were

  19. Grey water treatment systems: A review

    NARCIS (Netherlands)

    Abu-Ghunmi, L.N.A.H.; Zeeman, G.; Fayyad, M.; Lier, van J.B.

    2011-01-01

    This review aims to discern a treatment for grey water by examining grey water characteristics, reuse standards, technology performance and costs. The review reveals that the systems for treating grey water, whatever its quality, should consist of processes that are able to trap pollutants with a sm

  20. Comparison of two polarity measurements of hydrophobic organic matter for the evaluation of water treatment processes: XAD resin and PRAM.

    Science.gov (United States)

    Philibert, Marc; Rosario-Ortiz, Fernando; Suffet, Mel

    2012-01-01

    Dissolved organic matter (DOM) is a mixture of thousands of organic molecules wide-ranging in molecular weight, polarity and physicochemical properties. DOM is responsible for multiple water treatment issues such as trihalomethane (THM) formation potential and membrane fouling. Two methods of evaluating the polarity of DOM are being used for water treatment application: a serial XAD resin adsorption method at acid pH and the polarity rapid assessment method (PRAM) by parallel solid phase extraction (SPE) cartridges at natural pH. These two methods have been described by their authors as able to define a hydrophobic fraction though they do so by sorption onto different types of material at different pHs. The first part of this study compared the PRAM and XAD methods and showed that the hydrophobic fractions defined by the two approaches were not correlated. This result highlighted the difficulties in defining fractions as 'hydrophobic material'. It appeared that the sorbents for XAD-8 (an acrylic polymer containing oxygen) at pH <3 and C-18 (a pure hydrocarbon polymer coating on silica particles) at neutral or pH <3 did not retain similar hydrophobic fractions. This hypothesis was verified by fluorescence spectroscopy of the effluent of the XAD-8 resin and PRAM C-18 SPE cartridge. Finally the study concentrated on the use of fluorescence and ultrafiltration methods in series with PRAM to gain more insight into the structure and characteristics of the hydrophobic DOM present in drinking water sources. This evaluation showed that the smaller molecular weight fraction of DOM (<1 kDa) had a higher percentage of hydrophobic character and that the fluorescence-defined aromatic protein fraction was the most hydrophilic.

  1. The state-of-the art of produced water treatment by oxidative advanced processes; Atual estagio de desenvolvimento dos processos oxidativos avancados para o tratamento da agua produzida

    Energy Technology Data Exchange (ETDEWEB)

    Cortes, Marcela de A.H.; Marques, Jose Jailton; Rocha, Inaura C.C. da [Universidade Federal de Sergipe (UFS), Aracaju, SE (Brazil). Dept. de Engenharia Quimica

    2008-07-01

    The oily wastewater generated in petroleum exploration contains a sort of contaminants that may cause significant environmental impact. For this reason, the number of researchers that are looking for cleaner techniques to treat this kind of wastewater is growing. The advanced oxidation processes (AOPs) are clean and non-selective processes largely used to the treatment of wastewater containing critical substances like textile dyes, pesticides, PCBs, PAHs etc. The treatment systems using AOPs can be homogeneous or heterogeneous and they may use irradiation or not. This work presents a compilation of the results found by many researchers involving AOPs potentially applicable to the treatment of produced water, as follow: H{sub 2}O{sub 2}/UV, H{sub 2}O{sub 2} / Fe{sup 2+} / UV, O{sub 3}/UV, O{sub 3}/ H{sub 2}O{sub 2} etc., showing the state-of-art of oxidation advanced processes. (author)

  2. Integration of biofiltration and advanced oxidation processes for tertiary treatment of an oil refinery wastewater aiming at water reuse.

    Science.gov (United States)

    Nogueira, A A; Bassin, J P; Cerqueira, A C; Dezotti, M

    2016-05-01

    The combination of biological and chemical oxidation processes is an interesting approach to remove ready, poor, and non-biodegradable compounds from complex industrial wastewaters. In this study, biofiltration followed by H2O2/UV oxidation (or microfiltration) and final reverse osmosis (RO) step was employed for tertiary treatment of an oil refinery wastewater. Biofiltration alone allowed obtaining total organic carbon (TOC), chemical oxygen demand (COD), UV absorbance at 254 nm (UV254), ammonium, and turbidity removal of around 46, 46, 23, 50, and 61 %, respectively. After the combined biological-chemical oxidation treatment, TOC and UV254 removal amounted to 88 and 79 %, respectively. Whereas, the treatment performance achieved with different UV lamp powers (55 and 95 W) and therefore distinct irradiance levels (26.8 and 46.3 mW/cm(2), respectively) were very similar and TOC and UV254 removal rates were highly affected by the applied C/H2O2 ratio. Silt density index (SDI) was effectively reduced by H2O2/UV oxidation, favoring further RO application. C/H2O2 ratio of 1:4, 55 W UV lamp, and 20-min oxidation reaction corresponded to the experimental condition which provided the best cost/benefit ratio for TOC, UV254, and SDI reduction from the biofilter effluent. The array of treatment processes proposed in this study has shown to be adequate for tertiary treatment of the oil refinery wastewater, ensuring the mitigation of membrane fouling problems and producing a final effluent which is suitable for reuse applications.

  3. An evaluation of Hanford water treatment practices

    Energy Technology Data Exchange (ETDEWEB)

    Touhill, C.J.

    1965-09-01

    An evaluation of Hanford reactor process water treatment practices was made in an effort to ascertain the reasons for variations in the effluent activity between reactors. Recommendations are made for improvements in unit processes as well as for the over-all treatment process based on field inspection of the water treatment plants. In addition, a research program is proposed to supplement the recommendations. The proposed research is designed to uncover methods of more efficient filtration as well as other procedures which might eventually lead to significant effluent activity reductions. The recommendations and research results will be applied toward process optimization.

  4. Novel Water Treatment Processes Based on Hybrid Membrane-Ozonation Systems: A Novel Ceramic Membrane Contactor for Bubbleless Ozonation of Emerging Micropollutants

    Directory of Open Access Journals (Sweden)

    Stylianos K. Stylianou

    2015-01-01

    Full Text Available The aim of this study is the presentation of novel water treatment systems based on ozonation combined with ceramic membranes for the treatment of refractory organic compounds found in natural water sources such as groundwater. This includes, firstly, a short review of possible membrane based hybrid processes for water treatment from various sources. Several practical and theoretical aspects for the application of hybrid membrane-ozonation systems are discussed, along with theoretical background regarding the transformation of target organic pollutants by ozone. Next, a novel ceramic membrane contactor, bringing into contact the gas phase (ozone and water phase without the creation of bubbles (bubbleless ozonation, is presented. Experimental data showing the membrane contactor efficiency for oxidation of atrazine, endosulfan, and methyl tert-butyl ether (MTBE are shown and discussed. Almost complete endosulfan degradation was achieved with the use of the ceramic contactor, whereas atrazine degradation higher than 50% could not be achieved even after 60 min of reaction time. Single ozonation of water containing MTBE could not result in a significant MTBE degradation. MTBE mineralization by O3/H2O2 combination increased at higher pH values and O3/H2O2 molar ratio of 0.2 reaching a maximum of around 65%.

  5. Numerical Simulation and Experimental Studies of Air Treatment Process with Water Spray of One Row Counter Flow

    Institute of Scientific and Technical Information of China (English)

    倪波

    2001-01-01

    The present work is focused on heat and mass transfer in a direct evaporative air cooler of one row counter flow spray. Models of the two-phase flow in such a air treatment system have been developed. The fields of temperature and relative humidity in spray chamber, as well as the trajectories of sprayed drops have been obtained by numerical method. Experiments aiming at quantifying the system performance and its influence factors have been conducted. It indicates that the increase of air velocity and water/air ratio while the decrease of nozzle density are favorable. The performance of the system of parallel flow spray and counter flow spray have been compared by means of humidifying efficiency. Comparison between numerical simulation and experimental results demonstrate good agreement for outlet air temperature with a maximum error of 8% observed for air relative humidity.

  6. Comparison of different combined treatment processes to address the source water with high concentration of natural organic matter during snowmelt period

    Institute of Scientific and Technical Information of China (English)

    Pengfei Lin; Xiaojian Zhang; Jun Wang; Yani Zeng; Shuming Liu; Chao Chen

    2015-01-01

    The source water in one forest region of the Northeast China had very high natural organic matter (NOM) concentration and heavy color during snowmelt period.The efficiency of five combined treatment processes was compared to address the high concentration of NOM and the mechanisms were also analyzed.Conventional treatment can hardly remove dissolved organic carbon (DOC) in the source water.KMnO4 pre-oxidization could improve the DOC removal to 22.0%.Post activated carbon adsorption improved the DOC removal of conventional treatment to 28.8%.The non-sufficient NOM removal could be attributed to the dominance of large molecular weight organic matters in raw water,which cannot be adsorbed by the micropore upon activated carbon.O3 + activated carbon treatment are another available technology for eliminating the color and UV254 in water.However,its performance of DOC removal was only 36.4%,which could not satisfy the requirement for organic matter.The limited ozone dosage is not sufficient to mineralize the high concentration of NOM.Magnetic ion-exchange resin combined with conventional treatment could remove 96.2% of color,96.0% of UV254 and 87.1% of DOC,enabling effluents to meet the drinking water quality standard.The high removal efficiency could be explained by the negative charge on the surface of NOM which benefits the static adsorption of NOM on the anion exchange resin.The results indicated that magnetic ion-exchange resin combined with conventional treatment is the best available technology to remove high concentration of NOM.

  7. Optimizing the coagulation process in a drinking water treatment plant -- comparison between traditional and statistical experimental design jar tests.

    Science.gov (United States)

    Zainal-Abideen, M; Aris, A; Yusof, F; Abdul-Majid, Z; Selamat, A; Omar, S I

    2012-01-01

    In this study of coagulation operation, a comparison was made between the optimum jar test values for pH, coagulant and coagulant aid obtained from traditional methods (an adjusted one-factor-at-a-time (OFAT) method) and with central composite design (the standard design of response surface methodology (RSM)). Alum (coagulant) and polymer (coagulant aid) were used to treat a water source with very low pH and high aluminium concentration at Sri-Gading water treatment plant (WTP) Malaysia. The optimum conditions for these factors were chosen when the final turbidity, pH after coagulation and residual aluminium were within 0-5 NTU, 6.5-7.5 and 0-0.20 mg/l respectively. Traditional and RSM jar tests were conducted to find their respective optimum coagulation conditions. It was observed that the optimum dose for alum obtained through the traditional method was 12 mg/l, while the value for polymer was set constant at 0.020 mg/l. Through RSM optimization, the optimum dose for alum was 7 mg/l and for polymer was 0.004 mg/l. Optimum pH for the coagulation operation obtained through traditional methods and RSM was 7.6. The final turbidity, pH after coagulation and residual aluminium recorded were all within acceptable limits. The RSM method was demonstrated to be an appropriate approach for the optimization and was validated by a further test.

  8. Scaling up the chemical treatment of spent oil-in-water emulsions from a non-ferrous metal-processing plant

    Directory of Open Access Journals (Sweden)

    Lazarević Vesna B.

    2013-01-01

    Full Text Available The treatment of spent oil-in-water emulsion (SOWE from a non-ferrous metal-processing plant by using aluminum sulfate and hydrated lime was studied to determine the purification efficiency, to optimize the operating conditions and to scale up the treatment process. The purification efficiency was estimated by comparing the compositions of the SOWE and the processed wastewater. The treatment efficiency does not depend on the type of mineral oil and filter aid. The optimum doses of aluminum sulfate and hydrated lime must be experimentally determined for each batch of SOWEs, but the results obtained at laboratory level are applicable at pilot level. The processed wastewater and the filter cake from the process can be safely disposed into public sewage systems and at municipal waste landfills, respectively. The purification efficiency was higher than 98% with respect to total suspended solids, chemical oxygen demand and oil and grease, and was comparable to the known treatment processes based on coagulation/flocculation followed by sedimentation.

  9. [Energy Consumption Comparison and Energy Saving Approaches for Different Wastewater Treatment Processes in a Large-scale Reclaimed Water Plant].

    Science.gov (United States)

    Yang, Min; Li, Ya-ming; Wei, Yuan-song; Lü, Jian; Yu, Da-wei; Liu, Ji-bao; Fan, Yao-bo

    2015-06-01

    Energy consumption is the main performance indicator of reclaimed water plant (RWP) operation. Methods of specific energy consumption analysis, unit energy consumption analysis and redundancy analysis were applied to investigate the composition and spatio-temporal distribution of energy consumption in Qinghe RWP with inverted A2/O, A2/O and A2/O-MBR processes. And the A2/ O-MBR process was mainly analyzed to identify the main nodes and causes for high energy consumption, approaches for energy saving were explored, and the energy consumption before and after upgrading for energy saving was compared. The results showed that aeration was the key factor affecting energy consumption in both conventional and A2/O-MBR processes, accounting for 42.97% and 50.65% of total energy consumption, respectively. A pulsating aeration allowed an increasing membrane flux and remarkably reduced the energy consumption of the A2/O-MBR process while still meeting the effluent standard, e.g., the membrane flux was increased by 20%, and the energy consumptions per kiloton wastewater and kilogram COD(removed) were decreased by 42.39% to 0.53 kW-h-kg-3 and by 54.74% to 1.29 kW x h x kg(-1), respectively. The decrease of backflow ratio in the A2/O-MBR process within a certain range would not deteriorate the effluent quality due to its insignificant correlation with the effluent quality, and therefore may be considered as one of the ways for further energy saving.

  10. Treatment of oil sands process-affected water using moving bed biofilm reactors: With and without ozone pretreatment.

    Science.gov (United States)

    Shi, Yijing; Huang, Chunkai; Rocha, Ketley Costa; El-Din, Mohamed Gamal; Liu, Yang

    2015-09-01

    Two moving bed biofilm reactors (MBBRs) were operated to treat raw (untreated) and 30 mg/L ozone-treated oil sands process-affected water (OSPW). After 210 days, the MBBR process showed 18.3% of acid-extractable fraction (AEF) and 34.8% of naphthenic acids (NAs) removal, while the ozonation combined MBBR process showed higher removal of AEF (41.0%) and NAs (78.8%). Biodegradation of raw and ozone treated OSPW showed similar performance. UPLC/HRMS analysis showed a highest NAs removal efficiency with a carbon number of 14 and a -Z number of 4. Confocal laser scanning microscopy (CLSM) showed thicker biofilms in the raw OSPW MBBR (97 ± 5 μm) than in the ozonated OSPW MBBR (71 ± 12 μm). Quantitative polymerase chain reaction (q-PCR) results showed higher abundance of gene copies of total bacteria and nitrogen removal relevant bacteria in the ozonated OSPW MBBR, but no significant difference was found. MiSeq sequencing showed Proteobacteria, Nitrospirae, and Acidobacteria were dominant.

  11. Impact of ozonation pre-treatment of oil sands process-affected water on the operational performance of a GAC-fluidized bed biofilm reactor.

    Science.gov (United States)

    Islam, Md Shahinoor; Dong, Tao; McPhedran, Kerry N; Sheng, Zhiya; Zhang, Yanyan; Liu, Yang; Gamal El-Din, Mohamed

    2014-11-01

    Treatment of oil sands process-affected water (OSPW) using biodegradation has the potential to be an environmentally sound approach for tailings water reclamation. This process is both economical and efficient, however, the recalcitrance of some OSPW constituents, such as naphthenic acids (NAs), require the pre-treatment of raw OSPW to improve its biodegradability. This study evaluated the treatment of OSPW using ozonation followed by fluidized bed biofilm reactor (FBBR) using granular activated carbon (GAC). Different organic and hydraulic loading rates were applied to investigate the performance of the bioreactor over 120 days. It was shown that ozonation improved the adsorption capacity of GAC for OSPW and improved biodegradation by reducing NAs cyclicity. Bioreactor treatment efficiencies were dependent on the organic loading rate (OLR), and to a lesser degree, the hydraulic loading rate (HLR). The combined ozonation, GAC adsorption, and biodegradation process removed 62 % of chemical oxygen demand (COD), 88 % of acid-extractable fraction (AEF) and 99.9 % of NAs under optimized operational conditions. Compared with a planktonic bacterial community in raw and ozonated OSPW, more diverse microbial communities were found in biofilms colonized on the surface of GAC after 120 days, with various carbon degraders found in the bioreactor including Burkholderia multivorans, Polaromonas jejuensis and Roseomonas sp.

  12. 电镀工业园区污水处理部分工艺的选型%Process Selection of Waste Water Treatment for Electroplating Industrial Zone

    Institute of Scientific and Technical Information of China (English)

    文睿; 陆华

    2012-01-01

    According to the character of waste water effluent for electroplating industrial zones,the waste water is collected by category of chemicals.A process of chemical treatment + MBR(membrane bioreactor) + RO desalt is applied to treat the waste water such that reaches the standard of discharge and water reuse requirements.Comparing with the properties of regular processes including water reuse system,stress the importance of categorized collections of waste water.%依据电镀集中园区废水的特点采取有针对性的分类收集,采用化学法+膜生物(MBR)+RO膜脱盐处理工艺达标排放和回用,对比了部分常见工艺的特点,包括中水回用系统的设计注意事项,强调电镀污水源头分流的意义。

  13. Simultaneous heterotrophic and sulfur-oxidizing autotrophic denitrification process for drinking water treatment: control of sulfate production.

    Science.gov (United States)

    Sahinkaya, Erkan; Dursun, Nesrin; Kilic, Adem; Demirel, Sevgi; Uyanik, Sinan; Cinar, Ozer

    2011-12-15

    A long-term performance of a packed-bed bioreactor containing sulfur and limestone was evaluated for the denitrification of drinking water. Autotrophic denitrification rate was limited by the slow dissolution rate of sulfur and limestone. Dissolution of limestone for alkalinity supplementation increased hardness due to release of Ca(2+). Sulfate production is the main disadvantage of the sulfur autotrophic denitrification process. The effluent sulfate concentration was reduced to values below drinking water guidelines by stimulating the simultaneous heterotrophic and autotrophic denitrification with methanol supplementation. Complete removal of 75 mg/L NO(3)-N with effluent sulfate concentration of around 225 mg/L was achieved when methanol was supplemented at methanol/NO(3)-N ratio of 1.67 (mg/mg), which was much lower than the theoretical value of 2.47 for heterotrophic denitrification. Batch studies showed that sulfur-based autotrophic NO(2)-N reduction rate was around three times lower than the reduction rate of NO(3)-N, which led to NO(2)-N accumulation at high loadings.

  14. Onsite Waste Water Treatment System

    Directory of Open Access Journals (Sweden)

    T. Subramani

    2014-06-01

    Full Text Available Onsite wastewater treatment systems (OWTSs have evolved from the pit privies used widely throughout history to installations capable of producing a disinfected effluent that is fit for human consumption. Although achieving such a level of effluent quality is seldom necessary, the ability of onsite systems to remove settles able solids, floatable grease and scum, nutrients, and pathogens. From wastewater discharges defines their importance in protecting human health and environmental resources. In the modern era, the typical onsite system has consisted primarily of a septic tank and a soil absorption field, also known as a subsurface wastewater infiltration system, or SWIS. In this manual, such systems are referred to as conventional systems. Septic tanks remove most settle able and floatable material and function as an anaerobic bioreactor that promotes partial digestion of retained organic matter. Septic tank effluent, which contains significant concentrations of pathogens and nutrients, has traditionally been discharged to soil, sand, or other media absorption fields (SWISs for further treatment through biological processes, adsorption, filtration, and infiltration into underlying soils. Conventional systems work well if they are installed in areas with appropriate soils and hydraulic capacities; designed to treat the incoming waste load to meet public health, ground water, and surface water performance standards; installed properly; and maintained to ensure long-term performance. These criteria, however, are often not met. Only about one-third of the land area in the United States has soils suited for conventional subsurface soil absorption fields. System densities in some areas exceed the capacity of even suitable soils to assimilate wastewater flows and retain and transform their contaminants. In addition, many systems are located too close to ground water or surface waters and others, particularly in rural areas with newly installed public

  15. Circular economy in drinking water treatment: reuse of ground pellets as seeding material in the pellet softening process.

    Science.gov (United States)

    Schetters, M J A; van der Hoek, J P; Kramer, O J I; Kors, L J; Palmen, L J; Hofs, B; Koppers, H

    2015-01-01

    Calcium carbonate pellets are produced as a by-product in the pellet softening process. In the Netherlands, these pellets are applied as a raw material in several industrial and agricultural processes. The sand grain inside the pellet hinders the application in some high-potential market segments such as paper and glass. Substitution of the sand grain with a calcite grain (100% calcium carbonate) is in principle possible, and could significantly improve the pellet quality. In this study, the grinding and sieving of pellets, and the subsequent reuse as seeding material in pellet softening were tested with two pilot reactors in parallel. In one reactor, garnet sand was used as seeding material, in the other ground calcite. Garnet sand and ground calcite performed equally well. An economic comparison and a life-cycle assessment were made as well. The results show that the reuse of ground calcite as seeding material in pellet softening is technologically possible, reduces the operational costs by €38,000 (1%) and reduces the environmental impact by 5%. Therefore, at the drinking water facility, Weesperkarspel of Waternet, the transition from garnet sand to ground calcite will be made at full scale, based on this pilot plant research.

  16. Forward Osmosis in Wastewater Treatment Processes

    DEFF Research Database (Denmark)

    Korenak, Jasmina; Basu, Subhankar; Balakrishnan, Malini

    2017-01-01

    In recent years, membrane technology has been widely used in wastewater treatment and water purification. Membrane technology is simple to operate and produces very high quality water for human consumption and industrial purposes. One of the promising technologies for water and wastewater treatment...... briefly review some of the applications within water purification and new developments in forward osmosis membrane fabrication....... is the application of forward osmosis. Essentially, forward osmosis is a process in which water is driven through a semipermeable membrane from a feed solution to a draw solution due to the osmotic pressure gradient across the membrane. The immediate advantage over existing pressure driven membrane technologies...

  17. Technical Process in Advanced Treatment of Taihu Lake Source Water%太湖水源水深度处理直饮的技术工艺

    Institute of Scientific and Technical Information of China (English)

    胡孟春; 张永春; 唐晓燕; 沈海风; 王文林

    2013-01-01

    To address the problem of organic compound pollution in the Taihu Lake drinking water source, a combined process composed mainly of bio-filter and reverse osmosis membrane was developed. The process included pretreatment with BAF, the combined treatment system with ultrafiltration (UF) , micro-filtration (MF) and reverse osmosis (RO) membrane, and the product water system with ultraviolet sterilization. The design focused on key parts such as the pretreatment system with BAF, combined membranes treatment optimization, washing and backwashing system. The operation results showed that the combined process was suitable for advanced treatment of the organically polluted and eutrophicated source water of Taihu Lake. The product water met the standard for direct drinking quality.%针对太湖有机复合污染饮用水源的主要问题,设计了以生物过滤、反渗透膜为主的组合技术工艺,包括:曝气生物滤池前处理系统;超滤、微滤、反渗透膜组合处理系统;紫外消毒产品水出水系统.在设计中着重解决了关键部分的设计:生物滤池前处理系统;膜组合处理系统优化;清洗系统.设备运行结果表明,该工艺适合太湖有机污染富营养化水源水的深度净化处理,产品水可达到高品质直饮水水质标准.试验研究为太湖水源水的深度净化找到了一条可行的技术途径.

  18. Removal of Anabaena flos-aquae in water treatment process using Moringa oleifera and assessment of fatty acid profile of generated sludge.

    Science.gov (United States)

    Moreti, Livia O R; Coldebella, Priscila Ferri; Camacho, Franciele P; Carvalho Bongiovani, Milene; Pereira de Souza, Aloisio Henrique; Kirie Gohara, Aline; Matsushita, Makoto; Fernandes Silva, Marcela; Nishi, Letícia; Bergamasco, Rosângela

    2016-01-01

    This study aimed to evaluate the efficiency of the coagulation/flocculation/dissolved air flotation (C/F/DAF) process using the coagulant Moringa oleifera (MO) seed powder, and to analyse the profile of fatty acids present in the generated sludge after treatment. For the tests, deionized water artificially contaminated with cell cultures of Anabaena flos-aquae was used, with a cell density in the order of 10(4) cells mL(-1). C/F/DAF tests were conducted using 'Flotest' equipment. For fatty acid profile analyses, a gas chromatograph equipped with a flame ionization detector was used. It was seen that the optimal dosage (100 mg L(-1)) of MO used in the C/F/DAF process was efficient at removing nearly all A. flos-aquae cells (96.4%). The sludge obtained after treatment contained oleic acid (61.7%) and palmitic acid (10.8%). Thus, a water treatment process using C/F/DAF linked to integral MO powder seed was found to be efficient in removing cells of cyanobacteria, and produced a sludge rich in oleic acid that is a precursor favourable for obtaining quality biodiesel, thus becoming an alternative application for the recycling of such biomass.

  19. Application of the Washing Waste Water Recycling Process Ultrafiltration Treatment Process%洗车废水循环利用过程中超滤处理工艺的应用探讨

    Institute of Scientific and Technical Information of China (English)

    刘昕

    2015-01-01

    The main subway train car wash waste water recycling process ultrafiltration treatment process applied technology were discussed, in order to promote recycling car wash industry, water resources, increase economic efficiency subway train car wash library.%主要对地铁列车洗车废水循环利用过程中的超滤处理工艺应用技术进行了探讨,以促进洗车行业水资源的循环利用,提高地铁列车洗车库的经济效益。

  20. Innovations in nanotechnology for water treatment

    Directory of Open Access Journals (Sweden)

    Gehrke I

    2015-01-01

    Full Text Available Ilka Gehrke, Andreas Geiser, Annette Somborn-SchulzFraunhofer Institute for Environmental, Safety and Energy Technology UMSICHT, Oberhausen, GermanyAbstract: Important challenges in the global water situation, mainly resulting from worldwide population growth and climate change, require novel innovative water technologies in order to ensure a supply of drinking water and reduce global water pollution. Against this background, the adaptation of highly advanced nanotechnology to traditional process engineering offers new opportunities in technological developments for advanced water and wastewater technology processes. Here, an overview of recent advances in nanotechnologies for water and wastewater treatment processes is provided, including nanobased materials, such as nanoadsorbents, nanometals, nanomembranes, and photocatalysts. The beneficial properties of these materials as well as technical barriers when compared with conventional processes are reported. The state of commercialization is presented and an outlook on further research opportunities is given for each type of nanobased material and process. In addition to the promising technological enhancements, the limitations of nanotechnology for water applications, such as laws and regulations as well as potential health risks, are summarized. The legal framework according to nanoengineered materials and processes that are used for water and wastewater treatment is considered for European countries and for the USA.Keywords: nanotechnology, water technology, nanoadsorbents, nanometals, nanomembranes, photocatalysis

  1. Technology for Water Treatment

    Science.gov (United States)

    1992-01-01

    There are approximately 500,000 water cooling towers in the United States, all of which must be kept clear of "scale" and corrosion and free of pollutants and bacteria. Electron Pure, Ltd. manufactures a hydro cooling tower conditioner as well as an automatic pool sanitizer. The pool sanitizer consists of two copper/silver electrodes placed in a chamber mounted in the pool's recirculation system. The tower conditioner combines the ionization system with a water conditioner, pump, centrifugal solids separator and timer. The system saves water, eliminates algae and operates maintenance and chemical free. The company has over 100 distributors in the U.S. as well as others in 20 foreign countries. The buildup of scale and corrosion is the most costly maintenance problem in cooling tower operation. Jet Propulsion Laboratory successfully developed a non-chemical system that not only curbed scale and corrosion, but also offered advantages in water conservation, cost savings and the elimination of toxic chemical discharge. In the system, ozone is produced by an on-site generator and introduced to the cooling tower water. Organic impurities are oxidized, and the dissolved ozone removes bacteria and scale. National Water Management, a NASA licensee, has installed its ozone advantage systems at some 200 cooling towers. Customers have saved money and eliminated chemical storage and discharge.

  2. Quantification of water usage at a South African platinum processing ...

    African Journals Online (AJOL)

    water use will also lessen the dependence of mining opera- tions on water resources ..... available for the water footprints of the chemicals and electricity used within the process. ... A list of tasks, stores and treatment plants was also provided.

  3. The artificial water cycle: emergy analysis of waste water treatment.

    Science.gov (United States)

    Bastianoni, Simone; Fugaro, Laura; Principi, Ilaria; Rosini, Marco

    2003-04-01

    The artificial water cycle can be divided into the phases of water capture from the environment, potabilisation, distribution, waste water collection, waste water treatment and discharge back into the environment. The terminal phase of this cycle, from waste water collection to discharge into the environment, was assessed by emergy analysis. Emergy is the quantity of solar energy needed directly or indirectly to provide a product or energy flow in a given process. The emergy flow attributed to a process is therefore an index of the past and present environmental cost to support it. Six municipalities on the western side of the province of Bologna were analysed. Waste water collection is managed by the municipal councils and treatment is carried out in plants managed by a service company. Waste water collection was analysed by compiling a mass balance of the sewer system serving the six municipalities, including construction materials and sand for laying the pipelines. Emergy analysis of the water treatment plants was also carried out. The results show that the great quantity of emergy required to treat a gram of water is largely due to input of non renewable fossil fuels. As found in our previous analysis of the first part of the cycle, treatment is likewise characterised by high expenditure of non renewable resources, indicating a correlation with energy flows.

  4. Bacterial Oxidation and Reduction of Iron in the Processes of Creation and Treatment of Acid Mining Waters

    Directory of Open Access Journals (Sweden)

    Daniel Kupka

    2004-12-01

    Full Text Available Acid mine drainages (AMDs arise at the weathering of sulphidic minerals. The occurrence of acidic streams is commonly associated with the human mining activities. Due to the disruption and excavation of sulphide deposits, the oxidation processes have initiated. Acidic products of sulphide oxidation accelerate the degradation of accompanying minerals. AMDs typically contain high concentrations of sulfuric acid and soluble metals and cause serious ecological problems due to the water pollution and the devastation of adjacent country. Microbial life in these extremely acidic environments may be considerably diverse. AMDs are abundant in bacteria capable to oxidize and/or to reduce iron. The rate of bacterial oxidation of ferrous iron released from pyrite surfaces is up to one million times faster than the chemical oxidation rate at low pH. Bacterial regeneration of ferric iron maintains the continuity of pyrite oxidation and the production of AMDs. Another group of microorganisms living in these environments are acidophilic ferric iron reducing bacteria. This group of microorganisms has been discovered only relatively recently. Acidophilic heterotrophic bacteria reduce ferric iron in either soluble or solid forms to ferrous iron. The reductive dissolution of ferric iron minerals brings about a mobilization of iron as well as associated heavy metals. The Bacterial oxidation and reduction of iron play an important role in the transformation of either crystalline or amorphous iron-containing minerals, including sulphides, oxides, hydroxysulfates, carbonates and silicates. This work discusses the role of acidophilic bacteria in the natural iron cycling and the genesis of acidic effluents. The possibilities of application of iron bacteria in the remediation of AMDs are also considered.

  5. Removal of Natural Organic Matter Fractions by Anion Exchange: Impact on drinking water treatment processes and biological stability

    NARCIS (Netherlands)

    Grefte, A.

    2013-01-01

    This researched focused on improving drinking water quality, specifically the biological stability of the produced drinking water. Natural organic matter (NOM) can be a source of nutrients for bacteria present in the distribution system, which can cause regrowth. Specifically, small organic acids ca

  6. Validation Aspects of Water Treatment Systems for Pharmaceutical ...

    African Journals Online (AJOL)

    Validation Aspects of Water Treatment Systems for Pharmaceutical Products. ... that a process, when operated within established limits, produces a product of ... of validation including different approaches, components of water treatment ...

  7. Appropriate drinking water treatment processes for organic micropollutants removal based on experimental and model studies - A multi-criteria analysis study

    KAUST Repository

    Sudhakaran, Sairam

    2013-01-01

    The presence of organic micropollutants (OMPs), pharmaceuticals and personal care products (PPCPs) in potable water is of great environmental and public health concern. OMPs are included in the priority list of contaminants in United States EPA and European framework directives. Advanced treatment processes such as reverse osmosis, nanofiltration, ozonation and adsorption are the usual industry-recommended processes for OMPs removal, however, natural systems, e.g., riverbank filtration and constructed wetlands, are also potentially efficient options for OMPs removal. In this study, a decision support system (DSS) based on multi-criteria analysis (MCA) was created to compare processes for OMPs removal under various criteria. Multi-criteria analysis (MCA), a transparent and reliable procedure, was adopted. Models were built for both experimental and predicted percent-removals for a range of OMPs reflecting different physicochemical properties. The experimental percent-removals for several processes (riverbank filtration (RBF), ozonation, advanced oxidation, adsorption, reverse osmosis, and nanofiltration) were considered. The predicted percent-removals were taken from validated quantitative structure activity relationship (QSAR) models. Analytical methods to detect OMPs in water are very laborious, thus a modeling approach such as QSAR is an attractive option.A survey among two groups of participants including academics (PhD students and post-doctoral research associates) and industry (managers and operators) representatives was conducted to assign weights for the following criteria: treatability, costs, technical considerations, sustainability and time. The process rankings varied depending on the contaminant species and personal preferences (weights). The results indicated that RBF and oxidation were preferable over adsorption and membranes processes. The results also suggest that the use of a hybrid treatment process, e.g., combining a natural system with an

  8. Appropriate drinking water treatment processes for organic micropollutants removal based on experimental and model studies - a multi-criteria analysis study.

    Science.gov (United States)

    Sudhakaran, Sairam; Lattemann, Sabine; Amy, Gary L

    2013-01-01

    The presence of organic micropollutants (OMPs), pharmaceuticals and personal care products (PPCPs) in potable water is of great environmental and public health concern. OMPs are included in the priority list of contaminants in United States EPA and European framework directives. Advanced treatment processes such as reverse osmosis, nanofiltration, ozonation and adsorption are the usual industry-recommended processes for OMPs removal, however, natural systems, e.g., riverbank filtration and constructed wetlands, are also potentially efficient options for OMPs removal. In this study, a decision support system (DSS) based on multi-criteria analysis (MCA) was created to compare processes for OMPs removal under various criteria. Multi-criteria analysis (MCA), a transparent and reliable procedure, was adopted. Models were built for both experimental and predicted percent-removals for a range of OMPs reflecting different physicochemical properties. The experimental percent-removals for several processes (riverbank filtration (RBF), ozonation, advanced oxidation, adsorption, reverse osmosis, and nanofiltration) were considered. The predicted percent-removals were taken from validated quantitative structure activity relationship (QSAR) models. Analytical methods to detect OMPs in water are very laborious, thus a modeling approach such as QSAR is an attractive option. A survey among two groups of participants including academics (PhD students and post-doctoral research associates) and industry (managers and operators) representatives was conducted to assign weights for the following criteria: treatability, costs, technical considerations, sustainability and time. The process rankings varied depending on the contaminant species and personal preferences (weights). The results indicated that RBF and oxidation were preferable over adsorption and membranes processes. The results also suggest that the use of a hybrid treatment process, e.g., combining a natural system with an

  9. Water treatment technologies for CBM water, including cavitation

    Energy Technology Data Exchange (ETDEWEB)

    Makysmentz, B.; Lyon, F.L. [Newpark Resources Inc., Calgary, AB (Canada). Newpark Environmental Water Solutions

    2006-07-01

    The reasons for treating CBM water, end uses, reverse osmosis, pretreatment for reverse osmosis, and Newpark case studies are described. CBM water can be treated to make it suitable for injection, re-use, irrigation, or surface discharge. Usually the total dissolved solids (TDS) must be reduced by ion exchange or reverse osmosis with pretreatment. The concept of reverse osmosis and three types of applicable membrane processes are described: microfiltration and ultrafiltration, nanofiltration, and electrodialysis. The technologies used for pretreatment depend on the water quality and treatment goals, e.g. coagulation, flocculation and sand media filtration, softening, ion exchange, and nanofiltration. A Newpark case study is described for a water treatment plant at Boulder, Wyoming where evaporation was replaced by cavitation technology. The suitability of various treatment methods for Alberta CBM water is discussed. 21 figs., 1 tab.

  10. Application of novel Modified Biological Aerated Filter (MBAF) as a promising post-treatment for water reuse: Modification in configuration and backwashing process.

    Science.gov (United States)

    Nikoonahad, Ali; Ghaneian, Mohammad Taghi; Mahvi, Amir Hossein; Ehrampoush, Mohammad Hassan; Ebrahimi, Ali Asghar; Lotfi, Mohammad Hassan; Salamehnejad, Sima

    2017-12-01

    Biological Aerated Filter (BAF) reactors due to their plentiful biomass, high shockability, high efficiency, good filtration, availability and lack of need for large land areas, are enjoying from great importance in advanced wastewater treatment. Therefore, in this study, Polystyrene Coated by Sand (PCS) was produced as a novel media and its application in a modified down-flow BAF structure for advanced wastewater treatment was assessed in two steps. In step one, the backwash effluent did not return to the system, while in step two backwash effluent returned to increase the water reuse efficiency. The backwash process was also studied through three methods of Top Backwashing (TB), Bottom Backwashing (BB), as well as Top and Bottom Backwashing Simultaneously (TBBS). The results showed that return of backwash effluent had no significant effect on the BAF effluent quality. In the second step similar to the first one with slight differences, the residual average concentrations of TSS, BOD5, and COD at the effluent were about 2.5, 8.2, and 25.5 mg/L, respectively. Additionally, in step two, the mean volume of disposal sludge/volume of treated water (vds/vtw) decreased a large extent to about 0.088%. In other words, the water reuse has increased to more than 99.91%. The backwash time in methods of TB and BB were 65 and 35 min, respectively; however, it decreased in TBBS methods to 25 min. The concentrations of most effluent parameters in this system are in concordance with the 2012 EPA Agriculture Standards, even for irrigation of Non-processed agricultural crops and livestock water consumption. Copyright © 2017 Elsevier Ltd. All rights reserved.

  11. Water Treatment Technology - Distribution Systems.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on distribution systems provides instructional materials for six competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: types of pipe for distribution systems, types…

  12. Water Treatment Technology - Distribution Systems.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on distribution systems provides instructional materials for six competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: types of pipe for distribution systems, types…

  13. Influence of pH on hydrothermal treatment of swine manure: Impact on extraction of nitrogen and phosphorus in process water.

    Science.gov (United States)

    Ekpo, U; Ross, A B; Camargo-Valero, M A; Fletcher, L A

    2016-08-01

    This study investigates the influence of pH on extraction of nitrogen and phosphorus from swine manure following hydrothermal treatment. Conditions include thermal hydrolysis (TH) at 120°C and 170°C, and hydrothermal carbonisation (HTC) at 200°C and 250°C in either water alone or in the presence of 0.1M NaOH, H2SO4, CH3COOH or HCOOH. Phosphorus extraction is pH and temperature dependent and is enhanced under acidic conditions. The highest level of phosphorus is extracted using H2SO4 reaching 94% at 170°C. The phosphorus is largely retained in the residue for all other conditions. The extraction of nitrogen is not as significantly influenced by pH, although the maximum N extraction is achieved using H2SO4. A significant level of organic-N is extracted into the process waters following hydrothermal treatment. The results indicate that operating hydrothermal treatment in the presence of acidic additives has benefits in terms of improving the extraction of phosphorus and nitrogen.

