Optimization of the coke-oven activated sludge plants

Energy Technology Data Exchange (ETDEWEB)

Raizer Neto, Ernesto [Santa Catarina Univ., Florianopolis, SC (Brazil); Colin, Francois [Institut de Recherches Hydrologiques, 54 - Nancy (France); Prost, Christian [Laboratoire de Sciences de Genie Chimique, Nancy (France)

1994-12-31

In the coke-oven activated sludge plants one of the greatest problems of malfunction is due to inffluent variability. The composition and, or, concentration variations of the inffluent substrate, which can cause an unstable system, are function of the pollutant load. Nevertheless, the knowledge of the kinetic biodegradation of the coke-oven effluent represents the limiting factor to develop an effective biological treatment. This work describes a computational model of the biological treatment which was elaborated and validated from continuous pilot scale experiments and calibrated by comparing its predictions to the pilot experiment`s results. 12 refs., 9 figs., 3 tabs.

Optimization of the coke-oven activated sludge plants

Energy Technology Data Exchange (ETDEWEB)

Raizer Neto, Ernesto [Santa Catarina Univ., Florianopolis, SC (Brazil); Colin, Francois [Institut de Recherches Hydrologiques, 54 - Nancy (France); Prost, Christian [Laboratoire de Sciences de Genie Chimique, Nancy (France)

1993-12-31

In the coke-oven activated sludge plants one of the greatest problems of malfunction is due to inffluent variability. The composition and, or, concentration variations of the inffluent substrate, which can cause an unstable system, are function of the pollutant load. Nevertheless, the knowledge of the kinetic biodegradation of the coke-oven effluent represents the limiting factor to develop an effective biological treatment. This work describes a computational model of the biological treatment which was elaborated and validated from continuous pilot scale experiments and calibrated by comparing its predictions to the pilot experiment`s results. 12 refs., 9 figs., 3 tabs.

Remediation and demolition of coke by-products plants

Energy Technology Data Exchange (ETDEWEB)

Stiffler, M A; Gould, W C

1992-08-01

The programme undertaken by ICF Kaiser Engineers and LTV Steel Co. to clean up and demolish four closed coking plants is described, including PCB removal, asbestos abatement, pipe removal and cleaning, tank cleaning, demolition and soil bioremediation. Costs are discussed.

Physico-chemical treatment of coke plant effluents for control of water pollution in India

Energy Technology Data Exchange (ETDEWEB)

Ghose, M.K. [Indian School of Mines, Dhanbad (India). Center of Mining Environmental

2002-01-01

Coal carbonizing industries in India are important and are growing every year. Large quantities of liquid effluents produced in this industry contain a large amount of suspended solids, high biochemical oxygen demand (BOD), chemical oxygen demand (COD), phenols, ammonia and other toxic substances, which are causing serious surface water pollution in the area. There is a large number of coke plants in the vicinity of Jharia Coal Field (JCF). The working principle of a coke plant and the effluents produced is described. One large coke plant was chosen to evaluate characteristics of the effluent and to suggest a proper treatment method. Present effluent treatment system was found to be inadequate and a large quantity of a very good quality coke breeze is being lost, which is also causing siltation on the riverbed in addition to surface water pollution. Physico-chemical treatment has been considered as a suitable option for the treatment of coke plant effluents. A scheme has been proposed for the treatment, which can be suitably adopted for the recycling, reuse or safe disposal of the treated effluent. Various unit process and unit operations are discussed. The process may be useful on industrial scale for various sites so as to maintain a clean environment.

Raising lump coke formation capacity of semicoking briquets in the Deuben briquetting plant

Energy Technology Data Exchange (ETDEWEB)

Naundorf, W.; Trommer, D.; Schroeder, H.-W.; Dressler, H.

1988-01-01

Describes brown coal briquetting and coking experiments aimed at producing high quality lumpy coke suitable for heating, metallurgy and other industrial processes. The Deuben coking and gas plant produces low temperature carbonization briquets from coal with 13.2% ash content, 54.8% volatiles, 13.5% semicoking tar with the effect that coke produced from these briquets disintegrates completely into fines (0/15 mm grain size). The study centered on effects of briquetting and coking parameters including coal grain size, coal moisture, briquetting pressure, coking temperature, heating rate and application of sulfite liquor as binder. Graphs of briquetting and coking results are provided. The Deuben coal was shown to be suitable for producing lumpy coke (11.5 to over 20 MPa compression strength) from coal under the optimum briquetting parameters of 0/1 mm grain size, 11% coal moisture, briquetting temperature of 70 to 80 C and briquetting pressure over 120 MPa. Use of a binder was found to be advantageous but not necessary. The produced coke showed favorable combustion properties. 6 refs.

Priorities in the design of chemical shops at coke plants

Energy Technology Data Exchange (ETDEWEB)

V.I. Rudyka; Y.E. Zingerman; V.V. Grabko; L.A. Kazak [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15

Recent trends in the design of chemical equipment at coke plants are described, through the lens of experience at Giprokoks. The main priorities were to improve the removal of impurities from coke oven gas; to improve equipment design on the basis of new materials; to reduce reagent consumption; to reduce the materials and energy consumed in the construction of new equipment; and to minimize impacts on the environment and worker health. Some technological equipment is briefly characterized.

Consumption of fuels and energy in the coking industry and ways of reducing consumption

Energy Technology Data Exchange (ETDEWEB)

Vasil' ev, Yu.S.; Tsel' ik, M.P.; Belkina, T.V. (Khar' kovskii Nauchno-Issledovatel' skii Uglekhimicheski Institut (USSR))

1989-08-01

Coking plants in the USSR consume 4,000 million kWh electric energy, 100 million GJ heat energy and 35,000 million m{sup 3} gaseous fuels per year. Structure of energy consumption is the following: 68% gaseous fuels, 24% steam and 8% electric energy. Processes of coal preparation, crushing, mixing, coking and quenching are analyzed from the point of view of energy consumption. The following methods for reducing energy consumption are discussed: using the FM-25 flotation machines for flotation of coking coal slurries, briquetting the whole coal charge for coking, optimization of air supply rates for combustion of gases used for coke oven heating, use of control systems for coke oven heating considering coal charge density, waste heat utilization from quenching. 4 refs.

The Dawes Lane coke ovens by-products plant expert system

Energy Technology Data Exchange (ETDEWEB)

P. Warren [Corus Research Development and Technology (United Kingdom). Teeside Technology Department

2002-07-01

A system has been developed to provide comprehensive monitoring of the washer/scrubber processes on the by-products plant at Dawes Lane coke ovens where faulty operation may cause blockage of the gas stream leading to opening of the battery bleeders to release gas to atmosphere. The system developed and the additional instrumentation and practices have met the requirements for improved monitoring to reduce the likelihood of uncontrolled gas emissions. It is planned to further develop the system so that it will contribute towards optimisation of plant operation, and so to generate a financial benefit from the investment made. The paper was presented to the Midland Section of the Coke Oven Managers' Association at Corus Centre, Scunthorpe, UK on 20 May 2001. 11 figs., 1 tab.

Urgent reconstruction and re-equipping of coking plants

Energy Technology Data Exchange (ETDEWEB)

Kvitkin, I.A.; Martynenko, V.M.; Rozenfel' d, M.S.; Svyatogorov, A.A.; Shvartsman, I.G.

1986-03-01

This paper discusses the various options involved: complete or partial reconstruction of existing buildings and equipment or new construction with new equipment and new underground and surface communications. It explains that reconstruction work is divided into three phases: initial phase (clearance, dismantling, closing down coking batteries); basic phase (fitting heat-resistant materials, prestart-up assembly work); final phase (drying out, heating up, adjustments, start-up). A structured scheme for a typical initial phase is described and a method of calculating the durations of the various phases is discussed. Conclusion is that there is an urgent requirement for a document to be produced for the control of reconstruction work; it should contain standard durations and could serve as a standard for coking plant reconstruction work.

ECONOMIC MODEL AND TOOLS OF THE AIR PROTECTION MANAGEMENT BASED ON THE EXAMPLE OF A COKING PLANT

Directory of Open Access Journals (Sweden)

Danuta Hilse

2014-10-01

Full Text Available Legal-economic models of the air protection management at the Polish industrial plants, which take into account the regulations of the Act on “Environment protection law”, are far from being perfect. It is particularly noticeable in the coking industry where chargeable pollutions are chosen selectively, and unitary rates of emission charges are agreed at random. Tax deductions are not granted either to producers of fuel coke for reduction of pollutants emission in municipal-housing management after replacing coal with fuel coke. The proposed new economic model of the air protection management at coking plants eliminates the existing shortcomings.

Japanese coke plant follows US lead

Energy Technology Data Exchange (ETDEWEB)

1980-06-01

Nippon Steel has acquired the first licence for a US Steel/Firma Carl Still process for cleaning coke oven flushing liquor. The process is installed at 3 US Steel preheated coal batteries and is now being used at Nippon Steel's Muroran works. The process is important to the re-use of the water for quenching and is a vital first step in making the liquor harmless to the environment. It is particularly useful in plants using preheated coal where there is likely to be carry over of fine coal particles.

Utilization of HSC-ROSE residue as coking aid for the production of high quality coke from brown coal

Energy Technology Data Exchange (ETDEWEB)

Bohlmann, D.; Limmer, H.; Naundorf, W.; Hood, R.L.; Washimi, K. (VEB Petrolchemisches Kombinat, Schwedt (German Democratic Republic))

1989-04-01

Evaluates suitability of HSC-ROSE petroleum pitch as binder for production of brown coal coke. This pitch has been available in the GDR since installation in 1988 of a 750 kt/a HSC (high conversion soaker cracking) plant, which processes 360 C visbreaker residue from Soviet crude oil, and the building of a ROSE (residue oil supercritical reaction) plant. Laboratory as well as semi-industrial experiments were carried out at the Freiberg Academy, GDR on pulverizing, briquetting and coking various brown coal types with HSC-ROSE pitch. Briquetting and coking results are shown in tables. Experiments showed that the resulting coke has 124% higher compression strength and 100% higher abrasion strength than regular brown coal coke without HSC-ROSE binder. The high quality coke is adequate for use as metallurgical blast furnace coke. An economic assessment of modifying an existing brown coal coking plant to process 2 Mt/a brown coal with 10% pitch binder is made. Required investment amounts to 54 million US dollars, estimated annual profits based on 1987 prices are 19.5 million US dollars. 4 refs.

Application of flotational reagents obtained from coke-industry byproducts

Energy Technology Data Exchange (ETDEWEB)

N.I. Nikitin; I.N. Nikitin; N.I. Toporkova [Khar' kov Polytechnic Institute (Ukraine)

2007-06-15

Today, the operational efficiency of coal-preparation shops at coke plants largely depends on the flotation process, since flotation is the basic method of regenerating the slurry water in the water-slurry systems and the basic enrichment process for small-grain coal slurries. At The Coal-Chemistry Institute, attempts have been made to address the growing demand for readily available and relatively inexpensive flotational reagents. In particular, a list of promising coke-industry byproducts for use as flotational reagents has been compiled, and the possibility of reducing their toxicity has been established. In addition, various industrial byproducts and wastes have been investigated in terms of flotational activity.

Process of coke less without waste treatment of direct vanadium allowing steel melting

International Nuclear Information System (INIS)

Lisienko, V.G.; Droujinina, O.G.; Morozova, V.A.; Ladigina, N.V.; Yusfin, Yu.S.; Parenkev, A.E.

2003-01-01

The development of new methods of steel production are now conducted with the purpose of energy consumption and harmful emissions reduction. The choice of technology and equipment in this case plays a marginal role. It is well known that vanadium alloying steel has increased service properties. The known classical scheme of vanadium steel melting is very power-intensive, as includes such power-intensive processes as blast furnace process and chemical processing of vanadium slag therewith sintering and by-product coke processes are accompanied by significant harmful emissions. In so doing the vanadium losses may run to 60%. In view of requests of environment protection and economical efficiency the new process of coke less without wastes processing of vanadium-bearing raw material with direct vanadium allowing of steel - LP-process is developed. Its purpose is the melting on the basis of vanadium-bearing titanomagnetite of vanadium allowing steel with increase of vanadium concentration in steel and diminution of vanadium losses without application coke and natural gas with use of any coals and carbon-bearing wastes. LP-process consists of three aggregates and corresponding processes: process of liquid-phase reduction, process of vanadium-bearing pellets metallization in the shaft furnace, and process of alloying steel melting in the arc electric furnace. The obtained results have shown, that the LP-process is more energy saving on a comparison with other methods of vanadium allowing steel production. (Original)

Scientific Council of the State Committee for Science and Technology on the problem 'New processes in the coking industry', Coke-Chemistry Section of the Scientific-Technical Council of the Ministry of Ferrous Metallurgy of the USSR and of the Central Administration of the Scientific-Technical Branch of Ferrous Metallurgy

Energy Technology Data Exchange (ETDEWEB)

Bukvareva, O.F.

1986-12-01

A report is presented on 3 conferences on the development of the Soviet coking industry held in February and April 1986. Papers delivered at the conferences and selected recommendations for development of equipment for coking, coking systems, optimization of coal mixtures for coking, environmental protection and research programs on coking are reviewed. The following problems were discussed: modernization of coke oven design, selecting the optimum size of coke ovens, prospects for dry coke quenching in the USSR, evaluation of operation of systems for dry coke quenching, utilization of waste heat from coke quenching for heat treatment of coal mixtures for coking, research programs on coking in the 12th five-year plan (1986-1990), partial briquetting of coal mixtures for coking and selecting optimum binders for partial briqetting, formed coke processes, economic analysis of formed coke processes, fire-resistant bricks and elements for coke oven construction, new coking technologies, pollution control in coking plants.

Increasing efficiency of reconstruction and technological development of coking enterprises

Energy Technology Data Exchange (ETDEWEB)

Rozenfel' d, M.S.; Martynenko, V.M.; Tytyuk, Yu.A.; Ivanov, V.V.; Svyatogorov, A.A.; Kolomiets, A.F. (NIISP, Voroshilovgrad (USSR))

1989-07-01

Discusses problems associated with reconstruction of coking plants in the USSR. Planning coking plant reconstruction is analyzed. Duration of individual stages of plant reconstruction is considered. A method developed by the Giprokoks research institute for calculating reconstruction time considering duration of individual stages of coke oven battery repair is analyzed: construction of storage facilities, transport of materials and equipment, safety requirements, coke oven cooling, dismantling, construction of coke oven walls, installation of machines and equipment. Advantages of using the methods for analysis of coke oven battery reconstruction and optimization of repair time are discussed.

Investigations concerning the mechanism of action of brown-coal coke particles in aerobic biological waste water treatment

International Nuclear Information System (INIS)

Rieger, W.

1990-01-01

At the start of this work experience with the use of brown coal coke in the activated sludge process was lacking entirely. It therefore was necessary to carry through preliminary experiments in order to practically test the effect of Grown-coal coke. In two technical-scale experiments and a pilot test, very good results were obtained with the application of brown-coal coke to activated sludge. These, and previously published results, permitted to evolve moodel concepts of the mechanism of action of coal, especially brown coal coke, in activated sludge. According to these concepts the coal particles act as buffers and a temporary adsorbent of oxygen and waste water constituents. This in turn stimulates the colonization of the surface with microorganisms. In order to corroborate these model concepts, the - adsorption and desorption of solved oxygen to coal in a watery medium and - the effect of coal over a longer period of time were investigated. The results in essence confirm the model concepts. (UWa) [de

Special analyses reveal coke-deposit structure

International Nuclear Information System (INIS)

Albright, L.F.

1988-01-01

A scanning electron microscope (SEM) and an energy dispersive X-ray analyzer (EDAX) have been used to obtain information that clarifies the three mechanisms of coke formation in ethylene furnaces, and to analyze the metal condition at the exit of furnace. The results can be used to examine furnace operations and develop improved ethylene plant practices. In this first of four articles on the analyses of coke and metal samples, the coking mechanisms and coke deposits in a section of tube from an actual ethylene furnace (Furnace A) from a plant on the Texas Gulf Coast are discussed. The second articles in the series will analyze the condition of the tube metal in the same furnace. To show how coke deposition and metal condition dependent on the operating parameters of an ethylene furnace, the third article in the series will show the coke deposition in a Texas Gulf Coast furnace tube (Furnace B) that operated at shorter residence time. The fourth article discusses the metal condition in that furnace. Some recommendations, based on the analyses and findings, are offered in the fourth article that could help extend the life of ethylene furnace tubes, and also improve overall ethylene plant operations

The aquatic toxicity and chemical forms of coke plant effluent cyanide -- Implications for discharge limits

International Nuclear Information System (INIS)

Garibay, R.; Rupnow, M.; Godwin-Saad, E.; Hall, S.

1995-01-01

Cyanide is present in treated cokemaking process waters at concentrations as high as 8.0 mg/L. In assessing options for managing the discharge of a treated effluent, the development and implementation of discharge limits for cyanide became a critical issue. A study was initiated to evaluate possible alternatives to cyanide permit limits at the US Steel Gary Works Facility. The objectives of the study were to: (1) evaluation the forms of cyanide present in coke plant effluent; (2) determine whether these forms of cyanide are toxic to selected aquatic organisms; (3) compare the aquatic toxicity of various chemical forms of cyanide; (4) identify if the receiving water modifies cyanide bioavailability; and (5) confirm, with respect to water quality-based effluent limits, an appropriate analytical method for monitoring cyanide in a coke plant effluent. The results of aquatic toxicity tests and corresponding analytical data are presented. Toxicity tests were conducted with various pure chemical forms of cyanide as well as whole coke plant effluent (generated from a pilot-scale treatment system). Test species included the fathead minnow (Pimephales promelas), rainbow trout (Oncorhynchus mykiss), Ceriodaphnia dubia (C. dubia) and Daphnia magna (D. magna). Analytical measurements for cyanide included total, weak acid dissociable, diffusible cyanide and selected metal species of cyanide. The findings presented by the paper are relevant with respect to the application of cyanide water quality criteria for a coke plant effluent discharge, the translation of these water quality-based effluent limits to permit limits, and methods for compliance monitoring for cyanide

Coke production in large coke ovens

Energy Technology Data Exchange (ETDEWEB)

Zhuravskii, A.A.; Sytenko, I.V.; Zhupraner, Z.S.; Vasil' ev, Yu.S.; Karpukhin, E.A.; Pliner, G.E.; Rud' , A.I.; Bulyga, N.I. (NPO Koksokhimiya (USSR))

1990-08-01

Analyzes operation of the No 9 battery with coke ovens with a volume of 41.6 m{sup 3}. Factors that influence coke oven operation and coke quality are analyzed. The following problems are evaluated: composition of coal mixtures (G, Zh, K, OS, GZh coal types), methods for coal mixture preparation (crushing degree, selective crushing), temperature distribution in a coke oven and effects of heating system, coke shrinkage during coking and factors that influence shrinkage, optimizing pressure used for coke pushing, chemical, mechanical and physical properties of coke. Regression equations used for forecasting coke properties are derived: the M10 coke wear index, M25 coke strength index, ash content etc. Recommendations for optimum coking conditions are made. 6 refs.