  14. 深度处理工艺的系统选择研究%System selection of the advanced water treatment process

    Institute of Scientific and Technical Information of China (English)

    许嘉炯; 范玉柱

    2012-01-01

    Aiming at the removal of organics in the widely existing micro-polluted raw water in this country, this paper discussed the characteristics of several combined process with the core of activated carbon and ultra-filtration. Moreover, using the normal biological activated carbon and the new combined process of activated carbon and ultra-filtration for experiment study and engineering application analysis, this paper studied the removal effects of control indexes including organics, ammonia, and turbidity, and finally completed trie advanced water treatment system selection under different raw water qualities.%针对当前国内普遍存在的微污染原水有机物去除目标,探讨深度处理工艺中以活性炭吸附和超滤工艺为核心的多种组合工艺的特点.选择目前常用的生物活性炭工艺和开始应用的活性炭-超滤膜工艺进行试验研究和工程应用分析,探究各种工艺在不同条件下对有机物、氨氮和浊度等控制指标的去除效果,从而在不同原水水质条件下完成深度处理的系统选择.

  15. A pilot plant study using conventional and advanced water treatment processes: Evaluating removal efficiency of indicator compounds representative of pharmaceuticals and personal care products.

    Science.gov (United States)

    Zhang, Shuangyi; Gitungo, Stephen; Axe, Lisa; Dyksen, John E; Raczko, Robert F

    2016-11-15

    With widespread occurrence of pharmaceuticals and personal care products (PPCPs) in the water cycle, their presence in source water has led to the need to better understand their treatability and removal efficiency in treatment processes. Fifteen indicator compounds were identified to represent the large number of PPCPs reported worldwide. Criteria applied to determine the indicator compounds included PPCPs widely used, observed at great frequency in aqueous systems, resistant to treatment, persistent in the environment, and representative of classes of organics. Through a pilot plant investigation to understand the optimal combination of unit process for treating PPCPs, 12 treatment trains with their additive and synergistic contributions were investigated; processes included dissolved air flotation (DAF), pre- and intermediate-ozonation with and without H2O2, intermediate chlorination, dual media filtration, granular activated carbon (GAC), and UV/H2O2. Treatment trains that achieved the greatest removals involved 1. DAF followed by intermediate ozonation, dual media filtration, and virgin GAC; 2. pre-ozonation followed by DAF, dual media filtration, and virgin GAC; and, 3. DAF (with either pre- or intermediate oxidation) followed by dual media filtration and UV/H2O2. Results revealed significant removal efficiencies for virgin GAC (preceded by DAF and intermediate ozonation) and UV/H2O2 with an intensity of 700 mJ/cm(2), where more than 12 of the compounds were removed by greater than 90%. Reduced PPCP removals were observed with virgin GAC preceded by pre-ozonation and DAF. Intermediate ozonation was more effective than using pre-ozonation, demonstrating the importance of this process targeting PPCPs after treatment of natural organic matter. Removal efficiencies of indicator compounds through ozonation were found to be a function of the O3 rate constants (kO3). For compounds with low O3 rate constants (kO3 < 10 M(-1)s(-1)), H2O2 addition in the O3 reactor

  16. Basic Concepts of Magnetic Water Treatment

    Directory of Open Access Journals (Sweden)

    Oleg Mosin

    2014-06-01

    Full Text Available This review article outlines an overview of new trends and modern approaches for practical implementation of magnetic water treatment to eliminate scaling salts (carbonate, chloride and sulfate salts of Ca2+, Mg2+, Fe2+ and Fe3+ cations in power heat-exchanger devices and pipe lines. The principles of physical effects of the magnetic field on H2O molecules as well as the parameters of physico-chemical processes occurring in water and the behavior of the dissolved in water scaling salts subjected to the magnetic treatment are discussed. It is demonstrated that the effect of the magnetic field on water is a complex multifactorial phenomenon resulted in changes of the structure of hydrated ions as well as the physico-chemical properties and behavior of dissolved inorganic salts, changes in the rate of electrochemical coagulation and aggregate stability (clumping and consolidation, formation of multiple nucleation sites on the particles of fine dispersed precipitate consisting of crystals of substantially uniform size. There are also submitted data on constructive features of various magnetic water treatment devices produced by domestic industry, based on the permanent magnets and electromagnets (solenoids, such as hydro magnetic systems (HMS, magnetic transducers (MT and magnetic activators (MA of water. It was estimated the efficiency of using the various magnetic water treatment devices in water treatment technologies.

  17. The impact of water exchange rate and treatment processes on water-borne hormones in recirculation aquaculture systems containing sexually maturing Atlantic salmon Salmo salar

    Science.gov (United States)

    A controlled seven-month study was conducted in six replicated water recirculation aquaculture systems (WRAS) to assess post-smolt Atlantic salmon (Salmo salar) performance in relation to WRAS water exchange rate. Unexpectedly high numbers of precocious sexually mature fish were observed in all WRAS...

  18. Supported Nanosized α-FeOOH Improves Efficiency of Photoelectro-Fenton Process with Reaction-Controlled pH Adjustment for Sustainable Water Treatment

    Directory of Open Access Journals (Sweden)

    Chuan Wang

    2012-01-01

    Full Text Available The overall photoelectro-Fenton (PE-Fenton process for water treatment with neutral initial pH includes three steps of pH reduction, PE-Fenton reaction, and pH elevation. Reaction-controlled pH adjustment (RCpA, which utilizes the intrinsic electrochemical reactions instead of chemical addition, has been employed to lower the pH, maintain the lowered pH for the Fenton reaction, and recover the pH for final effluent discharge. This study demonstrated that the overall efficiency of this sustainable PE-Fenton process was improved by rapidly recycling the iron substance. Nanosized iron oxide was prepared and employed to ensure such rapid recycling. SEM and XRD results showed that the as-prepared iron oxide was α-FeOOH with 20 nm in size. The experimental results of dimethyl phthalate (DMP degradation showed that diatomite-supported α-FeOOH (N-α-FeOOH/diatomite could efficiently reduce the DMP concentration and total organic carbon. Furthermore, compared with Fe3+, the N-α-FeOOH/diatomite saved 160 min for iron settlement at 20 mg L−1 DMP concentration. Also, with the increment in the initial DMP concentration, extra energy consumed by the individual step of PE-Fenton reaction using the N-α-FeOOH/diatomite became negligible compared with that using free iron ions with the increment in the initial DMP concentration. This development is expected to be a major step of the PE-Fenton process with RCpA towards actual water treatment.

  19. Treatment Technology and Alternative Water Resources

    Science.gov (United States)

    Chapman, M. J.

    2014-12-01

    At this point in our settlement of the planet Earth, with over seven billion human inhabitants, there are very few unallocated sources of fresh water. We are turning slowly toward "alternatives" such as municipal and industrial wastewater, saline groundwater, the sea, irrigation return flow, and produced water that comes up with oil and gas deposits from deep beneath the surface of the earth. Slowly turning, not because of a lack in technological ability, but because it takes a large capital investment to acquire and treat these sources to a level at which they can be used. The regulatory system is not geared up for alternative sources and treatment processes. Permitting can be circular, contradictory, time consuming, and very expensive. The purpose for the water, or the value of the product obtained using the water, must be such that the capital and ongoing expense seem reasonable. There are so many technological solutions for recovering water quality that choosing the most reliable, economical, and environmentally sound technology involves unraveling the "best" weave of treatment processes from a tangled knot of alternatives. Aside from permitting issues, which are beyond the topic for this presentation, the "best" weave of processes will be composed of four strands specifically fitted to the local situation: energy, pretreatment, driving force for separation processes, and waste management. A range of treatment technologies will be examined in this presentation with a focus on how the quality of the feed water, available power sources, materials, and waste management opportunities aid in choosing the best weave of treatment technologies, and how innovative use of a wide variety of driving forces are increasing the efficiency of treatment processes.

  20. A new effective process for production of curdlan oligosaccharides based on alkali-neutralization treatment and acid hydrolysis of curdlan particles in water suspension.

    Science.gov (United States)

    Li, Jing; Zhu, Li; Zheng, Zhi-Yong; Zhan, Xiao-Bei; Lin, Chi-Chung; Zong, Yu; Li, Wei-Jiang

    2013-10-01

    Biologically active β-1,3-oligosaccharides with rapidly growing biomedical applications are produced from hydrolysis of curdlan polysaccharide. The water-insoluble curdlan impedes its hydrolysis efficiency which is enhanced by our newly developed alkali-neutralization treatment process to increase the stability of curdlan suspension to more than 20 days, while the untreated control settled within 5 min. A putative double-layer structure model comprising of a compact core and a hydrated outer layer was proposed to describe the treated curdlan particles based on sedimentation and scanning electron microscopy observation. This model was verified by single- and two-step acid hydrolysis, indicative of the reduced susceptibility to hydrolysis when close to the compact core. Electrospray ionization-mass spectrometry, thin-layer chromatography analyses, and effective HPLC procedure led to the development of improved process to produce purified individual β-1,3-oligosaccharides with degrees of polymerization from 2 to 10 and potential for biomedical applications from curdlan hydrolyzate. Our new curdlan oligosaccharide production process offers an even better alternative to the previously published processes.

  1. Improvement of the coagulation/flocculation process using a combination of Moringa oleifera lam with anionic polymer in water treatment.

    Science.gov (United States)

    Bongiovani, Milene Carvalho; Camacho, Franciele Pereira; Nishi, Letícia; Coldebella, Priscila Ferri; Valverde, Karina Cardoso; Vieira, Angélica Marquetotti Salcedo; Bergamasco, Rosângela

    2014-01-01

    The objective of this study is to investigate the impacts of anionic polymer as a flocculant aid on the coagulation/flocculation performance with a saline solution of Moringa oleifera as a coagulant to provide larger flocs and decrease the time sedimentation. For the tests, raw water was used from Pirapó River Basin (Maringá, Paraná, Brazil). Optimization of coagulation/flocculation tests was initially performed in a jar-test with a dosage of M. oleifera Lam (crude extract--MO, oil-extracted with ethanol--MO (et) and hexane--MO (hex) 1% m/v) as the coagulant that ranged from 10 to 60 mg L(-1) and of the anionic polymer 0.1% as a flocculant aid with a dosage that ranged from 0 to 0.4 mg L(-1). The parameters analysed were colour, turbidity and compounds with absorption in UV254nm. In view of the statistical analysis results, MO (hex) with a dosage of 30 mg L(-1) was chosen as a coagulant for the next tests of coagulation/flocculation. When anionic polymer was used alone (0.0 mg L(-1) of MO (hex)), parameters were not removed and there was no generation of heavy flocs as compared with the combination of MO (hex) with the anionic polymer. Statistical analysis showed that MO (hex) obtained the highest removals of the parameters analysed in lower dosages and no significant increase in parameters removal was observed when the polymer dosage was increased. The efficacy of the coagulant +/- anionic polymer was optimal when 30mg L(-1) of MO (hex) was used as a coagulant and 0.1 mg L(-1) of the anionic polymer was used as a flocculant aid, decreasing the time sedimentation from 1 h to 15 min.

  2. Surface Water Treatment Workshop Manual.

    Science.gov (United States)

    Ontario Ministry of the Environment, Toronto.

    This manual was developed for use at workshops designed to increase the knowledge of experienced water treatment plant operators. Each of the fourteen lessons in this document has clearly stated behavioral objectives to tell the trainee what he should know or do after completing that topic. Areas covered in this manual include: basic water…

  3. Water treatment processes in marine recirculating aquaculture systems: A review%海水循环养殖系统水处理工艺综述

    Institute of Scientific and Technical Information of China (English)

    姜妍君; 强志民; 董慧峪; 贲伟伟; 王磊

    2013-01-01

    This paper reviews the key water quality parameters and the related unit treatment processes in marine recirculating aquaculture systems ( RAS). Besides routinely monitoring and controlling salinity, pH, temperature, and dissolved oxygen, RAS usually adopts physical, chemical and biological combinational treatment processes to reduce the concentrations of solid particles, ammonia nitrogen, nitrite, nitrate, organic matter and pathogens. Solid particles can be removed by sedimentation, filtration, foam fractionation or biofiltration according to different particle sizes and settlabilities. Ammonia nitrogen, nitrite and nitrate are mainly removed by biological nitrification and denitrification. Organic matter can be decomposed by microorganisms. Chemical oxidants and ultraviolet radiation are commonly-used disinfection methods in RAS. Disinfectant residue and disinfection byproducts, two critical factors impacting water quality and animal health, should be primarily concerned when selecting appropriate disinfection method. Finally, several commonly-adopted combinational treatment processes for RAS are exemplified with suggestions for future improvement provided.%论述了海水循环养殖系统(RAS)需要控制的水质参数及相关单元水处理工艺.RAS需要对盐度、pH、温度、溶解氧等水质参数进行监测控制,并常采用物理、生物、化学处理的组合工艺,使固体物质、氨氮、亚硝酸盐、硝酸盐、有机物以及致病微生物等的浓度维持在安全范围内.固体物质根据粒径和可沉降性的不同,可采用沉降、过滤、泡沫分离或生物过滤法去除;氨氮、亚硝酸盐以及硝酸盐主要通过生物的硝化和反硝化作用去除;有机物主要通过生物降解去除;化学药剂消毒以及紫外辐照是RAS常用的消毒方法,消毒剂残余及消毒副产物对水质和动物健康的影响是选择合适消毒方法需要考虑的两个关键因素.最后,列举了几种海

  4. Use of an ultrafiltration system in the Gundremmingen nuclear power plant for the treatment of nuclear process water; Einsatz einer Ultrafiltration im Kernkraftwerk Gundremmingen zur Aufbereitung von nuklearen Prozesswaessern

    Energy Technology Data Exchange (ETDEWEB)

    Krumpholz, Udo [Kernkraftwerk Gundremmingen GmbH, Gundremmingen (Germany). Teilbereich Ueberwachung - Chemie/Entsorgung; George, Carsten [Kernkraftwerk Gundremmingen GmbH, Gundremmingen (Germany). Teilbereich Technik - Maschinentechnik; Berger, Joerg [Gruenbeck Wasseraufbereitung GmbH, Hoechstaedt a.d. Donau (Germany). Energiezentralen

    2014-07-01

    Over the years, membrane filtration systems have successfully been used in conventional water treatment systems. The use of an ultrafiltration system has proven effective in the treatment of particle contaminated process water. In 2012 an ultrafiltration system was designed, installed and commissioned for the treatment of particle contaminated backwash and transport water from the condensate polishing system in the Gundremmingen nuclear power plant, units B and C. Performance data surpass the client's requirements with respect to permeate quality, flow-rate and backwash behaviour. The technology applied has proven well. (orig.)

  5. WATER MICROPOLLUTANTS: CLASSIFICATION AND TREATMENT TECHNOLOGIES

    Directory of Open Access Journals (Sweden)

    Yolanda Patiño

    2014-06-01

    Full Text Available This article reviews the different kinds of emerging contaminants, their origin and use, and their presence in the Spanish waters, both in surface and groundwater. Micropollutants are compounds of different origin and chemical nature which had been unnoticed (due to their low concentration and don’t have specific regulation. They are divided into six major groups, and many of them behave as endocrine disruptors causing large negative effects on human health and environment. They are in waters because the waste water treatment plants are not designed for their removal, so they are being discharged. Different alternatives for their removal are discussed - physico- chemical, biological and hybrid treatment technologies -. Among the physicochemical process, the advance oxidation processes (AOPs are very promising.

  6. Particle separation options for emergency water treatment.

    Science.gov (United States)

    Dorea, C C; Bertrand, S; Clarke, B A

    2006-01-01

    Emergencies can result from the effects of unpredictable natural forces or from the cruelty of conflicts. The affected population is often left vulnerable to increased health risks. The victims' exposure to these risks can be reduced by timely public health interventions. Often, one of the first basic mitigations is the provision of water for essential needs. The quickest option, and generally more polluted, is of surface waters. We have reviewed particle separation options for emergency water treatment of surface waters. These vary from granular filtration package treatment facilities to ceramic candle filters and have therefore been broadly classified in three categories: modular, mobile and point-of-use (or household). The operational requirements and process limitations that can influence the choice of each option are discussed alongside with their underlying particle separation mechanisms and performance data.

  7. An overview on the advanced oxidation processes applied for the treatment of water pollutants defined in the recently launched Directive 2013/39/EU.

    Science.gov (United States)

    Ribeiro, Ana R; Nunes, Olga C; Pereira, Manuel F R; Silva, Adrián M T

    2015-02-01

    Environmental pollution is a recognized issue of major concern since a wide range of contaminants has been found in aquatic environment at ngL(-1) to μgL(-1) levels. In the year 2000, a strategy was defined to identify the priority substances concerning aquatic ecosystems, followed by the definition of environmental quality standards (EQS) in 2008. Recently it was launched the Directive 2013/39/EU that updates the water framework policy highlighting the need to develop new water treatment technologies to deal with such problem. This review summarizes the data published in the last decade regarding the application of advanced oxidation processes (AOPs) to treat priority compounds and certain other pollutants defined in this Directive, excluding the inorganic species (cadmium, lead, mercury, nickel and their derivatives). The Directive 2013/39/EU includes several pesticides (aldrin, dichlorodiphenyltrichloroethane, dicofol, dieldrin, endrin, endosulfan, isodrin, heptachlor, lindane, pentachlorophenol, chlorpyrifos, chlorfenvinphos, dichlorvos, atrazine, simazine, terbutryn, diuron, isoproturon, trifluralin, cypermethrin, alachlor), solvents (dichloromethane, dichloroethane, trichloromethane and carbon tetrachloride), perfluorooctane sulfonic acid and its derivatives (PFOS), polychlorinated biphenyls (PCBs), polycyclic aromatic hydrocarbons (PAHs), nonylphenol and octylphenol, as well as the three compounds included in the recommendation for the first watch list of substances (diclofenac, 17-alpha-ethinylestradiol (EE2) and 17-beta-estradiol (E2)). Some particular pesticides (aclonifen, bifenox, cybutryne, quinoxyfen), organotin compounds (tributyltin), dioxins and dioxin-like compounds, brominated diphenylethers, hexabromocyclododecanes and di(2-ethylhexyl)phthalate are also defined in this Directive, but studies dealing with AOPs are missing. AOPs are recognized tools to destroy recalcitrant compounds or, at least, to transform them into biodegradable species

  8. Rehabilitation Scheme and Water Purification Effect of Advanced Treatment Processes for Songjiang No.2 Water Treatment Plant%松江二水厂深度处理改造方案及净水效果

    Institute of Scientific and Technical Information of China (English)

    冯钧; 陶明; 徐建平

    2011-01-01

    In order to meet the new drinking water standards, the Songjiang No.2 Water Treatment Plant reconstructed the conventional horizontal-flow sedimentation basin into a short horizontal-flow sedimentation basin, an inclined-tube sedimentation basin and an up-flow GAC filter. To realize the goal of land and energy saving, an ozone-BAC advanced treatment system was designed and established. The effluent quality was improved.%为使出厂水达到新颁(GB 5749-2006)的要求,松江自来水公司二水厂将水平沉淀池改造为短水平沉淀池、斜管沉淀池及上向流活性炭滤池,利用两组沉淀池之间的空间安装臭氧设备.在节能、节地条件下,实现了臭氧生物活性炭水处理工艺,提高了出厂水水质.

  9. Components and Treatments of Oilfield Produced Water

    Directory of Open Access Journals (Sweden)

    Essam Abdul-Jalil Saeed

    2010-01-01

    Full Text Available In this study, a review of variety of processes that are used in the treatment produced water prior to reuse or to responsible disposal are presented with their environmental issues and economical benefits. Samples of produced water from five locations in Rumaila oilfield/in south of Iraq were taken and analyzed for their contents of brine, some heavy metals, total suspended solids and oil and grease. Moreover, two samples of water were treated using reverse osmosis technique which showed its ability to treat such contaminated water. The results showed that the environmental impact of produced water arises from its chemical composition; i.e., its salt content, its heavy metals, and hydrocarbon contents.

  10. A hybrid process of biofiltration of secondary effluent followed by ozonation and short soil aquifer treatment for water reuse.

    Science.gov (United States)

    Zucker, I; Mamane, H; Cikurel, H; Jekel, M; Hübner, U; Avisar, D

    2015-11-01

    The Shafdan reclamation project facility (Tel Aviv, Israel) practices soil aquifer treatment (SAT) of secondary effluent with hydraulic retention times (HRTs) of a few months to a year for unrestricted agricultural irrigation. During the SAT, the high oxygen demand (>40 mg L(-1)) of the infiltrated effluent causes anoxic conditions and mobilization of dissolved manganese from the soil. An additional emerging problem is the occurrence of persistent trace organic compounds (TrOCs) in reclaimed water that should be removed prior to reuse. An innovative hybrid process based on biofiltration, ozonation and short SAT with ∼22 d HRT is proposed for treatment of the Shafdan secondary effluent to overcome limitations of the existing system and to reduce the SAT's physical footprint. Besides efficient removal of particulate matter to minimize clogging, coagulation/flocculation and filtration (5-6 m h(-1)) operated with the addition of hydrogen peroxide as an oxygen source efficiently removed dissolved organic carbon (DOC, to 17-22%), ammonium and nitrite. This resulted in reduced effluent oxygen demand during infiltration and oxidant (ozone) demand during ozonation by 23 mg L(-1) and 1.5 mg L(-1), respectively. Ozonation (1.0-1.2 mg O3 mg DOC(-1)) efficiently reduced concentrations of persistent TrOCs and supplied sufficient dissolved oxygen (>30 mg L(-1)) for fully oxic operation of the short SAT with negligible Mn(2+) mobilization (process provided DOC reduction of 88% to a value of 1.2 mg L(-1), similar to conventional SAT, while improving the removal of TrOCs and efficiently preventing manganese dissolution. Copyright © 2015 Elsevier Ltd. All rights reserved.

  11. Optimization of Scheme Systems for Recirculated Cooling Water Treatment Processes Applied with Analytic Hierachy Process (AHP)%应用层次分析法(AHP)筛选循环冷却水处理优化方案

    Institute of Scientific and Technical Information of China (English)

    冯长春; 金杰; 朱康生; 高庆华; 陈康; 周国光

    2011-01-01

    该文提出根据循环冷却水的系统情况,运行成本及环境影响等构造层次分析法(AHP)的模型,建立判断矩阵,筛选最优水处理方案,供用户决策使用.AHP的最优水处理配方的筛选系统大大节约了筛选配方所花费的时间及人工费用,加强了水处理系统运行管理的成本控制,为用户提供有效决策管理.%On basis of circulating cooling water system, operation cost and environmental impact and so on, an analytic hierarchy process (AHP) model was constructed, which established judgment matrix and selected the optimal water treatment scheme for users to make decisions. The screening system based on AHP optimal water treatment formula greatly saved time and cost of screening formula, strengthened cost control of operation management, and provided users with effective decision-making management.

  12. Design of a fixed-bed ion-exchange process for the treatment of rinse waters generated in the galvanization process using Laminaria hyperborea as natural cation exchanger.

    Science.gov (United States)

    Mazur, Luciana P; Pozdniakova, Tatiana A; Mayer, Diego A; Boaventura, Rui A R; Vilar, Vítor J P

    2016-03-01

    In this study, the removal of zinc from galvanization wastewaters was performed in a fixed bed column packed with brown macro-algae Laminaria hyperborea, acting as a natural cation exchanger (resin). The rinse wastewater presents a zinc concentration between 9 and 22 mg/L, a high concentration of light metals (mainly Na and Ca), a high conductivity (0.5-1.5 mS/cm) and a low organic content (DOC = 7-15 mg C/L). The zinc speciation diagram showed that approximately 80% of zinc is in the form of Zn(2+) and ≅20% as ZnSO4, considering the effluent matrix. From all operational conditions tested for zinc uptake (17 treatment of 2.4 m(3)/day of galvanization wastewater, resulting in an estimated reactants cost of 2.44 €/m(3).

  13. Study and Application of Hydrolysis and Acidification Process in Waste Water Treatment of Pulp and Paper Industry%水解酸化在制浆造纸废水处理中的应用

    Institute of Scientific and Technical Information of China (English)

    晏令军; 蒋立人

    2011-01-01

    Because of low biodegradability of paper industry waste water, hydrolysis and acidification process is widely applied in paper industry waste water treatment.Aiming at different waste water from different material sources and processes, through experiment and analysis of the collected operation data, some engineering data and operating experiences for application of hydrolysis and acidification process in waste water treatment of pulp and paper industry are summarized.%针对不同原料不同工艺所产生制浆造纸废水的特点,通过对收集到的实验及实际运行数据的分析,总结出水解酸化工艺应用于制浆造纸废水处理中设计及运行管理的一些参数和经验.

  14. Treatment of oil sands process-affected water (OSPW) using a membrane bioreactor with a submerged flat-sheet ceramic microfiltration membrane.

    Science.gov (United States)

    Xue, Jinkai; Zhang, Yanyan; Liu, Yang; Gamal El-Din, Mohamed

    2016-01-01

    The release of oil sands process-affected water (OSPW) into the environment is a concern because it contains persistent organic pollutants that are toxic to aquatic life. A modified Ludzack-Ettinger membrane bioreactor (MLE-MBR) with a submerged ceramic membrane was continuously operated for 425 days to evaluate its feasibility on OSPW treatment. A stabilized biomass concentration of 3730 mg mixed liquor volatile suspended solids per litre and a naphthenic acid (NA) removal of 24.7% were observed in the reactor after 361 days of operation. Ultra Performance Liquid Chromatography/High Resolution Mass Spectrometry analysis revealed that the removal of individual NA species declined with increased ring numbers. Pyrosequencing analysis revealed that Betaproteobacteria were dominant in sludge samples from the MLE-MBR, with microorganisms such as Rhodocyclales and Sphingobacteriales capable of degrading hydrocarbon and aromatic compounds. During 425 days of continuous operation, no severe membrane fouling was observed as the transmembrane pressure (TMP) of the MLE-MBR never exceeded -20 kPa given that the manufacturer's suggested critical TMP for chemical cleaning is -35 kPa. Our results indicated that the proposed MLE-MBR has a good potential for removing recalcitrant organics in OSPW.

  15. Application of sludge-based carbonaceous materials in a hybrid water treatment process based on adsorption and catalytic wet air oxidation.

    Science.gov (United States)

    Julcour Lebigue, Carine; Andriantsiferana, Caroline; N'Guessan Krou; Ayral, Catherine; Mohamed, Elham; Wilhelm, Anne-Marie; Delmas, Henri; Le Coq, Laurence; Gerente, Claire; Smith, Karl M; Pullket, Suangusa; Fowler, Geoffrey D; Graham, Nigel J D

    2010-12-01

    This paper describes a preliminary evaluation of the performance of carbonaceous materials prepared from sewage sludges (SBCMs) in a hybrid water treatment process based on adsorption and catalytic wet air oxidation; phenol was used as the model pollutant. Three different sewage sludges were treated by either carbonisation or steam activation, and the physico-chemical properties of the resultant carbonaceous materials (e.g. hardness, BET surface area, ash and elemental content, surface chemistry) were evaluated and compared with a commercial reference activated carbon (PICA F22). The adsorption capacity for phenol of the SBCMs was greater than suggested by their BET surface area, but less than F22; a steam activated, dewatered raw sludge (SA_DRAW) had the greatest adsorption capacity of the SBCMs in the investigated range of concentrations (oxidation tests, the SBCMs demonstrated catalytic behaviour arising from their substrate adsorptivity and metal content. Recycling of SA_DRAW in successive oxidations led to significant structural attrition and a hardened SA_DRAW was evaluated, but found to be unsatisfactory during the oxidation step. In a combined adsorption-oxidation sequence, both the PICA carbon and a selected SBCM showed deterioration in phenol adsorption after oxidative regeneration, but a steady state performance was reached after 2 or 3 cycles.

  16. Research on variation of water quality chemical stability during the water treatment process%水质化学稳定性沿工艺流程变化研究

    Institute of Scientific and Technical Information of China (English)

    张庆; 梅红

    2012-01-01

    通过研究水质化学稳定性随水处理工艺流程的变化,探讨影响水质化学稳定性的因素.结果表明:水处理中碱度消耗工艺(混凝、生物活性炭和臭氧氧化工艺)均使水质化学稳定性下降.生物活性炭滤池运行初期生物膜未形成或尚不成熟时,对水质化学稳定性基本无影响,相反,初期活性炭表面金属溶出还可能改善水质化学稳定性.氯胺消毒基本不影响水质化学稳定性,投加NaClO可提高水质化学稳定性.混凝剂投加后增加水中无机阴离子(SO42-和Cl-),增加水体对管道的腐蚀倾向.%Through studying the variation of water quality chemical stability during the water treatment process, the factors influencing the water quality chemical stability were discussed. The results showed that: alkalinity consumption processes (coagulation, biological activated carbon and ozone oxidation) deteriorated the water quality chemical stability. There was almost no influence on water quality chemical stability when biofilm was not formed or not yet mature in the early operation period of biological activated carbon filter. On the contrary, the metal precipitation on the surface of the activated carbon happened in the initial stage might improve the water quality chemical stability. The water quality chemical stability was almost not influenced by chloramines disinfection, but was improved by adding NaClO. As coagulant dosing increased the concentration of the dissolved inorganic anions (SO24- and Cl-), the corrosion tendency of the iron pipe was also aggravated.

  17. Nanofiltration for water and wastewater treatment – a mini review

    Directory of Open Access Journals (Sweden)

    H. K. Shon

    2013-03-01

    Full Text Available The application of membrane technology in water and wastewater treatment is increasing due to stringent water quality standards. Nanofiltration (NF is one of the widely used membrane processes for water and wastewater treatment in addition to other applications such as desalination. NF has replaced reverse osmosis (RO membranes in many applications due to lower energy consumption and higher flux rates. This paper briefly reviews the application of NF for water and wastewater treatment including fundamentals of membrane process in general, mechanisms of NF process including few basic models. fouling challenges and their control mechanisms adopted.

  18. Water treatment: Chitosan associated with electrochemical methods

    Science.gov (United States)

    Tamiasso-Martinhon, Priscila; Marques Teixeira de Souza, João; Cruzeiro da Silva, Silvia Maria; Pellegrini Pessoa, Fernando Luiz; Sousa, Célia

    2017-04-01

    Pollution of water bodies due to the presence of toxic metals and organic compounds, bring out a series of environmental problems of public, government and social character. In addition, water pollution, has become the target and source of concern in many industrial sectors. Therefore, it is essential to develop technologies for treatment and purification of water. Chitosan is a natural product derived from chitin, extracted mainly from the shells of crustaceans. It is a low cost, renewable and biodegradable biopolymer of great socioeconomic and environmental importance. The classic treatment of wastewater containing metals involves physical chemistry processes of precipitation, ion exchange and electrochemistry. Electrochemical technology has been presented as the most promising methods for treating wastewater polluted with metals, colloids, dyes or oil in water emulsions; besides being used in removing organic compounds. Alternative methods like adsorption with biosorbents have been investigated. The great advantage of this latter over other techniques is the low generation of residues, easy recovery of metals and the possibility of reuse of the adsorbent. This article aimed to carry out an exploratory study, of bibliographical nature, on the use of chitosan in electrochemical methods for water treatment.

  19. Managing peatland vegetation for drinking water treatment

    Science.gov (United States)

    Ritson, Jonathan P.; Bell, Michael; Brazier, Richard E.; Grand-Clement, Emilie; Graham, Nigel J. D.; Freeman, Chris; Smith, David; Templeton, Michael R.; Clark, Joanna M.

    2016-11-01

    Peatland ecosystem services include drinking water provision, flood mitigation, habitat provision and carbon sequestration. Dissolved organic carbon (DOC) removal is a key treatment process for the supply of potable water downstream from peat-dominated catchments. A transition from peat-forming Sphagnum moss to vascular plants has been observed in peatlands degraded by (a) land management, (b) atmospheric deposition and (c) climate change. Here within we show that the presence of vascular plants with higher annual above-ground biomass production leads to a seasonal addition of labile plant material into the peatland ecosystem as litter recalcitrance is lower. The net effect will be a smaller litter carbon pool due to higher rates of decomposition, and a greater seasonal pattern of DOC flux. Conventional water treatment involving coagulation-flocculation-sedimentation may be impeded by vascular plant-derived DOC. It has been shown that vascular plant-derived DOC is more difficult to remove via these methods than DOC derived from Sphagnum, whilst also being less susceptible to microbial mineralisation before reaching the treatment works. These results provide evidence that practices aimed at re-establishing Sphagnum moss on degraded peatlands could reduce costs and improve efficacy at water treatment works, offering an alternative to ‘end-of-pipe’ solutions through management of ecosystem service provision.

  20. Influence of water quality on the embodied energy of drinking water treatment.

    Science.gov (United States)

    Santana, Mark V E; Zhang, Qiong; Mihelcic, James R

    2014-01-01

    Urban water treatment plants rely on energy intensive processes to provide safe, reliable water to users. Changes in influent water quality may alter the operation of a water treatment plant and its associated energy use or embodied energy. Therefore the objective of this study is to estimate the effect of influent water quality on the operational embodied energy of drinking water, using the city of Tampa, Florida as a case study. Water quality and water treatment data were obtained from the David L Tippin Water Treatment Facility (Tippin WTF). Life cycle energy analysis (LCEA) was conducted to calculate treatment chemical embodied energy values. Statistical methods including Pearson's correlation, linear regression, and relative importance were used to determine the influence of water quality on treatment plant operation and subsequently, embodied energy. Results showed that influent water quality was responsible for about 14.5% of the total operational embodied energy, mainly due to changes in treatment chemical dosages. The method used in this study can be applied to other urban drinking water contexts to determine if drinking water source quality control or modification of treatment processes will significantly minimize drinking water treatment embodied energy.

  1. Treatment of Oil & Gas Produced Water.

    Energy Technology Data Exchange (ETDEWEB)

    Dwyer, Brian P. [Sandia National Lab. (SNL-NM), Albuquerque, NM (United States)

    2016-02-01

    Production of oil and gas reserves in the New Mexico Four Corners Region results in large volumes of "produced water". The common method for handling the produced water from well production is re-injection in regulatory permitted salt water disposal wells. This is expensive (%7E $5/bbl.) and does not recycle water, an ever increasingly valuable commodity. Previously, Sandia National Laboratories and several NM small business tested pressure driven membrane-filtration techniques to remove the high TDS (total dissolved solids) from a Four Corners Coal Bed Methane produced water. Treatment effectiveness was less than optimal due to problems with pre-treatment. Inadequate pre-treatment allowed hydrocarbons, wax and biological growth to foul the membranes. Recently, an innovative pre-treatment scheme using ozone and hydrogen peroxide was pilot tested. Results showed complete removal of hydrocarbons and the majority of organic constituents from a gas well production water. ACKNOWLEDGEMENTS This report was made possible through funding from the New Mexico Small Business Administration (NMSBA) Program at Sandia National Laboratories. Special thanks to Juan Martinez and Genaro Montoya for guidance and support from project inception to completion. Also, special thanks to Frank McDonald, the small businesses team POC, for laying the ground work for the entire project; Teresa McCown, the gas well owner and very knowledgeable- fantastic site host; Lea and Tim Phillips for their tremendous knowledge and passion in the oil & gas industry.; and Frank Miller and Steve Addleman for providing a pilot scale version of their proprietary process to facilitate the pilot testing.

  2. Process for the biological purification of waste water

    DEFF Research Database (Denmark)

    1992-01-01

    Process for the biological purification of waste water by the activated sludge method, the waste water being mixed with recirculated sludge and being subjected to an anaerobic treatment, before the waste water thus treated is alternately subjected to anoxic and aerobic treatments and the waste...... water thus treated is led into a clarification zone for settling sludge, which sludge is recirculated in order to be mixed with the crude waste water. As a result, a simultaneous reduction of the content both of nitrogen and phosphorus of the waste water is achieved....

  3. Influence of main process variables on the treatment of waste waters using a new technology Mixer-Settler based on Phase Inversion (MSPI)

    Energy Technology Data Exchange (ETDEWEB)

    Moraes, N.A.; Paulo, J.B.A.; Medeiros, G.S. [Universidade Federal do Rio Grande do Norte (UFRN), Natal, RN (Brazil). Dept. de Engenharia Quimica], e-mail: norberto@eq.ufrn.br

    2011-04-15

    The prototype of a device on a semi-industrial scale to treat wastewaters from the oil industry has been widely studied as a viable alternative to conventional equipment. The device, called Mixer-Settler based on Phase Inversion (MSPI), uses the phase inversion method as operating principle. Using experimental planning (2{sup 4} factorial with four repetitions in the central point), it was determined the influence of the main variables on the oil/water separation process for waters containing between 30 and 100 mg of oil per liter of water. The following variables were evaluated: specific throughput, organic/aqueous phase ratio, agitation in the mixing chamber, and coconut oil concentration. The response variable was the oil/water separation efficiency. The results show that the separation efficiency of the device is a function of the effective throughput and the organic/aqueous phase ratio. (author)

  4. 臭氧-生物活性炭技术在水处理中的应用与研究%Study on the application of ozone-biological activated carbon process to water treatment

    Institute of Scientific and Technical Information of China (English)

    郭锋; 王潇; 肖强; 肖禾

    2011-01-01

    Ozone-biological activated carbon (O3-BAC) is a new type of efficient micro-polluted water treatment process. Its application to drinking water (surface water, ground water, domestic water, municipal water supply, etc. ) and industrial wastewater(membrane treatment discharge ,oilfield wastewater,oil refining wastewater, petrochemical wastewater, pharmaceutical wastewater, dyestuff wastewater, food processing wastewater, aquaculture wastewater, etc. ) and their research situations are introduced. The future development directions of the application of O3-BAC to water treatment are pointed out.%臭氧-生物活性炭(O-BAC)技术是一种新型高效的微污染水处理工艺.介绍了O-BAC技术在饮用水(地表水、地下水、生活污水、市政供水等制饮用水)及工业废水(膜处理排水、油田废水、炼油废水、石化废水、制药废水、焦化废水、印染废水、食品加工废水、水产养殖废水)等领域的应用和研究情况,指出了未来O-BAC技术在水处理中的发展研究方向.

  5. Process water - waste water - cooling water. Papers; Prozesswasser/Abwasser/Kuehlwasser. Vortraege

    Energy Technology Data Exchange (ETDEWEB)

    Liese, F. (comp.)