System for reducing emissions during coke oven charging

International Nuclear Information System (INIS)

Schuecker, Franz-Josef

2014-01-01

This article describes a process which reduces emissions from coke production in coke plants. The focus is on the charging process, which can be partly responsible for the fact that statutory emissions limits, which were originally met, are exceeded as coke plants get older. This article presents a solution in the form of a newly developed system that allows the oven charging system - the charging car - to respond to age-related changes in the geometry of a coke oven and thereby reduce the level of emissions.

Coke gasification costs, economics, and commercial applications

International Nuclear Information System (INIS)

Jahnke, F.C.; Falsetti, J.S.; Wilson, R.F.

1996-01-01

The disposition of petroleum coke remains a problem for modern high conversion refineries. Market uncertainty and the price for coke can prevent the implementation of otherwise attractive projects. The commercially proven Texaco Gasification Process remains an excellent option for clean, cost effective coke disposition as demonstrated by the new coke gasification units coming on-line and under design. Previous papers, have discussed the coke market and general economics of coke gasification. This paper updates the current market situation and economics, and provide more details on cost and performance based on recent studies for commercial plants

Young employees of the coking industry for technological progress

Energy Technology Data Exchange (ETDEWEB)

Ladyzhinskii, V.M.; Shul' ga, I.V.

1986-11-01

A conference is reported on technology development in the Soviet coking industry held on December 9-10, 1985 at the Khar'kov Scientific-Research Coal-Chemistry Institute. Representatives of leading research institutes and coking plants delivered 25 papers on the following topics: increasing flotation efficiency by means of new flotation reagents, drum feeders for charging cars, new design of coke oven doors, mathematical models of coal transport to coke ovens, some characteristics of packing coal mixtures in coke ovens, heat treatments of coal mixtures at the Khar'kov experimental coking plant, investigating properties of long-flame and gas coal from the Donbaas used for manufacturing formed coke, modernization of the IGI-DMeTI method for determining properties of coal mixtures for formed coke processes, basic problems associated with environmental protection in formed coke processes, specific problems of coal gasification at 900-1050 C and its effects on coking, evaluating properties of formed coke produced from black coal from the Western Donbass for metallurgy, mixing hot briquets with coal slurries during partial briquetting of the coal charge.

Catalytic wet air oxidation of coke-plant wastewater on ruthenium-based eggshell catalysts in a bubbling bed reactor.

Science.gov (United States)

Yang, M; Sun, Y; Xu, A H; Lu, X Y; Du, H Z; Sun, C L; Li, C

2007-07-01

Catalytic wet air of coke-plant wastewater was studied in a bubbling bed reactor. Two types of supported Ru-based catalysts, eggshell and uniform catalysts, were employed. Compared with the results in the wet air oxidation of coke-plant wastewater, supported Ru uniform catalysts showed high activity for chemical oxygen demand (COD) and ammonia/ammonium compounds (NH3-N) removal at temperature of 250 degrees C and pressure of 4.8 MPa, and it has been demonstrated that the catalytic activity of uniform catalyst depended strongly on the distribution of active sites of Ru on catalyst. Compared to the corresponding uniform catalysts with the same Ru loading (0.25 wt.% and 0.1 wt.%, respectively), the eggshell catalysts showed higher activities for CODcr removal and much higher activities for NH3-N degradation. The high activity of eggshell catalyst for treatment of coke-plant wastewater can be attributed to the higher density of active Ru sites in the shell layer than that of the corresponding uniform catalyst with the same Ru loading. It has been also evidenced that the active Ru sites in the internal core of uniform catalyst have very little or no contribution to CODcr and NH3-N removal in the total oxidation of coke-plant wastewater.

The Bricoke process for producing metallurgical coke in conventional ovens from blends containing a high percentage of non-coking coal

Energy Technology Data Exchange (ETDEWEB)

Vidal, R; Munnix, K; Dellieu, J

1980-06-01

The article discusses the following aspects:- description of the BRICOKE process; trials in pilot plant, showing the influence of the different parameters on the coke quality and delimiting the range of the suitable non-coking coals; industrial scale trials of long term with 33% of non-coking coal briquettes in the charge; influence on the coking process as well as on the blast furnace working and increase of the output of usual coke-oven by the BRICOKE process. (11 refs.)

Influence of fly dust from coking plants on some biological processes of plants

Energy Technology Data Exchange (ETDEWEB)

Masek, V

1972-03-01

The influence of three typical samples of fly dust from a coking plant on enzymatic reactions, photosynthesis, chlorophyll concentration in leaves of bean plants was studied. The hydrolysis of starch with amylases and of the albumen with pepsin at 37 C and the inversion of sacharosis by invertase in a buffered environment were also examined. None of the three dust samples had a significant effect on enzymatic reactions. Applying the dust samples to the leaves of young bean plants reduced the intensity of photosynthesis and chlorophyll concentration. In aqueous extracts, the dust samples liberated only small quantities of nutrients, plants which were grown in a dust suspension showed no increase of dry substance and growth rate. A stimulating effect of the dust samples on root growth was determined. Mixing the dust samples with the soil influenced the accessibility of water to plants. 17 references, 6 figures, 9 tables.

Coke, char and organic waste behaviour in the blast furnace with high injection rate

Directory of Open Access Journals (Sweden)

Gudenau, H. W.

2003-10-01

Full Text Available Blast furnace operation with low coke rate, high amount of auxiliary hydrocarbons and use of nut coke causes a change in coke quality requirements. In particular, not burned in the raceway residues of injected substances (char and ash can influence the coke behaviour. Therefore combustion efficiency of various organic wastes with and without pulverized coal injection (PCI and coal char has been investigated under the raceway simulation conditions. Mixing of various substances improves their combustion efficiency. Study on coke gasification by carbon dioxide in the presence of char showed that with the increase of char concentration, coke strength reduction becomes smaller. The reactivity of char with CO₂ is higher than that of coke. Therefore char is consumed preferentially. In presence of injected char, total pore volume in coke and its wear resistance were increased. Coke reactivity and microstructure in the presence of various kinds of ash has been studied. Many ash spheres were observed on the surface of coke matrix and its size was dependent on ash properties.

La operación del horno alto con una tasa baja de coque, una cantidad elevada de hidrocarburos auxiliares y el empleo de coque calibrado, origina un cambio en las necesidades de calidad del coque. En particular, pueden influir en el comportamiento del coque los residuos inquemados en el raceway (cavidad enfrente a las toberas del horno de las sustancias que se inyectan (char y cenizas. El char es el residuo de carbón que se origina después que el carbón libera sus sustancias volátiles. Por tanto, se ha investigado la eficiencia de la combustión de varios residuos orgánicos con y sin inyección de carbón pulverizado (ICP y char, bajo las condiciones de simulación del raceway. La mezcla de varias sustancias mejora la eficiencia a la combustión. El estudio de la gasificación del coque por el dióxido de carbono en la

PROSPECTS FOR COKE BREEZE RECOVERY

Directory of Open Access Journals (Sweden)

D. N. Mihnovets

2012-01-01

Full Text Available Researches give grounds to believe in the possibility of receiving briquettes from coke waste mixed with peat dry coal and their use for smelting iron in the cupola or as a household fuel.

The use of fractionated fly ash of thermal power plants as binder for production of briquettes of coke breeze and dust

Science.gov (United States)

Temnikova, E. Yu; Bogomolov, A. R.; Lapin, A. A.

2017-11-01

In this paper, we propose to use the slag and ash material of thermal power plants (TPP) operating on pulverized coal fuel. The elemental and chemical composition of fly ash of five Kuzbass thermal power plants differs insignificantly from the composition of the mineral part of coking coal because coke production uses a charge, whose composition defines the main task: obtaining coke with the required parameters for production of iron and steel. These indicators are as follows: CRI reactivity and strength of the coke residue after reaction with CO2 - CSR. The chemical composition of fly ash of thermal power plants and microsilica with bulk density of 0.3-0.6 t/m3 generated at production of ferroalloys was compared. Fly ash and microsilica are the valuable raw material for production of mineral binder in manufacturing coke breeze briquettes (fraction of 2-10 mm) and dust (0-200 μm), generated in large quantities during coking (up to 40wt%). It is shown that this binder is necessary for production of smokeless briquettes with low reactivity, high strength and cost, demanded for production of cupola iron and melting the silicate materials, basaltic rocks in low-shaft furnaces. It is determined that microsilica contains up to 90% of silicon oxide, and fly ash contains up to 60% of silicon oxide and aluminum oxide of up to 20%. On average, the rest of fly ash composition consists of basic oxides. According to calculation by the VUKHIN formula, the basicity index of briquette changes significantly, when fly ash is introduced into briquette raw material component as a binder. The technology of coke briquette production on the basis of the non-magnetic fraction of TPP fly ash in the ratio from 3.5:1 to 4.5:1 (coke breeze : coke dust) with the addition of the binder component to 10% is proposed. The produced briquettes meet the requirements by CRI and require further study on CSR requirements.

A temperature measurement system for coke-oven walls at the coke-oven plant Kaiserstuhl in Dortmund (Germany). Pomiar temperatury w scianach baterii koksowniczej w koksownii Kaisertuhl w Dortmund (Niemcy)

Energy Technology Data Exchange (ETDEWEB)

Chojnacki, M.; Sitek, A. (Hanslik Laboratorium Oprgramowania, Katowice (Poland))

1994-08-01

In the article, the software and hardware solutions developed by Hanslik Software Laboratory for Ruhrkohle AG are presented. The system was installed at Kaiserstuhl in Dortmund (Germany), the most modern coke-oven plant in the world. The project covered a temperature measurement system for the coke-oven walls as well as monitoring of the protection sensors in real-time. The article describes also the testing methodology we adopted, using computer aided testing. For the testing purposes, a simulator of the coke-oven and a testing program running under Windows were developed at our laboratory. The article shows the advantages of using off the shelf programmable components for ruggedized industrial applications. (author). 4 refs.

Production of fine coke in a hearth-type furnace (Report on ECSC contract 7720-EB/108)

Energy Technology Data Exchange (ETDEWEB)

1980-01-01

A balance was established for the hearth-type coking oven and waste heat boiler system. Tests concerning the operational safety showed that, in the case of breakdowns, the oven and waste heat boiler could be shut down without any danger. The quality of the brown coal fine coke produced, could be improved by optimizing the heights of the layer in the hearth-type, the degasification temperature of the oven, and the operation of the coke cooling system. Higher coking temperature caused a lower grain disintegration and lower abrasion rates. The range of size of coke production was enlarged to lump size by additional feeding of 2-inch briquettes to the coking oven.

Coke from partially briquetted preheated coal mixtures

Energy Technology Data Exchange (ETDEWEB)

Belitskii, A.N.; Sklyar, M.G.; Toryanik, Eh.I.; Bronshtein, A.P.

1988-07-01

Analyzes effects of partial coal charge briquetting on coking and on quality of coke for metallurgy. Effects of mixing hot coal briquets on temperature and moisture of coal were investigated on an experimental scale in a coking plant. Coal with a moisture content of 12% was used. Coking mixture consisted of 30% briquets and 70% crushed coal. Fifteen minutes after briquet mixing with coal, the mean coal charge temperature increased to 100-105 C and moisture content was lower than 2-5%. Results of laboratory investigations were verified by tests on a commercial scale. Experiments showed briquetting of weakly caking or non-caking coal charge components to be an efficient way of preventing coke quality decline. Adding 15-20% briquets consisting of weakly caking coal did not influence coke quality. Mixing hot coal briquets reduced moisture content in crushed coal, increased its temperature and reduced coking time.

Coal and coke applied to metallurgy. Vol. 2. Carvao e coque aplicados a metalurgia

Energy Technology Data Exchange (ETDEWEB)

Masuda, H.

1983-01-01

Papers include: coking; control of pollution from coking plants; handling and storage of coal; preparation of coal for coking; politics of the supply of coal; coke for blast furnaces; selective preparation and briquetting of coal for coking; cooling and drying of coke; preheating of coal for coking; formed coke.

The new coke oven battery heating control system at Rautaruukki Steel

Energy Technology Data Exchange (ETDEWEB)

Palmu, P.; Swanljung, J. [Rautaruukki Steel, Raahe (Finland)

1998-07-01

The heating control system of the coke oven batteries has been developed strongly during the existence of the coke oven plant. The first step of the heating control was a statistical model which had a good monitoring system. This was enough in those days due to bigger problems elsewhere. The second generation heating control system is designed for irregular coke oven battery operation. Coke production in Rautaruukki Steel is based on one coke-oven plant consisting of two batteries and a by-product plant. The whole coke production is cooled by three dry quenching units. The first coke-oven battery was taken into operation in October 1987 and the second in November 1992. Originally the plant was mainly designed and equipped by Ukrainian Giprokoks except Finnish CDQ-boilers, German ammonia recovery process and electric and automation designed by Rautaruukki. Before building of the second coke oven battery, there was a huge amount of development and modification work to do, to ensure the proper function of the coke production. For example all electronic and hydraulic systems of the Russian supplier were replaced by systems designed by Rautaruukki's own personnel. When the coke production capacity was doubled, the only design by Gibrokoks related to the battery and one additional dry quenching chamber. The expansion project itself was managed and executed by Rautaruukki. The expansion project consisted of: the second battery, third CDQ-unit, Desulphurization and Benzol plants for the by-product plant and upgrading of automation system. Battery and CDQ chamber refractory materials were Russian origin and all other main equipment were purchased by Rautaruukki from western and domestic manufacturers based on the operation difficulties and experience of coke oven battery No. 1. These modification practices made a good basis for later development in the field of coke oven battery automation. The hierarchy of the coke oven battery automation at Rautaruukki Steel consist

New processes in iron metallurgy discussed by the Coking Section of the Scientific Council of the Main Committee of Science and Technology of the USSR

Energy Technology Data Exchange (ETDEWEB)

Bukvareva, O.F.

1991-02-01

Discusses problems evaluated in October 1990 by the Section during the meeting devoted to research programs in the twelfth five-year plan, research and development of continuous coking methods, prospects for new coke quenching processes. Selected research programs, coordinated research programs and development programs as well as recommendations for future research programs are evaluated. The following research programs aimed at use of weakly caking and noncaking coals in the coking plants are evaluated: coal preheating and charging preheated mixtures to coke ovens, partial coal charge briquetting and equipment for coal briquetting, development of commercial systems for packing coal charges in coke ovens, production of formed coke for metallurgy, processes for coal gas cleaning (especially ammonia separation), development of systems for utilization of waste heat from dry coke quenching for coal charge preheating. Participation of individual research institutes in the programs is discussed. The most significant projects of individual institutes are discussed. Recommendations for research programs for the period 1991 to 1995 are made.

Ecological situation at the coke plant of the Nizhnii Tagil Integrated Iron and Steel Works (according to data from an expert commission of Gosstroi USSR)

International Nuclear Information System (INIS)

Filippov, B.S.

1990-01-01

A main source of pollution is the Nizhnii Tagil Integrated Iron and Steel Works (NTMK), whose share in the total emissions of harmful substances is very significant. Thus, in 1987 the mean annual dust content in the atmosphere of the city surpassed the maximum admissible concentrations 1.3 times, phenol 2 times, ammonia 2.5 times, benzopyrene 6 times. In 1988 an even higher content of harmful substances was noted. Reconstruction of the coke plant now underway has been called upon to ensure a significant improvement in the ecological conditions together with an overall increase in its technical level. Restoration of the existing capacity of the coke batteries at domestic coke plants is being accomplished according to two variants: first - relining of the batteries with retention of the existing dimensions or with a slight very limited increase, with modernization of the designs of the ovens and chemical departments, and also machines and equipment (technical refitting); second - withdrawal from operation of the existing batteries and construction of new higher capacity coke batteries in the plant area (reconstruction). From the standpoint of ecology and economy of capital investment it would be more expedient to restore capacity at NTMK according to the first variant. However, restoration here is being carried out according to the second variant with construction of coke batteries 9 and 10 in a new area with dry coke quenching. There are plans to decommission batteries 1-4. An analysis is given of the sources of pollution from the coke plant and measures are defined to reduce pollutants

The influence of microporosity on resistance and carboxyreactivity of cokes

Energy Technology Data Exchange (ETDEWEB)

Medek, J.; Weishauptova, Z. [Academy of Sciences, Prague (Czech Republic). Inst. of Rock Structure and Mechanics

1997-12-31

Large sample collection of metallurgical cokes from Ostrava-Karvina coking plants, were used for correlation of the resistivity of the coke matter (carbon solid phase plus micropores) and carboxyreactivity of cokes with the value of microporosity. It results, from this correlation, that the characteristic values of the two mentioned quantities appartain to the solid phase of all metallurgical cokes studied, while the individual values of these quantities are caused by the different microporosity of the coke matter. The microporosity as a structure characteristic is a consequence of the discontinuity of the coke solid phase and can be quantitatively expressed as the degree of solid phase dispersion. (orig.)

The Homecourt coke plant site: a successful redeveloped brown field case

International Nuclear Information System (INIS)

Charbonnier, P.; Piguet, O.; Lereboullet, L.

2006-01-01

The environmental diagnosis of the coke plant site in Homecourt has been carried out over the last 15 years. Bail Industrie has selected two zones on the site for a remediation program in view of their further redevelopment. The weakly polluted grounds were submitted to a bio treatment, while the more polluted grounds were treated by thermal desorption. Tars have been incinerated off site. To assess the effectiveness of the treatment, percolation tests are carried out. (authors)

Coke briquets for metallurgy based on a thermoreactive binder

Energy Technology Data Exchange (ETDEWEB)

Tjutjunnikov, J.B.; Florinskij, V.N.; Orechov, V.N.; Nefedov, P.J.; Sasmurin, V.I.; Kirenskij, V.N. (Khar' kovskii Inzhenerno-Ehkonomicheskii Institut (USSR))

1992-02-01

Describes a process for production of briquets for metallurgy with binder and coke fines or anthracite. The suggested binder is waste phenol resin from the production of phenol (cumene method). Resin properties are given. Possible reaction mechanisms yielding solidified matter are discussed. The production process requires 10-15% binder and applies charge heating up to 200 C over 30 min. Catalytic amounts of sodium hydroxide or sulfuric acid were also employed. The production process is shown in a flowsheet. Properties of produced briquets are tabulated. The briquets were used in a 8 t/h cupola furnace and their performance was compared to that of KL-1 coke. Performance was found to be comparable; the cost of coke briquets was less than that of heating coke. 2 refs.