    2002-07-01

    The 39th Metallurgical Seminar focused on water. Modern technologies for water purification and treatment were presented, legal boundary conditions were discussed, and aspects of process water, waste water and cooling water were gone into. Although the boundaries between these three types of water cannot be clearly defined, materials recovery is the prevalent aspect in process water treatment while waste water treatment primarily aims at reducing pollutant concentrations so that both environmental aspects and technical quality standards will be met. This proceedings volume attempts to give its readers a more precise picture of the issues at hand by presenting fundamental research, ecological and legal specifications, and selected examples of industrial applications. [German] Das 39. Metallurgische Seminar beschaeftigt sich mit Wasser. Neben der Praesentation grundsaetzlicher, moderner Techniken zur Reinhaltung und Aufbereitung von Wasser sowie der Darstellung der gesetzlichen Rahmenbedingungen umspannen die Fachvortraege Beitraege zu den Themen Prozesswasser, Abwasser, Kuehlwasser. Wenn auch die Grenzen innerhalb dieser Begriffe teilweise fliessend sind, so zeichnen sich die Prozesswaesser dadurch aus, dass man primaer - wie beispielsweise bei Waschsloesungen und Beizwaessern - an der Wiedergewinnung der Inhaltsstoffe interessiert ist, waehrend bei reinen Abwaessern und Kuehlturmwaessern bzw. deren Abschlaemmungen die massgebliche Aufgabe darin besteht, die Konzentration der Inhaltsstoffe so weit abzusenken, dass man einerseits den Umwelterfordernissen und andererseits den technischen Qualitaetsanforderungen gerecht wird. Ziel dieses Bandes ist es, an Hand von Grundlagen, der Darstellung der oekologischen und behoerdlichen Erfordernisse sowie ausgewaehlter Fallbeispiele aus der Industrie den Leserkreis naeher an diese Thematik heranzufuehren. (orig.)

  6. Waste water reuse pathways for processing tomato

    DEFF Research Database (Denmark)

    Battilani, A; Plauborg, Finn; Andersen, Mathias Neumann

    to use the lowest irrigation water quality without harming nor food safety neither yield and fruit or derivatives quality. The EU project SAFIR aims help farmers solve problems with low quality water and decreased access to water. New water treatment devices (prototypes) are under development to allow...... a safe use of waste water produced by small communities/industries (≤2000 EI) or of treated water discharged in irrigation channels. Water treatment technologies are coupled with irrigation strategies and technologies to obtain a flexible, easy to use, integrated management....

  7. Technology for Water Treatment (National Water Management)

    Science.gov (United States)

    1992-01-01

    The buildup of scale and corrosion is the most costly maintenance problem in cooling tower operation. Jet Propulsion Laboratory successfully developed a non-chemical system that not only curbed scale and corrosion, but also offered advantages in water conservation, cost savings and the elimination of toxic chemical discharge. In the system, ozone is produced by an on-site generator and introduced to the cooling tower water. Organic impurities are oxidized, and the dissolved ozone removes bacteria and scale. National Water Management, a NASA licensee, has installed its ozone advantage systems at some 200 cooling towers. Customers have saved money and eliminated chemical storage and discharge.

  8. Hydraulic modelling of drinking water treatment plant operations

    NARCIS (Netherlands)

    Worm, G.I.M.; Mesman, G.A.M.; Van Schagen, K.M.; Borger, K.J.; Rietveld, L.C.

    2009-01-01

    The flow through a unit of a drinking water treatment plant is one of the most important parameters in terms of a unit's effectiveness. In the present paper, a new EPAnet library is presented with the typical hydraulic elements for drinking water treatment processes well abstraction, rapid sand filt

  9. Tratamento de águas contaminadas por diesel/biodiesel utilizando processo Fenton Treatment of water contaminated by diesel/biodiesel using Fenton process

    Directory of Open Access Journals (Sweden)

    Teofani Koslides Mitre

    2012-06-01

    Full Text Available A contaminação de águas por misturas diesel/biodiesel pode causar grandes impactos ambientais, relacionados à presença de compostos orgânicos recalcitrantes e tóxicos, inviabilizando o uso de processos biológicos de tratamento. A avaliação da biodegradabilidade, nas proporções B0, B25, B50, B75 e B100 (os números especificam o percentual em massa de biodiesel na mistura, indicou que a adição de biodiesel em teores acima de 50% aumenta a biodegradabilidade, alcançando 60 e 80% para B50 e B75, respectivamente. Na aplicação do processo Fenton, a remoção da matéria orgânica foi superior a 80% em todas as misturas, exceto para B0, que apresentou remoção máxima de 50%. A oxidação por Fenton se ajustou a um modelo cinético de pseudo-segunda ordem em relação à concentração de matéria orgânica, e resultou em aumento da biodegradabilidade de até 150%.Waters contaminated with diesel/biodiesel and their blends can cause major environmental impacts, due to the presence of toxic and recalcitrant organic compounds, which invalidate the use of biological treatment processes. Evaluation of biodegradability of the blends B0, B25, B50, B75 and B100 (the numbers specify the mass percentage of biodiesel in the blend indicated that the addition of biodiesel at concentrations above 50% increased biodegradation, reaching 60 and 80% for B50 and B75, respectively. When the Fenton process was used, removal of organic matter was greater than 80 % in all blends, except for B0, which showed maximum removal of 60%. Oxidation by Fenton was fitted with a pseudo-second order kinetic model in relation to the concentration of organic matter and resulted in increased biodegradation of up to 150%.

  10. INVESTIGATIONS ON SEWAGE TREATMENT PROCESS USING COMBINED BIO-OXIDIZERS

    Directory of Open Access Journals (Sweden)

    V. N. Jaromsky

    2010-01-01

    Full Text Available The paper presents results of investigations on process of aerobic waste water treatment with combined bio-oxidizers at milk processing enterprises. It has been shown that attached biocenosis, free-floating biocenosis and also bio-module rotation frequency  have exerted a significant influence on the process of an aerobic sewage treatment. It has been established that combined bio-oxidizers can be used for cleaning high concentrated waste water at the enterprises of food industry.

  11. INVESTIGATIONS ON SEWAGE TREATMENT PROCESS USING COMBINED BIO-OXIDIZERS

    OpenAIRE

    V. N. Jaromsky; E. I. Mihnevich

    2010-01-01

    The paper presents results of investigations on process of aerobic waste water treatment with combined bio-oxidizers at milk processing enterprises. It has been shown that attached biocenosis, free-floating biocenosis and also bio-module rotation frequency  have exerted a significant influence on the process of an aerobic sewage treatment. It has been established that combined bio-oxidizers can be used for cleaning high concentrated waste water at the enterprises of food industry.

  12. Water Treatment Systems for Long Spaceflights

    Science.gov (United States)

    FLynn, Michael T.

    2012-01-01

    Space exploration will require new life support systems to support the crew on journeys lasting from a few days to several weeks, or longer. These systems should also be designed to reduce the mass required to keep humans alive in space. Water accounts for about 80 percent of the daily mass intake required to keep a person alive. As a result, recycling water offers a high return on investment for space life support. Water recycling can also increase mission safety by providing an emergency supply of drinking water, where another supply is exhausted or contaminated. These technologies also increase safety by providing a lightweight backup to stored supplies, and they allow astronauts to meet daily drinking water requirements by recycling the water contained in their own urine. They also convert urine into concentrated brine that is biologically stable and nonthreatening, and can be safely stored onboard. This approach eliminates the need to have a dedicated vent to dump urine overboard. These needs are met by a system that provides a contaminant treatment pouch, referred to as a urine cell or contaminant cell, that converts urine or another liquid containing contaminants into a fortified drink, engineered to meet human hydration, electrolyte, and caloric requirements, using a variant of forward osmosis (FO) to draw water from a urine container into the concentrated fortified drink as part of a recycling stage. An activated carbon pretreatment removes most organic molecules. Salinity of the initial liquid mix (urine plus other) is synergistically used to enhance the precipitation of organic molecules so that activated carbon can remove most of the organics. A functional osmotic bag is then used to remove inorganic contaminants. If a contaminant is processed for which the saline content is different than optimal for precipitating organic molecules, the saline content of the liquid should be adjusted toward the optimal value for that contaminant. A first urine

  13. 不同再生水处理工艺出水水质回用途径适应性分析%Analysis about reuse approach adaptability for effluent quality from different reclaimed water treatment processes

    Institute of Scientific and Technical Information of China (English)

    张庆康; 郝瑞霞; 刘峰; 赵继成; 杨英杰

    2013-01-01

    为分析典型再生水处理工艺出水的回用途径适应性,采用标准指数法评价了4座不同处理工艺的再生水厂出水质量,为再生水处理工艺选择和安全回用提供参考.结果表明,4种再生水处理工艺出水用于市政杂用水时基本是安全的;除反渗透(RO)工艺外,其他工艺出水回用于景观环境用水时都存在氮磷指标超标问题;膜处理工艺的出水可以满足工业用水标准,但是常规絮凝过滤工艺出水用作工业用水应注意氮磷等指标的进一步处理;各种再生水处理工艺出水质量均不能满足地下水回灌用水标准,主要是氨氮和环境激素DBP超标问题,用作地下水回灌用水时存在一定的环境风险.%The treated effluent quality of four different technologies types of reclaimed water treatment plants was evaluated with the standard index method in order to analyze the adaptability of the reuse approaches of treated effluents from typical reclaimed water treatment processes. This study could be a valuable reference to the selection of reclaimed water treatment processes and the security of reuse. The results of the study indicated that the reclaimed water treated by the four types of the treatment processes was basically safe to be used for municipal water usage. However, they all have different problems with meeting the relevant standards on certain kinds of water utilisation. The reclaimed waters treated by the treatment processes, except treated by RO process, all have problems with their nitrogen and phosphorus concentration exceeding the scandalised concentration in the case of being used for landscape purpose. The effluent water treated by membrane process could meet the requirements of the standard on industrial water usage. The reclaimed water treated by conventional floccula-tion filtration process requires further treatment on nitrogen and phosphorus removal. According to the water quality standard for recharging ground

  14. Mobil pilot unit of the advanced oxidation process for waste water treatment and reuse of the hydrics effluents; Unidade piloto movel de processo oxidativo avancado aplicado a tratamento e reuso de efluentes hidricos

    Energy Technology Data Exchange (ETDEWEB)

    Geraldo, Lucia Maria Limoeiro; Pereira Junior, Oswaldo de Aquino; Henriques, Sheyla de Oliveira Carvalho; Jacinto Junior, Agenor [PETROBRAS, Rio de Janeiro, RJ (Brazil)

    2004-07-01

    The chemical oxidation processes which generate free hydroxyl radicals are called Advanced Oxidation Process (AOP). These processes have been studied, in the last decades, as a new alternative for pollutants degradation. In the (AOP)'s there are in situ formation of hydroxyl radicals (OH{center_dot}), which are highly oxidant. Its high oxidation strength becomes it indicated in the treatment of effluent with highly refractory contaminants. It can be used as a partial treatment (taking the effluent to more degradable compounds), as a final treatment (taking the effluent to complete mineralization) or as a complementary treatment to other processes, allowing, for example, its reuse. The applicability of this technology in oily water effluents in all segments of the oil industry, has taken to the development, in the LARA (Laboratory of Treatment and Reuse of Waters - CENPES), of the Advanced Oxidation Process Mobile Pilot Unit (AOP's- MU) with capacity up to 1 m3/h. The (AOP's- MU) are able to produce hydroxyl radical from Fenton's reaction, titanium dioxide heterogeneous photo catalysis and hydrogen peroxide, photo-radiated or not. It is equipped with ultraviolet reactors of different wave lengths and power. (author)

  15. 居家桥水厂自动加氯工艺优化%Optimization of Technological Process of Automatic Chlorination Dosing System in Jujiaqiao Water Treatment Plant

    Institute of Scientific and Technical Information of China (English)

    陈志平; 胡介明

    2013-01-01

    自动加氯数学模型与加氯消毒理论相结合,对原有自动加氯工艺进行优化设计,改进国内加氯消毒控制模式,以出厂水余氯(一氯胺)目标值来自动控制整个工艺过程的加氯、加氨量;以滤后一氯胺和游离氨作为工艺控制参数,来监控出厂水的总氯和总氨值,使加氯和加氨量达到最小化,降低药耗,减少消毒副产物.%Optimization of the original automatic chlorination disinfection process was earned out by combining the mathematical model of the automatic chlorination with chlorination theory. The entire disinfection process of chlorine and ammonia dosing was automatically controlled by the target value of finished water residual chlorine (monochloramine). The total chlorine and total ammonia of the finished water were monitored by the filtered water monochloramine and free ammonia as process control parameter. As a result, chlorine and ammonia dosage were minimized, the chemical consumption and the disinfection by-products were reduced.

  16. 人工甜味剂在污水处理厂和自来水厂的归趋%Fate of Artificial Sweeteners in Waste Water and Drinking Water Treatment Processes

    Institute of Scientific and Technical Information of China (English)

    干志伟; 孙红文; 冯碧婷

    2012-01-01

    研究了7种常用的人工甜味剂[安赛蜜、三氯蔗糖、糖精、甜蜜素、纽甜、阿斯巴甜和NHDC(新橙皮苷二氢查耳酮)]在污水处理厂及自来水厂的分布.7种人工甜味剂在污水处理厂进水中均被检出,质量浓度为6.4 ~ 31 671.0 ng/L.安赛蜜、三氯蔗糖、糖精、甜蜜素在污水处理厂的出水中被检出,质量浓度为32.4 ~ 11 204.0 ng/L.这些甜味剂将随污水处理厂的出水排放而进入水环境.安赛蜜、三氯蔗糖、糖精、甜蜜素、纽甜在自来水厂进水中被检出,质量浓度为低于定量限~579.4 ng/L,其中前4种在自来水中被检出,质量浓度为23.3 ~504.2 ng/L.沉淀、絮凝、氯化消毒作用对人工甜味剂没有明显的去除作用.生物降解能有效去除糖精、甜蜜素、阿斯巴甜、纽甜和NHDC,但对安赛蜜和三氯蔗糖去除率不高,去除率均小于20%.%The occurrence and removal of seven commonly used artificial sweeteners, including acesulfame, sucralose, saccharin, cyclamate, neotame, aspartame and neohesperidin dihydrochalcone (NHDC) in waste water treatment processes ( WWTP) and drinking water treatment processes (DWTP) were assessed. All of the seven investigated artificial sweeteners were detected in the influent of WWTP, with concentrations ranging from 6. 4-31 ,671. 0 ng/L. The first four artificial sweeteners ( acesulfame, sucralose, saccharin and cyclamate) were detected in the effluent, with concentrations ranging from 32. 4-11 ,204. 0 ng/L. They might be a contaminant source for surface water. Acesulfame, sucralose, saccharin, cyclamate and neotame were found in the source water of DWTP, with concentrations between < LOQ and 579.4 ng/L. The first four artificial sweeteners were detected in drinking water, with concentrations ranging from 23.3-504.2 ng/L. The sedimentation, flocculation and chlorination in DWTP could not significantly remove the investigated artificial sweeteners. Compared with the other five

  17. Water surface capturing by image processing

    Science.gov (United States)

    An alternative means of measuring the water surface interface during laboratory experiments is processing a series of sequentially captured images. Image processing can provide a continuous, non-intrusive record of the water surface profile whose accuracy is not dependent on water depth. More trad...

  18. Water Treatment Technology - General Plant Operation.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on general plant operations provides instructional materials for seven competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: water supply regulations, water plant…

  19. Supercritical water oxidation treatment of textile sludge.

    Science.gov (United States)

    Zhang, Jie; Wang, Shuzhong; Li, Yanhui; Lu, Jinling; Chen, Senlin; Luo, XingQi

    2016-10-17

    In this work, we studied the supercritical water oxidation (SCWO) of the textile sludge, the hydrothermal conversion of typical textile compounds and the corrosion properties of stainless steel 316. Moreover, the influence mechanisms of NaOH during these related processes were explored. The results show that decomposition efficiency for organic matter in liquid phase of the textile sludge was improved with the increment of reaction temperature or oxidation coefficient. However, the organic substance in solid phase can be oxidized completely in supercritical water. Serious coking occurred during the high pressure water at 250-450°C for the Reactive Orange 7, while at 300 and 350°C for the polyvinyl alcohol. The addition of NaOH not only accelerated the destruction of organic contaminants in the SCWO reactor, but effectively inhibited the dehydration conversion of textile compounds during the preheating process, which was favorable for the treatment system of textile sludge. The corrosion experiment results indicate that the stainless steel 316 could be competent for the body materials of the reactor and the heat exchangers. Furthermore, there was prominent enhancement of sodium hydroxide for the corrosion resistance of 316 in subcritical water. On the contrary the effect was almost none during SCWO.

  20. A case study for orphaned chemicals: 4-methylcyclohexanemethanol (MCHM) and propylene glycol phenyl ether (PPH) in riverine sediment and water treatment processes.

    Science.gov (United States)

    Weidhaas, Jennifer; Lin, Lian-Shin; Buzby, Karen

    2017-01-01

    There are an estimated 30,000 chemicals in commerce used in quantities >1016kg per year in the US. Unfortunately there is limited information on the chemicals partitioning and reactivity properties. These orphaned or understudied chemicals are viewed as non-hazardous but can still pose serious economic, health, environmental and societal impacts as evidenced by the January 2014 spill of 37,900L of crude-MCHM (primarily 4-methylcyclohexanemethanol) and stripped-PPH (primarily dipropylene glycol phenyl ether and propylene glycol phenyl ether) into the Elk River near Charleston, WV. Using the Elk River spill as a case study of orphaned or understudied chemicals, experiments were undertaken to evaluate the adequacy of standard approaches to emergency drinking water treatment (oxidation and sorption to activated carbons). Further available sorption models for estimating the potential of these compounds to sorb to Elk River sediments and to activated carbons in drinking water systems were investigated. The results showed that powdered activated carbon (PAC) was the most effective sorbent. The trans-MCHM isomer was found to preferentially sorb compared to cis-MCHM. For MCHM concentrations ranging from 2 to 5mgL(-1) in the treatment plant, PAC concentrations of 0.1-1.4mgL(-1) would be required to lower both MCHM isomers to the CDC screening level. In most cases, published linear solvation energy relationships and quantitative structure activity relationships were inadequate to estimate the a priori likelihood of sorption of MCHM and PPH to sediments and GAC, but did fit the PAC results well. Permanganate and chlorine oxidation of the compounds showed limited to insignificant removal. The studies presented herein suggest that there are still inherent vulnerabilities to drinking water treatment systems that need to be addressed.

  1. Heuristic analysis of brackishwater treatment by reverse osmosis process

    OpenAIRE

    Ahmed, S

    1990-01-01

    Treatment of brackish water and sea water with the help of reverse osmosis process is feasible and a viable solution to meet the fresh water deficiency in an arid region. Total dissolved solids can be reduced to a level acceptable for drinking water. High purity water for industrial uses can also be obtained with the application of the RO process. Useful materials may also be recovered from the reject water. RO plants of various sizes (both large and small) have been in operation successfully...

  2. Effects of Suspended Particles in Water of Terkuza River on Drinking Water Treatments

    OpenAIRE

    , A. Shkurti; , I. Beqiraj; , M. Kodra

    2016-01-01

    The content of suspended matter in Tercuza water has varied significantly during the study period 2004-2010, depending on atmosphere conditions, especially during winter, when values up to 1000 NTU were occurred, consequently worsening the process of turbidity removal. In Tirana’s water supply plant is required a special water treatment process in order to meet the drinking water standard parameters. The pre hydrolysed poly-aluminium chloride sulphate (PACS) was used as coagulant in Jar tests...

  3. Water Reuse in Industrial food Processing

    African Journals Online (AJOL)

    subject of responsible care for the environment, water reuse is increasingly regarded as a tool for ... In this paper some hints are given for implementing water reuse in the food processing industry, ... The problem of rational use of industrial.

  4. Ionomer-Membrane Water Processing Apparatus

    Science.gov (United States)

    MacCallum, Taber K. (Inventor); Kelsey, Laura Katrina (Inventor)

    2017-01-01

    This disclosure provides water processing apparatuses, systems, and methods for recovering water from wastewater such as urine. The water processing apparatuses, systems, and methods can utilize membrane technology for extracting purified water in a single step. A containment unit can include an ionomer membrane, such as Nafion.RTM., over a hydrophobic microporous membrane, such as polytetrafluoroethylene (PTFE). The containment unit can be filled with wastewater, and the hydrophobic microporous membrane can be impermeable to liquids and solids of the wastewater but permeable to gases and vapors of the wastewater, and the ionomer membrane can be permeable to water vapor but impermeable to one or more contaminants of the gases and vapors. The containment unit can be exposed to a dry purge gas to maintain a water vapor partial pressure differential to drive permeation of the water vapor, and the water vapor can be collected and processed into potable water.

  5. Ionomer-Membrane Water Processing Apparatus

    Science.gov (United States)

    MacCallum, Taber K. (Inventor); Kelsey, Laura (Inventor)

    2016-01-01

    This disclosure provides water processing apparatuses, systems, and methods for recovering water from wastewater such as urine. The water processing apparatuses, systems, and methods can utilize membrane technology for extracting purified water in a single step. A containment unit can include an ionomer membrane, such as Nafion(Registered Trademark), over a hydrophobic microporous membrane, such as polytetrafluoroethylene (PTFE). The containment unit can be filled with wastewater, and the hydrophobic microporous membrane can be impermeable to liquids and solids of the wastewater but permeable to gases and vapors of the wastewater, and the ionomer membrane can be permeable to water vapor but impermeable to one or more contaminants of the gases and vapors. The containment unit can be exposed to a dry purge gas to maintain a water vapor partial pressure differential to drive permeation of the water vapor, and the water vapor can be collected and processed into potable water.

  6. Artificial Intelligence Based Alum Dosage Control in Water Treatment Plant

    Directory of Open Access Journals (Sweden)

    P Poongodi

    2013-08-01

    Full Text Available Supplying good quality of drinking water is a challenging task during the rainy season and floods. During this period water becomes highly polluted with suspended solids which increase the water turbidity. Alum is used to reduce the turbidity of the water. Typically in water treatment plants alum dosage is decided by the Jar test and the desired alum dosage is added manually. This research proposes an automatic alum dosage mixing process. The alum dosage is controlled by an intelligent controller which consists of a dosage predictor, an inverse model of the dosage pump and a Pulse Width Modulation (PWM controller. The optimal alum dosage is predicted by the dosage predictor. The PWM controller controls the flow rate of the alum dosing pump. This proposed method has been implemented in a laboratory based water treatment plant and it ensures the automation in water treatment plant to supply good quality drinking water.

  7. Membrane-based processes for sustainable power generation using water

    KAUST Repository

    Logan, Bruce E.

    2012-08-15

    Water has always been crucial to combustion and hydroelectric processes, but it could become the source of power in membrane-based systems that capture energy from natural and waste waters. Two processes are emerging as sustainable methods for capturing energy from sea water: pressure-retarded osmosis and reverse electrodialysis. These processes can also capture energy from waste heat by generating artificial salinity gradients using synthetic solutions, such as thermolytic salts. A further source of energy comes from organic matter in waste waters, which can be harnessed using microbial fuel-cell technology, allowing both wastewater treatment and power production. © 2012 Macmillan Publishers Limited. All rights reserved.

  8. Nanofiltration for water and wastewater treatment – a mini review

    Directory of Open Access Journals (Sweden)

    H. K. Shon

    2013-06-01

    Full Text Available The application of membrane technology in water and wastewater treatment is increasing due to stringent water quality standards. Nanofiltration (NF is one of the widely used membrane processes for water and wastewater treatment in addition to other applications such as desalination. NF has replaced reverse osmosis (RO membranes in many applications due to lower energy consumption and higher flux rates. This paper briefly reviews the application of NF for water and wastewater treatment including fundamentals, mechanisms, fouling challenges and their controls.

  9. Crow Nation Water Treatment Plant NPDES Permit

    Science.gov (United States)

    Under NPDES permit MT-0030538, the U.S. Bureau of Indian Affairs is authorized to discharge from the Crow Agency water treatment plants via the wastewater treatment facility located in Bighorn County, Montana to the Little Bighorn River.

  10. Impact of diatomite on the slightly polluted algae-containing raw water treatment process using ozone oxidation coupled with polyaluminum chloride coagulation.

    Science.gov (United States)

    Hu, Wenchao; Wu, Chunde; Jia, Aiyin; Zhang, Zhilin; Chen, Fang

    2014-01-01

    The impact of adding diatomite on the treatment performance of slightly polluted algae-containing raw water using ozone pre-oxidation and polyaluminum chloride (PAC) coagulation was investigated. Results demonstrated that the addition of diatomite is advantageous due to reduction of the PAC dose (58.33%) and improvement of the removal efficiency of algae, turbidity, and dissolved organic matter (DOM) in raw water. When the ozone concentration was 1.0 mg L⁻¹ and the PAC dosage was 2.5 mg L⁻¹, the removal rates of algae, turbidity, UV254, and TOC were improved by 6.39%, 7.06%, 6.76%, and 4.03%, respectively, with the addition of 0.4 g L⁻¹ diatomite. It has been found that the DOM presented in the Pearl River raw water mainly consisted of small molecules ( 50 kDa). After adding diatomite (0.4 g L⁻¹), the additional removal of 5.77% TOC and 14.82% UV254 for small molecules (50 kDa) could be achieved, respectively, at an ozone concentration of 1.0 mg L⁻¹ and a PAC dose of 2.5 mg L⁻¹. The growth of anabaena flos-aquae (A.F.) was observed by an atomic force microscope (AFM) before and after adding diatomite. AFM images demonstrate that diatomite may have a certain adsorption on A.F.

  11. Sustainable treatment of municipal waste water

    DEFF Research Database (Denmark)

    Hansen, Peter Augusto; Larsen, Henrik Fred

    treatment technologies are to be assessed. This paper will present the first LCA results from running existing life cycle impact assessment (LCIA) methodology on some of the waste water treatment technologies. Keywords: Sustainability, LCA, micropollutants, waste water treatment technologies.......The main goal of the EU FP6 NEPTUNE program is to develop new and improve existing waste water treatment technologies (WWTT) and sludge handling technologies for municipal waste water, in accordance with the concepts behind the EU Water Framework Directive. As part of this work, the project.......e. heavy metals, pharmaceuticals and endocrine disruptors) in the waste water. As a novel approach, the potential ecotoxicity and human toxicity impacts from a high number of micropollutants and the potential impacts from pathogens will be included. In total, more that 20 different waste water and sludge...

  12. Waste water reuse pathways for processing tomato

    DEFF Research Database (Denmark)

    Battilani, A; Plauborg, Finn; Andersen, Mathias Neumann

    to use the lowest irrigation water quality without harming nor food safety neither yield and fruit or derivatives quality. The EU project SAFIR aims help farmers solve problems with low quality water and decreased access to water. New water treatment devices (prototypes) are under development to allow......  Direct or indirect water reuse involves several aspects: contamination by faecal, inorganic and xenobiotic pollutants; high levels of suspended solids and salinity; rational use of the dissolved nutrients (particularly nitrogen). The challenge is apply new strategies and technologies which allows...... a safe use of waste water produced by small communities/industries (≤2000 EI) or of treated water discharged in irrigation channels. Water treatment technologies are coupled with irrigation strategies and technologies to obtain a flexible, easy to use, integrated management....

  13. Monitoring and controlling the biological purification process in a waste water treatment plant using a respirometry analyser; Vigilancia y control del proceso de la depuracion biologica en una EDAR por medio de un analizador de respirometria

    Energy Technology Data Exchange (ETDEWEB)

    Serrano, J. E.

    2004-07-01

    In a waste water biological treatment, we have to take into account that the activated sludge is a living and breathing process, and a lack of bioactivity information might cause serious confusion about control criteria on the biological reactor. For this reason, to get bioactivity information in a timely manner through the respiration analysis would be a real breakthrough in better process control. Therefore, to identify the respiration rates and calculate their derived parameters represents the guidelines of respirometry and can be considered as the most sensitive variables on the basis of which activated sludge process theory can be validated. (Author)

  14. Removal of heavy metal ions from oil shale beneficiation process water by ferrite process

    Energy Technology Data Exchange (ETDEWEB)

    Mehta, R.K.; Zhang, L.; Lamont, W.E.; Schultz, C.W. [Alabama Univ., University, AL (United States). Mineral Resources Inst.

    1991-12-31

    The ferrite process is an established technique for removing heavy metals from waste water. Because the process water resulting from oil shale beneficiation falls into the category of industrial waste water, it is anticipated that this process may turn out to be a potential viable treatment for oil shale beneficiation process water containing many heave metal ions. The process is chemoremedial because not only effluent water comply with quality standards, but harmful heavy metals are converted into a valuable, chemically stable by-product known as ferrite. These spinel ferrites have magnetic properties, and therefore can be use in applications such as magnetic marker, ferrofluid, microwave absorbing and scavenging material. Experimental results from this process are presented along with results of treatment technique such as sulfide precipitation.

  15. Removal of heavy metal ions from oil shale beneficiation process water by ferrite process

    Energy Technology Data Exchange (ETDEWEB)

    Mehta, R.K.; Zhang, L.; Lamont, W.E.; Schultz, C.W. (Alabama Univ., University, AL (United States). Mineral Resources Inst.)

    1991-01-01

    The ferrite process is an established technique for removing heavy metals from waste water. Because the process water resulting from oil shale beneficiation falls into the category of industrial waste water, it is anticipated that this process may turn out to be a potential viable treatment for oil shale beneficiation process water containing many heave metal ions. The process is chemoremedial because not only effluent water comply with quality standards, but harmful heavy metals are converted into a valuable, chemically stable by-product known as ferrite. These spinel ferrites have magnetic properties, and therefore can be use in applications such as magnetic marker, ferrofluid, microwave absorbing and scavenging material. Experimental results from this process are presented along with results of treatment technique such as sulfide precipitation.

  16. An alternative process to treat boiler feed water for reuse.

    Science.gov (United States)

    Guirgis, Adel; Ghosh, Jyoti P; Achari, Gopal; Langford, Cooper H; Banerjee, Daliya

    2012-09-01

    A bench-scale process to treat boiler feed water for reuse in steam generation was developed. Industrial water samples from a steam-assisted gravity drainage plant in northern Alberta, Canada, were obtained and samples characterized. The technology, which consists of coagulation-settling to remove oil/grease and particulates followed by an advanced oxidative treatment, led to clean water samples with negligible organic carbon. Coagulation followed by settling removed most particulates and some insoluble organics. The advanced oxidative treatment removed any remaining color in the samples, decreased the organic content to near-zero, and provided water ready for reuse.

  17. Model-Based Control of Drinking-Water Treatment Plants

    NARCIS (Netherlands)

    Van Schagen, K.M.

    2009-01-01

    The drinking water in the Netherlands is of high quality and the production cost is low. This is the result of extensive research in the past decades to innovate and optimise the treatment processes. The processes are monitored and operated by motivated and skilled operators and process technologist

  18. Waste water treatment technology for aggregate processing and concrete production of Xiangjiaba Hydropower Station%向家坝电站砂石加工及混凝土生产废水处理技术

    Institute of Scientific and Technical Information of China (English)

    徐翔

    2015-01-01

    砂石加工及混凝土生产系统所产生的废水是水电站施工中废水排放的主要来源。传统的废水处理工艺存在着占用场地面积大、沉淀池排泥困难、污泥脱水能力不足或循环时间长等问题。向家坝工程砂石加工的废水处理系统设计结合当地条件采用水库型沉淀池,解决了传统废水处理工艺带来的难题。详细介绍了该废水处理系统的生产工况、主要参数、经济效益及改进方向等。向家坝水电站废水处理技术的应用与探索,为水电站施工废水处理实现“零排放”目标拓展了新的思路。%The waste water from aggregate processing and concrete production system is the main sources of the waste water in hydropower station construction .The problems of large land occupation , difficult sludge discharge of settling pool , insufficient sludge dewatering capacity and long circular period etc .trouble the traditional waste water treatment .According to local condi-tion, the reservoir-type settling pool was adopted for the waster water treatment system , which successfully solved the above dif-ficulties.The detail production situation , main parameters , economic benefit and improvement direction etc .of the waste water treatment system are introduced .The application and exploration of waste water treatment technology provides a new thought for realizing "zero release"of waste water .

  19. Fazenda Belem (PETROBRAS, UN-RNCE) produced water treatment using membrane processes; Tratamento da agua produzida do Campo de Fazenda Belem (PETROBRAS, UN-RNCE) utilizando processos de separacao por membranas

    Energy Technology Data Exchange (ETDEWEB)

    Louvisse, Ana Maria Travalloni; Melo, Marcel Vasconcelos; Pereira Junior, Oswaldo A. [PETROBRAS S.A., Rio de Janeiro, RJ (Brazil). Centro de Pesquisas (CENPES); Schulz, Cintia K. [Fundacao Gorceix, Ouro Preto, MG (Brazil)

    2008-07-01

    The aim of this paper is to evaluate the possibility to reuse the produced water at FZB/UN-RNCE. Therefore, the used processes is reverse osmosis, but the feed water for this processes must shows specific parameters, wi ch are not remove with the existing processes in wastewater treatment system at FZB. A microfiltration pilot scale unit with 8m{sup 3}/h treatment capacity has been installed, to improve the quality of produced water to feed the reverse osmosis. The wastewater used were water/oil separator and sand filters (pH = 7,0 and 10,0). The permeate flux, and oil phase and total suspended solids removal were evaluated. Under controlled operational conditions, the best system performance in terms of permeate flux and solids removal was verified when it was fed with sand filters wastewater (pH=10,0). The pH change influences the particle size and probably its removal efficiency. During the tests it was observed an oil removal around 85%, in some cases, showing that a second microfiltration is required for the total oil removal achievement. (author)

  20. Household Water Treatments in Developing Countries

    Science.gov (United States)

    Smieja, Joanne A.

    2011-01-01

    Household water treatments (HWT) can help provide clean water to millions of people worldwide who do not have access to safe water. This article describes four common HWT used in developing countries and the pertinent chemistry involved. The intent of this article is to inform both high school and college chemical educators and chemistry students…

  1. Off shore produced water treatment with pertraction

    NARCIS (Netherlands)

    Klaassen, R.

    2004-01-01

    During the production of oil and gas also water is produced. This produced water contains dispersed and dissolved oil components. The impact of offshore emissions of produced water on the environment and the treatment of technologies for it are currently under discussion. Emission limits tend to bec

  2. Household Water Treatments in Developing Countries

    Science.gov (United States)

    Smieja, Joanne A.

    2011-01-01

    Household water treatments (HWT) can help provide clean water to millions of people worldwide who do not have access to safe water. This article describes four common HWT used in developing countries and the pertinent chemistry involved. The intent of this article is to inform both high school and college chemical educators and chemistry students…

  3. Water retention in mushroom during sustainable processing

    NARCIS (Netherlands)

    Paudel, E.

    2015-01-01

    This thesis deals with the understanding of the water holding capacity of mushroom, in the context of a redesign of their industrial processing. For designing food process the retention of food quality is of the utmost importance. Water holding capacity is an important quality aspect of mushrooms. A

  4. Water retention in mushroom during sustainable processing

    NARCIS (Netherlands)

    Paudel, E.

    2015-01-01

    This thesis deals with the understanding of the water holding capacity of mushroom, in the context of a redesign of their industrial processing. For designing food process the retention of food quality is of the utmost importance. Water holding capacity is an important quality aspect of mushrooms. A

  5. Washing water treatment process for UF{sub 6} cylinder by adjusting evaporation technology in a low temperature and low pressure

    Energy Technology Data Exchange (ETDEWEB)

    Kim, Ki-tae; Ju, Young-jong; Cho, Nam-chan [KEPCO Nuclear Fuel Co., Daejeon (Korea, Republic of); Kim, Yun-kwan; Jin, Chang-suk [Jeontech CO., Suwon (Korea, Republic of)

    2016-10-15

    The liquid waste is treated in this procedure; 1) Add NaOH to the liquid waste and filter the mixture with a screen. 2) Screened residue is dried and then stored in a uranium storage. 3) liquid part is moved to a storage tank and radioactivity is measured in the liquid. 5) If the concentration of radioactivity is lower than corresponding regulation limit, the liquid moved to a reaction tank and evaporated with additional low concentration HF in 105℃. 6) Radioactivity of distillate is measured and the value is lower than regulation, it is treated with a thermal decomposition process and discharged to the atmosphere in gas state. 7) Solid waste produced in the evaporation step is managed as solid nuclear waste. The treatment procedure mentioned above has disadvantageous points, producing large amount of solid waste as well as, high energy and chemical consumption. In this study, liquid waste from a real scaled cylinder wash process is applied to evaporation system to confirm feasibility of the application of evaporation and, to reduce waste production and energy consumption. Liquid radioactive wastewater from a real scaled UF6 cylinder wash process was applied to evaporation treatment system. Radioactive concentration in gross alpha was removed 99.9% in the evaporation system. And the concentration in distillate was lower than the discharge regulation. Removal of U-235 was 99.9% in the process. And 15 other kinds of radionuclides in the raw wastewater were removed completely. Secondary waste production of the evaporation system is 15g/L.

  6. Waste Water Management and Infectious Disease. Part II: Impact of Waste Water Treatment

    Science.gov (United States)

    Cooper, Robert C.

    1975-01-01

    The ability of various treatment processes, such as oxidation ponds, chemical coagulation and filtration, and the soil mantle, to remove the agents of infectious disease found in waste water is discussed. The literature concerning the efficiency of removal of these organisms by various treatment processes is reviewed. (BT)

  7. Waste Water Management and Infectious Disease. Part II: Impact of Waste Water Treatment

    Science.gov (United States)

    Cooper, Robert C.

    1975-01-01

    The ability of various treatment processes, such as oxidation ponds, chemical coagulation and filtration, and the soil mantle, to remove the agents of infectious disease found in waste water is discussed. The literature concerning the efficiency of removal of these organisms by various treatment processes is reviewed. (BT)

  8. Advanced water treatment as a tool in water scarcity management

    DEFF Research Database (Denmark)

    Harremoes, Poul

    2000-01-01

    until recently. This paper sets the stage with respect to perspective and management options related to implementation of water reuse. Water treatment has to be interpreted as the means by which to purify the water from any degree of impurity to any degree of purity that fits the desired use, including......The water resource is under increasing pressure, both from the increase in population and from the wish to improve the living standards of the individual. Water scarcity is defined as the situation where demand is greater than the resource. Water scarcity has two distinctly different dimensions......: water availability and water applicability. The availability is a question of quantitative demand relative to resource. The applicability is a question of quality suitability for the intended use of the water. There is a significant difference in this regard with respect to rural versus urban use...

  9. The production process for water penetrated brick

    Institute of Scientific and Technical Information of China (English)

    SunGuofeng

    2005-01-01

    Waste penetrated brick, which is a green building material with good water penetration, high strength, lower firing temperature, lower production cost, good appearance and good structure, can holding ground water lever. This article analysis the production process and related factor for water penetrated brick:proper particle size distribution, proper shaping method, proper press and proper firing can ensure to produce good quality water penetrated brick.

  10. Review on Chemical treatment of Industrial Waste Water | Sahu ...

    African Journals Online (AJOL)

    Review on Chemical treatment of Industrial Waste Water. ... used and lot of wastewater generated from industries due their processes and washing purpose. A large number of chemicals are used for the production of potable water and ... powdered activated carbon (PAC) can remove taste and odour compounds and micro ...