On-line determination of moisture in coke on conveyor belts

International Nuclear Information System (INIS)

Millen, M.J.; Rafter, P.T.; Sowerby, B.D.

1988-01-01

A fast neutron and γ-ray transmission technique is being developed for the on-line determination of moisture in coke on conveyor belts. Calculations show that the technique is capable of determining coke moisture to within 0.3 wt% for coke thicknesses down to 50 mm provided that count rates are measured to within 0.1% relative. Laboratory measurements on static and moving coke samples showed that coke moisture can be determined to within 0.25 and 0.45 wt% for crushed and lump coke, respectively. It is planned to carry out a long-term plant trial of the technique on lump coke feed to the No. 3 blast furnace at BHP, Newcastle, NSW, Australia. (author)

Briquetting and coking behavior of Bobov-Dol coal

Energy Technology Data Exchange (ETDEWEB)

Naundorf, W.

1987-01-01

Hard Bulgarian glance brown coal (23.2% ash content, 16% coal moisture 2.39% sulfur) was studied for its general suitability for partial black coal coke substitution in coking plants and for the possibility of producing pyrolysis briquets for coking purposes. Laboratory briquetting variants include coal briquetting without binders, with sulfite lye as binder, briquetting after partial demineralization by wet classification, briquetting of different screening fractions (0 to 4 mm), briquetting as a mixture with type 35 caking black coal as well as mixed with type 34 less caking black coal under addition of black coal tar, pitch or bitumen. Coking of the briquets produced was carried at with and without charge compacting. Graphs and tables provide briquetting and coking results. It is concluded that high strength coke can be produced from this brown coal, but it can only be used commercially as heating coke due to its high ash and sulfur content. Briquetting and coking of partially demineralized brown coal in a mixture with black coal and binders resulted in suitable metallurgical coke. Maximum percentage of brown coal in the briquetting mixture was 30%. 4 refs.

Bio-coke as an alternative to petroleum coke and metallurgical coke; Bio-cokes als alternatief voor petroleumcokes en metallurgische cokes

Energy Technology Data Exchange (ETDEWEB)

Croezen, H.J.; Van Lieshout, M. [CE Delft, Delft (Netherlands); Sevenster, M.N. [Sevenster Environmental Consultancy, Australian Capital Territory ACT (Australia)

2012-11-15

In the framework of elaborating the Dutch Roadmap Chemistry 2030), CE Delft has conducted an exploratory study for the Association of the Dutch Chemical Industry (VNCI) on the options of replacing (petroleum) coke in the chemical sector by biocokes. Coke is used as a reducing agent and/or raw material in four companies in the Dutch chemical industry (Tronox, ESD-SIC, Thermphos, Aluchemie). Replacing coke at these four companies can potentially yield a direct CO2 reduction of expectedly several hundreds of kilotons per year. For a first exploration of the options of bio-coke, CE Delft first conducted a desk study to get information on the quality and production costs for bio-coke. Subsequently, CE Delft had contact with the four chemical companies and a made a number of company visits. Moreover, the technical, economic and organizational capabilities, constraints and requirements with regard to a possible (partial) switch to biocokes have been explored. Based on the information available so far it can be concluded that biocokes seems to be a technically and economically interesting innovation. For implementation to finally take place, it is necessary to gain better insight in the technical and economic potential [Dutch] In verband met de uitwerking van de Routekaart Chemie 2030 heeft CE Delft voor VNCI een verkenning uitgevoerd naar de mogelijkheden voor vervanging van (petroleum)cokes in de chemische sector door biocokes. Cokes wordt gebruikt als reductiemiddel en/of grondstof bij een viertal bedrijven in de Nederlandse chemie (Tronox, ESD-SIC, Thermphos, Aluchemie). Het vervangen van cokes bij deze vier bedrijven kan in potentie een directe CO2-reductie van naar verwachting enkele honderden kilotonnen/jaar opleveren. Voor een eerste verkenning van de mogelijkheden van bio-cokes heeft CE Delft eerst een bureaustudie uitgevoerd naar informatie over kwaliteit van en productiekosten voor bio-cokes. Vervolgens heeft CE Delft contact gehad met de vier chemische

Effect of nut coke on the performance of the ironmaking blast furnace

NARCIS (Netherlands)

Song, Q.

2013-01-01

The blast furnace consumes a large amount of high quality metallurgy coke (size 35-80 mm) in addition to ore in the form of pellets and sinter. This coke is the coarse fraction, derived from the coke plant. The fine fraction (8 -35 mm), arise after sieving, named nut coke, can’t be directly used in

Utilization coke dust as fuel in the cement industry

International Nuclear Information System (INIS)

Nawaz, S.

2006-01-01

Utilization of coke dust available from coal carbonization plants, as a fuel in the cement industry has been undertaken and discussed in this research paper. The parameters studied include physical and chemical evaluation of the coke dust and its economic feasibility/ suitability as fuel for the cement plants. Detailed studies have been carried out on the above referred parameters. In addition a comparative study has been done to access its suitability in comparison to other fuels especially imported coal. It has been found that the coke dust contained about 66% fixed carbon, 29% ash, 4% volatile matter, 1% moisture and 0.48% sulphur. It gross calorific value was found to be 5292 Kcal/kg. The detailed analysis of coke dust ash was also performed to determine as to how its constituents will compare with the cement constituents. Keeping in view the experimental results/ data generated on the coke dust, it has been concluded that it can be quite a good substitute for imported coal. In doing so a substantial financial saving can be achieved which ranges 40-45%. (author)

Materials for making coke

Energy Technology Data Exchange (ETDEWEB)

Kern, L

1936-08-19

In the preparation of carbonized fuel briquettes, material such as bituminous, lignitic, or anthracitic coal, slack, waste or shale is treated with an electropositive solution such as hydrochloric acid or an acidic chloride to bring ash-forming constituents into colloidal form. The mixture is pressed with a colloid precipitating electro-negative solution such as sodium hydroxide, and moulded, the product being heated in the absence of air and coked. In an example bituminous coal is ground and then masticated with dilute hydrochloric acid. Some dilute manganese chloride is added followed by a solution of sodium hydroxide which precipitates the metals and silica as colloidal gels while the mixture is thoroughly agitated. The plastic mass is briquetted and dried at about 125/sup 0/C and then coked in vertical ovens at 700/sup 0/C. Chlorides recovered with the distillate gases may be utilized as solvent instead of hydrochloric acid. If the coal contains a large amount of sulfur acidified manganese chloride including a large proportion of iron is used as colloid forming material, the oxides of manganese and iron subsequently precipitated forming stable compounds with the non-volatile sulfur on coking or combustion.

The mechanism of coking pressure generation I: Effect of high volatile matter coking coal, semi-anthracite and coke breeze on coking pressure and plastic coal layer permeability

Energy Technology Data Exchange (ETDEWEB)

Seiji Nomura; Merrick Mahoney; Koichi Fukuda; Kenji Kato; Anthony Le Bas; Sid McGuire [Nippon Steel Corporation, Chiba (Japan). Environment and Process Technology Center

2010-07-15

One of the most important aspects of the cokemaking process is to control and restrain the coking pressure since excessive coking pressure tends to lead to operational problems and oven wall damage. Therefore, in order to understand the mechanism of coking pressure generation, the permeability of the plastic coal layer and the coking pressure for the same single coal and the same blended coal were measured and the relationship between them was investigated. Then the 'inert' (pressure modifier) effect of organic additives such as high volatile matter coking coal, semi-anthracite and coke breeze was studied. The coking pressure peak for box charging with more uniform bulk density distribution was higher than that for top charging. It was found that the coking pressure peaks measured at different institutions (NSC and BHPBilliton) by box charging are nearly the same. The addition of high volatile matter coking coal, semi-anthracite and coke breeze to a low volatile matter, high coking pressure coal greatly increased the plastic layer permeability in laboratory experiments and correspondingly decreased the coking pressure. It was found that, high volatile matter coking coal decreases the coking pressure more than semi-anthracite at the same plastic coal layer permeability, which indicates that the coking pressure depends not only on plastic coal layer permeability but also on other factors. Coking pressure is also affected by the contraction behavior of the coke layer near the oven walls and a large contraction decreases the coal bulk density in the oven center and hence the internal gas pressure in the plastic layer. The effect of contraction on coking pressure needs to be investigated further. 33 refs., 18 figs., 5 tabs.