  11. Optimizing the solar photo-Fenton process in the treatment of contaminated water. Determination of intrinsic kinetic constants for scale-up

    Energy Technology Data Exchange (ETDEWEB)

    Rodriguez, Miguel [Universidad de Los Andes, Escuela Basica de Ingenieria, La Hechicera, Merida (Venezuela); Malato, Sixto [Plataforma Solar de Almeria, Tabernas (PSA) (Spain); Pulgarin, Cesar [Institute of Environmental Engineering, Laboratory for Environmental Biotechnology, Swiss Federal Institute of Technology (EPFL), CH-1015 Lausanne (Switzerland); Contreras, Sandra; Curco, David; Gimenez, Jaime; Esplugas, Santiago [Department d' Enginyeria Quimica i Metallurgia, Universitat de Barcelona, Marti i Franques 1, 08028 Barcelona (Spain)

    2005-10-01

    The elimination of aromatic compounds present in surface water by photo-Fenton with sunlight as the source of radiation was studied. The concentrations of Fe{sup 3+} and H{sub 2}O{sub 2} are key factors for this process. A solar simulator and a prototype parabolic collector were used as laboratory-scale reactors to find the parameters of those key factors to be used in the CPC (compound parabolic collector) pilot plant reactor. The initial mineralization rate constant (k{sub obs}) was determined and evaluated at different Fe{sup 3+} and H{sub 2}O{sub 2} concentrations to find the best values for maximum efficiency. In all the experiments the mineralization of an aqueous phenol solution was described by assuming a pseudo-first-order reaction. The intrinsic kinetic constants not dependent on the lighting conditions were also estimated for scale-up. (author)

  12. Integrated approach to industrial sewage water treatment - a way of water resources rational use and protection

    Directory of Open Access Journals (Sweden)

    Alekseyev Evgeny

    2016-01-01

    Full Text Available Ion-exchange softening plants wash water treatment studies are provided in order to bring them back to the process. Poorly soluble Ca and Mg compounds formation conditions have been studied during the course of such water caustic treatment using the potentiometric titration method. Information has been provided about the Ca and Mg hydroxide sludge sorption properties with regard to the characteristic contaminants of the sewage water generated by the textile industry enterprise. Suitability of the hydroxide sludge has been established for use in the sewage water treatment technology in order to remove the persisting organic compounds, such as the synthetic dyes.

  13. Hydraulic modelling of drinking water treatment plant operations

    Directory of Open Access Journals (Sweden)

    K. J. Borger

    2008-10-01

    Full Text Available For a drinking water treatment plant simulation, water quality models, a hydraulic model, a process-control model, an object model, data management, training and decision-support features and a graphic user interface have been integrated. The integration of a hydraulic model in the simulator is necessary to correctly determine the division of flows over the plant's lanes and, thus, the flow through the individual treatment units, based on valve positions and pump speeds. The flow through a unit is one of the most important parameters in terms of a unit's effectiveness. In the present paper, a new EPAnet library is presented with the typical hydraulic elements for drinking water treatment processes. Using this library, a hydraulic model was set up and validated for the drinking water treatment plant Harderbroek.

  14. Integrated water management system - Description and test results. [for Space Station waste water processing

    Science.gov (United States)

    Elden, N. C.; Winkler, H. E.; Price, D. F.; Reysa, R. P.

    1983-01-01

    Water recovery subsystems are being tested at the NASA Lyndon B. Johnson Space Center for Space Station use to process waste water generated from urine and wash water collection facilities. These subsystems are being integrated into a water management system that will incorporate wash water and urine processing through the use of hyperfiltration and vapor compression distillation subsystems. Other hardware in the water management system includes a whole body shower, a clothes washing facility, a urine collection and pretreatment unit, a recovered water post-treatment system, and a water quality monitor. This paper describes the integrated test configuration, pertinent performance data, and feasibility and design compatibility conclusions of the integrated water management system.

  15. Integrated water management system - Description and test results. [for Space Station waste water processing

    Science.gov (United States)

    Elden, N. C.; Winkler, H. E.; Price, D. F.; Reysa, R. P.

    1983-01-01

    Water recovery subsystems are being tested at the NASA Lyndon B. Johnson Space Center for Space Station use to process waste water generated from urine and wash water collection facilities. These subsystems are being integrated into a water management system that will incorporate wash water and urine processing through the use of hyperfiltration and vapor compression distillation subsystems. Other hardware in the water management system includes a whole body shower, a clothes washing facility, a urine collection and pretreatment unit, a recovered water post-treatment system, and a water quality monitor. This paper describes the integrated test configuration, pertinent performance data, and feasibility and design compatibility conclusions of the integrated water management system.

  16. A Primer on Waste Water Treatment.

    Science.gov (United States)

    Department of the Interior, Washington, DC. Federal Water Pollution Control Administration.

    This information pamphlet is for teachers, students, or the general public concerned with the types of waste water treatment systems, the need for further treatment, and advanced methods of treating wastes. Present day pollution control methods utilizing primary and secondary waste treatment plants, lagoons, and septic tanks are described,…

  17. Sustainable treatment of municipal waste water

    DEFF Research Database (Denmark)

    Hansen, Peter Augusto; Larsen, Henrik Fred

    The main goal of the EU FP6 NEPTUNE program is to develop new and improve existing waste water treatment technologies (WWTT) and sludge handling technologies for municipal waste water, in accordance with the concepts behind the EU Water Framework Directive. As part of this work, the project...... treatment technologies are to be assessed. This paper will present the first LCA results from running existing life cycle impact assessment (LCIA) methodology on some of the waste water treatment technologies. Keywords: Sustainability, LCA, micropollutants, waste water treatment technologies....... will develop and implement a methodology to compare and prioritize these technologies and optimizations based on a holistic approach. This will be achieved through the use of life cycle assessment (LCA) along with cost/efficiency analysis with focus on the effects of nutrients, pathogens and micropollutants (i...

  18. Risk management in waste water treatment.

    Science.gov (United States)

    Wagner, M; Strube, I

    2005-01-01

    With the continuous restructuring of the water market due to liberalisation, privatisation and internationalisation processes, the requirements on waste water disposal companies have grown. Increasing competition requires a target-oriented and clearly structured procedure. At the same time it is necessary to meet the environment-relevant legal requirements and to design the processes to be environment-oriented. The implementation of risk management and the integration of such a management instrument in an existing system in addition to the use of modern technologies and procedures can help to make the operation of the waste water treatment safer and consequently strengthen market position. The risk management process consists of three phases, risk identification, risk analysis/risk assessment and risk handling, which are based on each other, as well as of the risk managing. To achieve an identification of the risks as complete as possible, a subdivision of the kind of risks (e.g. legal, financial, market, operational) is suggested. One possibility to assess risks is the portfolio method which offers clear representation. It allows a division of the risks into classes showing which areas need handling. The determination of the appropriate measures to handle a risk (e.g. avoidance, reduction, shift) is included in the concluding third phase. Different strategies can be applied here. On the one hand, the cause-oriented strategy, aiming at preventive measures which aim to reduce the probability of occurrence of a risk (e.g. creation of redundancy, systems with low susceptibility to malfunction). On the other hand, the effect-oriented strategy, aiming to minimise the level of damage in case of an undesired occurrence (e.g. use of alarm systems, insurance cover).

  19. Ispra Mark-10 water splitting process

    Science.gov (United States)

    1975-01-01

    A thermochemical water splitting process, the Ispra Mark-10 chemical reaction cycle, was chosen for examining the possibility of using water to produce hydrogen on a large scale for fuel and major industrial chemical uses. The assumed energy source for the process is an HTGR (helium cooled). A process flow diagram, a material balance, and an energy balance were developed for the thermochemical reaction cycle. Principal reactions which constitute the cycle are included.

  20. 强化混凝法处理煤气冷凝水%Treatment of Gas Condensate Water by Enhanced Coagulation Process

    Institute of Scientific and Technical Information of China (English)

    高英; 肖作义; 高峰; 杜雪松; 万淑芳

    2013-01-01

    Taking the gas condensate water from blast furnace in Baotou Iron and Steel (Group) Co.Ltd.as treatment object,the static coagulation comparative experiments were carried out.The experimental results show that when the dosage of PAC and nano chlorine-removing agent are 20 mg/L and 2.0 mL/L respectively,the effluent SS is less than 10 mg/L,the turbidity is less than 10 NTU,the removal rate of chloride ion is more than 80%,and other ions in the wastewater are partly removed.The quality of the effluent is closed to the recycle index for industrial cooling water.%以包头钢铁(集团)有限责任公司高炉煤气冷凝水为处理对象,采用强化混凝法进行静态混凝沉淀对比实验.实验结果表明,当聚合氯化铝加入量为20 mg/L、高分子纳米除氯剂加入量为2.0 mL/L时,处理后出水SS小于10 mg/L,浊度小于10 NTU,氯离子去除率在80%以上,而且对废水中的其他离子也有一定的去除效果,出水水质基本接近工业冷却循环水回用指标.

  1. Treatment of ASP produced water with hydrophilic fibre ball filtration

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    The conventional treatment process cannot meet the need for treatment of produced water from alkaline/surfactant/polymer flooding( ASP produced water) in Daqing oilfield. In this study, a new type of hydrophilic fibre ball medium was developed through surface modification method. The hydrophilic property of the surface modified fibre ball was tested with ASP produced liquid at laboratory. The results showed that this fibre ball had higher oil degreasing efficiency. The surface components were also observed by Scanning Electron Microscope and X-ray Photoelectron Spectroscopy, the result showed that the hydrophilic fibre' s surface was covered by sulfonic group. Using hydrophilic fibre ball as filter medium, a new type of filter was designed to treat ASP produced water in pilot-scale experiments. The obtained results indicated that this type of filter had high capability and efficiency for the treatment of ASP produced water. This filter should have a better application prospect in oilfield produced water treatment.

  2. Comparative study of the effect of pharmaceutical additives on the elimination of antibiotic activity during the treatment of oxacillin in water by the photo-Fenton, TiO2-photocatalysis and electrochemical processes.

    Science.gov (United States)

    Serna-Galvis, Efraim A; Silva-Agredo, Javier; Giraldo, Ana L; Flórez-Acosta, Oscar A; Torres-Palma, Ricardo A

    2016-01-15

    Synthetic pharmaceutical effluents loaded with the β-lactam antibiotic oxacillin were treated using advanced oxidation processes (the photo-Fenton system and TiO2 photocatalysis) and chloride mediated electrochemical oxidation (with Ti/IrO2 anodes). Combinations of the antibiotic with excipients (mannitol or tartaric acid), an active ingredient (calcium carbonate, i.e. bicarbonate ions due to the pH) and a cleaning agent (sodium lauryl ether sulfate) were considered. Additionally, urban wastewater that had undergone biological treatment was doped with oxacillin and treated with the tested systems. The evolution of antimicrobial activity was monitored as a parameter of processes efficiency. Although the two advanced oxidation processes (AOPs) differ only in the way they produce OH, marked differences were observed between them. There were also differences between the AOPs and the electrochemical system. Interestingly, each additive had a different effect on each treatment. For water loaded with mannitol, electrochemical treatment was the most suitable option because the additive did not significantly affect the efficiency of the system. Due to the formation of a complex with Fe(3+), tartaric acid accelerated the elimination of antibiotic activity during the photo-Fenton process. For TiO2 photocatalysis, the presence of bicarbonate ions contributed to antibiotic activity elimination through the possible formation of carbonate and bicarbonate radicals. Sodium lauryl ether sulfate negatively affected all of the processes. However, due to the higher selectivity of HOCl compared with OH, electrochemical oxidation showed the least inhibited efficiency. For the urban wastewater doped with oxacillin, TiO2 photocatalysis was the most efficient process. These results will help select the most suitable technology for the treatment of water polluted with β-lactam antibiotics.

  3. Hydraulic modelling of drinking water treatment plant operations

    OpenAIRE

    L. C. Rietveld; Borger, K.J.; Van Schagen, K.M.; Mesman, G.A.M.; G. I. M. Worm

    2008-01-01

    For a drinking water treatment plant simulation, water quality models, a hydraulic model, a process-control model, an object model, data management, training and decision-support features and a graphic user interface have been integrated. The integration of a hydraulic model in the simulator is necessary to correctly determine the division of flows over the plant's lanes and, thus, the flow through the individual treatment units, based on valve positions and pump speeds. The flow through a un...

  4. Sterilization of Fungus in Water by Pulsed Power Gas Discharge Reactor Spraying Water Droplets for Water Treatment

    Science.gov (United States)

    Saito, Tsukasa; Handa, Taiki; Minamitani, Yasushi

    We study sterilization of bacteria in water using pulsed streamer discharge of gas phase. This method enhances efficiency of water treatment by spraying pretreatment water in a streamer discharge area. In this paper, yeast was sterilized because we assumed a case that fungus like mold existed in wastewater. As a result, colony forming units decreased rapidly for 2 minutes of the processing time, and all yeast sterilized by 45 minutes of the processing time.

  5. Removal of the anti-cancer drug methotrexate from water by advanced oxidation processes: Aerobic biodegradation and toxicity studies after treatment.

    Science.gov (United States)

    Lutterbeck, Carlos Alexandre; Baginska, Ewelina; Machado, Ênio Leandro; Kümmerer, Klaus

    2015-12-01

    Anti-cancer drugs are discussed as high risk substances in regard to human health and considered as problematic for the environment. They are of potential environmental relevance due to their poor biodegradability and toxicological properties. Methotrexate (MTX) is an antimetabolite that was introduced in the pharmaceutical market in the 40's and still today is one of the most consumed cytotoxic compounds around the world. In the present study MTX was only partially biodegraded in the closed bottle test (CBT). Therefore, it was submitted to three different advanced oxidation processes (AOPs): UV/H2O2, UV/Fe(2+)/H2O2 and UV/TiO2. The irradiation was carried out with a Hg medium-pressure lamp during 256min whereas the analytical monitoring was done through LC-UV-MS/MS and DOC analysis. MTX was easily removed in all the irradiation experiments, while the highest mineralization values and rates were achieved by the UV/Fe(2+)/H2O2 treatment. The lowest resulted from the UV/H2O2 reactions. The UV/H2O2 treatment resulted in little biodegradable transformation products (TPs). However, the same treatment resulted in a reduction of the toxicity of MTX by forming less toxic TPs. Analysis by LC-UV-MS/MS revealed the existence of nine TPs formed during the photo-catalytic treatments. The pH of the solutions decreased from 6.4 (t 0min) to 5.15 in the UV/H2O2 and from 6.4 (t 0min) to 5.9 in the UV/TiO2 at the end of the experiments. The initial pH of the UV/Fe(2+)/H2O2 experiments was adjusted to 5 and after the addition of H2O2 the pH decreased to around 3 and remained in this range until the end of the treatments.

  6. Anoxic selectors with regeneration in activated sludge waste water treatment processes; Selectores anoxicos con regeneracion en procesos de depuracion de aguas residuales por fangos activados

    Energy Technology Data Exchange (ETDEWEB)

    Sancho Seuma, L.; Lopetigue Garnica, J.; Paredes, J.A.; Alonso, E.; Plaza, F.I.; Diaz chozas, M.

    1998-12-01

    The aim of this study is to produce a reduction in the concentration of filamentous bulking or foaming related microorganisms, such as usually appear in connection with nutrient elimination processes, where sludge retention times are high and loads are small. The Research Institute Centa has established, annexed to the sewage treatment plant Norte I. Seville, a pilot plant with the classical DN layout, and an anoxic selector, as well as a regeneration tank . This tank is meant to eliminate the remaining substratum associated with the cells after being settled in a high-concentration environment the selector. We endeavor therefore to select by kinetic and metabolic procedures the flock formers microorganisms to the expense of the filamentous microorganisms. (Author)

  7. POOL WATER TREATMENT AND COOLING SYSTEM DESCRIPTION DOCUMENT

    Energy Technology Data Exchange (ETDEWEB)

    V. King

    2000-06-19

    The Pool Water Treatment and Cooling System is located in the Waste Handling Building (WHB), and is comprised of various process subsystems designed to support waste handling operations. This system maintains the pool water temperature within an acceptable range, maintains water quality standards that support remote underwater operations and prevent corrosion, detects leakage from the pool liner, provides the capability to remove debris from the pool, controls the pool water level, and helps limit radiological exposure to personnel. The pool structure and liner, pool lighting, and the fuel staging racks in the pool are not within the scope of the Pool Water Treatment and Cooling System. Pool water temperature control is accomplished by circulating the pool water through heat exchangers. Adequate circulation and mixing of the pool water is provided to prevent localized thermal hotspots in the pool. Treatment of the pool water is accomplished by a water treatment system that circulates the pool water through filters, and ion exchange units. These water treatment units remove radioactive and non-radioactive particulate and dissolved solids from the water, thereby providing the water clarity needed to conduct waste handling operations. The system also controls pool water chemistry to prevent advanced corrosion of the pool liner, pool components, and fuel assemblies. Removal of radioactivity from the pool water contributes to the project ALARA (as low as is reasonably achievable) goals. A leak detection system is provided to detect and alarm leaks through the pool liner. The pool level control system monitors the water level to ensure that the minimum water level required for adequate radiological shielding is maintained. Through interface with a demineralized water system, adequate makeup is provided to compensate for loss of water inventory through evaporation and waste handling operations. Interface with the Site Radiological Monitoring System provides continuous

  8. Biogenic metals in advanced water treatment.

    Science.gov (United States)

    Hennebel, Tom; De Gusseme, Bart; Boon, Nico; Verstraete, Willy

    2009-02-01

    Microorganisms can change the oxidation state of metals and concomitantly deposit metal oxides and zerovalent metals on or into their cells. The microbial mechanisms involved in these processes have been extensively studied in natural environments, and researchers have recently gained interest in the applications of microbe-metal interactions in biotechnology. Because of their specific characteristics, such as high specific surface areas and high catalytic reactivity, biogenic metals offer promising perspectives for the sorption and (bio)degradation of contaminants. In this review, the precipitation of biogenic manganese and iron species and the microbial reduction of precious metals, such as palladium, platinum, silver and gold, are discussed with specific attention to the application of these biogenic metals in innovative remediation technologies in advanced water treatment.

  9. Water Supply and Treatment Equipment

    Science.gov (United States)

    2009-09-15

    for the specific membrane ; b. For technologies employing membrane ultrafiltration and/or membrane microfiltration , identification of the...interesting challenges. Source water temperatures must remain below 35 oC (95 oF) during test conduct to prevent damage to the RO membranes . If employing a...below 35 °C (95 °F) during test conduct to prevent damage to the RO membranes . Due to the extended storage requirement for this test procedure, a

  10. Water/Wastewater Treatment Plant Operator Qualifications.

    Science.gov (United States)

    Water and Sewage Works, 1979

    1979-01-01

    This article summarizes in tabular form the U.S. and Canadian programs for classification of water and wastewater treatment plant personnel. Included are main characteristics of the programs, educational and experience requirements, and indications of requirement substitutions. (CS)

  11. Interim Enhanced Surface Water Treatment Rule Documents

    Science.gov (United States)

    The IESWTR balances the need for treatment with potential increases in disinfection by -products. The materials found on this page are intended to assist public water systems and state in the implementation of the IESWTR.

  12. ALTERNATIVE DISINFECTION FOR DRINKING WATER TREATMENT

    Science.gov (United States)

    During a one-yr study at Jefferson Parish, La., the chemical, microbiological, and mutagenic effects os using the major drinkgin water disinfectants (chlorine, chlorine dioxide, chloramine, ozone) were evaluated. Tests were performed on samples collected from various treatment s...

  13. Modelling of Water Turbidity Parameters in a Water Treatment Plant

    Directory of Open Access Journals (Sweden)

    A. S. KOVO

    2005-01-01

    Full Text Available The high cost of chemical analysis of water has necessitated various researches into finding alternative method of determining portable water quality. This paper is aimed at modelling the turbidity value as a water quality parameter. Mathematical models for turbidity removal were developed based on the relationships between water turbidity and other water criteria. Results showed that the turbidity of water is the cumulative effect of the individual parameters/factors affecting the system. A model equation for the evaluation and prediction of a clarifier’s performance was developed:Model: T = T0(-1.36729 + 0.037101∙10λpH + 0.048928t + 0.00741387∙alkThe developed model will aid the predictive assessment of water treatment plant performance. The limitations of the models are as a result of insufficient variable considered during the conceptualization.

  14. Upgrading and reconstruction process design for the Gaobeidian Reclaimed Water Treatment Plant in Beijing City%北京高碑店再生水处理厂升级改造工艺方案设计

    Institute of Scientific and Technical Information of China (English)

    冯凯

    2012-01-01

    为实现污水的资源化利用,通过改造工程将高碑店污水处理厂升级成为再生水处理厂,规模100万m3/d,出水主要水质指标要求达到《地表水环境质量标准》(GB 3838-2002) Ⅳ类水体水质标准.通过对现状污水处理厂及改造目标的分析,综合考虑技术、经济、可实施性等多方面因素,选取升级改造主体为A2/O(填料)工艺,新建的深度处理部分采用反硝化生物滤池+膜过滤+臭氧脱色工艺.介绍了水处理和污泥处理部分的工艺设计方案及设计参数,分析了工艺方案特点.%To realize the resourcization of wastewater, Gaobeidian Wastewater Treatment Plant was upgraded to reclaimed water treatment plant. Its production scale was 1×106 m3/d and the effluent quality was required to meet the IV category water quality standards of Environmental quality standards for surface -water (GB 3838—2002). Through the analysis of the existing wastewater treatment plant and upgrading goal and the comprehensive consideration of multiple aspects including technology,economy,and possibility,the A2/O (filler) process was selected as the major upgrading process and the combination of denitrification biofilter, film filter and ozone decoloring process was adopted for the newly built advanced treatment. This paper introduced the process design plan and design parameters for the wastewater treatment and sludge treatment and analyzed the features of the process plan.

  15. Nanotechnology for water treatment and purification

    CERN Document Server

    Apblett, Allen

    2014-01-01

    This book describes the latest progress in the application of nanotechnology for water treatment and purification. Leaders in the field present both the fundamental science and a comprehensive overview of the diverse range of tools and technologies that have been developed in this critical area. Expert chapters present the unique physicochemical and surface properties of nanoparticles and the advantages that these provide for engineering applications that ensure a supply of safe drinking water for our growing population. Application areas include generating fresh water from seawater, preventing contamination of the environment, and creating effective and efficient methods for remediation of polluted waters. The chapter authors are leading world-wide experts in the field with either academic or industrial experience, ensuring that this comprehensive volume presents the state-of-the-art in the integration of nanotechnology with water treatment and purification. Covers both wastewater and drinking water treatmen...

  16. 批处理工艺处理水基切削废液工程实例%Engineering example of the treatment of water-based waste cutting fluid by batch processing

    Institute of Scientific and Technical Information of China (English)

    吴琦平; 衡祥; 乔春生

    2011-01-01

    介绍了采用批处理工艺对金属水基切削废液进行预处理的工程实例.通过批处理槽的破乳、絮凝、气浮作用,使废水COD和油类的去除率分别达到84.8%、92.3%.批处理槽出水与生活污水混合后通过生物处理和深度处理,系统总的出水优于(GB 8978-1996)一级标准.%An engineering example of using batch processing for the pretreatment of metal water-based waste cutting fluid is introduced. The COD and oil removal rate of the wastewater are 84.8% ,92.3% ,respectively,by means of demulsification, flocculation and air-flotation processes in the batch processing tank. After mixing the effluent from the batch processing tank with domestic sewage ,and through biological treatment and advanced treatment ,the quality of the total effluent water of the system is superior to the first grade of the Integrated Wastewater Discharge Standard(GB 8978-1996).

  17. The Use of Water Plants for Storm Water Runoff Treatment

    Directory of Open Access Journals (Sweden)

    Lina Varneckaitė

    2011-04-01

    Full Text Available The popularity of using water plants for storm water runoff treatment has been largely due to the fact that pond and wetland based systems offer the advantages of providing a relatively passive, natural, low-maintenance and operationally simple treatment solution while enhancing habitat and aesthetic values at the same time. While ponds are generally effective at removing coarse suspended sediments, they are less effective at removing finer particulates and dissolved contaminants. To provide enhanced treatment, a wetland can be placed downstream of a pond.Article in Lithuanian

  18. Cellulose Nanomaterials in Water Treatment Technologies

    OpenAIRE

    Carpenter, Alexis Wells; de Lannoy, Charles François; Mark R. Wiesner

    2015-01-01

    Cellulose nanomaterials are naturally occurring with unique structural, mechanical and optical properties. While the paper and packaging, automotive, personal care, construction, and textiles industries have recognized cellulose nanomaterials’ potential, we suggest cellulose nanomaterials have great untapped potential in water treatment technologies. In this review, we gather evidence of cellulose nanomaterials’ beneficial role in environmental remediation and membranes for water filtration, ...

  19. Water Treatment Technology - Taste, Odor & Color.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on taste, odor, and color provides instructional materials for three competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on the following areas: taste and odor determination, control of…

  20. Water Treatment Technology - Cross-Connections.

    Science.gov (United States)

    Ross-Harrington, Melinda; Kincaid, G. David

    One of twelve water treatment technology units, this student manual on cross connections provides instructional materials for two competencies. (The twelve units are designed for a continuing education training course for public water supply operators.) The competencies focus on cross connections terminology and control devices. For each…

  1. Adaptation to the KMT Fixed Biomass on Moving Bed process in the waste water treatment plant in Tafalla and Olite, Navarra, Spain; Adaptacion al proceso KMT de Biomasa Fija sobre Lecho Movil en la EDAR de Tafalla y Olite

    Energy Technology Data Exchange (ETDEWEB)

    Cortacans, J. A.; Rodrigo, J. C.; Garcia Gamuza, J.

    2001-07-01

    This article describes the remodeling carried out on the Tafalla and Olite waste water treatment plant in 2000to enable it to cope with a larger flow and load without having to construct new treatment lines. This was made possible by adapting the existing conventional active sludge process to the KMT Fixed Biomass on Moving Bed process. The article also shows how the final two-stage design was verified by means of pilot plant trials. These experiments tested the technical viability of installing a first high-load reactor prior to the existing primary decantation as a way of dealing with the seasonal effluents from the wine-cellars in the region and of obtaining partial nitrification in the last biological tank of the second stage during the rest of the year. (Author) 7 refs.

  2. Process-integrated slag treatment; Prozessintegrierte Schlackebehandlung

    Energy Technology Data Exchange (ETDEWEB)

    Koralewska, R.; Faulstich, M. [Technische Univ., Garching (Germany). Lehrstuhl fuer Wasserguete- und Abfallwirtschaft

    1998-09-01

    The present study compares two methods of washing waste incineration slag, one with water only, and one which uses additives during wet deslagging. The presented aggregate offers ideal conditions for process-integrated slag treatment. The paper gives a schematic description of the integrated slag washing process. The washing liquid serves to wash out the readily soluble constituents and remove the fines, while the additives are for immobilising heavy metals in the slag material. The study is based on laboratory and semi-technical trials on the wet chemical treatment of grate slag with addition of carbon dioxide and phosphoric acid. [Deutsch] Die dargestellten Untersuchungen beziehen sich auf den Vergleich zwischen einer Waesche der Muellverbrennungsschlacke mit Wasser und unter Zugabe von Additiven im Nassentschlacker. In diesem Aggregat bieten sich optimale Voraussetzungen fuer eine prozessintegrierte Schlackebehandlung. Die Durchfuehrung der integrierten Schlackewaesche wird schematisch gezeigt. Durch die Waschfluessigkeit sollen die leichtloeslichen Bestandteile ausgewaschen und die Feinanteile ausgetragen sowie durch die Additive zusaetzlich die Schwermetalle im Schlackematerial immobilisiert werden. Dazu erfolgten Labor- und halbtechnische Versuche zur nasschemischen Behandlung der Rostschlacken unter Zugabe von Kohlendioxid und Phosphorsaeure. (orig./SR)

  3. Avaliação em escala laboratorial da utilização do processo eletrolítico no tratamento de águas Laboratory scale assessment of an electrolytic process for water treatment

    Directory of Open Access Journals (Sweden)

    Marcelo Henrique Otenio

    2008-01-01

    Full Text Available Water treatment uses chlorine for disinfection causing formation of trihalomethanes. In this work, an electrolytic water pre-treatment was studied and applied to the water from a fountainhead. The action against microorganisms was evaluated using cast-iron and aluminum electrodes. Assays were made in laboratory using the electrolytic treatment. After 5 min of electrolysis the heterotrophic bacteria count was below 500 cfu/mL and complete elimination of total and fecal coliforms was observed. Using electrolytic treatment as a pretreatment of conventional tap water treatment is proposed.

  4. 机械蒸汽再压缩技术处理反渗透浓水的中试研究%Pilot Study on Mechanical Vapor Recompression Technology for Treatment of Concentrated Water from Reverse Osmosis Process

    Institute of Scientific and Technical Information of China (English)

    张金鸿; 侯霙; 李海芳; 唐运平

    2011-01-01

    近年来,反渗透(RO)在污水厂二级出水深度处理中的应用越来越多.然而,RO浓水的含盐量较高、有机物难于降解,采用常规方法处理时出水水质难于达到排放标准.采用机械蒸汽再压缩技术(MVR)对某污水厂的反渗透浓水进行了6倍浓缩的中试,其出水COD≤50 mg/L、NH-N≤10 mg/L,可以达到(GB/T 18920-2002)的要求;COD、TDS、Mg和色度等指标的浓缩倍数与体系的浓缩倍数基本一致,而浓缩水中的TP、SiO、TN、NH-N浓度却低于原水的,这主要是由于磷酸盐、硅酸盐的沉淀和氨气逸出所致.另外,钙盐等的沉淀作用还造成浓缩水中SS浓度的增加.由此可见,利用MVR处理反渗透浓水在技术上是可行的,但是需要增加沉淀物的预处理和排出气体的收集处理装置.%Recently, the application of reverse osmosis (RO) in advanced treatment of effluent form WWTP becomes very popular. However, due to high salinity and refractory organic compounds in concentrated water of RO, the effluent treated by traditional processes can not meet the discharge standard. A pilot experiment at a concentration factor of 6 was conducted to treat concentrated water from reverse osmosis (RO) process in a sewage treatment plant using mechanical vapor recompression (MVR)technology. COD and NH3 -N in the effluent from MVR process are equal to or less than 50 mg/L and 10 mg/L, meeting the Reuse of Urban Recycling Water-Water Quality Standard for Urban Miscellaneous Water Consumption (GB/T 18920 -2002). The concentration factors of COD, TDS, Mg2+ and color in concentrated water of MVR are similar to those in concentrated water of RO. However, the concentration factors of TP, SiO2, TN and NH3 - N are lower than those in concentrated water of RO due to escape of ammonia and precipitation of phosphate and silicate. In addition, precipitation of calcium salt causes increase of SS in concentrated water of MVR. The experiment shows that MVR technology is

  5. Plant wide chemical water stability modelling with PHREEQC for drinking water treatment

    NARCIS (Netherlands)

    Van der Helm, A.W.C.; Kramer, O.J.I.; Hooft, J.F.M.; De Moel, P.J.

    2015-01-01

    In practice, drinking water technologists use simplified calculation methods for aquatic chemistry calculations. Recently, the database stimela.dat is developed especially for aquatic chemistry for drinking water treatment processes. The database is used in PHREEQC, the standard in geohydrology for

  6. Plant wide chemical water stability modelling with PHREEQC for drinking water treatment

    NARCIS (Netherlands)

    Van der Helm, A.W.C.; Kramer, O.J.I.; Hooft, J.F.M.; De Moel, P.J.

    2015-01-01

    In practice, drinking water technologists use simplified calculation methods for aquatic chemistry calculations. Recently, the database stimela.dat is developed especially for aquatic chemistry for drinking water treatment processes. The database is used in PHREEQC, the standard in geohydrology for

  7. Innovative Treatment Technologies for Natural Waters and Wastewaters

    Energy Technology Data Exchange (ETDEWEB)

    Childress, Amy E.

    2011-07-01

    The research described in this report focused on the development of novel membrane contactor processes (in particular, forward osmosis (FO), pressure retarded osmosis (PRO), and membrane distillation (MD)) in low energy desalination and wastewater treatment applications and in renewable energy generation. FO and MD are recently gaining national and international attention as viable, economic alternatives for removal of both established and emerging contaminants from natural and process waters; PRO is gaining worldwide attention as a viable source of renewable energy. The interrelationship of energy and water are at the core of this study. Energy and water are inextricably bound; energy usage and production must be considered when evaluating any water treatment process for practical application. Both FO and MD offer the potential for substantial energy and resource savings over conventional treatment processes and PRO offers the potential for renewable energy or energy offsets in desalination. Combination of these novel technologies with each other, with existing technologies (e.g., reverse osmosis (RO)), and with existing renewable energy sources (e.g., salinity gradient solar ponds) may enable much less expensive water production and also potable water production in remote or distributed locations. Two inter-related projects were carried out in this investigation. One focused on membrane bioreactors for wastewater treatment and PRO for renewable energy generation; the other focused on MD driven by a salinity gradient solar pond.

  8. 氯胺消毒工艺在郊区水厂的应用实践%Applications and Practice of Disinfection Process with Chloramine in Suburban Water Treatment Plants

    Institute of Scientific and Technical Information of China (English)

    张华军

    2012-01-01

    Raw water of Nanhui district suburb water plant is of high concentration of CODMn, and NH3-N with large seasonal variation. Ammonia dosing system was added in water treatment processes, which made effluent NH,-N maintain 0.5 mg/L at the outlet sedimentation tank. The results show this measure is helpful to ensure the residual chlorine stability in distribution network and lower the concentrations of disinfection by-products (DBPs). However, water treatment cost increases by 0.008 RMB/t, removal rate of total bacteria count and color decreases after this measures is used.%该文介绍了上海浦东新区南汇地区郊区水厂的原水具有高耗氧量、高氨氮、季节性变化大的特点.通过在自来水制水工艺中增添加氨装置,控制沉淀池出水氨氮为0.5 mg/L左右;采用化合氯消毒后,可有效保证管网余氯稳定性和控制消毒副产物,但该方法也存在菌落总数检出率和色度升高及制水成本提高约0.008元/t的问题.

  9. Waste water treatment in Bukkerup (VB)

    DEFF Research Database (Denmark)

    Thomsen, Rikke; Overgaard, Morten; Jørgensen, Michael Søgaard

    1999-01-01

    In connection to the new waste water plan of Tølløse municipal the technical and environmental board has suggested that Bukkerup get a sewer system which brings the waste water to the treatment plant for Tysinge. All though the residents would like to list alternative suggestions which improve...... the local water environment but is still competitive.In this report the alternatives are listed, e.i. root system plants, sand filters and mini treatment plants.The conclusion is that root system plants and a combination of root system plants and sand filters are better that the sewer system....

  10. Effect of Magnetic Treatment of Water on Evapotranspiration of Tomato

    Directory of Open Access Journals (Sweden)

    K. O. Yusuf

    2017-02-01

    Full Text Available This study was conducted to determine the effect of magnetic treatment of water on the evapotranspiration of tomato plant. Evapotranspiration is important to plant for metabolic processes and it also cools the plant. Three magnetic flux densities of 124, 319 and 719 G produced from electromagnet (the treatments labelled as T1, T2 and T3 were used to treat the water and a control experiment (TC was also set up which was irrigated with non-magnetic treatment water. Equal amount of water was applied to all the tomato plant (variety UC82B at the same time. Each treatment was replicated seven times given a total of 28 buckets containing tomato plant. The tomato was planted in the 28 buckets in a transparent garden shed for 130 days (23/09/2014 – 30/01/2015. A complete randomized design (CRD experimental layout was used. The amount of water lost due to evapotranspiration per day was determined by weight lost in the bucket (lysimetric weighing method. The mean values of daily evapotranspiration for two stands of tomato plants per bucket over a period of 65 days for T1, T2, T3 and TC were 9.38, 9.28, 9.18 and 8.03 mm/day respectively. The result of the evapotranspiration due to mass of water lost from the buckets containing tomato plants irrigated with magnetic water were all higher than the values of evapotranspiration from non-magnetic water. This indicated that tomato plant irrigated with magnetic treatment of water absorbed more water from the soil easily and grew faster than the tomato plant irrigated with non-magnetic treatment water with the same quantity of water applied to the tomato plant.

  11. Fate of Carbamazepine during Water Treatment

    DEFF Research Database (Denmark)

    Kosjek, T.; Andersen, Henrik Rasmus; Kompare, Boris;

    2009-01-01

    Seven transformation products of carbamazepine generated by at least one of three common water treatment technologies (W-radiation, oxidation with chlorine dioxide (ClO2), and biological treatment with activated Sludge) were identified by complementary use of ion trap, single quadrupole...

  12. Study on brackish water treatment technology

    Institute of Scientific and Technical Information of China (English)

    HE Xu-wen(何绪文); Xu De-ping (许德平); WU Bing(吴兵); WANG Tong(王通)

    2003-01-01

    Based on the characters of deep well-water quality in Fenxi Mining Group in Liulin, the feasibilities of two treatment technologies which use electrodialysis and reverse osmosis are analyzed. Through analyzing and comparing, reverse osmosis technology has several advantages, such as good treatment effect, convenient operating management and low run-cost.

  13. Rational design of nanomaterials for water treatment

    Science.gov (United States)

    Li, Renyuan; Zhang, Lianbin; Wang, Peng

    2015-10-01

    The ever-increasing human demand for safe and clean water is gradually pushing conventional water treatment technologies to their limits. It is now a popular perception that the solutions to the existing and future water challenges will hinge upon further developments in nanomaterial sciences. The concept of rational design emphasizes on `design-for-purpose' and it necessitates a scientifically clear problem definition to initiate the nanomaterial design. The field of rational design of nanomaterials for water treatment has experienced a significant growth in the past decade and is poised to make its contribution in creating advanced next-generation water treatment technologies in the years to come. Within the water treatment context, this review offers a comprehensive and in-depth overview of the latest progress in rational design, synthesis and applications of nanomaterials in adsorption, chemical oxidation and reduction reactions, membrane-based separation, oil-water separation, and synergistic multifunctional all-in-one nanomaterials/nanodevices. Special attention is paid to the chemical concepts related to nanomaterial design throughout the review.

  14. Rational design of nanomaterials for water treatment

    KAUST Repository

    Li, Renyuan

    2015-08-26

    The ever-increasing human demand for safe and clean water is gradually pushing conventional water treatment technologies to their limits and it is now a popular perception that the solutions to the existing and future water challenges will highly hinge upon the further development of nanomaterial sciences. The concept of rational design emphasizes ‘design-for-purpose’ and it necessitates a scientifically clear problem definition to initiate the nanomaterial design. The field of rational design of nanomaterials for water treatment has experienced a significant growth in the past decade and is poised to make its contribution in creating advanced next-generation water treatment technologies in the years to come. Within the water treatment context, this review offers a comprehensive and in-depth overview of the latest progress of the rational design, synthesis and applications of nanomaterials in adsorption, chemical oxidation and reduction reactions, membrane-based separation, oil/water separation, and synergistic multifunctional all-in-one nanomaterials/nanodevices. Special attention is paid on chemical concepts of the nanomaterial designs throughout the review.

  15. A new approach for water treatment

    CERN Document Server

    Principe, R

    1999-01-01

    A quantity of up to 4000 m3/h of water is used at CERN for cooling purposes: experiments, magnets and radio frequency cavities are refrigerated by closed circuits filled with deionized water; other utilities, such as air-conditioning, use chilled/hot water, also in closed circuits. All these methods all employ a cold source, the primary supply of water, coming from the cooling towers. About 500 kCHF are spent every year on water treatment in order to keep the water within these networks in operational conditions. In the line of further rationalization of resources, the next generation of contracts with the water treatment industry will aim for improved performance and better monitoring of quality related parameters in this context. The author will provide a concise report based upon an examination of the state of the installations and of the philosophy followed up until now for water treatment. Furthermore, he/she will propose a new approach from both a technical and contractual point of view, in preparation ...

  16. Water Footprint Assessment in Waste Water Treatment Plant: Indicator of the sustainability of urban water cycle.

    Science.gov (United States)

    Gómez Llanos, Eva; Durán Barroso, Pablo; Matías Sánchez, Agustín; Fernández Rodríguez, Santiago; Guzmán Caballero, Raúl

    2017-04-01

    The seventeen Sustainable Development Goals (SDG) represent a challenge for citizens and countries around the world by working together to reduce social inequality, to fight poverty and climate change. The Goal six water and sanitation aims for ensuring, among others, the protection and restoration of water-related ecosystem (target 6.6) and encouraging the water use efficiency (target 6.3). The commitment to this goal is not only the development of sanitation infrastructure, but also incorporates the necessity of a sustainable and efficient management from ecological and economic perspectives. Following this approach, we propose a framework for assessing the waste water treatment plant (WWTP) management based on the Water Footprint (WF) principles. The WF as indicator is able to highlight the beneficial role of WWTPs within the environment and provide a complementary information to evaluate the impact of a WWTP regarding to the use of freshwater and energy. Therefore, the footprint family provides an opportunity to relate the reduction of pollutant load in a WWTP and the associated consumptions in terms of electricity and chemical products. As a consequence, the new methodology allows a better understanding of the interactions among water and energy resources, economic requirements and environmental risks. Because of this, the current technologies can be improved and innovative solutions for monitoring and management of urban water use can be integrated. The WF was calculated in four different WWTP located in the North East of Extremadura (SW Spain) which have activated sludge process as secondary treatment. This zone is characterized by low population density but an incipient tourism development. The WF estimation and its relationship with the electricity consumption examines the efficiency of each WWTP and identifies the weak points in the management in terms of the sustainability. Consequently, the WF establishes a benchmark for multidisciplinary decision

  17. Hydraulic modelling of drinking water treatment plant operations

    Directory of Open Access Journals (Sweden)

    L. C. Rietveld

    2009-06-01

    Full Text Available The flow through a unit of a drinking water treatment plant is one of the most important parameters in terms of a unit's effectiveness. In the present paper, a new EPAnet library is presented with the typical hydraulic elements for drinking water treatment processes well abstraction, rapid sand filtration and cascade and tower aeration. Using this treatment step library, a hydraulic model was set up, calibrated and validated for the drinking water treatment plant Harderbroek. With the actual valve position and pump speeds, the flows were calculated through the several treatment steps. A case shows the use of the model to calculate the new setpoints for the current frequency converters of the effluent pumps during a filter backwash.

  18. Bacterial Cyanuric Acid Hydrolase for Water Treatment.

    Science.gov (United States)

    Yeom, Sujin; Mutlu, Baris R; Aksan, Alptekin; Wackett, Lawrence P

    2015-10-01

    Di- and trichloroisocyanuric acids are widely used as water disinfection agents, but cyanuric acid accumulates with repeated additions and must be removed to maintain free hypochlorite for disinfection. This study describes the development of methods for using a cyanuric acid-degrading enzyme contained within nonliving cells that were encapsulated within a porous silica matrix. Initially, three different bacterial cyanuric acid hydrolases were compared: TrzD from Acidovorax citrulli strain 12227, AtzD from Pseudomonas sp. strain ADP, and CAH from Moorella thermoacetica ATCC 39073. Each enzyme was expressed recombinantly in Escherichia coli and tested for cyanuric acid hydrolase activity using freely suspended or encapsulated cell formats. Cyanuric acid hydrolase activities differed by only a 2-fold range when comparing across the different enzymes with a given format. A practical water filtration system is most likely to be used with nonviable cells, and all cells were rendered nonviable by heat treatment at 70°C for 1 h. Only the CAH enzyme from the thermophile M. thermoacetica retained significant activity under those conditions, and so it was tested in a flowthrough system simulating a bioreactive pool filter. Starting with a cyanuric acid concentration of 10,000 μM, more than 70% of the cyanuric acid was degraded in 24 h, it was completely removed in 72 h, and a respike of 10,000 μM cyanuric acid a week later showed identical biodegradation kinetics. An experiment conducted with water obtained from municipal swimming pools showed the efficacy of the process, although cyanuric acid degradation rates decreased by 50% in the presence of 4.5 ppm hypochlorite. In total, these experiments demonstrated significant robustness of cyanuric acid hydrolase and the silica bead materials in remediation.

  19. Space Station Water Processor Process Pump

    Science.gov (United States)

    Parker, David

    1995-01-01

    This report presents the results of the development program conducted under contract NAS8-38250-12 related to the International Space Station (ISS) Water Processor (WP) Process Pump. The results of the Process Pumps evaluation conducted on this program indicates that further development is required in order to achieve the performance and life requirements for the ISSWP.

  20. Integration and demonstration of the pre-treatment process and improved conventional treatment process for seasonally polluted raw water%季节性污染原水预处理和常规处理工艺强化技术集成与示范

    Institute of Scientific and Technical Information of China (English)

    张晓健; 张锡辉; 陆少鸣; 王建平; 盛德洋; 田家宇

    2012-01-01

    针对珠江下游普遍存在的水源季节性氨氮和有机物污染问题,采用原水生物预处理和强化常规处理工艺技术路线,开发了三种主要的集成工艺技术,包括高速生物过滤强化常规工艺、高锰酸钾与粉末活性炭、纯氧曝气及活性无烟煤联合强化常规工艺、以平板陶瓷膜为主的集成工艺等,建立了中试基地和示范工程,有效处理氨氮浓度为3~5 mg/L的原水,出水水质达到GB 5749-2006标准,经济有效,稳定可靠,为常规工艺升级改造提供了多样化技术选择.%According to common seasonal ammonia and organic pollution in water resource in downstream river basin of Zhujiang River, the upgrading technology route of biological pre-treatment and improved conventional treatment process was used in this research. In this paper, three main integrated technologies were developed, including the improved conventional treatment process by high-speed biological filter, the improved conventional treatment process with the combination of potassium permanganate, powdered activated carbon, pure oxygen aeration and activated anthracite, and the panel ceramic membrane technology. The pilot experiment basement and example project were built up. It was shown that the project could treat the raw water with the ammonia concentration of 3~5 mg/L effectively, and the effluent could meet the GB 5749-2006 standards. This project was economical, stable, and offered multiple technology choices for the conventional treatment process upgrading reconstruction.

  1. Nanotechnology-based water treatment strategies.

    Science.gov (United States)

    Kumar, Sandeep; Ahlawat, Wandit; Bhanjana, Gaurav; Heydarifard, Solmaz; Nazhad, Mousa M; Dilbaghi, Neeraj

    2014-02-01

    The most important component for living beings on the earth is access to clean and safe drinking water. Globally, water scarcity is pervasive even in water-rich areas as immense pressure has been created by the burgeoning human population, industrialization, civilization, environmental changes and agricultural activities. The problem of access to safe water is inevitable and requires tremendous research to devise new, cheaper technologies for purification of water, while taking into account energy requirements and environmental impact. This review highlights nanotechnology-based water treatment technologies being developed and used to improve desalination of sea and brackish water, safe reuse of wastewater, disinfection and decontamination of water, i.e., biosorption and nanoadsorption for contaminant removal, nanophotocatalysis for chemical degradation of contaminants, nanosensors for contaminant detection, different membrane technologies including reverse osmosis, nanofiltration, ultrafiltration, electro-dialysis etc. This review also deals with the fate and transport of engineered nanomaterials in water and wastewater treatment systems along with the risks associated with nanomaterials.

  2. Potential of Using Solar Energy for Drinking Water Treatment Plant

    Science.gov (United States)

    Bukhary, S. S.; Batista, J.; Ahmad, S.

    2016-12-01

    Where water is essential to energy generation, energy usage is integral to life cycle processes of water extraction, treatment, distribution and disposal. Increasing population, climate change and greenhouse gas production challenges the water industry for energy conservation of the various water-related operations as well as limiting the associated carbon emissions. One of the ways to accomplish this is by incorporating renewable energy into the water sector. Treatment of drinking water, an important part of water life cycle processes, is vital for the health of any community. This study explores the feasibility of using solar energy for a drinking water treatment plant (DWTP) with the long-term goal of energy independence and sustainability. A 10 MGD groundwater DWTP in southwestern US was selected, using the treatment processes of coagulation, filtration and chlorination. Energy consumption in units of kWh/day and kWh/MG for each unit process was separately determined using industry accepted design criteria. Associated carbon emissions were evaluated in units of CO2 eq/MG. Based on the energy consumption and the existing real estate holdings, the DWTP was sized for distributed solar. Results showed that overall the motors used to operate the pumps including the groundwater intake pumps were the largest consumers of energy. Enough land was available around DWTP to deploy distributed solar. Results also showed that solar photovoltaics could potentially be used to meet the energy demands of the selected DWTP, but warrant the use of a large storage capacity, and thus increased costs. Carbon emissions related to solar based design were negligible compared to the original case. For future, this study can be used to analyze unit processes of other DWTP based on energy consumption, as well as for incorporating sustainability into the DWTP design.

  3. Photocatalytic Water Treatment by Titanium Dioxide: Recent Updates

    Directory of Open Access Journals (Sweden)

    Manoj A. Lazar

    2012-12-01

    Full Text Available Photocatalytic water treatment using nanocrystalline titanium dioxide (NTO is a well-known advanced oxidation process (AOP for environmental remediation. With the in situ generation of electron-hole pairs upon irradiation with light, NTO can mineralize a wide range of organic compounds into harmless end products such as carbon dioxide, water, and inorganic ions. Photocatalytic degradation kinetics of pollutants by NTO is a topic of debate and the mostly reporting Langmuir-Hinshelwood kinetics must accompanied with proper experimental evidences. Different NTO morphologies or surface treatments on NTO can increase the photocatalytic efficiency in degradation reactions. Wisely designed photocatalytic reactors can decrease energy consumption or can avoid post-separation stages in photocatalytic water treatment processes. Doping NTO with metals or non-metals can reduce the band gap of the doped catalyst, enabling light absorption in the visible region. Coupling NTO photocatalysis with other water-treatment technologies can be more beneficial, especially in large-scale treatments. This review describes recent developments in the field of photocatalytic water treatment using NTO.

  4. Drinking water contamination and treatment techniques

    Science.gov (United States)

    Sharma, S.; Bhattacharya, A.

    2016-08-01

    Water is of fundamental importance for life on earth. The synthesis and structure of cell constituents and transport of nutrients into the cells as well as body metabolism depend on water. The contaminations present in water disturb the spontaneity of the mechanism and result in long/short-term diseases. The probable contaminations and their possible routes are discussed in the present review. Continued research efforts result in some processes/technologies to remove the contaminations from water. The review includes concepts and potentialities of the technologies in a comprehensible form. It also includes some meaningful hybrid technologies and promising awaited technologies in coming years.

  5. Drinking water contamination and treatment techniques

    Science.gov (United States)

    Sharma, S.; Bhattacharya, A.

    2017-06-01

    Water is of fundamental importance for life on earth. The synthesis and structure of cell constituents and transport of nutrients into the cells as well as body metabolism depend on water. The contaminations present in water disturb the spontaneity of the mechanism and result in long/short-term diseases. The probable contaminations and their possible routes are discussed in the present review. Continued research efforts result in some processes/technologies to remove the contaminations from water. The review includes concepts and potentialities of the technologies in a comprehensible form. It also includes some meaningful hybrid technologies and promising awaited technologies in coming years.

  6. Use of radionuclides at small water purification plants and in industrial waste water treatment by radiation adsorption method

    Energy Technology Data Exchange (ETDEWEB)

    Brusentseva, S.A.; Egorov, G.F.; Shubin, V.N. [and others

    1993-12-31

    An irradiation technique for potable water treatment is described. Use of radionuclides as a source of radiation allows for the automation of the process. The treatment is considered to be effective in waste water treatment to remove phenols, pesticides, and other toxic compounds.

  7. Using phytoremediation technologies to upgrade waste water treatment in Europe.

    Science.gov (United States)

    Schröder, Peter; Navarro-Aviñó, Juan; Azaizeh, Hassan; Goldhirsh, Avi Golan; DiGregorio, Simona; Komives, Tamas; Langergraber, Günter; Lenz, Anton; Maestri, Elena; Memon, Abdul R; Ranalli, Alfonso; Sebastiani, Luca; Smrcek, Stanislav; Vanek, Tomas; Vuilleumier, Stephane; Wissing, Frieder

    2007-11-01

    industrial processes. The EU should stimulate research to upgrade existing waste water treatment by implementing phytoremediation modules and demonstrating their reliability to the public.

  8. Linking ceragenins to water-treatment membranes to minimize biofouling.

    Energy Technology Data Exchange (ETDEWEB)

    Hibbs, Michael R.; Altman, Susan Jeanne; Feng, Yanshu (Brigham Young University, Provo, Utah); Savage, Paul B. (Brigham Young University, Provo, Utah); Pollard, Jacob (Brigham Young University, Provo, Utah); Branda, Steven S.; Goeres, Darla (Montana State University, Bozeman, MT); Buckingham-Meyer, Kelli (Montana State University, Bozeman, MT); Stafslien, Shane (North Dakota State University, Fargo, ND); Marry, Christopher; Jones, Howland D. T.; Lichtenberger, Alyssa; Kirk, Matthew F.; McGrath, Lucas K. (LMATA, Albuquerque, NM)

    2012-01-01

    Ceragenins were used to create biofouling resistant water-treatment membranes. Ceragenins are synthetically produced antimicrobial peptide mimics that display broad-spectrum bactericidal activity. While ceragenins have been used on bio-medical devices, use of ceragenins on water-treatment membranes is novel. Biofouling impacts membrane separation processes for many industrial applications such as desalination, waste-water treatment, oil and gas extraction, and power generation. Biofouling results in a loss of permeate flux and increase in energy use. Creation of biofouling resistant membranes will assist in creation of clean water with lower energy usage and energy with lower water usage. Five methods of attaching three different ceragenin molecules were conducted and tested. Biofouling reduction was observed in the majority of the tests, indicating the ceragenins are a viable solution to biofouling on water treatment membranes. Silane direct attachment appears to be the most promising attachment method if a high concentration of CSA-121a is used. Additional refinement of the attachment methods are needed in order to achieve our goal of several log-reduction in biofilm cell density without impacting the membrane flux. Concurrently, biofilm forming bacteria were isolated from source waters relevant for water treatment: wastewater, agricultural drainage, river water, seawater, and brackish groundwater. These isolates can be used for future testing of methods to control biofouling. Once isolated, the ability of the isolates to grow biofilms was tested with high-throughput multiwell methods. Based on these tests, the following species were selected for further testing in tube reactors and CDC reactors: Pseudomonas ssp. (wastewater, agricultural drainage, and Colorado River water), Nocardia coeliaca or Rhodococcus spp. (wastewater), Pseudomonas fluorescens and Hydrogenophaga palleronii (agricultural drainage), Sulfitobacter donghicola, Rhodococcus fascians, Rhodobacter

  9. Essentials of water systems design in the oil, gas, and chemical processing industries

    CERN Document Server

    Bahadori, Alireza; Boyd, Bill

    2013-01-01

    Essentials of Water Systems Design in the Oil, Gas and Chemical Processing Industries provides valuable insight for decision makers by outlining key technical considerations and requirements of four critical systems in industrial processing plants—water treatment systems, raw water and plant water systems, cooling water distribution and return systems, and fire water distribution and storage facilities. The authors identify the key technical issues and minimum requirements related to the process design and selection of various water supply systems used in the oil, gas, and chemical processing industries. This book is an ideal, multidisciplinary work for mechanical engineers, environmental scientists, and oil and gas process engineers.

  10. Treatment of Sewer Water Using Alum Salt

    OpenAIRE

    Qaid M. Saleem; Yousif Mohamed Algamal; Majed H. Shtaiwi; Mohammad S. Aldahmashi

    2014-01-01

    This investigation was carried out to study the effect of addition of different concentrations of alum salt used in the treatment of sewer water of the pond and also to study the physico-chemical parameters such as pH ,electrical conductivity ,salinity and total sediments besides that the bacteriological analysis such as total viable count (TVC) or standard plate count (SPC) and total coliform count (MPN) content were analysed in the water sample collected from the pond estimation of viable...

  11. MSWT-01, flood disaster water treatment solution from common ideas

    Science.gov (United States)

    Ananto, Gamawan; Setiawan, Albertus B.; Z, Darman M.

    2013-06-01

    Indonesia has a lot of potential flood disaster places with clean water problems faced. Various solution programs always initiated by Government, companies CSR, and people sporadical actions to provide clean water; with their advantages and disadvantages respectively. One solution is easy to operate for instance, but didn't provide adequate capacity, whereas the other had ideal performance but more costly. This situation inspired to develop a water treatment machine that could be an alternative favor. There are many methods could be choosed; whether in simple, middle or high technology, depends on water source input and output result quality. MSWT, Mobile Surface Water Treatment, is an idea for raw water in flood area, basically made for 1m3 per hour. This water treatment design adopted from combined existing technologies and related literatures. Using common ideas, the highlight is how to make such modular process put in compact design elegantly, and would be equipped with mobile feature due to make easier in operational. Through prototype level experiment trials, the machine is capable for producing clean water that suitable for sanitation and cooking/drinking purposes although using contaminated water input source. From the investment point of view, such machine could be also treated as an asset that will be used from time to time when needed, instead of made for project approach only.

  12. Microwaves energy in curing process of water glass molding sands

    Directory of Open Access Journals (Sweden)

    Granat K.

    2007-01-01

    Full Text Available This work presents the results of investigation of microwave heating on hardening process of water glass molding sands. Essential influence of this heating process on basic properties such as: compression, bending and tensile strength as well as permeability and abrasion resistance has been found. It has been proved, that all investigated sorts of sodium water glass with a module between 2.0 and 3.3 can be used as a binder of molding sands in microwave curing process. It has been found during analysis of research results of sands with 2.5 % water glass addition that they are practically the same as in case of identical molding sands dried for 120 minutes at the temperature of 110°C, used for comparative purposes. Application of microwave curing of molding sands with water glass, however, guarantees reduction of hardening time (from 120 to 4 minutes as well as significant reduction of energy consumption. Attempts of two stage hardening of the investigated water glass molding sands have also been carried out, that is after an initial hardening during a classical CO2 process (identical sands have also been tested for comparison after CO2 blowing process and additional microwave heating. It has been found that application of this kind of treatment for curing sands with 2.5 % sodium water glass content and module from 2.0 up to 3.3 results in the improvement of properties in comparison to classical CO2 process.

  13. Advanced Methods for Treatment of Organic Compounds Contamined Water

    Directory of Open Access Journals (Sweden)

    PREDESCU Andra

    2009-08-01

    Full Text Available The progress recorded in the field of science and advanced engineering at nanometric scale supplies largeopportunities for more efficient (from the point of view of the costs and more ecological approach of the processes ofwater purifying. This paper delivers a short description of the possibilities of using advanced materials in purifying thecontamined water with toxic metallic ions, organic and anorganic compounds. The opportunities and challenges werealso emphasized when nanomaterials were used for the surface, underground and industrial used waters treatment.

  14. Some Aspects of Surface Water Treatment Technology in Tirana Drinking Water Treatment Plant

    OpenAIRE

    , Tania Floqi; , Aleksandër Trajçe; , Daut Vezi

    2009-01-01

    Tirana’s Bovilla treatment plant was the Şrst of its kind for Albania, which treats surface water. The input water comes from the Bovilla artiŞcial lake, around which, the presence of villages induces pollution in the surface water and therefore affects the efŞciency of treatment plant and consequently the quality of drinking water. The treatment plant is a simple conventional system and includes pre-oxidation, coagulation, şocculation & sedimentation, fast Şltration, post-oxidation. ...

  15. Factors influencing biological treatment of MTBE contaminated ground water

    Energy Technology Data Exchange (ETDEWEB)

    Stringfellow, William T.; Hines Jr., Robert D.; Cockrum, Dirk K.; Kilkenny, Scott T.

    2001-09-14

    Methyl tert-butyl ether (MTBE) contamination has complicated the remediation of gasoline contaminated sites. Many sites are using biological processes for ground water treatment and would like to apply the same technology to MTBE. However, the efficiency and reliability of MTBE biological treatment is not well documented. The objective of this study was to examine the operational and environmental variables influencing MTBE biotreatment. A fluidized bed reactor was installed at a fuel transfer station and used to treat ground water contaminated with MTBE and gasoline hydrocarbons. A complete set of chemical and operational data was collected during this study and a statistical approach was used to determine what variables were influencing MTBE treatment efficiency. It was found that MTBE treatment was more sensitive to up-set than gasoline hydrocarbon treatment. Events, such as excess iron accumulation, inhibited MTBE treatment, but not hydrocarbon treatment. Multiple regression analysis identified biomass accumulation and temperature as the most important variables controlling the efficiency of MTBE treatment. The influent concentration and loading of hydrocarbons, but not MTBE, also impacted MTBE treatment efficiency. The results of this study suggest guidelines for improving MTBE treatment. Long cell retention times in the reactor are necessary for maintaining MTBE treatment. The onset of nitrification only occurs when long cell retention times have been reached and can be used as an indicator in fixed film reactors that conditions favorable to MTBE treatment exist. Conversely, if the reactor can not nitrify, it is unlikely to have stable MTBE treatment.

  16. Coagulation-flocculation pretreatment of oil sands process affected water

    Energy Technology Data Exchange (ETDEWEB)

    Pourrezaei, P.; El-Din, M.G. [Alberta Univ., Edmonton, AB (Canada). Dept. of Civil and Environmental Engineering

    2008-07-01

    This presentation addressed the issue of water use in the oil sands industry and efforts to use this limited resource more efficiently. Three wastewater treatment schemes for oil sands tailings ponds were proposed, notably primary, secondary and tertiary treatment. Primary treatment involves the removal of suspended solids using physical-chemical treatments. Secondary treatment involves the removal of dissolved solids and organics using chemical oxidation, ultrafiltration or nanofiltration. Tertiary treatment involves removal of residual organics/solids using biological activated carbon filtration, sand filtration or reverse osmosis. The composition of oil sands process water (OSPW) was also discussed with reference to suspended solids, salts, hydrocarbons, other dissolved organics (such as naphthenic acids and phenols), ammonia, inorganic compounds and trace elements. The conventional coagulation/flocculation process is essential in industrial wastewater treatment. It is cost effective, easy to operate and energy efficient. The process is used because small suspended and colloidal particles and dissolved constituents cannot be removed quickly by sedimentation. A chemical method must be used. Coagulation/flocculation brings small suspended and colloidal particles into contact so that they collide, stick and grow to a size that settles readily. Alum is the predominant and least expensive water treatment coagulant used for the coagulation/flocculation process. It provides positively charged ions to neutralize the negative charge of colloidal particles resulting in aggregation. It creates big settling flocs that enmesh colloids as it settles. The factors affecting the process include pH, chemical type, chemical concentration, rapid mixing intensity, slow mixing intensity and time. tabs., figs.

  17. Synthesis and Design of Integrated Process and Water Networks

    DEFF Research Database (Denmark)

    2015-01-01

    possible options with respect to the topology of the process and water networks, leading to Mixed Integer Non Linear Programming (MINLP) problem. A solution strategy to solve the multi-network problem accounts explicitly the interactions between the networks by selecting suitable technologies in order......This work presents the development of a systematic framework for a simultaneous synthesis and design of process and water networks using the superstructure-based optimization approach. In this framework, a new superstructure combining both networks is developed by attempting to consider all...... to transform raw materials into products and produce clean water to be reused in the process at the early stage of design. Since the connection between the process network and the wastewater treatment network is not a straight forward connection, a new converter interval is introduced in order to convert...

  18. F- and H-Area Seepage Basins Water Treatment System Process Optimization and Alternative Chemistry Ion Exchange/Sorbent Material Screening Clearwell Overflow Study

    Energy Technology Data Exchange (ETDEWEB)

    Serkiz, S.M.

    2000-08-30

    This study investigated alternative ion exchange/sorbent materials and polishing chemistries designed to remove specific radionuclides not removed during the neutralization/precipitation/clarification process.

  19. Design of Simple Water Treatment System for Cleaning Dirty Water in the Rural Area

    Science.gov (United States)

    Nandiyanto, A. B. D.; Haristiani, N.

    2017-03-01

    The purpose of this study was to introduce our simple home-made water treatment system for solving the clean water supply problem in rural area. We designed a water system using several materials: activated sand, activated carbon, manganese, and zeolite. As a model, we investigated the water treatment system on two wells that placed in one of the rural area (far from the main city) in West Java, Indonesia. Experimental results showed that our designed water treatment system succeeded to purify dirty water and the properties and the chemical composition of the purified water is fit with the minimum standard requirement of clean water. Analysis and discussion about the way for the cleaning water process were also presented in the paper. Finally, since the wells are installed in the elementary school and the water is typically used for daily life activity for the neighbour people, this water system can be used for educational purposes and the school can become a center of life in this rural area.

  20. Water-Energy Correlations: Analysis of Water Technologies, Processes and Systems in Rural and Urban India

    Science.gov (United States)

    Murumkar, A. R.; Gupta, S.; Kaurwar, A.; Satankar, R. K.; Mounish, N. K.; Pitta, D. S.; Virat, J.; Kumar, G.; Hatte, S.; Tripathi, R. S.; Shedekar, V.; George, K. J.; Plappally, A. K.

    2015-12-01

    In India, the present value of water, both potable and not potable, bears no relation to the energy of water production. However, electrical energy spent on ground water extraction alone is equivalent to the nation's hydroelectric capacity of 40.1 GWh. Likewise, desalinating 1m3 water of the Bay of Bengal would save three times the energy for potable ground water extraction along the coast of the Bay. It is estimated that every second woman in rural India expends 0.98 kWhe/m3/d for bringing water for household needs. Yet, the water-energy nexus remains to be a topic which is gravely ignored. This is largely caused by factors such as lack of awareness, defective public policies, and intrusive cultural practices. Furthermore, there are instances of unceasing dereliction towards water management and maintenance of the sparsely distributed water and waste water treatment plants across the country. This pollutes the local water across India apart from other geogenic impurities. Additionally, product aesthetics and deceptive advertisements take advantage of the abulia generated by users' ignorance of technical specifications of water technologies and processes in mismanagement of water use. Accordingly, urban residents are tempted to expend on energy intensive water technologies at end use. This worsens the water-energy equation at urban households. Cooking procedures play a significant role in determining the energy expended on water at households. The paper also evaluates total energy expense involved in cultivating some major Kharif and Rabi crops. Manual and traditional agricultural practices are more prominent than mechanized and novel agricultural techniques. The specific energy consumption estimate for different water technologies will help optimize energy expended on water in its life cycles. The implication of the present study of water-energy correlation will help plan and extend water management infrastructure at different locations across India.

  1. Treatment of Highly Turbid Water by Polyaluminum Ferric Chloride (PAFCL

    Directory of Open Access Journals (Sweden)

    Fazel Fazel Mohammadi-Moghaddam

    2015-10-01

    Full Text Available Background & Aims of the Study: In some situation like rainfall seasons raw water become very turbid so it affected the water treatment plant processes and quality of produced water. Treatment of very high turbid water has some concerns like precursors for disinfection by-products and very loading rate of particle on filter's media and consequently increases in water consumption for filter backwash. This paper investigates the performance of a composite inorganic polymer of aluminium and ferric salt, Polyaluminium ferric chloride (PAFCl, for the removal of turbidity, color and natural organic matter (NOM from high turbid water. Materials and Methods: Experiments were carried out by Jar test experiment by synthetic water samples with 250 and 500 NTU turbidity that prepared in laboratory. Results: The results of conventional jar test showed that the optimum pH for coagulation of water sample was 7.5 to 8 and optimum dosage of the coagulant was 10 mg/L. Removal efficiency of turbidity, color and UV adsorbent at 254 nm at optimum dose and pH without filtration was 99.92%, 100% and 80.6% respectively for first sample (250 NTU and 99.95%, 99.49% and 84.77 for second sample (500 NTU respectively. Conclusion: It concluded that polyaluminium ferric chloride has a very good efficiency for the removal of turbidity, color and organic matter in high turbid water. Also it can be select as a coagulant for high turbid water and some waste water from water treatment plant like filter backwash water.

  2. Treatment for hydrazine-containing waste water solution

    Science.gov (United States)

    Yade, N.

    1986-01-01

    The treatment for waste solutions containing hydrazine is presented. The invention attempts oxidation and decomposition of hydrazine in waste water in a simple and effective processing. The method adds activated charcoal to waste solutions containing hydrazine while maintaining a pH value higher than 8, and adding iron salts if necessary. Then, the solution is aerated.

  3. POU/POE TREATMENT OF ARSENIC IN GROUND WATER

    Science.gov (United States)

    Point-of-use/Point-of-entry (POU/POE) arsenic removal systems were installed in seventeen homes that were found to have high levels of arsenic (50-480ug/L) in their well water. This presetation will describe the process and the problems encountered in selecting the treatment syst...

  4. Radioactive Dry Process Material Treatment Technology Development

    Energy Technology Data Exchange (ETDEWEB)

    Park, J. J.; Hung, I. H.; Kim, K. K. (and others)

    2007-06-15

    The project 'Radioactive Dry Process Material Treatment Technology Development' aims to be normal operation for the experiments at DUPIC fuel development facility (DFDF) and safe operation of the facility through the technology developments such as remote operation, maintenance and pair of the facility, treatment of various high level process wastes and trapping of volatile process gases. DUPIC Fuel Development Facility (DFDF) can accommodate highly active nuclear materials, and now it is for fabrication of the oxide fuel by dry process characterizing the proliferation resistance. During the second stage from march 2005 to February 2007, we carried out technology development of the remote maintenance and the DFDF's safe operation, development of treatment technology for process off-gas, and development of treatment technology for PWR cladding hull and the results was described in this report.

  5. Nanotechnology for a safe and sustainable water supply: enabling integrated water treatment and reuse.

    Science.gov (United States)

    Qu, Xiaolei; Brame, Jonathon; Li, Qilin; Alvarez, Pedro J J

    2013-03-19

    Ensuring reliable access to clean and affordable water is one of the greatest global challenges of this century. As the world's population increases, water pollution becomes more complex and difficult to remove, and global climate change threatens to exacerbate water scarcity in many areas, the magnitude of this challenge is rapidly increasing. Wastewater reuse is becoming a common necessity, even as a source of potable water, but our separate wastewater collection and water supply systems are not designed to accommodate this pressing need. Furthermore, the aging centralized water and wastewater infrastructure in the developed world faces growing demands to produce higher quality water using less energy and with lower treatment costs. In addition, it is impractical to establish such massive systems in developing regions that currently lack water and wastewater infrastructure. These challenges underscore the need for technological innovation to transform the way we treat, distribute, use, and reuse water toward a distributed, differential water treatment and reuse paradigm (i.e., treat water and wastewater locally only to the required level dictated by the intended use). Nanotechnology offers opportunities to develop next-generation water supply systems. This Account reviews promising nanotechnology-enabled water treatment processes and provides a broad view on how they could transform our water supply and wastewater treatment systems. The extraordinary properties of nanomaterials, such as high surface area, photosensitivity, catalytic and antimicrobial activity, electrochemical, optical, and magnetic properties, and tunable pore size and surface chemistry, provide useful features for many applications. These applications include sensors for water quality monitoring, specialty adsorbents, solar disinfection/decontamination, and high performance membranes. More importantly, the modular, multifunctional and high-efficiency processes enabled by nanotechnology provide a

  6. 不同水处理工艺的自来水出厂水中有机物的遗传毒性%Genotoxicity of organic extracts from finished water with different treatment process in six water plants

    Institute of Scientific and Technical Information of China (English)

    方道奎; 余淑苑; 张隽; 张振; 周国宏; 李思果; 吴辉; 翟卉; 唐非

    2011-01-01

    目的:检测和评价某市6家A,B,C,D,E和F厂采用不同水处理工艺自来水厂出厂水中有机物的遗传毒性.方法通过鼠伤寒沙门菌致突变实验、微核实验及微量波动实验检测与比较各水样中有机物的致突变性.结果:6家自来水厂出厂水中有机物的鼠伤寒沙门菌致突变实验结果均为阳性;各厂出厂水中有机物诱导的小鼠骨髓细胞微核率由高至低依次为:D>E=A>C>F>B;C厂后加氯单元出水中有机物在每板0.25L的剂量下,微量波动实验对于TA98,TA100均出现阳性结果,并且各剂量的阳性反应孔存在明显的剂量反应关系(P<0.05).结论:某市6家自来水厂出厂水中的有机物具有明显的致突变作用,且以移码突变为主;微核实验与Ames实验对水中有机物遗传毒性检测与评价结果基本一致;微量波动实验可提高对水中有机物致突变性检测的灵敏度.%OBJECTIVE To explore the genotoxicity of organic extracts from finished water in 6 water plants A, B, C, D, E and F in a particular city. METHODS The following in vitro and in vivo tests were conducted: Ames test with Salmonella typhimurium strains TA98 and TA100 with and without mammalian S9 activation component, microscale fluctuation test with S. typhimurium strains TA98 and TA100 without mammalian S9 activation component, and mouse micronucleus test in mice polychromatic erythrocyte (PCE) stem cells. RESULTS Positive results were obtained by Ames test and micronucleus assay from all the finished water samples in six water plants. The micronucleus frequency was shown in the following order: D > E = A > C > F > B. Microscale fluctuation test showed that at the concentration of 0.25 L every plate and after post-chlorination treatment of plant C, the positive results in TA98 ( - S9 ) and TA100 ( - S9 ) ( P < 0. 05 ) were obtained.CONCLUSION Mutagenicity of finished water from 6 water plants in this city is relatively high and the type of mutagenicity

  7. Underwater plasma discharge and its water treatment applications

    Science.gov (United States)

    Ma, Sukhwal; Huh, Jin Young; Kim, Kangil; Hong, Yong Cheol; National Fusion Research Institute Team; Chonbuk National University Team; Kwangwoon University Team; NPAC Team

    2016-09-01

    In recent, the quality of water has been exacerbated by the influx of wastewater and water pollutants. There have been frequent occurrences of water blooms due to the eutrophication of river. Therefore, the needs for water treatment are increased through effective and environment-friendly method. In this work, we propose the plasma system to overcome the problems mentioned above using underwater discharge plasma. The underwater discharges are generated by capillary electrode, and have the advantages of low cost, high efficiency and eco-friendly processing. The proposed technologies can be suitable for eliminating cyanobacteria, decreasing the concentration of oil dissolved in water, and purifying wastewater. Cyanobacteria is killed directly by the underwater discharge and water-dissolved oil and heavy-metal wastewater are purified by coagulation effect, which may result from the chemical reactions of underwater plasma. Consequently, these technologies using underwater discharge can be alternative methods to replace the existing technologies.

  8. Multiphase simulation of mine waters and aqueous leaching processes

    Directory of Open Access Journals (Sweden)

    Pajarre Risto

    2016-01-01

    Full Text Available Managing of large amounts of water in mining and mineral processing sites remains a concern in both actively operated and closed mining areas. When the mining site with its metal or concentrate producing units is operational, the challenge is to find either ways for economical processing with maximum yields, while minimizing the environmental impact of the water usage and waste salt treatments. For safe closure of the site, the environmental control of possible drainage will be needed. For both challenges, the present-day multiphase process simulations tools can be used to provide improved accuracy and better economy in controlling the smooth and environmentally sound operation of the plant. One of the pioneering studies in using the multiphase thermodynamic software in simulation of hydrometallurgical processes was that of Koukkari et al. [1]. The study covered the use of Solgasmix equilibrium software for a number of practical acid digesters. The models were made for sulfuric acid treatments in titania pigment production and in NPK fertilizer manufacturing. During the past two decades the extensive data assessment has taken place particularly in geochemistry and a new versions of geochemical multiphase equilibrium software has been developed. On the other hand, there has been some progress in development of the process simulation software in all the aforementioned fields. Thus, the thermodynamic simulation has become a tool of great importance in development of hydrometallurgical processes. The presentation will cover three example cases of either true pilot or industrial systems including a South African acid mine water drainage treatment, hydrometallurgical extraction of rare earths from uranium leachate in Russia and a multistage process simulation of a Finnish heap leaching mine with its subsequent water treatment system.

  9. Cellulose nanomaterials in water treatment technologies.

    Science.gov (United States)

    Carpenter, Alexis Wells; de Lannoy, Charles-François; Wiesner, Mark R

    2015-05-05

    Cellulose nanomaterials are naturally occurring with unique structural, mechanical and optical properties. While the paper and packaging, automotive, personal care, construction, and textiles industries have recognized cellulose nanomaterials' potential, we suggest cellulose nanomaterials have great untapped potential in water treatment technologies. In this review, we gather evidence of cellulose nanomaterials' beneficial role in environmental remediation and membranes for water filtration, including their high surface area-to-volume ratio, low environmental impact, high strength, functionalizability, and sustainability. We make direct comparison between cellulose nanomaterials and carbon nanotubes (CNTs) in terms of physical and chemical properties, production costs, use and disposal in order to show the potential of cellulose nanomaterials as a sustainable replacement for CNTs in water treatment technologies. Finally, we comment on the need for improved communication and collaboration across the myriad industries invested in cellulose nanomaterials production and development to achieve an efficient means to commercialization.

  10. Sonication for advanced drinking water treatment

    Institute of Scientific and Technical Information of China (English)

    ZHANG Guang-ming; WEI Xi-zhu; LI Xiang-kun; ZHANG Jie; DOU Zi-bo

    2009-01-01

    This paper investigated the feasibility of sonication as an advanced treatment method for drinking water production and used comprehensive indexes of water quality to examine its efficiency. Results show that sonication significantly reduces the toxicity of water. Sonication with 5 W/L at 90 kHz lasting for 30 min decreases he water SUVA and the disinfection byproduct formation potential (DBPFP) by 38.7% and 27.2% respective ly. Sonieation also decreases the UV254 by more than 50% through destroying unsaturated chemical bonds.Higher sound intensity and higher frequency benefit the reduction of TOC and UV254, Besides, sonication significantly increases the affinity of organics with granular activated carbon (GAC), and thus the hybrid sonication-GAC method reduces the water TOC, COD, UV254, and DBPFP by 78. 3%, 69.4%, 75.7%, and 70. 0% respectively. Therefore, sonieation and the hybrid sonieation-GAC method are proposed as advanced treatment methods for drinking water.