Programmed heating of coke ovens for increased coke size

Energy Technology Data Exchange (ETDEWEB)

Jenkins, D.R.; Mahoney, M.R. [University of Newcastle, Callaghan, NSW (Australia)

2010-11-15

Large, uniform sized coke is desirable for blast furnace use. It has previously been shown that the coke oven flue temperature in the first few hours of coking is a key determinant of coke size. In this paper, the authors present a new programmed heating approach, which is called pulsed heating, aiming to increase coke mean size at a given average flue temperature. The approach takes into account the charging sequence in coke oven batteries and the authors demonstrate how existing operating practice can be modified in batteries with suitable heating systems to achieve the desired heating programme. A mathematical model of fissure formation provides a prediction of the increase in coke mean size using pulsed heating, compared with standard heating. Pilot scale experiments have also been performed to validate the modelling approach. The results of the modelling indicate that the mean coke size can be increased by several millimetres in some cases, although results from the pilot scale show that pulsed heating increases coke size, but by a smaller amount than that predicted by the model. The potential advantages and limitations of pulsed heating are discussed, as well as opportunities for further investigation of the approach.

The mechanism of coking pressure generation II: Effect of high volatile matter coking coal, semi-anthracite and coke breeze on coking pressure and contraction

Energy Technology Data Exchange (ETDEWEB)

Merrick Mahoney; Seiji Nomura; Koichi Fukuda; Kenji Kato; Anthony Le Bas; David R. Jenkins; Sid McGuire [BHP Billiton Technology, Shortland, NSW (Australia)

2010-07-15

One of the most important aspects of the cokemaking process is to control and limit the coking pressure since excessive coking pressure can lead to operational problems and oven wall damage. Following on from a previous paper on plastic layer permeability we have studied the effect of contraction of semi-coke on coking pressure and the effect of organic additives on contraction. A link between contraction (or simulated contraction) outside the plastic layer and coking pressure was demonstrated. The interaction between this contraction, local bulk density around the plastic layer and the dependence of the permeability of the plastic layer on bulk density was discussed as possible mechanisms for the generation of coking pressure. The effect of blending either a high volatile matter coal or one of two semi-anthracites with low volatile matter, high coking pressure coals on the coking pressure of the binary blends has been explained using this mechanism. 25 refs., 10 figs., 4 tabs.

The coke dilemma

Energy Technology Data Exchange (ETDEWEB)

Champagne, P E; Lewis, J A

1989-08-01

Coke-making capacity reductions and the current status of coke oven batteries in the USA are surveyed, as well as prior forecasts of the steel and coke markets. The future position is then analysed and it is concluded that the US coke supply situation should improve up to 1995, but that there could be major domestic coke production deficits in the period 1996-2000; critical decisions will soon have to be made about replacement of coking capacity.

Proceedings - Alternate Fuels II: The disposal and productive use of industrial wastes

International Nuclear Information System (INIS)

Anon.

1991-01-01

The proceedings contain 26 papers dealing with the following topics: fuels (biomass, coal, petroleum coke, landfill gas, hazardous and toxic wastes, liquid wastes, and digester gas); combustion systems; plant systems (pollution control, combustion control, and materials handling systems); external factors (public relations, markets, hazardous waste, vitrification for waste management); and case histories of resource recovery facilities, process heating plants, and retrofits to alternative fuels. All papers have been processed separately for inclusion on the data base

Possibilities of using pulverized non coking coals in ironmaking

Energy Technology Data Exchange (ETDEWEB)

Wijk, Olle; Mathiesen, Mihkel; Eketorp, Sven

1977-08-01

The use of pulverized coal in iron making suggests solutions to the mounting problems created by the increasing scarcity of coking coals, and other fossil fuels such as oil and natural gas. The unavailability of coke can be met with two principally different measures. Blast furnace coke rates can be decreased by substituting injected pulverized coal or other carbon containing fuels for part of the coke burden, and the coke itself may be substituted by formed coke. A more radical solution is to abandon the blast furnace process, and instead produce the raw iron in processes not requiring coke. Two such processes are discussed in the paper, the Inred process, developed by Boliden Kemi AB, Sweden, and the smelting reduction process by means of injection, currently being developed at the Royal Institute of Technology in Stockholm. Both processes have potential advantages over the coke oven/sintering plant/blast furnace-complex especially concerning energy requirements and structure, but also in economical terms. The injection process seems to present a further advantage in the possibility of gasifying coal in the process, thus yielding a synthesis gas for methanol production in addition to the raw iron.

Fractionation of trace elements and human health risk of submicron particulate matter (PM1) collected in the surroundings of coking plants.

Science.gov (United States)

Zajusz-Zubek, Elwira; Radko, Tomasz; Mainka, Anna

2017-08-01

Samples of PM1 were collected in the surroundings of coking plants located in southern Poland. Chemical fractionation provided information on the contents of trace elements As, Cd, Co, Cr, Hg, Mn, Ni, Pb, Sb and Se in all mobile (F1-F3) and not mobile (F4) fractions of PM1 in the vicinity of large sources of emissions related to energochemical processing of coal during the summer. The determined enrichment factors indicate the influence of anthropogenic sources on the concentration of the examined elements contained in PM1 in the areas subjected to investigation. The analysis of health risk for the assumed scenario of inhabitant exposure to the toxic effect of elements, based on the values of the hazard index, revealed that the absorption of the examined elements contained in the most mobile fractions of particulate matter via inhalation by children and adults can be considered potentially harmless to the health of people inhabiting the surroundings of coking plants during the summer (HI PM1, approximately four adults and one child out of one million people living in the vicinity of the coking plants may develop cancer.

Adsorption of organic pollutants from coking and papermaking wastewaters by bottom ash.

Science.gov (United States)

Sun, Wei-ling; Qu, Yan-zhi; Yu, Qing; Ni, Jin-ren

2008-06-15

Bottom ash, a power plant waste, was used to remove the organic pollutants in coking wastewater and papermaking wastewater. Particular attention was paid on the effect of bottom ash particle size and dosage on the removal of chemical oxygen demand (COD). UV-vis spectra, fluorescence excitation-emission matrix (FEEM) spectra, Fourier transform infrared (FTIR) spectra, and scanning electron microscopic (SEM) photographs were investigated to characterize the wastewaters and bottom ash. The results show that the COD removal efficiencies increase with decreasing particle sizes of bottom ash, and the COD removal efficiency for coking wastewater is much higher than that for papermaking wastewater due to its high percentage of particle organic carbon (POC). Different trends of COD removal efficiency with bottom ash dosage are also observed for coking and papermaking wastewaters because of their various POC concentrations. Significant variations are observed in the FEEM spectra of wastewaters after treatment by bottom ash. New excitation-emission peaks are found in FEEM spectra, and the fluorescence intensities of the peaks decrease. A new transmittance band in the region of 1400-1420 cm(-1) is observed in FTIR spectra of bottom ash after adsorption. The SEM photographs reveal that the surface of bottom ash particles varies evidently after adsorption.

Adsorption of organic pollutants from coking and papermaking wastewaters by bottom ash

International Nuclear Information System (INIS)

Sun Weiling; Qu Yanzhi; Yu Qing; Ni Jinren

2008-01-01

Bottom ash, a power plant waste, was used to remove the organic pollutants in coking wastewater and papermaking wastewater. Particular attention was paid on the effect of bottom ash particle size and dosage on the removal of chemical oxygen demand (COD). UV-vis spectra, fluorescence excitation-emission matrix (FEEM) spectra, Fourier transform infrared (FTIR) spectra, and scanning electron microscopic (SEM) photographs were investigated to characterize the wastewaters and bottom ash. The results show that the COD removal efficiencies increase with decreasing particle sizes of bottom ash, and the COD removal efficiency for coking wastewater is much higher than that for papermaking wastewater due to its high percentage of particle organic carbon (POC). Different trends of COD removal efficiency with bottom ash dosage are also observed for coking and papermaking wastewaters because of their various POC concentrations. Significant variations are observed in the FEEM spectra of wastewaters after treatment by bottom ash. New excitation-emission peaks are found in FEEM spectra, and the fluorescence intensities of the peaks decrease. A new transmittance band in the region of 1400-1420 cm -1 is observed in FTIR spectra of bottom ash after adsorption. The SEM photographs reveal that the surface of bottom ash particles varies evidently after adsorption

System for reducing emissions during coke oven charging; System zur Emissionsverringerung beim Fuellen von Koksoefen

Energy Technology Data Exchange (ETDEWEB)

Schuecker, Franz-Josef [ThyssenKrupp Industrial Solutions AG, Dortmund (Germany). Head of Oven Machine Dept., Coke Plant Technologies

2014-10-01

This article describes a process which reduces emissions from coke production in coke plants. The focus is on the charging process, which can be partly responsible for the fact that statutory emissions limits, which were originally met, are exceeded as coke plants get older. This article presents a solution in the form of a newly developed system that allows the oven charging system - the charging car - to respond to age-related changes in the geometry of a coke oven and thereby reduce the level of emissions.

World coking coal markets

International Nuclear Information System (INIS)

McCloskey, G.

2010-01-01

This article discussed conditions in world coking coal markets. There is increased demand from Asia for metallurgical coal imports. World iron production was up 22 percent in first 7 months of 2010. Supply is up in Australia, the United States, Canada, New Zealand, Russia, and Mongolia, but the unexpected surge in supply caused prices to drop following a robust start to the year. Coking coal exports are up for the United States and Australia, but a delay in expanded production is expected until 2014. There is increased demand from Brazil, India, Taiwan, South Korea, and Japan as well as new plants in Thailand, Indonesia, and Brazil. Unexpectedly, Australia is backing out of the Chinese market but increasing exports to Japan and South Korea. India is seeing flat performance in iron production and imports, and the United States has surged back into Asia. A considerable increase is expected in the seaborne import requirement by 2020. Prices are expected to fall and then rise. This presentation also discussed whether coking coal index pricing is impossible or inevitable. 3 tabs., 5 figs.

Steam versus coking coal and the acid rain program

International Nuclear Information System (INIS)

Lange, Ian

2010-01-01

The Clean Air Act of 1990 initiated a tradable permit program for emissions of sulfur dioxide from coal-fired power plants. One effect of this policy was a large increase in the consumption of low-sulfur bituminous coal by coal-fired power plants. However, low-sulfur bituminous coal is also the ideal coking coal for steel production. The analysis presented here will attempt to determine how the market responded to the increased consumption of low-sulfur bituminous coal by the electricity generation sector. Was there a decrease in the quality and/or quantity of coking coal consumption or did extraction increase? Most evidence suggests that the market for coking coal was unaffected, even as the extraction and consumption of low-sulfur bituminous coal for electricity generation increased substantially.

Problems of new processes in coking industry discussed at the Scientific Council of the GKNT and the Section of Coking Industry of the Scientific and Technological Council of the Ministry of Iron and Steel Industry of the USSR

Energy Technology Data Exchange (ETDEWEB)

Ermolova, V.P.

1983-03-01

A report is given from the conference on new processes in the Soviet coking industry held in Moscow on 28-29 October 1982. The following papers were delivered: implementing research programs on new coking processes, new trends in coking plant design and construction in the 11th 5 year plan and in the time period until 1990, increasing efficiency of coking industry, research program of the Scientific Council in 1983. The report concentrates on new trends in coking plant design. Considering that the raw material basis of the Eastern regions of the USSR is poor in high quality coking coal the new coking processes and technologies should use weakly coking coal. The following schemes are discussed: heat treatments (especially useful in the case of black coal from the Kuzbass characterized by intensive fluctuations of petrology), selective crushing (schemes developed by the VUKhIN Institute), partial briquetting of coal mixtures (experiments carried out by the UKhIN in the Donbass in 1982). Other problems of coking such as development of new systems of smokeless fuel feeding to coke ovens, dry coke quenching, increasing capacity of coke chambers to 41.6 m/sup 3/, environmental protection in coking industry and production of special coke types from poor quality coal for metallurgy are also described.

Using helical compressors for coke gas condensation

Energy Technology Data Exchange (ETDEWEB)

Privalov, V E; Rezunenko, Yu I; Lelyanov, N V; Zarnitzkii, G Eh; Gordienko, A A; Derebenko, I F; Venzhega, A G; Leonov, N P; Gorokhov, N N

1982-08-01

Coke oven gas compression is discussed. Presently used multilevel piston compressors are criticized. The paper recommends using helical machines which combine advantages of using volume condensing compressors and compact high-efficiency centrifugal machines. Two kinds of helical compressors are evaluated: dry and oil-filled; their productivities and coke oven gas chemical composition are analyzed. Experiments using helical compressors were undertaken at the Yasinovskii plant. Flowsheet of the installation is shown. Performance results are given in a table. For all operating conditions content of insolubles in oil compounds is found to be lower than the acceptable value (0.08%). Compressor productivity measurements with variable manifold pressure are evaluated. Figures obtained show that efficient condensation of raw coke oven gas is possible. Increasing oil-filled compressor productivity is recommended by decreasing amount of oil injected and simultaneously increasing rotation speed. The dry helical compressor with water seal is found to be most promising for raw coke oven gas condensation. (10 refs.)

Method of determining coking temperature of coke. [Experimental method of determining final coking temperature using a small sample and calibration graph

Energy Technology Data Exchange (ETDEWEB)

Mel' nichuk, A.Yu.; Bondarenko, A.K.; Fialkov, B.S.; Khegay, L.U.; Khvan, L.A.; Muzyzhuk, V.D.; Zakharov, A.G.; Zelenskiy, V.P.

1985-01-01

The coking temperature of coke should be determined from the magnitude of the ionization current of the medium during heating (3/sup 0//min) of a coke sample (2 g, fraction < 0.2 mm) in an oxidation medium with air supply (1 1/min). The coking temperature is determined from the maximum magnitude of current using a graduated graph constructed during analysis of coke samples obtained with different final coking temperatures. The discrepancy between the established coking temperature and that defined from the proposed method is 8-19/sup 0/, and that defined from electrical resistance of coke is 26-43/sup 0/. In addition to high accuracy, this method reduces the time outlays for making the analysis.

Environmental impact of heavy metals on the soils and plants around a coke-making factory of Jiyuan city, China

Science.gov (United States)

Lun Leung, Kwun

2010-05-01

The combustion of coal usually leads to many different kinds of pollution around coke-making factories. Among these pollutions, the heavy metal contamination in the soil and plants is one of the major concerns by people living around. Heavy metals are highly attracted to the biological tissue, and can stay in bodies of organisms for long period of time, causing a lot of hazardous diseases to human beings, animal and plants. In the developing regions of China, developing of industries has been based on the sacrifices of environments and human health. In order to evaluate the danger of heavy metal contamination from a coke factory to citizens of close inhabitants, a survey on soil and plants was conducted in the region around a coke-making factory in Jiyuan city, which is a major electricity supplying city for the Henan Province in China. In this study, 8 surface soil samples and 11 plant samples were collected from 8 different places around the coke-making factory in Jiyuan city. The collected samples are then treated in the laboratory, and 8 types of heavy metals, which include arsenic, cadmium, chromium, cobalt, copper, lead, nickel and zinc, are analyzed by Inductively Coupled Plasma Mass Spectrometry (ICP-MS) and Inductively Coupled Plasma Atomic Emission Spectroscopy (ICP-AES). The concentration data of heavy metals that collected from the analysis are then used to evaluate their toxicity towards living organisms and ecology by applying several biological effect standards, such as effect-range low (ERL), effect-range median (ERM) and several maximum allowances standards of heavy metal concentrations in soils and plants that established by different countries. Moreover, the relationship between the distance from the factory and the concentration of heavy metals in soils and plants are also evaluated in order to find out the contamination ranges of those heavy metals from the source. The result shows that the concentration of these 8 types of heavy metals in the

The reaction of Polish market to last year's changes on international coke and steel market

Energy Technology Data Exchange (ETDEWEB)

Czornik, G.; Gabriel, D. [Polski Koks S.A. (Poland)

2004-07-01

The presentation, outlined in 16 slides/overheads, discussed the following: Poland's position in the world market; the Polish coking industry and the world coke and steel industry; the reaction of Polish coke plants; the effect of the increase in coke prices; ownership changes in Poland's coking industry scenarios for the future; the role of Polski Koks in Poland's coking industry; and sales and exports of coke by Polski Koks.

Dale Coke: Coke Farm

OpenAIRE

Farmer, Ellen

2010-01-01

Dale Coke grew up on an apricot orchard in California’s Santa Clara Valley. In 1976 he bought ten acres of farmland near Watsonville in Santa Cruz County but continued to work repairing fuel injection systems rather than farming at his new home. In 1981, a struggle with cancer inspired him to rethink his life and become an organic farmer. His neighbor, who had grown strawberries using pesticides and chemical fertilizers, asserted that strawberries could not be grown organically. Coke set out ...

Dust emission from wet, low-emission coke quenching process

Science.gov (United States)

Komosiński, Bogusław; Bobik, Bartłomiej; Konieczny, Tomasz; Cieślik, Ewelina

2018-01-01

Coke plants, which produce various types of coke (metallurgical, foundry or heating), at temperatures between 600 and 1200°C, with limited access to oxygen, are major emitters of particulates and gaseous pollutants to air, water and soils. Primarily, the process of wet quenching should be mentioned, as one of the most cumbersome. Atmospheric pollutants include particulates, tar substances, organic pollutants including B(a)P and many others. Pollutants are also formed from the decomposition of water used to quench coke (CO, phenol, HCN, H2S, NH3, cresol) and decomposition of hot coke in the first phase of quenching (CO, H2S, SO2) [1]. The development of the coke oven technology has resulted in the changes made to different types of technological installations, such as the use of baffles in quench towers, the removal of nitrogen oxides by selective NOx reduction, and the introduction of fabric filters for particulates removal. The BAT conclusions for coke plants [2] provide a methodology for the measurement of particulate emission from a wet, low-emission technology using Mohrhauer probes. The conclusions define the emission level for wet quenching process as 25 g/Mgcoke. The conducted research was aimed at verification of the presented method. For two of three quench towers (A and C) the requirements included in the BAT conclusions are not met and emissions amount to 87.34 and 61.35 g/Mgcoke respectively. The lowest particulates emission was recorded on the quench tower B and amounted to 22.5 g/Mgcoke, therefore not exceeding the requirements.

Coking industry of China (conclusion of visit to People's Republic of China)

Energy Technology Data Exchange (ETDEWEB)

Sklyar, M.G. (NPO Koksokhimiya (USSR))

1990-12-01

Presents a report on the coking industry in China, in particular, research programs on coking. The report was prepared by Soviet specialists who visited China in March 1990 within the framework of an exchange program. The following aspects are discussed: characteristics of iron metallurgy and the coking industry in China, research institutes that specialize in problems of iron metallurgy and coking, main research programs of Chinese research institutes (development of a 12-category classification of black coal from China, coal preparation prior to coking including selective crushing, formed coke processes, quality of the products of bituminous coal coking, coal gasification and hydrogenation), installations used for research programs in China (delayed coking of black coal, hydrogenation of long-flame coal, coal briquetting), characteristics of selected coking plants in China, training for specialists in the coking industry in China.