  11. Treatment for purification water of biodiesel using electrofloculation

    Directory of Open Access Journals (Sweden)

    Juliana Ferreira de Brito

    2012-01-01

    Full Text Available Biodiesel was created as a solution for a great economic and enviromental problem of petroleum, a resource with sustainable characteristics. But its production still needs optimization, because it uses a lot of water and generates a large volume of this residue, which appears improper to disposal without correct treatment. This work propose an economic, viable and efficient way to treat the Biodiesel purification water, not only aiming at a proper disposal, but the reuse as input in the process, generating a large industrial economy, and greater environmental progress. For both treatment uses the electrofloculation technique.

  12. Improving the process of preparing waste water at Kamennolozhskiy UPPN

    Energy Technology Data Exchange (ETDEWEB)

    Abashev, R.G.

    1982-01-01

    The main reasons are examined for low efficient operation of treatment works at the Kamennolozhskiy UPPN and efficient ways to improve quality of waste water by introducing separate collection and preparation of individual types of water, organization of preliminary discharge at the main structures and pinpointing the duration of settling. The process of settling was studied on waste water under field conditions using sampling from a strictly defined level of the settling tank in definite time intervals and analysis of samples for the content of mechanical admixtures and petroleum products. The duration of settling in the reservoir was corrected according to the curve for the dependence of the contaminant content in the waste water on the duration of settling. It was indicated that introduction of recommendations guarantees quality of water of the required condition for injection into productive beds to maintain bed pressure.

  13. 合流污水处理系统中水回用改建工程的效果分析%Process and Effect Analysis of Reclaimed Water Reuse Reconstruction Project in Combined Sewerage Treatment System

    Institute of Scientific and Technical Information of China (English)

    林翌栋; 程晓波; 王松

    2011-01-01

    The reconstruction process of realizing reclaimed water reuse on combined sewer advanced treatment was introduced.Basing on the practical case of reconstruction project of the Pengyuepu substation, new and old techniques were compared and the actual effect of new techniques was analyzed.Result shows the sewage of combined sewer treatment after reconstruction meets the standard of reclaimed water reuse and can satisfy the demand of vehicle washing and greening.%介绍了实现中水回用的合流污水深度处理改建过程.结合上海合流污水管理所彭越浦分所内原中水回用设施改造的实际案例,对比了新老工艺并分析了新工艺的实际效果.结果表明污水经改建后的合流污水处理可达到中水回用标准,同时可以满足周边停车场车辆清洗和附近绿化的用水需求.

  14. Enhanced drinking water supply through harvested rainwater treatment

    Science.gov (United States)

    Naddeo, Vincenzo; Scannapieco, Davide; Belgiorno, Vincenzo

    2013-08-01

    Decentralized drinking water systems represent an important element in the process of achieving the Millennium Development Goals, as centralized systems are often inefficient or nonexistent in developing countries. In those countries, most water quality related problems are due to hygiene factors and pathogens. A potential solution might include decentralized systems, which might rely on thermal and/or UV disinfection methods as well as physical and chemical treatments to provide drinking water from rainwater. For application in developing countries, decentralized systems major constraints include low cost, ease of use, environmental sustainability, reduced maintenance and independence from energy sources. This work focuses on an innovative decentralized system that can be used to collect and treat rainwater for potable use (drinking and cooking purposes) of a single household, or a small community. The experimented treatment system combines in one compact unit a Filtration process with an adsorption step on GAC and a UV disinfection phase in an innovative design (FAD - Filtration Adsorption Disinfection). All tests have been carried out using a full scale FAD treatment unit. The efficiency of FAD technology has been discussed in terms of pH, turbidity, COD, TOC, DOC, Escherichia coli and Total coliforms. FAD technology is attractive since it provides a total barrier for pathogens and organic contaminants, and reduces turbidity, thus increasing the overall quality of the water. The FAD unit costs are low, especially if compared to other water treatment technologies and could become a viable option for developing countries.

  15. Water recovery and solid waste processing for aerospace and domestic applications. Volume 1: Final report

    Science.gov (United States)

    Murray, R. W.

    1973-01-01

    A comprehensive study of advanced water recovery and solid waste processing techniques employed in both aerospace and domestic or commercial applications is reported. A systems approach was used to synthesize a prototype system design of an advanced water treatment/waste processing system. Household water use characteristics were studied and modified through the use of low water use devices and a limited amount of water reuse. This modified household system was then used as a baseline system for development of several water treatment waste processing systems employing advanced techniques. A hybrid of these systems was next developed and a preliminary design was generated to define system and hardware functions.

  16. Comet assay with gill cells of Mytilus galloprovincialis end point tools for biomonitoring of water antibiotic contamination: Biological treatment is a reliable process for detoxification.

    Science.gov (United States)

    Mustapha, Nadia; Zouiten, Amina; Dridi, Dorra; Tahrani, Leyla; Zouiten, Dorra; Mosrati, Ridha; Cherif, Ameur; Chekir-Ghedira, Leila; Mansour, Hedi Ben

    2016-04-01

    This article investigates the ability of Pseudomonas peli to treat industrial pharmaceuticals wastewater (PW). Liquid chromatography-mass spectrometry (MS)/MS analysis revealed the presence, in this PW, of a variety of antibiotics such as sulfathiazole, sulfamoxole, norfloxacine, cloxacilline, doxycycline, and cefquinome.P. peli was very effective to be grown in PW and inducts a remarkable increase in chemical oxygen demand and biochemical oxygen demand (140.31 and 148.51%, respectively). On the other hand, genotoxicity of the studied effluent, before and after 24 h of shaking incubation with P. peli, was evaluated in vivo in the Mediterranean wild mussels Mytilus galloprovincialis using comet assay for quantification of DNA fragmentation. Results show that PW exhibited a statistically significant (pcomet assay genotoxicity end points are useful tools to biomonitor the physicochemical and biological quality of water. Also, it could be concluded that P. peli can treat and detoxify the studied PW.

  17. ANAEROBIC BIOLOGICAL TREATMENT OF PRODUCED WATER

    Energy Technology Data Exchange (ETDEWEB)

    John R. Gallagher

    2001-07-31

    During the production of oil and gas, large amounts of water are brought to the surface and must be disposed of in an environmentally sensitive manner. This is an especially difficult problem in offshore production facilities where space is a major constraint. The chief regulatory criterion for produced water is oil and grease. Most facilities have little trouble meeting this criterion using conventional oil-water separation technologies. However, some operations have significant amounts of naphthenic acids in the water that behave as oil and grease but are not well removed by conventional technologies. Aerobic biological treatment of naphthenic acids in simulated-produced water has been demonstrated by others; however, the system was easily overloaded by the large amounts of low-molecular-weight organic acids often found in produced waters. The objective of this research was to determine the ability of an anaerobic biological system to treat these organic acids in a simulated produced water and to examine the potential for biodegradation of the naphthenic acids in the anaerobic environment. A small fixed-film anaerobic biological reactor was constructed and adapted to treat a simulated produced water. The bioreactor was tubular, with a low-density porous glass packing material. The inocula to the reactor was sediment from a produced-water holding pond from a municipal anaerobic digester and two salt-loving methanogenic bacteria. During start-up, the feed to the reactor contained glucose as well as typical produced-water components. When glucose was used, rapid gas production was observed. However, when glucose was eliminated and the major organic component was acetate, little gas was generated. Methane production from acetate may have been inhibited by the high salt concentrations, by sulfide, or because of the lack, despite seeding, of microbes capable of converting acetate to methane. Toluene, a minor component of the produced water (0.1 g/L) was removed in the

  18. Advances in chemical technologies for water and wastewater treatment: preface

    Institute of Scientific and Technical Information of China (English)

    Xiaochang WANG

    2009-01-01

    @@ Chemical technologies have been applied for water and wastewater treatment since more than 150 year ago, and are still playing the leading role in this field. With the fast development of sciences and technologies especially in the last two decades, chemical technologies which are applicable for solving water quality and water environmental problems underwent a great development not only in traditional areas such as coagulation, solid/liquid separation, oxidation, adsorption etc., but also in the emerging multidisciplinary fields. Nowadays, an increasing number of chemists and chemical engineers has broadened research interests. Biochemical/biological technologies, ecological technologies and process modeling and simulation have become important branches of chemical technologies. Such a tendency has been well reflected in the activities of the Group of Chemists for Water and Wastewater Treatment (GCWWT), a subdivision of Chinese Chemical Society (CCS).

  19. Large area radiation source for water and wastewater treatment

    Science.gov (United States)

    Mueller, Michael T.; Lee, Seungwoo; Kloba, Anthony; Hellmer, Ronald; Kumar, Nalin; Eaton, Mark; Rambo, Charlotte; Pillai, Suresh

    2011-06-01

    There is a strong desire for processes that improve the safety of water supplies and that minimize disinfection byproducts. Stellarray is developing mercury-free next-generation x-ray and UV-C radiation sources in flat-panel and pipe form factors for water and wastewater treatment applications. These new radiation sources are designed to sterilize sludge and effluent, and to enable new treatment approaches to emerging environmental concerns such as the accumulation of estrogenic compounds in water. Our UV-C source, based on cathodoluminescent technology, differs significantly from traditional disinfection approaches using mercury arc lamps or UV LEDs. Our sources accelerate electrons across a vacuum gap, converting their energy into UV-C when striking a phosphor, or x-rays when striking a metallic anode target. Stellarray's large area radiation sources for wastewater treatment allow matching of the radiation source area to the sterilization target area for maximum coverage and improved efficiency.

  20. Studies on water treatment by adsorption. Kyuchaku ni yoru mizushori

    Energy Technology Data Exchange (ETDEWEB)

    Suzuki, M. (The University of Tokyo, Tokyo (Japan). Institute of Industrial Science)

    1994-06-05

    This paper summarizes studies on the water treatment by adsorption, as for the adsorption during water treatment, reactivation of activated charcoal, and clarification of heating process. Reactivation of activated charcoal for the water treatment is carried out through drying in the heating furnace. Basic problems are the recovery degree of adsorption performance of reactivated activated charcoal and the recovery yield. Behavior of the activated charcoal in the heating reactivation furnace is divided into three stages including drying process, heating process, and gasification process. Among these processes, behaviors of organic matters during heating process are described. Thermogravimetric analyses (TGA) were conducted for activated charcoals adsorbing various organic matters in aqueous solutions. Three types of organic matters were classified from the TGA pattern, i.e., organic matters with relatively low boiling point (type-I), organic matters with higher boiling point (type-II), and phenol and lignin (type-III). Organic matters belonging to type-I and type-II are desorbed or decomposed, to be disappeared. Effectiveness of alkali cleaning is suggested for the type-III organic matters. 3 refs., 5 figs.

  1. Nanofiltration technology in water treatment and reuse: applications and costs.

    Science.gov (United States)

    Shahmansouri, Arash; Bellona, Christopher

    2015-01-01

    Nanofiltration (NF) is a relatively recent development in membrane technology with characteristics that fall between ultrafiltration and reverse osmosis (RO). While RO membranes dominate the seawater desalination industry, NF is employed in a variety of water and wastewater treatment and industrial applications for the selective removal of ions and organic substances, as well as certain niche seawater desalination applications. The purpose of this study was to review the application of NF membranes in the water and wastewater industry including water softening and color removal, industrial wastewater treatment, water reuse, and desalination. Basic economic analyses were also performed to compare the profitability of using NF membranes over alternative processes. Although any detailed cost estimation is hampered by some uncertainty (e.g. applicability of estimation methods to large-scale systems, labor costs in different areas of the world), NF was found to be a cost-effective technology for certain investigated applications. The selection of NF over other treatment technologies, however, is dependent on several factors including pretreatment requirements, influent water quality, treatment facility capacity, and treatment goals.

  2. Performance of small water treatment plants: The case study of Mutshedzi Water Treatment Plant

    Science.gov (United States)

    Makungo, R.; Odiyo, J. O.; Tshidzumba, N.

    The performance of small water treatment plants (SWTPs) was evaluated using Mutshedzi WTP as a case study. The majority of SWTPs in South Africa (SA) that supply water to rural villages face problems of cost recovery, water wastages, limited size and semi-skilled labour. The raw and final water quality analyses and their compliance were used to assess the performance of the Mutshedzi WTP. Electrical conductivity (EC), pН and turbidity were measured in the field using a portable multimeter and a turbidity meter respectively. Atomic Absorption Spectrometry and Ion Chromatography were used to analyse metals and non-metals respectively. The results were compared with the Department of Water Affairs (DWA) guidelines for domestic use. The turbidity levels partially exceeded the recommended guidelines for domestic water use of 1 NTU. The concentrations of chemical parameters in final water were within the DWA guidelines for domestic water use except for fluoride, which exceeded the maximum allowable guideline of 1.5 mg/L in August 2009. Mutshedzi WTP had computed compliance for raw and final water analyses ranging from 79% to 93% and 86% to 93% throughout the sampling period, respectively. The results from earlier studies showed that the microbiological quality of final water in Mutshedzi WTP complied with the recommended guidelines, eliminating the slight chance of adverse aesthetic effects and infectious disease transmission associated with the turbidity values between 1 and 5 NTU. The study concluded that Mutshedzi WTP, though moving towards compliance, is still not producing adequate quality of water. Other studies also indicated that the quantity of water produced from Mutshedzi WTP was inadequate. The findings of the study indicate that lack of monitoring of quantity of water supplied to each village, dosage of treatment chemicals, the treatment capacity of the WTP and monitoring the quality of water treated are some of the factors that limit the performance of

  3. Carotenes in processed tomato after thermal treatment

    NARCIS (Netherlands)

    Luterotti, S.; Bicanic, D.D.; Markovic, K.; Franko, M.

    2015-01-01

    This report adds to the ongoing vivid dispute on the fate of carotenes in tomato upon thermal processing. Although many papers dealing with changes in the raw tomatoes during industrial treatment have already appeared, data on the fate of finished, processed tomato products when they are additionall

  4. Miniaturized Temperature-Controlled Planar Chromatography (Micro-TLC) as a Versatile Technique for Fast Screening of Micropollutants and Biomarkers Derived from Surface Water Ecosystems and During Technological Processes of Wastewater Treatment.

    Science.gov (United States)

    Ślączka-Wilk, Magdalena M; Włodarczyk, Elżbieta; Kaleniecka, Aleksandra; Zarzycki, Paweł K

    2017-07-01

    There is increasing interest in the development of simple analytical systems enabling the fast screening of target components in complex samples. A number of newly invented protocols are based on quasi separation techniques involving microfluidic paper-based analytical devices and/or micro total analysis systems. Under such conditions, the quantification of target components can be performed mainly due to selective detection. The main goal of this paper is to demonstrate that miniaturized planar chromatography has the capability to work as an efficient separation and quantification tool for the analysis of multiple targets within complex environmental samples isolated and concentrated using an optimized SPE method. In particular, we analyzed various samples collected from surface water ecosystems (lakes, rivers, and the Baltic Sea of Middle Pomerania in the northern part of Poland) in different seasons, as well as samples collected during key wastewater technological processes (originating from the "Jamno" wastewater treatment plant in Koszalin, Poland). We documented that the multiple detection of chromatographic spots on RP-18W microplates-under visible light, fluorescence, and fluorescence quenching conditions, and using the visualization reagent phosphomolybdic acid-enables fast and robust sample classification. The presented data reveal that the proposed micro-TLC system is useful, inexpensive, and can be considered as a complementary method for the fast control of treated sewage water discharged by a municipal wastewater treatment plant, particularly for the detection of low-molecular mass micropollutants with polarity ranging from estetrol to progesterone, as well as chlorophyll-related dyes. Due to the low consumption of mobile phases composed of water-alcohol binary mixtures (less than 1 mL/run for the simultaneous separation of up to nine samples), this method can be considered an environmentally friendly and green chemistry analytical tool. The described

  5. Selective Oxidation of Organic Compounds in Waste Water by ozone-based oxidation processes

    NARCIS (Netherlands)

    Boncz, M.A.

    2002-01-01

    For many different types of waste water, treatment systems have been implemented in the past decades. Waste water treatment is usually performed by biological processes, either aerobic or anaerobic, complemented with physical / chemical post treatment techniques. However, in so

  6. 泥渣回流对慢速脱碳处理城市中水的影响研究%The Study on the Effect of Recycling Activated Sludge Used to Slow Decarburization Treatment Process for City Water

    Institute of Scientific and Technical Information of China (English)

    韩琳; 尹萍; 程勇明; 魏强

    2014-01-01

    The effect using recycling activated sludge in slow decarburization treatment process is studied for city water .The results show that the right amount of recycling activated sludge can effectively improve the slow decarburization processing ef-ficiency .When the sludge reflux ratio is 10% ,the total alkalinity removal rate increases by 10% ,the hardness removal rate increases by 17% ,the COD removal rate increases by 11% compared with no recycling activated sludge .After treatment ,the water sample turbidity is 0 .76 NTU ,hardness is 3 .36 mmol/L ,alkalinity is 1 .55 mmol/L ,total phosphorus is 0 .07 mg/L and COD is 20 mg/L .%以城市中水作为试验水源,通过分析试验结果,研究了泥渣回流对慢速脱碳处理工艺的影响。结果表明,适量的泥渣回流能够有效提高慢速脱碳处理效率,在泥渣回流比为10%时,相比无泥渣回流,总碱度去除率提高10%,硬度去除率提高17%,COD去除率提高11%,处理后水样浊度为0.76NTU ,硬度为3.36 mmol/L ,碱度为1.55 mmol/L ,总磷为0.07 mg/L ,COD为20 mg/L。

  7. Process for the treatment of lignocellulosic biomass

    Science.gov (United States)

    Dale, Bruce E.

    2014-07-08

    A process for the treatment of biomass to render structural carbohydrates more accessible and/or digestible using concentrated ammonium hydroxide with or without anhydrous ammonia addition, is described. The process preferably uses steam to strip ammonia from the biomass for recycling. The process yields of monosaccharides from the structural carbohydrates are good, particularly as measured by the enzymatic hydrolysis of the structural carbohydrates. The monosaccharides are used as animal feeds and energy sources for ethanol production.

  8. Process for the treatment of lignocellulosic biomass

    Science.gov (United States)

    Dale, Bruce E.; Lynd, Lee R.; Laser, Mark

    2013-03-12

    A process for the treatment of biomass to render structural carbohydrates more accessible and/or digestible using concentrated ammonium hydroxide with or without anhydrous ammonia addition, is described. The process preferably uses steam to strip ammonia from the biomass for recycling. The process yields of monosaccharides from the structural carbohydrates are good, particularly as measured by the enzymatic hydrolysis of the structural carbohydrates. The monosaccharides are used as animal feeds and energy sources for ethanol production.

  9. 改性磁种-活性炭工艺处理油污染深井地下水%Treatment of oil polluted ground water by modified magnetic seed-activated carbon process

    Institute of Scientific and Technical Information of China (English)

    曹雨平; 邓阳清; 刘亚凯

    2011-01-01

    Oil polluted groundwater was collected from Hougao 3# deep well, Qilu Petrochemical Corporation,the method of modified magnetic seed-activated carbon process was established and performed on these water samples to investigated the effect of demulsifier (PAC) dosage, modified magnetic seed dosage and activated carbon dosage on the oil removal efficiency. Results showed that the modified magnetic seed-activated carbon process presented perfect performance for oil removal and the optimum dosage for PAC, modified magnetic seed and activated carbon was 50,100, 200 mg/L respectively. After treated under these optimum conditions, mass concentration of oil in polluted ground water could decrease below 1 mg/L, given the average oil removal efficiency of 96.7%, which could meet the requirement of “Urban Sewage Reuse and Utilization, Industrial Water Quality Standard” (GB/T 19923-2005). The modified magnetic seed could be recycled and used again, which could reduce the second pollution and save the treatment cost.%采用改性磁种-活性炭工艺处理油污染深井地下水,考察了破乳剂、改性磁种及活性炭投加量对除油效果的影响,并在最佳除油条件下对原水进行除油效果验证.结果表明,采用改性磁种-活性炭工艺处理油污染深井地下水效果较为明显,出水含油质量浓度在1 mg/L以下,除油率平均达96.7%,出水满足(GB/T 19923-2005)要求;改性磁种可回收再利用,既减少二次污染,又降低成本.

  10. Linking water treatment practices and fish welfare

    DEFF Research Database (Denmark)

    Zubiaurre, Claire; Pedersen, Lars-Flemming

    2016-01-01

    Peracetic acids can be used as sanitizers to control water quality in aquaculture systems. As an alternative to formalin, chloramine-T or copper sulphate, PAA has strong anti-microbial effects, degrades quickly and is relatively safe to use. Its mode of action and associated rapid decay can make...... optimizing treatment protocols a challenge. Continuous low-dose applications seem to be a promising solution. In this preliminary study behavioral response was used to assess potential correlations with PAA dosage. A behavioral change or response is not necessarily an indication of compromised welfare....... Supportive enzymatic, biochemical and physiological biomarkers can be used along with gill and epidermal histological measures to evaluate the effects on water treatment regimens. The ultimate goal is to define the therapeutic window where fish welfare is not compromised.PAA is among the few disinfectants...

  11. Water in Biological and Chemical Processes

    Science.gov (United States)

    Bagchi, Biman

    2013-11-01

    Part I. Bulk Water: 1. Uniqueness of water; 2. Anomalies of water; 3. Dynamics of water: molecular motions and hydrogen bond breaking kinetics; 4. Inherent structures of liquid water; 5. pH of water; Part II. Water in Biology: Dynamical View and Function: 6. Biological water; 7. Explicit role of water in biological functions; 8. Hydration of proteins; 9. Can we understand protein hydration layer: lessons from computer simulations; 10. Water in and around DNA and RNA; 11. Role of water in protein-DNA interaction; 12. Water surrounding lipid bilayers; 13. Water in Darwin's world; Part III. Water in Complex Chemical Systems: 14. Hydrophilic effects; 15. Hydrophobic effects; 16. Aqueous binary mixtures: amphiphilic effect; 17. Water in and around micelles, reverse micelles and microemulsions; 18. Water in carbon nanotubes; Part IV. Bulk Water: Advanced Topics: 19. Entropy of water; 20. Freezing of water into ice; 21. Supercritical water; 22. Microscopic approaches to understand water anomalies.

  12. Experimental Study of Advanced Treatment of Coking Wastewater Using MBR-RO Combined Process

    Science.gov (United States)

    Zhang, Lei; Hwang, Jiannyang; Leng, Ting; Xue, Gaifeng; Chang, Hongbing

    A membrane bioreactor-reverse osmosis (MBR-RO) combined process was used for advanced treatment of coking wastewater from secondary biological treatment. MBR and RO units' treatment efficiency for the pollution removal were conducted, and effects of raw water conductivity and trans-membrane pressure on water yield and desalination rate in RO unit were investigated in detail. The experimental results proved that MBR-RO combined process ran steadily with good treatment effect, which could obtain stable effluent water quality and met the requirement of "Design Criterion of the Industrial Circulating Cooling Water Treatment" (GB 50050-2007).

  13. Feasibility of electrochemical oxidation process for treatment of saline wastewater

    Directory of Open Access Journals (Sweden)

    Kavoos Dindarloo

    2015-09-01

    Full Text Available Background: High concentration of salt makes biological treatment impossible due to bacterial plasmolysis. The present research studies the process of electrochemical oxidation efficiency and optimal levels as important factors affecting pH, salt concentration, reaction time and applied voltage. Methods: The sample included graphite electrodes with specifications of 2.5 cm diameter and 15 cm height using a reactor with an optimum capacity of 1 L. Sixty samples were obtained with the aid of the experiments carried out in triplicates for each factor at 5 different levels. The entire experiments were performed based on standard methods for water and waste water treatments. Results: Analysis of variance carried out on effect of pH, salt concentration, reaction time and flow intensity in elimination of chemical oxygen demand (COD showed that they are significant factors affecting this process and reduce COD with a coefficient interval of 95% and test power of 80%. Scheffe test showed that at optimal level, a reaction time of 1 hour, 10 g/L concentration, pH = 9 and 15 V electrical potential difference were obtained. Conclusion: Waste waters containing salt may contribute to the electro-oxidation process due to its cations and anions. Therefore, the process of electrochemical oxidation with graphite electrodes could be a proper strategy for the treatment of saline wastewater where biological treatment is not possible.

  14. Energy requirements for waste water treatment.

    Science.gov (United States)

    Svardal, K; Kroiss, H

    2011-01-01

    The actual mathematical models describing global climate closely link the detected increase in global temperature to anthropogenic activity. The only energy source we can rely on in a long perspective is solar irradiation which is in the order of 10,000 kW/inhabitant. The actual primary power consumption (mainly based on fossil resources) in the developed countries is in the range of 5 to 10 kW/inhabitant. The total power contained in our nutrition is in the range of 0.11 kW/inhabitant. The organic pollution of domestic waste water corresponds to approximately 0.018 kW/inhabitant. The nutrients contained in the waste water can also be converted into energy equivalents replacing market fertiliser production. This energy equivalent is in the range of 0.009 kW/inhabitant. Hence waste water will never be a relevant source of energy as long as our primary energy consumption is in the range of several kW/inhabitant. The annual mean primary power demand of conventional municipal waste water treatment with nutrient removal is in the range of 0.003-0.015 kW/inhabitant. In principle it is already possible to reduce this value for external energy supply to zero. Such plants should be connected to an electrical grid in order to keep investment costs low. Peak energy demand will be supported from the grid and surplus electric energy from the plant can be is fed to the grid. Zero 'carbon footprint' will not be affected by this solution. Energy minimisation must never negatively affect treatment efficiency because water quality conservation is more important for sustainable development than the possible reduction in energy demand. This argument is strongly supported by economical considerations as the fixed costs for waste water infrastructure are dominant.

  15. STUDY ON WASTE WATER TREATMENT PLANTS

    Directory of Open Access Journals (Sweden)

    Mariana DUMITRU

    2015-04-01

    Full Text Available Biogas is more and more used as an alternative source of energy, considering the fact that it is obtained from waste materials and it can be easily used in cities and rural communities for many uses, between which, as a fuel for households. Biogas has many energy utilisations, depending on the nature of the biogas source and the local demand. Generally, biogas can be used for heat production by direct combustion, electricity production by fuel cells or micro-turbines, Combined Hest and Power generation or as vehicle fuel. In this paper we search for another uses of biogas and Anaerobe Digestion substrate, such as: waste water treatment plants and agricultural wastewater treatment, which are very important in urban and rural communities, solid waste treatment plants, industrial biogas plants, landfill gas recovery plants. These uses of biogas are very important, because the gas emissions and leaching to ground water from landfill sites are serious threats for the environment, which increase more and more bigger during the constant growth of some human communities. That is why, in the developed European countries, the sewage sludge is treated by anaerobe digestion, depending on national laws. In Romania, in the last years more efforts were destined to use anaerobe digestion for treating waste waters and management of waste in general. This paper can be placed in this trend of searching new ways of using with maximum efficiency the waste resulted in big communities.

  16. 40 CFR 141.83 - Source water treatment requirements.

    Science.gov (United States)

    2010-07-01

    ... 40 Protection of Environment 22 2010-07-01 2010-07-01 false Source water treatment requirements... water treatment requirements. Systems shall complete the applicable source water monitoring and... monitoring (§ 141.88(d)). (b) Description of source water treatment requirements—(1) System...

  17. Pilot-scale UV/H2O2 advanced oxidation process for surface water treatment and downstream biological treatment: effects on natural organic matter characteristics and DBP formation potential.

    Science.gov (United States)

    Sarathya, Siva R; Stefan, Mihaela I; Royce, Alan; Mohseni, M

    2011-12-01

    The effects of the advanced oxidation process (AOP) of ultraviolet radiation in combination with hydrogen peroxide (UV/H2O2) on the structure and biodegradability of dissolved natural organic matter (NOM) and on the formation of disinfection by-products (DBPs) through the post-UV/H2O2 chlorination were investigated using UV reactors equipped with either low-pressure amalgam lamps or medium-pressure mercury vapour lamps. With electrical energy doses and H2O2 concentrations typically applied in full-scale UV systems for water remediation, the UV/H2O2 AOP partially oxidized NOM, reducing its degree of aromaticity and leading to an increase in the level of biodegradable species. Also, when combined with a downstream biological activated carbon (BAC) filter, UV/H2O2 AOP reduced the formation of DBPs by up to 60% for trihalomethanes and 75% for haloacetic acids. Biological activated carbon was also shown to effectively remove biodegradable by-products and residual H2O2.

  18. Pilot-scale Study on Hybrid PAC-UF Process for Settled Water Treatment%一体式PAC-UF工艺处理水厂待滤水的中试研究

    Institute of Scientific and Technical Information of China (English)

    邵森林; 梁恒; 谢观体; 陈杰; 李圭白

    2013-01-01

    Pilot-scale study was performed to investigate the hybrid PAC-UF process for settled water treatment in terms of validity and economic efficiency of it as a substitute of the conventional sand filter. The performance of the hybrid PAC-UF process was also compared with that of the conventional sand filter in the full-scale drinking water treatment plant and UF. Results showed that, the hybrid PAC-UF process could ensure the biological-safety with (0.041 ±0.010) NTU and (13 ±8)/mL for the effluent of turbidity and particle number (particle size 〉2 μm). The process reduced influent CODMn and UV254 by (21.0 ±9. 9)% and (51.0 ± 10. 7)% , respectively. The process had a better performance for organic matter and turbidity removal compared with the conventional process, but it couldn't remove NH+4 -N effectively. The process could running stably under the experimental condition . The hybrid PAC-UF process was suitable for the raw water with high concentration organic matter and low concentration NH+4 -N. It could ensure the chemical-safety and biological-safety of effluent.%通过中试,研究一体式PAC-UF工艺取代传统砂滤池工艺的适用性和经济性,并将其与单独超滤和水厂砂滤池比较.结果表明,PAC-UF工艺平均出水浊度为(0.041±0.010)NTU,粒径>2 μm的颗粒数平均为(13±8)/mL,可保证出水良好的生物安全性.在PAC投加20 mg/L情况下,PAC-UF工艺对CODMn的去除率为(21.0±9.9)%,对不含亚硝酸盐部分CODMn的去除率为(33.7±11.1)%,对UV254的去除率为(51.0+10.7)%,PAC-UF工艺对浊度和有机物的去除效果明显优于传统砂滤.但PAC-UF工艺对NH4+-N去除效果不佳.在实验工况条件下,工艺能稳定运行,可以维持运行3个月左右化学清洗1次.PAC-UF工艺适用于高有机污染、低NH4+-N的原水水质,它可以有效地提高水厂出水的生物安全性和化学安全性.

  19. Characterization of water treatment sludge and its reuse as coagulant.

    Science.gov (United States)

    Ahmad, Tarique; Ahmad, Kafeel; Ahad, Abdul; Alam, Mehtab

    2016-11-01

    Coagulation-flocculation process results in the generation of large volume of waste or residue, known as water treatment sludge (WTS), in the purification of surface water for potable supplies. Sustainable management of the inevitable waste requires careful attention from the plant operators and sludge managers. In this study, WTS produced with the optimum alum dose of 30 ml/L at the laboratory scale has been treated with sulphuric acid to bring forth a product known as sludge reagent product (SRP). The performance of SRP is evaluated for its efficiency in removing the colloidal suspensions from the Yamuna river water over wide pH range of 2-13. 1% sludge acidified with sulphuric acid of normality 2.5 at the rate of 0.05 ml/ml sludge has been observed as the optimum condition for preparing SRP from WTS. The percentage turbidity removal is greater at higher pH value and increases with increasing the dosage of SRP. The optimum SRP dosage of 8 ml/L in the pH range of 6-8 performed well in removing the colloidal suspension and other impurities from the Yamuna water. The quality of treated water met the prescribed standards for most of the quality parameters. Thus, SRP has the potential to substitute the conventional coagulants partially or completely in the water treatment process, depending on the quality needed at the users end. Copyright © 2016 Elsevier Ltd. All rights reserved.

  20. Occurrence of Mycobacteria in Water Treatment Lines and in Water Distribution Systems

    Science.gov (United States)

    Le Dantec, Corinne; Duguet, Jean-Pierre; Montiel, Antoine; Dumoutier, Nadine; Dubrou, Sylvie; Vincent, Véronique

    2002-01-01

    The frequency of recovery of atypical mycobacteria was estimated in two treatment plants providing drinking water to Paris, France, at some intermediate stages of treatment. The two plants use two different filtration processes, rapid and slow sand filtration. Our results suggest that slow sand filtration is more efficient for removing mycobacteria than rapid sand filtration. In addition, our results show that mycobacteria can colonize and grow on granular activated carbon and are able to enter distribution systems. We also investigated the frequency of recovery of mycobacteria in the water distribution system of Paris (outside buildings). The mycobacterial species isolated from the Paris drinking water distribution system are different from those isolated from the water leaving the treatment plants. Saprophytic mycobacteria (present in 41.3% of positive samples), potentially pathogenic mycobacteria (16.3%), and unidentifiable mycobacteria (54.8%) were isolated from 12 sites within the Paris water distribution system. Mycobacterium gordonae was preferentially recovered from treated surface water, whereas Mycobacterium nonchromogenicum was preferentially recovered from groundwater. No significant correlations were found among the presence of mycobacteria, the origin of water, and water temperature. PMID:12406720

  1. Testing large volume water treatment and crude oil ...

    Science.gov (United States)

    Report EPA’s Homeland Security Research Program (HSRP) partnered with the Idaho National Laboratory (INL) to build the Water Security Test Bed (WSTB) at the INL test site outside of Idaho Falls, Idaho. The WSTB was built using an 8-inch (20 cm) diameter cement-mortar lined drinking water pipe that was previously taken out of service. The pipe was exhumed from the INL grounds and oriented in the shape of a small drinking water distribution system. Effluent from the pipe is captured in a lagoon. The WSTB can support drinking water distribution system research on a variety of drinking water treatment topics including biofilms, water quality, sensors, and homeland security related contaminants. Because the WSTB is constructed of real drinking water distribution system pipes, research can be conducted under conditions similar to those in a real drinking water system. In 2014, WSTB pipe was experimentally contaminated with Bacillus globigii spores, a non-pathogenic surrogate for the pathogenic B. anthracis, and then decontaminated using chlorine dioxide. In 2015, the WSTB was used to perform the following experiments: • Four mobile disinfection technologies were tested for their ability to disinfect large volumes of biologically contaminated “dirty” water from the WSTB. B. globigii spores acted as the biological contaminant. The four technologies evaluated included: (1) Hayward Saline C™ 6.0 Chlorination System, (2) Advanced Oxidation Process (A

  2. 天然有机物对纳滤水处理工艺的影响%Effect of Natural Organic Matter on Nanofiltration Membrane Process in Water Treatment

    Institute of Scientific and Technical Information of China (English)

    刘艳妮; 程爱华; 畅飞

    2014-01-01

    天然有机物(NOM)广泛存在于天然水体中,对纳滤处理过程产生较大影响。该文在介绍NOM的组成和物化性质的基础上,讨论了NOM对截留率和膜通量的影响,阐述了纳滤过程中NOM的亲、疏水性,浓差极化效应,静电排斥作用,氢键作用,二价离子络合等对纳滤过程的影响机理,对提高纳滤膜过滤性能有重要意义。%Natural organic matter (NOM)is ubiquitous in natural surface waters and has major effect on the water treatment during the nanofiltration (NF)process. The compositions and properties of NOM were introduced and its influences on the rejection and flux of NF were discussed. These influences of hydrophilicity/hydrophobicity of NOM,concentration polarization effect,electrostatic repulsion effect,the hydrogen bonding interaction and divalent ion chelating on nanofiltration were expunded. The effect mechanisms have important significance to improve the nanofiltration membrane performance.

  3. Physical chemical properties of sludges of a chemical treatment of boilers feed water and ways of their utilization

    Directory of Open Access Journals (Sweden)

    T. Krasnenko

    2013-03-01

    Full Text Available Water is a necessary process for TPP power plant operation. To the power station, in the production of electricity and heat as a result of the preparation of large amounts of water to compensate for losses associated with the release of process steam for production, produce large quantities of waste water treatment - water treatment chemical sludge (WTCS.

  4. Pollution of Municipal Water Supply System by Phthalates and Evaluation on Purification Effects of Current Water Treatment Process%邻苯二甲酸脂对城镇供水的污染及现行水处理工艺净化效果的评价

    Institute of Scientific and Technical Information of China (English)

    韩关根; 吴平谷; 王惠华; 方跃强; 马冰洁; 赵莹

    2001-01-01

    Objective To understand the pollution of municipal water supply system by phthalates and the purification effects of current water treatment process on phthalates were carried out.Methods The water samples of source water and finished water were determined for phthalate by comparative method.5 kinds of isomers of phthalate in water samples were detected by gas chromatography technique.Results In treated water samples the detectable rate and maximum contents in water samples were 100% and 76μg/L for di-n-butyl phthalate,50% and 17 μg/L for di(2-ethylhexyl) phthalate respectively.Di-methyl phthalate,di-ethyl phthalate and butyl benzyl phthalate were not found in water samples.There was no significant difference in geometric means of the contents of phthalates between source water (19.74μg/L) and finished water (18.35 μg/L),P>0.05.Conclusion The main pollutants of phthalates were di-nbulyl phthalate and di(2-ethylhexyl) phthalate in municipal water supply system.The effectiveness of removing phthalates from drinking water by current water treatment process in city and town was not satisfied.The water treatment process special for removing phthatates from drinking water should be studied and explored in further.%目的了解邻苯二甲酸酯类化合物对城镇供水的污染情况以及现行水处理工艺对该类物质的净化效果。方法采用处理前、后对照的方法,对源水和出厂水进行检测。色谱分析测试邻苯二甲酸酯类化合物五只异构体。结果出厂水中邻苯二甲酸二丁酯检出率100%,最高含量达76 μg/L。邻苯二甲酸二(2-乙基己基)酯检出率50%,最高含量17μg/L;邻苯二甲酸二甲酯、邻苯二甲酸二乙酯和邻苯二甲酸丁基苄酯三只异构体均未测出。源水中邻苯二甲酸酯类化合物的平均含量(G)为19.74 μ/L,出厂水18.35μ/L,两者差别无显著意义(P>0.05)。结论城镇供水中的邻苯二甲酸酯类化合物污染以邻苯

  5. System and process for biomass treatment

    Science.gov (United States)

    Dunson, Jr., James B; Tucker, III, Melvin P; Elander, Richard T; Lyons, Robert C

    2013-08-20

    A system including an apparatus is presented for treatment of biomass that allows successful biomass treatment at a high solids dry weight of biomass in the biomass mixture. The design of the system provides extensive distribution of a reactant by spreading the reactant over the biomass as the reactant is introduced through an injection lance, while the biomass is rotated using baffles. The apparatus system to provide extensive assimilation of the reactant into biomass using baffles to lift and drop the biomass, as well as attrition media which fall onto the biomass, to enhance the treatment process.

  6. Characterization of drinking water treatment sludge after ultrasound treatment.

    Science.gov (United States)

    Zhou, Zhiwei; Yang, Yanling; Li, Xing; Zhang, Yang; Guo, Xuan

    2015-05-01

    Ultrasonic technology alone or the combination of ultrasound with alkaline or thermal hydrolysis as pretreatment for anaerobic digestion of activated sludge has been extensively documented. However, there are few reports on ultrasound as pretreatment of drinking water treatment sludge (DWTS), and thereby the characteristic variability of sonicated DWTS has not been fully examined. This research presents a lab-scale study on physical, chemical and biological characteristics of a DWTS sample collected from a water plant after ultrasonic treatment via a bath/probe sonoreactor. By doing this work, we provide implications for using ultrasound as pretreatment of enhanced coagulation of recycling sludge, and for the conditioning of water and wastewater mixed sludge by ultrasound combined with polymers. Our results indicate that the most vigorous DWTS disintegration quantified by particles' size reduction and organic solubilization is achieved with 5 W/ml for 30 min ultra-sonication (specific energy of 1590 kWh/kg TS). The Brunauer, Emmett and Teller (BET) specific surface area of sonicated DWTS flocs increase as ultra-sonication prolongs at lower energy densities (0.03 and 1 W/ml), while decrease as ultra-sonication prolongs at higher energy densities (3 and 5 W/ml). Additionally, the pH and zeta potential of sonicated DWTS slightly varies under all conditions observed. A shorter sonication with higher energy density plays a more effective role in restraining microbial activity than longer sonication with lower energy density.

  7. ACTIVATED CARBON FROM LIGNITE FOR WATER TREATMENT

    Energy Technology Data Exchange (ETDEWEB)

    Edwin S. Olson; Daniel J. Stepan

    2000-07-01

    High concentrations of humate in surface water result in the formation of excess amounts of chlorinated byproducts during disinfection treatment. These precursors can be removed in water treatment prior to disinfection using powdered activated carbon. In the interest of developing a more cost-effective method for removal of humates in surface water, a comparison of the activities of carbons prepared from North Dakota lignites with those of commercial carbons was conducted. Previous studies indicated that a commercial carbon prepared from Texas lignite (Darco HDB) was superior to those prepared from bituminous coals for water treatment. That the high alkali content of North Dakota lignites would result in favorable adsorptive properties for the very large humate molecules was hypothesized, owing to the formation of larger pores during activation. Since no standard humate test has been previously developed, initial adsorption testing was performed using smaller dye molecules with various types of ionic character. With the cationic dye, methylene blue, a carbon prepared from a high-sodium lignite (HSKRC) adsorbed more dye than the Darco HDB. The carbon from the low-sodium lignite was much inferior. With another cationic dye, malachite green, the Darco HDB was slightly better. With anionic dyes, methyl red and azocarmine-B, the results for the HSKRC and Darco HDB were comparable. A humate test was developed using Aldrich humic acid. The HSKRC and the Darco HDB gave equally high adsorption capacities for the humate (138 mg/g), consistent with the similarities observed in earlier tests. A carbon prepared from a high-sodium lignite from a different mine showed an outstanding improvement (201 mg/g). The carbons prepared from the low-sodium lignites from both mines showed poor adsorption capacities for humate. Adsorption isotherms were performed for the set of activated carbons in the humate system. These exhibited a complex behavior interpreted as resulting from two types

  8. A review of water treatment membrane nanotechnologies

    KAUST Repository

    Pendergast, MaryTheresa M.

    2011-01-01

    Nanotechnology is being used to enhance conventional ceramic and polymeric water treatment membrane materials through various avenues. Among the numerous concepts proposed, the most promising to date include zeolitic and catalytic nanoparticle coated ceramic membranes, hybrid inorganic-organic nanocomposite membranes, and bio-inspired membranes such as hybrid protein-polymer biomimetic membranes, aligned nanotube membranes, and isoporous block copolymer membranes. A semi-quantitative ranking system was proposed considering projected performance enhancement (over state-of-the-art analogs) and state of commercial readiness. Performance enhancement was based on water permeability, solute selectivity, and operational robustness, while commercial readiness was based on known or anticipated material costs, scalability (for large scale water treatment applications), and compatibility with existing manufacturing infrastructure. Overall, bio-inspired membranes are farthest from commercial reality, but offer the most promise for performance enhancements; however, nanocomposite membranes offering significant performance enhancements are already commercially available. Zeolitic and catalytic membranes appear reasonably far from commercial reality and offer small to moderate performance enhancements. The ranking of each membrane nanotechnology is discussed along with the key commercialization hurdles for each membrane nanotechnology. © 2011 The Royal Society of Chemistry.

  9. Electron beam flue gas treatment process. Review

    Energy Technology Data Exchange (ETDEWEB)

    Honkonen, V.A. [Kuopio Univ. (Finland). Dept. of Physics; Chmielewski, A.G. [Institute of Nuclear Chemistry and Technology, Warsaw (Poland)

    1996-12-31

    The basis of the process for electron beam flue gas treatment are presented in the report. In tabular form the history of the research is reviewed. Main dependences of SO{sub 2} and NO{sub x} removal efficiencies on different physico-chemical parameters are discussed. Trends concerning industrial process implementation are presented in the paper,finally. (author). 74 refs, 11 figs, 1 tab.

  10. Pilot study of integrated process of activated carbon-ultrafiltration-nanofiltration for advanced water treatment%活性炭结合超滤及纳滤工艺深度处理饮用水的中试研究

    Institute of Scientific and Technical Information of China (English)

    杨忠盛; 芦敏; 袁东星; 翁自保; 陈世保

    2011-01-01

    金门岛内水库的富营养化程度严重,藻类所产生的臭味物质、有机碳及消毒副产物的浓度非常高,影响岛内民众健康.研究利用活性炭结合超滤及纳滤工艺,将甲基异莰醇-2、土臭素处理嗅阈值以下,将不可挥发溶解性有机炭(NPDOC)从6.4 mg/L降至0.2 mg/L;三卤甲烷生成势(THMFP)和卤乙酸生成势(HAAFP)可分别从489μg/L和656μg/L去除至38μg/L及17.6 μg/L,去除率分别为92%及97%.中试结果表明,各检测项目均符合台湾地区饮用水标准.由32位金门县自来水厂员工测试3种水的适饮性,其中经活性炭结合超滤及纳滤组合工艺处理后的水样水质为多数测试人员所接受.%There is serious eutrophia in Jinmen reservoir. The super high concentrations of odor gases, organic carbon, and disinfection by-products from algae do harm to the people's health. In this study by adopting the integrated process of activated carbon-ultrafiltration-nanofiltration, the concentrations of 2-MIB and geosmin were controlled to below the odor thresholds, and the non-purgeable dissolved organic carbon (NPDOC) was decreased from 6.4 mg/L to 0. 2 mg/L; the trihalomethane formation potential (THMFP) and haloacetic acid formation potential (HAAFP) were removed from 489 μg/L and 656 μg/L to 38μg/L and 17. 6 μg/L respectively, and the removal ratio was 92% and 977 respectively. The pilot research result showed that all water quality indexes could meet the drinking water standards in Taiwan. Through the drinkability test held by 32 Jinmen water treatment plant employees, the water quality of the effluent from activated carbon-ultrafiltration-nanofiltration process was accepted by most of people.

  11. Sterols indicate water quality and wastewater treatment efficiency.

    Science.gov (United States)

    Reichwaldt, Elke S; Ho, Wei Y; Zhou, Wenxu; Ghadouani, Anas

    2017-01-01

    As the world's population continues to grow, water pollution is presenting one of the biggest challenges worldwide. More wastewater is being generated and the demand for clean water is increasing. To ensure the safety and health of humans and the environment, highly efficient wastewater treatment systems, and a reliable assessment of water quality and pollutants are required. The advance of holistic approaches to water quality management and the increasing use of ecological water treatment technologies, such as constructed wetlands and waste stabilisation ponds (WSPs), challenge the appropriateness of commonly used water quality indicators. Instead, additional indicators, which are direct measures of the processes involved in the stabilisation of human waste, have to be established to provide an in-depth understanding of system performance. In this study we identified the sterol composition of wastewater treated in WSPs and assessed the suitability of human sterol levels as a bioindicator of treatment efficiency of wastewater in WSPs. As treatment progressed in WSPs, the relative abundance of human faecal sterols, such as coprostanol, epicoprostanol, 24-ethylcoprostanol, and sitostanol decreased significantly and the sterol composition in wastewater changed significantly. Furthermore, sterol levels were found to be correlated with commonly used wastewater quality indicators, such as BOD, TSS and E. coli. Three of the seven sterol ratios that have previously been used to track sewage pollution in the environment, detected a faecal signal in the effluent of WSPs, however, the others were influenced by high prevalence of sterols originating from algal and fungal activities. This finding poses a concern for environmental assessment studies, because environmental pollution from waste stabilisation ponds can go unnoticed. In conclusion, faecal sterols and their ratios can be used as reliable indicators of treatment efficiency and water quality during wastewater

  12. Study on the treatment of the refractory chemical waste water by new Fe/C Micro Electrolysis process%新型铁碳内电解处理难降解化工废水的工艺研究

    Institute of Scientific and Technical Information of China (English)

    陈亮; 周晓燕; 金辉; 郭朝晖

    2014-01-01

    The high concentrate chemical waister water is difficult to treat due to containing complicated composition and recalcitrant organic compounds.In order to improve the efficiency of waste water treatment.,we designed a new type of multi metal catalyzed iron-carbon activated coke micro-electrolysis materials, analyzed the influencing factors of the iron-carbon micro-electrolysis process which include aeration time, PH, copper-plating time and nickel-plating time, the ratio of Fe/C. The analyzed results indicated when PH was 4, the time of copper plating was 2min, the time of copper plating was 2min,the ration of Fe/C was 2:1,aeration time was 2h, the CODCr removal efficiency could approach 50%after this iron-carbon micro-electrolysis process.%高浓度化工废水难降解有机污染物含量高,成分复杂,可生化性差,处理难度大。为提高废水的处理效率,我们设计了新型多元金属催化铁碳内电解填料,并考察了曝气时间、PH、镀铜时间和镀镍时间、铁碳比等因数对处理效率的影响。分析结果表明当pH=4,铁屑镀铜2min,镀镍2min,铁炭比为2:1。经过曝气2.5h后,CODCr去除率接近50%。

  13. UV-based technologies for marine water disinfection and the application to ballast water: Does salinity interfere with disinfection processes?

    Science.gov (United States)

    Moreno-Andrés, Javier; Romero-Martínez, Leonardo; Acevedo-Merino, Asunción; Nebot, Enrique

    2017-03-01

    Water contained on ships is employed in the majority of activities on a vessel; therefore, it is necessary to correctly manage through marine water treatments. Among the main water streams generated on vessels, ballast water appears to be an emerging global challenge (especially on cargo ships) due to the transport of invasive species and the significant impact that the ballast water discharge could have on ecosystems and human activities. To avoid this problem, ballast water treatment must be implemented prior to water discharge in accordance with the upcoming Ballast Water Management Convention. Different UV-based treatments (photolytic: UV-C and UV/H2O2, photocatalytic: UV/TiO2), have been compared for seawater disinfection. E. faecalis is proposed as a biodosimeter organism for UV-based treatments and demonstrates good properties for being considered as a Standard Test Organism for seawater. Inactivation rates by means of the UV-based treatments were obtained using a flow-through UV-reactor. Based on the two variables responses that were studied (kinetic rate constant and UV-Dose reductions), both advanced oxidation processes (UV/H2O2 and photocatalysis) were more effective than UV-C treatment. Evaluation of salinity on the processes suggests different responses according to the treatments: major interference on photocatalysis treatment and minimal impact on UV/H2O2.

  14. 高频电磁水处理器处理腔的电磁场仿真分析及实验%Electromagnetic Field Simulation Analysis and Experiment on Processing Chambers of High-frequency Electromagnetic Water Treatment Devices

    Institute of Scientific and Technical Information of China (English)

    熊兰; 伍懿美; 杨子康; 石岭岭; 苗雪飞; 何为

    2012-01-01

    Processing chamber is an important part of high-frequency electromagnetic water treatment devices,in order to determine which one has better anti-scaling effect between two chambers,one is set with coaxial electrodes and the other is wrapped by spirals,we analyzed the quasi-static electromagnetic field distribution in these two chambers.It was proved that the majority field in processing chamber with coaxial electrodes was electric field and that in processing chamber wrapped by spirals was magnetic field.Meantime,we simulated electromagnetic energy distribution in two processing chambers by using the Ansoft Maxwell software,which was based on the finite element method.According to the simulation data,electromagnetic energy of processing chamber with coaxial electrodes is much bigger than that of processing chamber wrapped by spirals.Meanwhile,a mini-circulating water system is built and water quality experiments are completed by self preparing CaCO3 solution in which the concentration of Ca2+ is 5 mmol/L.Moreover,we observed the microscopic structures of crystal morphology and electric conductivity,and also determined the scale-inhibition rate by weight-loss method.Analysis results from experimental data illustrate that both processing chambers under high-frequency pulsed field have anti-scaling effects,but the processing chamber with coaxial electrodes is more effective.%处理腔是高频电磁水处理器的重要组成部件,为了确定何种处理腔结构对高频电磁阻垢除垢具有更佳的效果,利用准静态学方法对2种常见的处理腔即同轴式处理腔和螺线管式处理腔进行了电磁场分析,得到了同轴式处理腔主导场为电场、螺线管式处理腔主导场为磁场的结论;利用Ansoft Maxwell软件建立了有限元模型,仿真分析其内部的电磁场能量的分布,仿真分析表明:当施加相同的激励源并处理相同体积的水时,同轴式处理腔内的电磁能量大于螺线管式处

  15. 高浓度泥浆法(HDS)-铁盐处理工业污酸废水半工业试验%Pilot-plant Test of Acid Waste Water Treatment by High Density Slurry(HDS) Ferrous Salt Process

    Institute of Scientific and Technical Information of China (English)

    宋文涛

    2011-01-01

    对高浓度泥浆(HDS)-铁盐法处理冶炼企业污酸工业废水进行半工业试验.结果表明,在pH=10条件下,HDS出水的Pb、Zn均可达到国家排放标准,As出水控制在10 mg/L以下,再经后续铁盐除砷工序,As排放也可达到国家排放标准.HDS产生底泥固含可达27%左右,显著高于石灰法的水平(2%以下).%The semi-industrial experiment for acid waste water treatment in nonferrous smelter was conducted via High Density Slurry (HDS)-ferrous salt process. The results indicate that, both Pb and Zn could meet the requirement of the national emission standards through the HDS-ferrous salt process at pHIO as concentration in HDS system effluent could be controlled to less than 10 mg/L. The solid content in HDS sludge is up to 27%, which is significantly higher than that in LDS sludge(<2%).

  16. Emissions from Produced Water Treatment Ponds, Uintah Basin, Utah, USA

    Science.gov (United States)

    Mansfield, M. L.; Lyman, S. N.; Tran, H.; O'Neil, T.; Anderson, R.

    2015-12-01

    An aqueous phase, known as "produced water," usually accompanies the hydrocarbon fluid phases that are extracted from Earth's crust during oil and natural gas extraction. Produced water contains dissolved and suspended organics and other contaminants and hence cannot be discharged directly into the hydrosphere. One common disposal method is to discharge produced water into open-pit evaporation ponds. Spent hydraulic fracturing fluids are also often discharged into the same ponds. It is obvious to anyone with a healthy olfactory system that such ponds emit volatile organics to the atmosphere, but very little work has been done to characterize such emissions. Because oil, gas, and water phases are often in contact in geologic formations, we can expect that more highly soluble compounds (e.g., salts, alcohols, carbonyls, carboxyls, BTEX, etc.) partition preferentially into produced water. However, as the water in the ponds age, many physical, chemical, and biological processes alter the composition of the water, and therefore the composition and strength of volatile organic emissions. For example, some ponds are aerated to hasten evaporation, which also promotes oxidation of organics dissolved in the water. Some ponds are treated with microbes to promote bio-oxidation. In other words, emissions from ponds are expected to be a complex function of the composition of the water as it first enters the pond, and also of the age of the water and of its treatment history. We have conducted many measurements of emissions from produced water ponds in the Uintah Basin of eastern Utah, both by flux chamber and by evacuated canister sampling with inverse modeling. These measurements include fluxes of CO2, CH4, methanol, and many other volatile organic gases. We have also measured chemical compositions and microbial content of water in the ponds. Results of these measurements will be reported.

  17. Laser removal of water repellent treatments on limestone

    Science.gov (United States)

    Gómez-Heras, Miguel; Alvarez de Buergo, Mónica; Rebollar, Esther; Oujja, Mohamed; Castillejo, Marta; Fort, Rafael

    2003-12-01

    Protective and water repellent treatments are applied on stone materials used on buildings or sculptures of artistic value to reduce water intrusion without limiting the natural permeability to water vapour of the material. The effect of the wavelength associated with the laser removal of two water repellent treatments applied on limestone, Paraloid B-72, a copolymer of methyl acrylate and ethyl methacrylate, and Tegosivin HL-100, a modified polysiloxane resin, was investigated by using the four harmonics of a Q-switched Nd:YAG laser (1064, 532, 355 and 266 nm). The modifications induced on the surface of limestone samples by laser irradiation were studied using colorimetry, roughness measurements and scanning electron microscopy (SEM). The removal of the treatments was found to be dependent on the laser irradiation conditions and on the characteristics of the coatings. The fundamental laser radiation was effective in removing both treatments, but thermal alteration processes were induced on the constituent calcite crystals. The best results were obtained by irradiation in the near UV at 355 nm.

  18. Laser removal of water repellent treatments on limestone

    Energy Technology Data Exchange (ETDEWEB)

    Gomez-Heras, Miguel; Alvarez de Buergo, Monica; Rebollar, Esther; Oujja, Mohamed; Castillejo, Marta; Fort, Rafael

    2003-12-15

    Protective and water repellent treatments are applied on stone materials used on buildings or sculptures of artistic value to reduce water intrusion without limiting the natural permeability to water vapour of the material. The effect of the wavelength associated with the laser removal of two water repellent treatments applied on limestone, Paraloid B-72, a copolymer of methyl acrylate and ethyl methacrylate, and Tegosivin HL-100, a modified polysiloxane resin, was investigated by using the four harmonics of a Q-switched Nd:YAG laser (1064, 532, 355 and 266 nm). The modifications induced on the surface of limestone samples by laser irradiation were studied using colorimetry, roughness measurements and scanning electron microscopy (SEM). The removal of the treatments was found to be dependent on the laser irradiation conditions and on the characteristics of the coatings. The fundamental laser radiation was effective in removing both treatments, but thermal alteration processes were induced on the constituent calcite crystals. The best results were obtained by irradiation in the near UV at 355 nm.

  19. Integrated modeling of ozonation for optimization of drinking water treatment

    NARCIS (Netherlands)

    van der Helm, A.W.C.

    2007-01-01

    Drinking water treatment plants automation becomes more sophisticated, more on-line monitoring systems become available and integration of modeling environments with control systems becomes easier. This gives possibilities for model-based optimization. In operation of drinking water treatment

  20. Waste Water Treatment of Dye Contamination

    OpenAIRE

    Pattana Boonyaprapa

    2009-01-01

    The objectives of this research were to study tie-dye process data and wastewater characteristics from 60 entrepreneurs, and to study the colour density treatment in pilot scale by using upflow anaerobic filters. From 60 filled-out questionnaires, it was found that all tie-dye entrepreneurs used reactive dyes by a hot method. Ninety-eight percent of the tie-dye enterpreneurs produced wastewater at the rate of not more than 1500 liters per day. All of them lacked tie-dye wastewater treatment s...

  1. Wetlans, compact and built water treatment systems

    OpenAIRE

    Pečečnik, Denis

    2014-01-01

    In the thesis we discuss small waste water treatment plants (WWTP) up to 2000 PE and we focus on the comparison of different types and strive to extract the best available options for Slovenian users. While different types of WWTP operate on different principles, the particularly important point of use are the enviromantal and economic aspects. In this regard, the most effective are shown to be plant and lagoon WWTP, but their use is limited by the spatial and capacity aspects. If these restr...

  2. Problems of drinking water treatment along Ismailia Canal Province, Egypt.

    Science.gov (United States)

    Geriesh, Mohamed H; Balke, Klaus-Dieter; El-Rayes, Ahmed E

    2008-03-01

    The present drinking water purification system in Egypt uses surface water as a raw water supply without a preliminary filtration process. On the other hand, chlorine gas is added as a disinfectant agent in two steps, pre- and post-chlorination. Due to these reasons most of water treatment plants suffer low filtering effectiveness and produce the trihalomethane (THM) species as a chlorination by-product. The Ismailia Canal represents the most distal downstream of the main Nile River. Thus its water contains all the proceeded pollutants discharged into the Nile. In addition, the downstream reaches of the canal act as an agricultural drain during the closing period of the High Dam gates in January and February every year. Moreover, the wide industrial zone along the upstream course of the canal enriches the canal water with high concentrations of heavy metals. The obtained results indicate that the canal gains up to 24.06x10(6) m3 of water from the surrounding shallow aquifer during the closing period of the High Dam gates, while during the rest of the year, the canal acts as an influent stream losing about 99.6x10(6) m3 of its water budget. The reduction of total organic carbon (TOC) and suspended particulate matters (SPMs) should be one of the central goals of any treatment plan to avoid the disinfectants by-products. The combination of sedimentation basins, gravel pre-filtration and slow sand filtration, and underground passage with microbiological oxidation-reduction and adsorption criteria showed good removal of parasites and bacteria and complete elimination of TOC, SPM and heavy metals. Moreover, it reduces the use of disinfectants chemicals and lowers the treatment costs. However, this purification system under the arid climate prevailing in Egypt should be tested and modified prior to application.

  3. Phyto-treatment of domestic waste water using artificial marshes

    Energy Technology Data Exchange (ETDEWEB)

    Vaca, Rodrigo; Sanchez, Fabian [Oleoducto de Crudos Pesados (OCP), Quito (Ecuador)

    2009-12-19

    The phyto-treatment of domestic waste water by the use of artificial marshes system consists in beds of treatment working in series, this beds are constituted basically by inverse filters of inert granular material where the nutrients are cached from the residual water. Most of the treatment is carried in roots steams and leaves of defined species of plants. The rest of the treatment is performed by anaerobic and aerobic bacteria that grow within the beds. In the proximities of the roots and the area near the bed surface, aerobic processes take place and in deepest zones, anaerobic processes take place. It is desirable that the aerobic process will be the predominant one, mainly to avoid bad odors; this is obtained with the correct selection of plants which must have dense and deep roots. The economic factor is also important for the selection of this type of treatment system, the cost of operation and maintenance is minimum compared with other type of systems. The operation cost is practically zero because it is not required provision of electrical energy for its operation; energy used is the solar energy through the photosynthesis process. The maintenance is reduced to pruning and cleaning that can be performed twice a year. The goals of this paper is to show our experiences during the construction, stabilization and operation of these systems installed in 13 OCP locations with different types of weather and explain the conclusions arrived after construction and operation; present this kind of systems as an alternative of economic wastewater treatment in terms of construction, operation and maintenance and as environment friendly treatment. (author)

  4. Electrochemical Treatment of Water Contaminated with Methylorange

    Directory of Open Access Journals (Sweden)

    Valica Martin

    2016-06-01

    Full Text Available This study examines electrochemical degradation of water artificially contaminated by azo dye Methyl Orange (MO. Degradation is based on chemical electro-oxidation of MO molecules. Graphite was used as an electrode material for electrochemical oxidation of MO. In this work, the different operative parameters (electric current, NaCl content and their effect on effectiveness as well as the treatment time/duration of MO degradation were tested. The highest dye removal (91.0 % was obtained during the electrolysis at current density 3.032 mA/cm2, electrolyte with the content of NaCl 4 g/dm3 (NaCl and the treatment time 35 min.

  5. Fast switching water processable electrochromic polymers.

    Science.gov (United States)

    Shi, Pengjie; Amb, Chad M; Dyer, Aubrey L; Reynolds, John R

    2012-12-01

    This paper describes the synthesis of two new blue to transmissive donor-acceptor electrochromic polymers: a polymer synthesized using an alternating copolymerization route (ECP-Blue-A) and a polymer synthesized using a random copolymerization (ECP-Blue-R) by Stille polymerization. These polymers utilize side chains with four ester groups per donor moiety, allowing organic solubility in the ester form, and water solubility upon saponification to their carboxylate salt form. We demonstrate that the saponified polymer salts of ECP-Blue-A and ECP-Blue-R (WS-ECP-Blue-A and WS-ECP-Blue-R) can be processed from aqueous solutions into thin films by spray-casting. Upon the subsequent neutralization of the thin films, the resulting polymer acid films are solvent resistant and can be electrochemically switched between their colored state and a transmissive state in a KNO(3)/water electrolyte solution. The polymer acids, WS-ECP-Blue-A-acid and WS-ECP-Blue-R-acid, show electrochromic contrast Δ%T of 38% at 655 nm and 39% at 555 nm for a 0.5 s switch, demonstrating the advantage of an aqueous compatible electrochrome switchable in high ionic conductivity aqueous electrolytes. The results of the electrochromic properties study indicate that these polymers are promising candidates for aqueous processable and aqueous switching electrochromic materials and devices as desired for applications where environmental impact is of importance.

  6. Assessment of didecyldimethylammonium chloride as a ballast water treatment method

    NARCIS (Netherlands)

    van Slooten, Cees; Buma, Anita; Peperzak, Louis

    Ballast water-mediated transfer of aquatic invasive species is considered a major threat to marine biodiversity, marine industry and human health. A ballast water treatment is needed to comply with International Maritime Organization (IMO) ballast water discharge regulations. Didecyldimethylammonium

  7. Assessment of didecyldimethylammonium chloride as a ballast water treatment method

    NARCIS (Netherlands)

    van Slooten, C.; Peperzak, L.; Buma, A.G.J.

    2015-01-01

    Ballast water-mediated transfer of aquatic invasive species is considered a major threat to marine biodiversity, marine industry and human health. A ballast water treatment is needed to comply with International Maritime Organization (IMO) ballast water discharge regulations. Didecyldimethylammonium

  8. Assessment of didecyldimethylammonium chloride as a ballast water treatment method

    NARCIS (Netherlands)

    van Slooten, Cees; Buma, Anita; Peperzak, Louis

    2015-01-01

    Ballast water-mediated transfer of aquatic invasive species is considered a major threat to marine biodiversity, marine industry and human health. A ballast water treatment is needed to comply with International Maritime Organization (IMO) ballast water discharge regulations. Didecyldimethylammonium

  9. Case study treatment of waste water for 17α-ethinylestradiol and microorganisms with UV and photocatalysis in an on-going process of introducing AOP techniques in the Danish water sector

    DEFF Research Database (Denmark)

    Madsen, Henrik Tækker; Søgaard, Erik Gydesen

    2012-01-01

    Failure to obtain a sufficient disinfection of waste water, initiated an investigation of the use of UV light and photocatalysis with TiO2 for treating the waste water. Furthermore, the ability of such a system to degrade endocrine disrupting chemicals was investigated through experiments...... with the estrogen 17α-ethinylestradiol (EE2). This study found LP UV lamps to be the optimal solution for disinfection, while photocatalysis with TiO2 was found to be the best method for removal of EE2. The experiments were carried out in a mobile test unit with solution volumes of 30 L. By use of data from...

  10. Treatment of petroleum contaminated soils by hot alkaline water combined with mechanical dewatering process%热碱水洗-机械脱水工艺处理石油污染土壤

    Institute of Scientific and Technical Information of China (English)

    谭蔚; 邢帅; 贡皓霜; 刘丽艳

    2016-01-01

    The treatment of petroleum contaminated soils by hot alkaline water combined with mechanical dewatering process is conducted in an oil field in China.The effect of NaOH concentration,alkaline water-oily sludge ratio and temperature on the oil-removal effect is studied.The factors affecting the filtration and dewatering performance of the petroleum contaminated soils treated by hot alkaline water,such as the types and contents flocculating agents,are also investigated.The results show that residual oil is firstly decreased and then increased with increasing the concentration of NaOH and alkaline water-oily sludge ratio.But,the increase in temperature leds to th drastical decrease in residual oil.The proper parameters for hot alkaline water treatment are 0.2% of NaOH,4:1 of alkaline water-oily sludge ratio and 80℃ of temperature.In the experiments of dewatering,the flocculation capability of AlCl3,Fe2 (SO4) 3 and PAC are strongly influenced by pH.The Ca2+ ions effectively incresase the flocculation of tiny particles by forming Ca(OH) + and Ca(OH) 2,thus greatly improving the filtration and dewatering performance.When the concentration of CaCl2 is 0.8%,the best filtration and dewatering performance can be achieved based on the filtration rate,moisture content and residual oil ratio in the petroleum contaminated soils.%采用热碱水洗-机械脱水工艺对国内某油田区的石油污染土壤进行处理.考察了热碱水洗条件(包括NaOH质量分数、液固比、洗涤温度)对含油土壤脱油效果的影响,及絮凝剂种类、质量分数对热碱水洗法处理后的含油污泥过滤脱水性能的影响.结果表明,残余油质量分数随NaOH质量分数及液固比的升高呈现先下降后上升的趋势,而随温度的升高呈现持续下降的趋势.在探究含油污泥脱水性能实验中发现铝盐及铁盐类絮凝剂对于高碱性污泥的适应性较差,而钙盐可以很好地破坏油水细砂混合层,有效地改善含油

  11. Wastewater treatment process of organic impurities by Fenton reaction

    Directory of Open Access Journals (Sweden)

    Talgat Mauletuly

    2013-09-01

    Full Text Available The method is for the oxidative degradation of organic contaminants of natural, recycled and waste water. As oxidative degradation of the catalyst, compounds of iron, generated directly in the purification process, wherein the oxidation of the organic impurities by molecular oxygen, activated by a pair H2O2/Fe2 , and hydrogen peroxide taken in an amount of 30 - 40% of that stoichiometrically required. The proposed method has the following advantages: improved performance and efficiency of the water treatment while reducing the cost of its holding.

  12. Sodium dichromate as a process water additive: An evaluation

    Energy Technology Data Exchange (ETDEWEB)

    Lutton, J.M.

    1953-03-19

    For several years-after the start-up of the Hanford Piles, little concern was felt for the quality of process water. Techniques developed by CMX and improved in the course of operating experience were substantially successful for controlling and removing pressure drop film; and corru%ion rates at the early power levels were uniformly low and not a matter of concern, particularly since slugs were not exposed for more than 250 MWD/ton. As power and exposure levels were drastically increased, however, corrosion rates began to become serious and now threaten to limit future increases. Whether or not corrosion was causing these latter problems, it was clearly imperative to seek ways to reduce the corrobivity of the water. It was recognized that subtantial savings could be made by the elimination of sodium dichromate as a process water additive. Since the rather high pH of process water was neceasary primarily to prevent dichromate reduction, the way would then be open for reducing the pH, and it was hoped that this would improve in-pile corrosion and materially reduce water treatment costs. There is a large amount of data in the project literature pertaining to the dichromate problem, and it seemed urgent in view of recent experiences to re-evaluate this information to learn whether the issues might not be clarified and firm conclusions reached. This document presents such a re-evaluation and drawn conclusions which pending the completion of experiments now in progress, will serve as a primary basis for technical recommendations concerning dichromate addition to process water at all existing 100 areas and at the 100-K areas now under construction.

  13. Diel biogeochemical processes in terrestrial waters

    Science.gov (United States)

    Compiled and Edited by Nimick, David A.; Gammons, Christopher H.

    2011-01-01

    Many biogeochemical processes in rivers and lakes respond to the solar photocycle and produce persistent patterns of measureable phenomena that exhibit a day-night, or 24-h, cycle. Despite a large body of recent literature, the mechanisms responsible for these diel fluctuations are widely debated, with a growing consensus that combinations of physical, chemical, and biological processes are involved. These processes include streamflow variation, photosynthesis and respiration, plant assimilation, and reactions involving photochemistry, adsorption and desorption, and mineral precipitation and dissolution. Diel changes in streamflow and water properties such as temperature, pH, and dissolved oxygen concentration have been widely recognized, and recently, diel studies have focused more widely by considering other constituents such as dissolved and particulate trace metals, metalloids, rare earth elements, mercury, organic matter, dissolved inorganic carbon (DIC), and nutrients. The details of many diel processes are being studied using stable isotopes, which also can exhibit diel cycles in response to microbial metabolism, photosynthesis and respiration, or changes in phase, speciation, or redox state. In addition, secondary effects that diel cycles might have, for example, on biota or in the hyporheic zone are beginning to be considered. This special issue is composed primarily of papers presented at the topical session "Diurnal Biogeochemical Processes in Rivers, Lakes, and Shallow Groundwater" held at the annual meeting of the Geological Society of America in October 2009 in Portland, Oregon. This session was organized because many of the growing number of diel studies have addressed just a small part of the full range of diel cycling phenomena found in rivers and lakes. This limited focus is understandable because (1) fundamental aspects of many diel processes are poorly understood and require detailed study, (2) the interests and expertise of individual

  14. Characterization of hydraulic fracturing flowback water in Colorado: Implications for water treatment

    Science.gov (United States)

    Lester, Yaal; Ferrer, Imma; Thurman, E. Michael; Sitterley, Kurban A.; Korak, Julie A.; Aiken, George R.; Linden, Karl G.

    2015-01-01

    A suite of analytical tools was applied to thoroughly analyze the chemical composition of an oil/gas well flowback water from the Denver–Julesburg (DJ) basin in Colorado, and the water quality data was translated to propose effective treatment solutions tailored to specific reuse goals. Analysis included bulk quality parameters, trace organic and inorganic constituents, and organic matter characterization. The flowback sample contained salts (TDS = 22,500 mg/L), metals (e.g., iron at 81.4 mg/L) and high concentration of dissolved organic matter (DOC = 590 mgC/L). The organic matter comprised fracturing fluid additives such as surfactants (e.g., linear alkyl ethoxylates) and high levels of acetic acid (an additives' degradation product), indicating the anthropogenic impact on this wastewater. Based on the water quality results and preliminary treatability tests, the removal of suspended solids and iron by aeration/precipitation (and/or filtration) followed by disinfection was identified as appropriate for flowback recycling in future fracturing operations. In addition to these treatments, a biological treatment (to remove dissolved organic matter) followed by reverse osmosis desalination was determined to be necessary to attain water quality standards appropriate for other water reuse options (e.g., crop irrigation). The study provides a framework for evaluating site-specific hydraulic fracturing wastewaters, proposing a suite of analytical methods for characterization, and a process for guiding the choice of a tailored treatment approach.

  15. Fixed-biofilm reactors applied to waste water treatment and aquacultural water recirculating systems

    OpenAIRE

    Bovendeur, J.

    1989-01-01

    Fixed-biofilm waste water treatment may be regarded as one of the oldest engineered biological waste water treatment methods. With the recent introduction of modern packing materials, this type of reactor has received a renewed impuls for implementation in a wide field of water treatment.

    In this thesis the possibilities are presented for fixed-film post-treatment of anaerobically digested domestic sewage and water reconditioning in aquacultural water recirculation systems. Emphasis i...

  16. Cooling water systems design using process integration

    CSIR Research Space (South Africa)

    Gololo, KV

    2010-09-01

    Full Text Available Cooling water systems are generally designed with a set of heat exchangers arranged in parallel. This arrangement results in higher cooling water flowrate and low cooling water return temperature thus reducing cooling tower efficiency. Previous...

  17. Case study treatment of waste water for 17α-ethinylestradiol and microorganisms with UV and photocatalysis in an on-going process of introducing AOP techniques in the Danish water sector

    DEFF Research Database (Denmark)

    Madsen, Henrik Tækker; Søgaard, Erik Gydesen

    2012-01-01

    Failure to obtain a sufficient disinfection of waste water, initiated an investigation of the use of UV light and photocatalysis with TiO2 for treating the waste water. Furthermore, the ability of such a system to degrade endocrine disrupting chemicals was investigated through experiments...... with the estrogen 17α-ethinylestradiol (EE2). This study found LP UV lamps to be the optimal solution for disinfection, while photocatalysis with TiO2 was found to be the best method for removal of EE2. The experiments were carried out in a mobile test unit with solution volumes of 30 L. By use of data from...... the real UV system, the effect found in the experiments were extrapolated and used to evaluate the efficiency of the current system....

  18. Research progress of novel adsorption processes in water purification:A review

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    As an effective, efficient, and economic approach for water purification, adsorbents and adsorption processes have been widely studied and applied in different aspects for a long time. In the recent years, a lot of novel adsorption processes have been developed for enhancing the efficiency of removing the organic and inorganic contaminants from water. This article reviews some new adsorbents and advanced adsorption methods that specialize in their compositions, structures, functions, and characteristics used in water treatment. The review emphasizes adsorption/catalytic oxidation process, adsorption/catalytic reduction process, adsorption coupled with redox process, biomimetic sorbent and its sorption behaviors of POPs, and modified adsorbents and their water purification efficiency.

  19. 微絮凝过滤工艺在建筑景观水处理中的应用%Application of micro lfocculation ifltration process in water treatment of architectural landscape

    Institute of Scientific and Technical Information of China (English)

    高文琪

    2016-01-01

    In this paper, micro-flocculation filtration process as the theme, to explore the issues related to water treatment applications in architectural landscape.First, a brief overview of them,mainly from the raw water quality, reagents, detection methods, experimental apparatus aspects of the experiments described, focusing on the experimental data obtained by analyzing the coagulant dosage in addition to the effects of pollution on the effect of the coagulant effect of dosage of decontamination effect, the filtration rate of addition to the effect of pollution impact. We hope to provide some valuable information through the preliminary analysis of this paper can work for respect, for reference.%本文以微絮凝过滤工艺为主题,探讨其在建筑景观水处理应用方面的相关问题。首先对其进行了简要概述,主要从原水水质、试剂、检测方法、实验装置方面进行了实验说明,重点通过实验所得数据,分析了混凝剂投加量对除污染效果的影响、助凝剂投加量对除污染效果的影响、滤速对除污染效果的影响。希望通过本文初步分析可以为该方面的研究工作提供一些有价值的信息,以供参考。

  20. Costs of water treatment due to diminished water quality: A case study in Texas

    Science.gov (United States)

    Dearmont, David; McCarl, Bruce A.; Tolman, Deborah A.

    1998-04-01

    The cost of municipal water treatment due to diminished water quality represents an important component of the societal costs of water pollution. Here the chemical costs of municipal water treatment are expressed as a function of raw surface water quality. Data are used for a 3-year period for 12 water treatment plants in Texas. Results show that when regional raw water contamination is present, the chemical cost of water treatment is increased by 95 per million gallons (per 3785 m3) from a base of 75. A 1% increase in turbidity is shown to increase chemical costs by 0.25%.

  1. 7 CFR 305.22 - Hot water immersion treatment schedules.

    Science.gov (United States)

    2010-01-01

    ... 7 Agriculture 5 2010-01-01 2010-01-01 false Hot water immersion treatment schedules. 305.22 Section 305.22 Agriculture Regulations of the Department of Agriculture (Continued) ANIMAL AND PLANT HEALTH INSPECTION SERVICE, DEPARTMENT OF AGRICULTURE PHYTOSANITARY TREATMENTS Heat Treatments § 305.22 Hot water immersion treatment schedules. (a) T102-d...

  2. Treatment of municipal sewage sludge in supercritical water: A review.

    Science.gov (United States)

    Qian, Lili; Wang, Shuzhong; Xu, Donghai; Guo, Yang; Tang, Xingying; Wang, Laisheng

    2016-02-01

    With increasing construction of wastewater treatment plants and stricter policies, municipal sewage sludge (MSS) disposal has become a serious problem. Treatment of MSS in supercritical water (SCW) can avoid the pre-drying procedure and secondary pollution of conventional methods. SCW treatment methods can be divided into supercritical water gasification (SCWG), supercritical water partial oxidation (SCWPO) and supercritical water oxidation (SCWO) technologies with increasing amounts of oxidants. Hydrogen-rich gases can be generated from MSS by SCWG or SCWPO technology using oxidants less than stoichiometric ratio while organic compounds can be completely degraded by SCWO technology with using an oxidant excess. For SCWG and SCWPO technologies, this paper reviews the influences of different process variables (MSS properties, moisture content, temperature, oxidant amount and catalysts) on the production of gases. For SCWO technology, this paper reviews research regarding the removal of organics with or without hydrothermal flames and the changes in heavy metal speciation and risk. Finally, typical systems for handling MSS are summarized and research needs and challenges are proposed.

  3. Application of preparation process of high pure chlorine dioxide by electrolysis method in water treatment%电解法制高纯二氧化氯工艺在水处理中的应用

    Institute of Scientific and Technical Information of China (English)

    刘艳霞; 韩瑞雄; 赵红; 周俊波

    2011-01-01

    为了开发经济实用的二氧化氯消毒工艺,对电解法制备高纯二氧化氯工艺在水处理中的运用进行了研究.在最佳条件下,电解氯酸盐自动催化循环制备的二氧化氯纯度可达98%左右.通过二氧化氯杀菌除藻试验,讨论了二氧化氯用量以及原水pH对细菌、叶绿素a、藻类的去除率的影响.结果表明,二氧化氯用量在2 mg/L以上时,3者的去除率均达到90%以上.当二氧化氯用量为2 mg/L、原水pH为6~9时,3者的去除率不发生显著变化,并且二氧化氯的剩余质量浓度均控制在0.5 mg/L以下.消毒成本:生产1 kg二氧化氯成本可以控制在6元以内,当二氧化氯用量在0.5 ~2 mg/L时,1 t水的消毒成本为0.003~ 0.012元.%To develop an economical and practical disinfection technology of chlorine dioxide, the application of preparation process of high pure chlorine dioxide by electrolysis method in water treatment was studied. Under the best conditions, the purity of chlorine dioxide, which was prepared by electrolysis of chlorate solution with auto-catalytic cycling,can reach about 98% . Through the experiments of algae removal and sterilization,the influences of concentration of chlorine dioxide and pH of raw water on the removal rate of bacteria,chlorophyll A ,and algal were discussed. Results showed that when the mass concentration of chlorine dioxide was above 2 mg/L, the removal rates of bacteria, chlorophyll A, and algal could all reached above 90% . When the mass concentration of chlorine dioxide was 2 mg/L and pH of raw water was at 6 ~9,the removal rates of them could not occur significant change, and the mass concentration of residual chlorine dioxide was all under 0. 5 mg/L. Though accounting for the cost of water disinfection, the cost of per kilogram chlorine dioxide in the process can be controlled less than RMB 6 Yuan. When the invested amount of chlorine dioxide was at 0.5 ~2 mg/L,and the cost of per ton water disinfection

  4. Natural/mine water deep treatment modular system

    Energy Technology Data Exchange (ETDEWEB)

    Averin, G.V.; Biochenko, V. [Makeyevka Safety in Mines Research Institute, Makeyevka (Ukraine)

    1997-12-31

    Shortage of water of service and drinking standards is heavily felt in some industries and residential areas in Donetsk region. Modifications of a natural/mine water deep treatment modular system can be used: to produce service water from mine and natural water sources for further use in industry and household applications; to restore industrial waste waters to ecological standards; to provide tertiary treatment, producing the highest quality of drinking water. The system is briefly described and its specifications are given. Three modifications of modular design are expected to be made of the mine/natural water treatment system. 1 fig., 1 tab.

  5. Establishing solar water disinfection as a water treatment method at household level

    Directory of Open Access Journals (Sweden)

    Regula Meierhofer

    2006-12-01

    Full Text Available 1.1 billion People worldwide do not have access to safe drinking water and therefore are exposed to a high risk for diarrhoeal diseases. As a consequence, about 6,000 children die each day of dehydration due to diarrhoea. Adequate water treatment methods and safe storage of drinking water, combined with hygiene promotion, are required to prevent the population without access to safe drinking water from illness and death. Solar water disinfection (SODIS is a new water treatment to be applied at household level with a great potential to reduce diarrhoea incidence of users. The method is very simple and the only resources required for its application are transparent PET plastic bottles (or glass bottles and sufficient sunlight: microbiologically contaminated water is filled into the bottles and exposed to the full sunlight for 6 hours. During solar exposure, the diarrhoea causing pathogens are killed by the UV-A radiation of the sunlight. At present, SODIS is used by about 2 Million users in more than 20 countries of the South. Diarrhoea incidence of users significantly has been reduced by 30 to 70 %. A careful and long-term community education process that involves creating awareness on the importance of treating drinking water and initiates behaviour change is required to establish the sustainable practice of SODIS at community level. In Madagascar, more than 160 children younger than 5 years die each day from malaria, diarrhoea and acute respiratory illnesses. The application of household water treatment methods such as SODIS significantly could contribute to improve their health.

  6. Concentration of Trichloronitromethane in Conventional Water Treatment Process%常规净水工艺中三氯硝基甲烷质量浓度分布调查

    Institute of Scientific and Technical Information of China (English)

    高乃云; 方诚; 楚文海

    2012-01-01

    A sampling survey investigated the formation of a nitrogenous disinfection by-product trichloronitromethane (TCNM) from pre-chlorination, and the reduction of TCNM concentrations by subsequent conventional water treatment processes, i. e. coagulation, sedimentation, and filtration, with different seasons. The level of the measured TCNM had little change with the seasons, and were closely correlated with the dissolved organic nitrogen (DON), suggesting that DON plays an essential role in the formation of TCNM. The conventional treatment-filtration had a certain effect on the reduction of TCNM.%对采用预氯化工艺的上海某水厂常规净水工艺出水中的典型含氮消毒副产物( N-DBPs)三氯硝基甲烷(TCNM)进行了取样调查,研究了不同季节各工艺单元出水中TCNM 的质量浓度分布,以及过滤工艺对TCNM的去除效果;同时也初步探讨了TCNM与溶解性有机氮(DON)和溶解性有机碳(DOC)之间的关系.研究表明,在该水厂的常规净水工艺中,普遍检测到TCNM的存在,其质量浓度随季节变化并不明显,与水中DON的质量浓度存在较密切的联系;此外,传统净水工艺中,过滤对三氯硝基甲烷有着良好的去除效果.

  7. Treatment of waste thermal waters by ozonation and nanofiltration.

    Science.gov (United States)

    Kiss, Z L; Szép, A; Kertész, S; Hodúr, C; László, Z

    2013-01-01

    After their use for heating, e.g. in greenhouses, waste thermal waters may cause environmental problems due to their high contents of ions, and in some cases organic matter (associated with an oxygen demand) or toxic compounds. The aims of this work were to decrease the high organic content of waste thermal water by a combination of ozone treatment and membrane separation, and to investigate the accompanying membrane fouling. The results demonstrated that the chemical oxygen demand and the total organic content can be effectively decreased by a combination of ozone pretreatment and membrane filtration. Ozone treatment is more effective for phenol elimination than nanofiltration alone: with a combination of the two processes, 100% elimination efficiency can be achieved. The fouling index b proved to correlate well with the fouling and polarization layer resistances.

  8. Waste Water Treatment of Dye Contamination

    Directory of Open Access Journals (Sweden)

    Pattana Boonyaprapa

    2009-01-01

    Full Text Available The objectives of this research were to study tie-dye process data and wastewater characteristics from 60 entrepreneurs, and to study the colour density treatment in pilot scale by using upflow anaerobic filters. From 60 filled-out questionnaires, it was found that all tie-dye entrepreneurs used reactive dyes by a hot method. Ninety-eight percent of the tie-dye enterpreneurs produced wastewater at the rate of not more than 1500 liters per day. All of them lacked tie-dye wastewater treatment systems. Eighty-five percent of tie-dye entrepreneurs agreed that there must be wastewater treatment before release into the environment. From group discussions, it was found that the entrepreneurs realized the wastewater problem and wanted to carry out environment friendly tie-dyeing. Our study demonstrated that the average value of the colour density, chemical oxygen demand (COD, total dissolved solids (TDS and pH of the wastewater characteristics were 170 SU (space units, 1584 mg/l, 2487 mg/l and 8, respectively. For the upflow anaerobic filter, 5 sets of experiments, with 24 hours retention time, were designed, with 0, 1, 2, 3 and 4 % of cow’s feces ferment, respectively (sets 1st-5th. The result showed decreasing colour densities from 170 SU to 160 SU (dark colour, 60 SU (very light colour, 12 SU (no colour, 10 SU (no colour and 10 SU (no colour, respectively. We conclude that the upflow anaerobic filter, containing 2% cow’s feces ferment is an efficient way to reduce colour density of the wastewater. Mixing cow’s feces ferment with tie-dye wastewater increased COD and TDS in wastewater. Mean COD was increased by residual organic matter from 1584 mg/l (before treatment to (after-treatment, sets 2nd- 5th 1600 mg/l, 1680 mg/l, 1710 mg/l and 1750 mg/l, respectively. COD aftertreatment was higher than the industrial effluence standard (400 mg/l. Further treatment COD might include wetland procedures. TDS was increased by some residual organic matter

  9. Treatment of waste water from a colloid sulfur washing department

    Energy Technology Data Exchange (ETDEWEB)

    Stepanenko, E.K.; Pivovarova, L.I.; Gumarova, M.M.; Kulik, G.I.; Khrapunova, G.G.

    1988-08-01

    Discusses a method for treatment of waste water from arsenic-sodium purification of coal gas in the Moscow gasworks. Waste water from sulfur washing is characterized: total content of various chemical compounds 90-120 g/l, pH value 8, arsenic content 300-500 mg/l, sulfur content 1.5-2.3 g/l. The flotation separation process used on a laboratory scale is evaluated: a 200 ml waste water sample was mixed intensively with 1 ml surfactants for 1.5-2.0 min. The mixture was then fed into a flotation column. Air supply rate of 20 m/h was used. Three flotation schemes are comparatively evaluated: without surfactants, with polyacrylamide and with polyvinyl alcohol with desulfurization efficiency of 86.7%, 87.5% and 96.6% respectively. Consumption rate of polyvinyl alcohol was 125 mg/l. 4 refs.

  10. Advanced water treatment as a tool in water scarcity management

    DEFF Research Database (Denmark)

    Harremoes, Poul

    2000-01-01

    The water resource is under increasing pressure, both from the increase in population and from the wish to improve the living standards of the individual. Water scarcity is defined as the situation where demand is greater than the resource. Water scarcity has two distinctly different dimensions......: water availability and water applicability. The availability is a question of quantitative demand relative to resource. The applicability is a question of quality suitability for the intended use of the water. There is a significant difference in this regard with respect to rural versus urban use...... of water. In the former case, the water is lost by evaporation and polluted. In the latter case, the water is not lost but heavily polluted. With increasing scarcity, the value of water and the need for controls increase. In this situation, water reuse becomes an option that has been considered exotic...

  11. QSAR enabled predictions in water treatment: from data to mechanisms and vice-versa

    NARCIS (Netherlands)

    Vries, D.; Wols, B.A.; de Voogt, P.

    2012-01-01

    The efficiency of water treatment systems to remove emerging (chemical) substances is often unknown. Consequently, the prediction of the removal of contaminants in the treatment and supply chain of drinking water is of great interest. By collecting and processing existing chemical properties of

  12. QSAR enabled predictions in water treatment: from data to mechanisms and vice-versa

    NARCIS (Netherlands)

    Vries, D.; Wols, B.A.; de Voogt, P.

    2012-01-01

    The efficiency of water treatment systems to remove emerging (chemical) substances is often unknown. Consequently, the prediction of the removal of contaminants in the treatment and supply chain of drinking water is of great interest. By collecting and processing existing chemical properties of cont

  13. QSAR enabled predictions in water treatment: from data to mechanisms and vice-versa

    NARCIS (Netherlands)

    Vries, D.; Wols, B.A.; de Voogt, P.

    2012-01-01

    The efficiency of water treatment systems to remove emerging (chemical) substances is often unknown. Consequently, the prediction of the removal of contaminants in the treatment and supply chain of drinking water is of great interest. By collecting and processing existing chemical properties of cont

  14. Evaluation of appropriate technologies for grey water treatments and reuses.

    Science.gov (United States)

    Li, Fangyue; Wichmann, Knut; Otterpohl, Ralf

    2009-01-01

    As water is becoming a rare resource, the onsite reuse and recycling of grey water is practiced in many countries as a sustainable solution to reduce the overall urban water demand. However, the lack of appropriate water quality standards or guidelines has hampered the appropriate grey water reuses. Based on literature review, a non-potable urban grey water treatment and reuse scheme is proposed and the treatment alternatives for grey water reuse are evaluated according to the grey water characteristics, the proposed standards and economical feasibility.

  15. Water quality and treatment of river bank filtrate

    Directory of Open Access Journals (Sweden)

    W. W. J. M. de Vet

    2010-06-01

    Full Text Available In drinking water production, river bank filtration has the advantages of dampening peak concentrations of many dissolved components, substantially removing many micropollutants and removing, virtually completely, the pathogens and suspended solids. The production aquifer is not only fed by the river bank infiltrate but also by water percolating through covering layers. In the polder areas, these top layers consist of peat and deposits from river sediments and sea intrusions.

    This paper discusses the origin and fate of macro components in river bank filtrate, based on extensive full-scale measurements in well fields and treatment systems of the Drinking Water Company Oasen in the Netherlands. First, it clarifies and illustrates redox reactions and the mixing of river bank filtrate and PW as the dominant processes determining the raw water quality for drinking water production. Next, full-scale results are elaborated on to evaluate trickling filtration as an efficient and proven one-step process to remove methane, iron, ammonium and manganese. The interaction of methane and manganese removal with nitrification in these systems is further analyzed. Methane is mostly stripped during trickling filtration and its removal hardly interferes with nitrification. Under specific conditions, microbial manganese removal may play a dominant role.

  16. Petroleum coke adsorption as a water management option for oil sands process-affected water

    Energy Technology Data Exchange (ETDEWEB)

    Zubot, Warren [Syncrude Canada Ltd., Research and Development, Edmonton, Alberta, Canada T6N 1H4 (Canada); MacKinnon, Michael D. [OSPM Solutions Ltd., Hamilton, Ontario, Canada L8H 6X2 (Canada); Chelme-Ayala, Pamela; Smith, Daniel W. [University of Alberta, Department of Civil and Environmental Engineering, Edmonton, Alberta, Canada T6G 2W2 (Canada); Gamal El-Din, Mohamed, E-mail: mgamalel-din@ualberta.ca [University of Alberta, Department of Civil and Environmental Engineering, Edmonton, Alberta, Canada T6G 2W2 (Canada)

    2012-06-15

    Water is integral to both operational and environmental aspects of the oil sands industry. A water treatment option based on the use of petroleum coke (PC), a by-product of bitumen upgrading, was examined as an opportunity to reduce site oil sands process-affected water (OSPW) inventories and net raw water demand. Changes in OSPW quality when treated with PC included increments in pH levels and concentrations of vanadium, molybdenum, and sulphate. Constituents that decreased in concentration after PC adsorption included total acid-extractable organics (TAO), bicarbonate, calcium, barium, magnesium, and strontium. Changes in naphthenic acids (NAs) speciation were observed after PC adsorption. A battery of bioassays was used to measure the OSPW toxicity. The results indicated that untreated OSPW was toxic towards Vibrio fischeri and rainbow trout. However, OSPW treated with PC at appropriate dosages was not acutely toxic towards these test organisms. Removal of TAO was found to be an adsorption process, fitting the Langmuir and Langmuir-Freundlich isotherm models. For TAO concentrations of 60 mg/L, adsorption capacities ranged between 0.1 and 0.46 mg/g. This study demonstrates that freshly produced PC from fluid cokers provides an effective treatment of OSPW in terms of key constituents' removal and toxicity reduction. - Highlights: Black-Right-Pointing-Pointer Treatment of oil sands process-affected water (OSPW) using petroleum coke (PC) adsorption was investigated. Black-Right-Pointing-Pointer PC was effective at adsorbing naphthenic acids with higher cyclicity. Black-Right-Pointing-Pointer OSPW treated with PC at appropriate dosages was not toxic towards Vibrio fisheri and rainbow trout. Black-Right-Pointing-Pointer The adsorption of organic acids fitted the Langmuir and Langmuir-Freundlich isotherm models. Black-Right-Pointing-Pointer PC has the potential to be an effective adsorbent to treat OSPW either directly or as a pretreatment step.

  17. Effectiveness of Integrated Device of Ultrafiltration Process for Treatment of High Algae-Laden Raw Water from Minjiang River%超滤一体化装置处理闽江高含藻原水的效果

    Institute of Scientific and Technical Information of China (English)

    林茜; 范功端; 魏忠庆; 黄功洛; 苏昭越; 陈丽茹; 林茹晶

    2015-01-01

    考察了集混凝—斜管沉淀—超滤于一体的装置在高藻水期对闽江水的净水效果。结果表明超滤一体化装置出水浊度小于0.1 NTU,浊度去除率达到99%以上;出水CODMn均值为1.40 mg/L,出水UV254为0.024 cm-1,CODMn和UV254去除率分别为57.3%和50.1%;出水细菌含量低于《生活饮用水标准》( GB 5749—2006)的限值,细菌去除率大于99%。超滤组合工艺对藻类处理效果优于水厂工艺,藻类总去除率为99.3%。当膜通量下降时,缩短过滤时间、延长反冲洗时间可以使膜通量恢复;当超滤膜出现不可逆污染时,通过CIP清洗恢复膜过滤性能。在高藻水期,水温对膜通量和TMP影响较小,在保证出水水质的前提下,较大的膜通量运行更节能。%An integrated device of ultrafiltration in combination with coagulation and sedimentation was built to treat Minjiang river water, and the treatment effect during high algae laden period was investigated.The results show that turbidity of effluent is less than 0.1 NTU, and removal rate of turbidity is 99%.CODMn and UV254 of effluent are 1.40 mg/L and 0.024 cm-1 , respectively, and the corresponding removal rates are 57.3%and 50.1%.The number of bacteria of effluent is less than the limit value from Drinking Water Standards (GB 5749—2006), and removal rate is higher than 99%.The removal effect of algae with combined process is better than that with traditional process in water plant at present, the removal rate of algae is 99.3%.Decreasing the filtering time and prolonging the back flushing time is able to restore the membrane flux.If there is irreversible pollution on ultrafiltration membrane, cleaning in place ( CIP) is effective restoring the membrane filtration performance.In the high algae-laden period, water temperature has no significant influence on membrane flux and trans-membrane pressure ( TMP) , and therefore using larger membrane flux

  18. DECOLORIZATION OF PROCESS WATERS IN DEINKING MILLS AND SIMILAR APPLICATIONS: A REVIEW

    Directory of Open Access Journals (Sweden)

    Patrick Huber,

    2012-01-01

    Full Text Available Process waters in deinking mills often feature a strong coloration, due to dyes and pigments released from the recovered paper. This can usually be remediated by pulp bleaching treatment with appropriate chemicals. However, the red shade (from rhodamine dye is resistant to conventional bleaching treatments. This largely limits the use of deinked pulp in white paper grades. In this review, the available technologies for process water decolorization are discussed (chemical methods, physico-chemical methods and biological treatments. Ozonation of the process water appears to be the most promising technique for decolorization of process water in deinking mills. Other emerging technologies such as photo-catalytic treatment or mineralization by white-rot fungi (after adsorption on low-cost agricultural residues should be considered as well.

  19. Design of a process for supercritical water desalination with zero liquid discharge

    NARCIS (Netherlands)

    Odu, Samuel Obarinu; van der Ham, Aloysius G.J.; Metz, S.; Kersten, Sascha R.A.

    2015-01-01

    Conventional desalination methods have a major drawback; the production of a liquid waste stream which must be disposed. The treatment of this waste stream has always presented technical, economic, and environmental challenges. The supercritical water desalination (SCWD) process meets these

  20. Tertiary Treatment Process of Preserved Wastewater

    Directory of Open Access Journals (Sweden)

    Wang Qingyu

    2016-01-01

    Full Text Available The effects of the composite coagulants on coagulation sedimentation for the preserved wastewater was investigated by changing the composite coagulant dosages, and the coagulant was composed of polymeric ferric sulfate (PFS, polyaluminium chloride (PAC, and polyaluminum ferric silicate (PAFSC, while the effect of the tertiary treatment process on the preserved wastewater was tested, which was exceeded the standard seriously. The results showed that 400 mg/L was the optimum composite coagulant dosage. The removal rates of salt and sugar were as high as 99.1% and 99.5% respectively, and the removal rates of CODCr and SS were 99.3% and 96.0%, respectively after the preserved wastewater was treated by the tertiary treatment technology, which both reached the primary standard of “The Integrated Wastewater Discharge Standard” (GB8978-1996.

  1. Overview on Treatment and Control Technology for Water Eutrophication

    Institute of Scientific and Technical Information of China (English)

    Anfeng; LI; Tao; PAN; Chong; YANG; Xiang; HU; Jianping; LIU; Chengxi; WU

    2013-01-01

    Eutrophication is one of the important reasons for water pollution and is also the problem for water pollution treatment at home and abroad. This article takes an overview on various technical methods and their characteristics applicable for treatment and control of water eutrophication from the aspects of physics, chemistry, biochemistry and environmental factors regulation, and discusses the application and development trend for relevant technologies.

  2. Investigation Of Ballast Water Treatment’s Effect On Corrosion

    Science.gov (United States)

    2013-03-01

    treatment methods on various alloys routinely encountered in ballast tanks and ballast water systems aboard both fresh water and ocean going vessels...Controlled laboratory tests were conducted using simulated chlorination, deoxygenation and chlorine dioxide disinfection. Materials were exposed to three...far as is practicable. 17. Key Words Corrosion, ballast water treatment, deoxygenation , chlorination, chlorine dioxide 18. Distribution

  3. Desalting a process cooling water using nanofiltration

    NARCIS (Netherlands)

    Radier, R.G.J.; van Oers, C.W.; Steenbergen, A.; Wessling, Matthias

    2001-01-01

    The cooling water system of a chemical plant of Akzo Nobel is a partly open system. The site is located at the North Sea. The air in contact with the cooling water contains seawater droplets dissolving and increasing the chloride concentration. The cooling water contains chromate to protect the inst

  4. Characterization of NORM material produced in a water treatment plant

    Energy Technology Data Exchange (ETDEWEB)

    Suursoo, S.; Kiisk, M.; Jantsikene, A.; Koch, R.; Isakar, K.; Realo, E. [University of Tartu, Institute of Physics (Estonia); Lumiste, L. [Tallinn University of Technology (Estonia)

    2014-07-01

    In February 2012 a water treatment plant was opened in Viimsi, Estonia. The plant is designed for removal of iron, manganese, and radium from groundwater. The first 2 years of operation have shown that the purification process generates significant amounts of materials with elevated radium levels. The treatment plant is fed by nine wells, which open to radium-rich aquifers. Purification is achieved by aeration and filtration processes. Aerated water is led through two successive filter columns, first of them is filled with MnO{sub 2} coated material FMH and filtration sand, the second one with zeolite. The plant has five parallel treatment lines with a total of 95 tons of FMH + filtration sand, and 45 tons of zeolite. The average capacity of the facility has been 2400 m{sup 3}/day. Yearly input of radium to the plant is estimated to be 325 MBq for Ra-226, and 420 MBq for Ra-228. Most of the radium (about 90%) accumulates in the filter columns. Some 8-9% of it is removed by backwash water during regular filter backwash cycles. To characterize radium accumulation and its removal by backwash in detail, treatment line no. 5 is sampled monthly for filter materials and backwash water. A steady growth of radium activity concentrations is apparent in both filter materials. In the top layer of the first stage filter (FMH+sand), Ra-226 and Ra-228 activity concentrations (per unit dry weight) reached (1540 ± 60) Bq/kg and (2510 ± 50) Bq/kg (k=2), respectively, by April 2013. At the same time, radium content in the top layer of the second stage filter (zeolite) was an order of magnitude higher: (19 600 ± 130) Bq/kg for Ra-226, and (22 260 ± 170) Bq/kg for Ra-228 (k=2). Radium is not evenly distributed throughout the filter columns. A rough estimate can be given that after 1.25 years of operation (by April 2013) the accumulated activities in treatment line no. 5 reached 1000 MBq for Ra-226 and 1200 MBq for Ra-228. Although filters are the most important type of NORM

  5. Impact of Untreated Sedimentation Tank Sludge Water Recycle on Water Quality During Treatment of Low Turbidity Water

    Institute of Scientific and Technical Information of China (English)

    Ronggang Xu; Yongpeng Xu; Fuyi Cui; Li He; Dong Wang; Qingfeng Su

    2015-01-01

    The overall purpose of this research is to examine the impact of untreated sedimentation tank sludge water ( USTSW) recycle on water quality during treatment of low turbidity water in coagulation—sedimentation processes. 950 mL of raw water and different concentrations of 50 mL USTSW are injected into six 1 000 mL beakers without coagulant.The results indicate that USTSW characterized as accumulated suspended solids and organic matter has active ingredients, which possess the equivalent function of coagulant. The optimal blended water turbidity is in the range of 10-20 NTU, within which USTSW recycle achieves the highest save coagulant rate. The mechanism of strengthening coagulation effect when USTSW recycle mainly depends on the chemical effect and physical effect. What is more, through scanning electron microscopy ( SEM) , it is found that the floc structures with USTSW recycle are more compact than those without USTSW recycle. Besides, the water quality parameters of color, NH3⁃N, CODMn , UV254 , total aluminum, total manganese when USTSW recycle is better than the raw water without recycle, indicating that USTSW recycle can improve water quality with strengthening coagulation effect.

  6. Fixed-biofilm reactors applied to waste water treatment and aquacultural water recirculating systems

    NARCIS (Netherlands)

    Bovendeur, J.

    1989-01-01

    Fixed-biofilm waste water treatment may be regarded as one of the oldest engineered biological waste water treatment methods. With the recent introduction of modern packing materials, this type of reactor has received a renewed impuls for implementation in a wide field of water treatment.

    In

  7. Fixed-biofilm reactors applied to waste water treatment and aquacultural water recirculating systems.

    NARCIS (Netherlands)

    Bovendeur, J.

    1989-01-01

    Fixed-biofilm waste water treatment may be regarded as one of the oldest engineered biological waste water treatment methods. With the recent introduction of modern packing materials, this type of reactor has received a renewed impuls for implementation in a wide field of water treatment.In this the

  8. Aluminum-Based Water Treatment Residue Reuse for Phosphorus Removal

    Directory of Open Access Journals (Sweden)

    Lai Yoke Lee

    2015-04-01

    Full Text Available Aluminum-based water treatment residue (Al-WTR generated during the drinking water treatment process is a readily available recycled material with high phosphorus (P adsorption capacity. The P adsorption capacity of Al-WTR generated from Singapore’s water treatment plant was evaluated with reference to particle size range, adsorption pH and temperature. Column tests, with WTR amendments in sand with and without compost, were used to simulate the bioretention systems. The adsorption rate decreased with increasing WTR sizes. Highest P adsorption capacity, 15.57 mg PO43−-P/g WTR, was achieved using fine WTR particles (>50% particles at less than 0.30 mm. At pH 4, the contact time required to reduce effluent P concentration to below the detectable range was half compared with pH 7 and 9. The adsorption rate observed at 40 ± 2 °C was 21% higher compared with that at 30 ± 2 °C. Soil mixes amended with 10% WTR and compost were able to maintain consistently high (90% total phosphorus (TP removal efficiency at a TP load up to 6.45 g/m3. In contrast, TP removal efficiencies associated with columns without WTR amendment decreased to less than 45% as the TP load increased beyond 4.5 g/m3. The results showed that WTR application is beneficial for enhanced TP removal in bioretention systems.

  9. 反渗透水处理工艺在米脂天然气处理厂的应用%Reverse osmosis water treatment process in the application of Mizhi gas treatment plant

    Institute of Scientific and Technical Information of China (English)

    徐东; 张祥光; 杜燕丽; 龚浩研; 马鹏飞

    2011-01-01

    Counter-seepage technology has already been widespreadly applied in each domain. In my factory,it uses the counter-seepage aqueous plant to provide Mizhi shifts the life tap water.Also it has the very vital practical significance regarding the counter-see%反渗透已经广泛应用在各个领域,本厂利用反渗透水处理装置来提供米脂倒班点的生活饮用水。对于反渗透的研究也就有很重要的现实意义。本文主要从本厂反渗透的工艺流程的介绍对反渗透装置有足够认识,在通过生产现状的描述记录,找出反渗透装置的运行不足之处。并且测得实际本厂反渗透水回收率,找到了影响本厂节能节耗的主要因素。最后分析反渗透装置在生产中常见的事故。以便日常生产维修。

  10. [Immediate cooling with water: emergency treatment of burns].

    Science.gov (United States)

    Latarjet, J

    1990-01-01

    Experimental data have demonstrated that prolonged immediate cooling with cold water is the best first-aid treatment for burn injuries. However in France, this treatment is rarely applied; instead old, inefficient and aggravating methods are still very popular. Pediatricians must help to change this practice by recommending immediate cold water treatment for burns in children.

  11. Minding your R and Q's. Improving water treatment plant performance

    Energy Technology Data Exchange (ETDEWEB)

    Weir, Judy [Thermal Chemistry Limited, Hamilton (New Zealand); Addison, David

    2012-09-15

    Water treatment plants need to reliably produce water with the correct quality and required quantity for boiler and heat recovery steam generator feedwater, gas turbine water injection, or co-generation plant feedwater. Without the quality guarantees, the process that utilises the water will suffer from corrosion and/or deposition issues, and if the quantity is not produced reliably, then the process which uses the final water product cannot operate correctly. This paper discusses the practical tools to ensure ''Reliability'', ''Quality'' and ''Quantity'' - the ''R and Q's'' of a water treatment plant, in the form of a performance management plan and two water treatment plant case studies.

  12. Automatic devices for electrochemical water treatment with cooling of electrolyte

    Directory of Open Access Journals (Sweden)

    Trišović Tomislav Lj.

    2016-01-01

    Full Text Available The most common disinfectants for water treatment are based on chlorine and its compounds. Practically, water treatments with chlorine compounds have no alternative, since they provide, in comparison to other effective processes such as ozonization or ultraviolet irradiation, high residual disinfection capacity. Unfortunately, all of chlorine-based compounds for disinfection tend to degrade during storage, thus reducing the concentration of active chlorine. Apart from degradation, additional problems are transportation, storage and handling of such hazardous compounds. Nowadays, a lot of attention is paid to the development of electrochemical devices for in situ production of chlorine dioxide or sodium hypochlorite as efficient disinfectants for water treatment. The most important part of such a device is the electrochemical reactor. Electrochemical reactor uses external source of direct current in order to produce disinfectants in electrochemical reactions occurring at the electrodes. Construction of an electrochemical device for water treatment is based on evaluation of optimal conditions for electrochemical reactions during continues production of disinfectants. The aim of this study was to develop a low-cost electrochemical device for the production of disinfectant, active chlorine, at the place of its usage, based on newly developed technical solutions and newest commercial components. The projected electrochemical device was constructed and mounted, and its operation was investigated. Investigations involved both functionality of individual components and device in general. The major goal of these investigations was to achieve maximal efficiency in extreme condition of elevated room temperature and humidity with a novel device construction involving coaxial heat exchanger at the solution inlet. Room operation of the proposed device was investigated when relative humidity was set to 90% and the ambient temperature of 38°C. The obtained

  13. Application of particle counter in biological activated carbon process of some water treatment plant in southern China%颗粒计数仪在南方某水厂BAC工艺中的应用

    Institute of Scientific and Technical Information of China (English)

    尢志磊; 蒋福春; 华伟

    2011-01-01

    Based on the operation condition of biological activated carbon process (BAC) in some water treatment plant in southern China in winter, the factors effecting effluent particle concentration were studied, and the relationship between traversing risk of microbe and particle concentration was also explored. The results showed: the longer BAC operation cycle, the larger the bacteria quantity variance range in effluent, and the higher risk of bacteria concentration in effluent ; if the turbidity in BAC effluent≤0. 1 NTU and the concentration of particle with diameter larger than 2 μm was still high, the potential risk of Cryptosporidium with size of 2~5 μm would exist%结合南方某水厂生物活性炭(BAC)池在冬季低温天气下的运行情况,研究分析了各工艺因素对出水颗粒物浓度的影响,探讨了微生物穿透BAC池的风险与颗粒物浓度之间的相关性.结果表明:BAC池运行周期越长,运行周期中的出水细菌数波动范围就越大,出厂水中细菌被检出的风险也越高;在生物活性炭池出水浊度≤0.1 NTU的情况下,出水中2 μm以上粒径的颗粒物浓度依然偏高,存在尺寸2~5 μm范围的隐孢子虫潜在威胁.

  14. Fenton工艺深度处理制浆造纸废水的常见问题及其解决措施%The problems and its solutions in advanced treatment of paper mill waste water by Fenton process

    Institute of Scientific and Technical Information of China (English)

    赵全伟

    2014-01-01

    通过调节Fenton试剂的投加量及反应pH探讨不同加药量及反应条件对二沉池出水CODCr去除效率的影响。结果表明:当硫酸亚铁和双氧水的投加量分别为0.9g/L和0.11g/L,反应pH为3.0,反应时间为15min时,CODCr的去除效率最高可达85%。并对在实际运行过程中存在的问题进行讨论,提出解决措施,以期为高级氧化技术在废水的深度处理提供相关经验。%The effect of different conditions and different chemicals dosage on CODCr removal rate in eflfuent of the secondary sedimentation pool was studied by adjustment of Fenton agent dosage and pH value. The results show that when the mass concentrations of ferrous sulfate and hydrogen peroxide are 0.9g/l and 0.11g/l, respectively, the reaction pH is 3.0 and reaction time is 15min, the removal rate of CODCr can be up to 85%. In this article were also discussed the problems in the actual operation with the Fenton reaction process and put forward the solving solutions to provide relevant references for the practical application with advanced oxidation technology in waste water advance treatment.

  15. Reviewing efficacy of alternative water treatment techniques.

    Science.gov (United States)

    Hambidge, A

    2001-06-01

    This section is designed to provide a brief summary of some of the findings. A good deal of work has been conducted by Mr N. L. Pavey and the team at BSRIA, Bracknell. The BSRIA publications are an excellent source of further information. Ultraviolet radiation: UV radiation of wavelength 254 nm destroys bacteria by a mechanism of damaging nucleic acids by producing thymine dimers which disrupt DNA replication [Gavdy and Gavdy, 1980]. L. pneumophila has been reported as sensitive to UV dosages of 2,500-7,000 uW.s/cm2 [Antopol & Ellner, 1979; Knudson, 1985]. Antopol and Ellner [1979] examined the susceptibility of L. pneumophila to UV dosage. Their results indicated that 50% of the organisms were killed by 380 uWs/cm2 and 90% were killed by 920 uWs/cm2. Kills of 99 and 99.9% were obtained using 1,840 and 2,760 uWs/cm2 respectively. Muraca et al [1987] showed that continuous UV irradiation resulted in a 5 logarithm decrease in waterborne L. pneumophila in a circulating system. Gilpin [1984] reported that in laboratory buffer solutions, exposure to 1 uW of UV radiation per cm2 achieved a 50% kill of L longbeachae in 5 minutes, L. gormanii in 2-30 minutes and L pneumophila in 17 minutes. Exposure times for 99% kills for L. longbeachae, L pneumophila and L. Gormanii were 33, 48 and 63 minutes respectively. The same research worker conducted experiments using a 3 litre circulating water system, connected to a stainless steel housing containing a UV source. The UV lamp output was 7 ergs/mm2 per second per 100 cm at 254 nm. L. pneumophila was killed within 15 seconds, that is within their first pass through the system. Continuous disinfection with UV has the advantages of imparting no taste, odour or harmful chemical by-products and requires minimal operation and maintenance [Muraca et al 1988]. Keevil et al [1989] state that UV irradiation fails to clear systems of biofilm because of poor penetration into microflocs of the micro-organisms. Copper/silver ionisation: A

  16. Continuous water treatment by adsorption and electrochemical regeneration.

    Science.gov (United States)

    Mohammed, F M; Roberts, E P L; Hill, A; Campen, A K; Brown, N W

    2011-05-01

    This study describes a process for water treatment by continuous adsorption and electrochemical regeneration using an air-lift reactor. The process is based on the adsorption of dissolved organic pollutants onto an adsorbent material (a graphite intercalation compound, Nyex(®)1000) and subsequent electrochemical regeneration of the adsorbent leading to oxidation of the adsorbed pollutant. Batch experiments were carried out to determine the adsorption kinetics and equilibrium isotherm for adsorption of a sample contaminant, the organic dye Acid Violet 17. The adsorbent circulation rate, the residence time distribution (RTD) of the reactor, and treatment by continuous adsorption and electrochemical regeneration were studied to investigate the process performance. The RTD behaviour could be approximated as a continuously stirred tank. It was found that greater than 98% removal could be achieved for continuous treatment by adsorption and electrochemical regeneration for feed concentrations of up to 300 mg L(-1). A steady state model has been developed for the process performance, assuming full regeneration of the adsorbent in the electrochemical cell. Experimental data and modelled predictions (using parameters for the adsorbent circulation rate, adsorption kinetics and isotherm obtained experimentally) of the dye removal achieved were found to be in good agreement.

  17. Integrated Chemical and Toxicological Investigation of UV-Chlorine/Chloramine Drinking Water Treatment

    Science.gov (United States)

    As the use of alternative drinking water treatment increases, it is important to understand potential public health•implications associated with these processes. The objective of this study was to evaluate the formation of disinfection byproducts (DBPs) and cytotoxicity of ...

  18. Integrated Chemical and Toxicological Investigation of UV-Chlorine/Chloramine Drinking Water Treatment

    Science.gov (United States)

    As the use of alternative drinking water treatment increases, it is important to understand potential public health•implications associated with these processes. The objective of this study was to evaluate the formation of disinfection byproducts (DBPs) and cytotoxicity of ...

  19. TREATMENT SYSTEM FOR WASTEWATER AT VILLA CLARA WATER MANAGEMENT COMPANY

    Directory of Open Access Journals (Sweden)

    Floramis Pérez Martín

    2016-04-01

    Full Text Available The aim of this paper is to assess the current operating and safety conditions of biological treatment systems for wastewater in the centers of swinish and poultry breeding at Villa Clara Water Management Company, with the purpose of setting a group of organizational, technical and human measures that contributes to prevent contamination and minimize biological risks. In this way it can be guaranteed the protection to the workers, the facilities, community and the environment, to have a sure occupational atmosphere in the organization. As a result of the evaluation the factors that affect the operation of the biodigestion system and the security of the process are defined.

  20. Impact of chlorine dioxide and ozone on the oxidation of NTA during drinking water treatment