A complex approach to the health states of pitch coking plant workers

Energy Technology Data Exchange (ETDEWEB)

Kandus, J.

1976-01-01

206 workers of three pitch coking plants, who had been exposed for an average of 4 years to fumes containing 3,4 benzopyrene, were examined. No occupational carcinoma or precancerous foci were detected. The only statistically significant findings were chronic atrophic inflammations of upper respiratory pathways (26%). This investigation is the initial stage in a long-term study of this group of workers. A plan for preventive examinations (including specialized ones), contraindications applicable for this type of job, methods for epidemiological investigations and the follow-up of workers after leaving this work, are described in detail.

Emission and profile characteristic of volatile organic compounds emitted from coke production, iron smelt, heating station and power plant in Liaoning Province, China.

Science.gov (United States)

Shi, Jianwu; Deng, Hao; Bai, Zhipeng; Kong, Shaofei; Wang, Xiuyan; Hao, Jiming; Han, Xinyu; Ning, Ping

2015-05-15

107 kinds of C₂-C₁₂ volatile organic compound (VOC) mass concentrations and profiles for four types of coal-fired stationary sources in Liaoning Province were studied by a dilution sampling system and GC-MS analysis method, which are of significant importance with regard to VOC emissions in northeast of China. The results showed that there were some differences among these VOC source profiles. The total mass concentrations of analyzed 107 VOC species varied from 10,917 to 19,652 μg m(-3). Halogenated hydrocarbons exhibited higher mass percentages for the VOC source profiles of iron smelt (48.8%) and coke production plant (37.7%). Aromatic hydrocarbons were the most abundant in heating station plant (69.1%). Ketones, alcohols and acetates held 45.0% of total VOCs in thermal power plant. For non-methane hydrocarbons (NMHCs), which are demanded for photochemical assessment in the USA, toluene and n-hexane were the most abundant species in the iron smelt, coke production and thermal power plant, with the mass percentages of 64.8%, 52.7% and 38.6%, respectively. Trimethylbenzene, n-propylbenzene and o,m-ethyltoluene approximately accounted for 70.0% in heating station plant. NMHCs emitted from coke production, iron smelt, heating station and power plant listed above presented different chemical reactivities. The average OH loss rate of NMHCs from heating station, was 4 to 5.6 times higher than that of NMHCs from iron smelt, coke production and power plant, which implies that VOCs emitted from heating station in northeast of China should be controlled firstly to avoid photochemical ozone pollution and protect human health. There are significant variations in the ratios of benzene/toluene and m, p-xylene/ethylbenzene of these coal-fired source profiles. The representativeness of the coal-fired sources studied and the VOC samples collected should be more closely examined. The accuracy of VOC source profiles related to coal-fired processes is highly dependent on

Study of phenol extraction from coke-chemical sources

Energy Technology Data Exchange (ETDEWEB)

Catana, E.; Mateescu, I.; Giurcaneanu, V.; Bota, T.

1990-09-01

The paper presents an experimental study of the phase equilibrium in the coke-chemical tarphenols-solvent system (NaOH) solution and (phenolate solution) implied in the extraction of the phenols from coke-chemical sources. The possibility of using the phenolate solution as an extraction agent, thus making possible the improvement of the specific consumption and also simplifying the problem of the corrosion and of the waste water at the same time is presented. The influence of the solvent tar mass ratio on the selectivity of the process is discussed, this criterion being considered for establishing the conditions of the extraction. 2 figs., 7 tabs., 13 refs.

Emissions and emission reduction systems in the coal derivative production facilities of a coking plant. Emissionsquellen in Kohlenwertstoffbetrieben von Kokereien und Massnahmen zu ihrer Verminderung

Energy Technology Data Exchange (ETDEWEB)

1985-01-01

Coking plants may present odour unisances to their vicinity although these odours are no health problem. Typical odorants emitted by a coking plant are: Hydrogen sulfide, mercaptanes, carbon sulfide, naphthaline, phenol and ammonia. The odour threshold of these substances may be quite close to the analytical detection limit. There are a large number of emission sources, e.g. production and storage containers, baths, tar sinks, and ventilation systems. The report describes the possible sources of emissions as well as the countermeasures available at the present state of the art.

Hot testing of coke

Energy Technology Data Exchange (ETDEWEB)

Balon, I D

1976-07-01

Earlier investigations failed to take full account of the factors affecting coke behavior within the blast furnace. An apparatus was accordingly developed for testing coke, based on a cyclone furnace where the sample could be held in a flow of hot oxidizing gases, simulating conditions in the blast furnace hearth. The results are said to be suitable for comprehensive assessment of the coke, including abrasive strength and its rate of gasification in a flow of carbon dioxide. Coke of size 6-10 mm tested at 1,100/sup 0/C in an atmosphere of oxidizing gases close to those obtaining in the blast furnace hearth, indicated that destruction and total gasification of the coke occurs after 5 minutes for a weak coke and 8 minutes for strong coke, depending on the physico-chemical and physico-mechanical properties of the particular coke. When samples were treated for a fixed period (3 minutes), the amount of coke remaining, and the percentage over 6 mm varied between 22 and 40 and between 4 and 7 percent respectively.

Fissure formation in coke. 3: Coke size distribution and statistical analysis

Energy Technology Data Exchange (ETDEWEB)

D.R. Jenkins; D.E. Shaw; M.R. Mahoney [CSIRO, North Ryde, NSW (Australia). Mathematical and Information Sciences

2010-07-15

A model of coke stabilization, based on a fundamental model of fissuring during carbonisation is used to demonstrate the applicability of the fissuring model to actual coke size distributions. The results indicate that the degree of stabilization is important in determining the size distribution. A modified form of the Weibull distribution is shown to provide a better representation of the whole coke size distribution compared to the Rosin-Rammler distribution, which is generally only fitted to the lump coke. A statistical analysis of a large number of experiments in a pilot scale coke oven shows reasonably good prediction of the coke mean size, based on parameters related to blend rank, amount of low rank coal, fluidity and ash. However, the prediction of measures of the spread of the size distribution is more problematic. The fissuring model, the size distribution representation and the statistical analysis together provide a comprehensive capability for understanding and predicting the mean size and distribution of coke lumps produced during carbonisation. 12 refs., 16 figs., 4 tabs.

New technological solutions in construction and operation of batteries with large coke ovens

Energy Technology Data Exchange (ETDEWEB)

Volokita, G.I.; Bulyga, N.I.

1988-11-01

Describes design modifications to the No. 7 coke oven battery with 7.0 m high coke ovens in the Avdeevka coking plant. Temperature distribution in the large coke ovens was irregular due to the specific design of the heating system, distribution and dimensions of flue channels and thickness of flue channel walls. During coke battery reconstruction length of the peripheral flue channels was reduced by 70 mm, coke oven volume was reduced from 41.6 to 41.3 m/sup 3/. These design changes resulted in a more regular temperature distribution and reduced temperature difference between the coke oven center and zones close to the machine and pusher sides. Thickness of flue channel walls was reduced from 130 to 105 mm. Special reinforcing elements that guarantee more regular temperature distribution and increased wall service life were used.

Fine art of coking

Energy Technology Data Exchange (ETDEWEB)

Dresner, S.

1984-01-01

The art and science of coking are discussed. Coke is the solid carbon made from the heavy, viscous residue left after the more useful products such as gasoline and diesel fuel have been refined out of the crude oil. Fuel grade coke can be a substitute for steam coal in many applications. Low-sulfur fuel coke is used in blast furnaces for steelmaking. The operations of Conoco's refineries for producing coke is described.

Integrated process for synthetic natural gas production from coal and coke-oven gas with high energy efficiency and low emission

International Nuclear Information System (INIS)

Man, Yi; Yang, Siyu; Qian, Yu

2016-01-01

Highlights: • A novel coal and coke-oven gas to SNG (CGtSNG) process is proposed. • Energy efficiency of CGtSNG increases 8% compared to coal-to-SNG process. • CGtSNG reduces 60% CO_2 emission and 72% effluent discharge. • CGtSNG proposes an idea of using redundant coke-oven gas for producing SNG production. - Abstract: There was a rapid development of coal to synthetic natural gas (SNG) projects in the last few years in China. The research from our previous work and some other researchers have found coal based SNG production process has the problems of environmental pollution and emission transfer, including CO_2 emission, effluent discharge, and high energy consumption. This paper proposes a novel co-feed process of coal and coke-oven gas to SNG process by using a dry methane reforming unit to reduce CO_2 emissions, more hydrogen elements are introduced to improve resource efficiency. It is shown that the energy efficiency of the co-feed process increases by 4%, CO_2 emission and effluent discharge is reduced by 60% and 72%, whereas the production cost decreases by 16.7%, in comparison to the conventional coal to SNG process. As coke-oven gas is a waste gas in most of the coking plant, this process also allows to optimize the allocation of resources.

Closed-cycle process of coke-cooling water in delayed coking unit

International Nuclear Information System (INIS)

Zhou, P.; Bai, Z.S.; Yang, Q.; Ma, J.; Wang, H.L.

2008-01-01

Synthesized processes are commonly used to treat coke-cooling wastewater. These include cold coke-cut water, diluting coke-cooling water, adding chemical deodorization into oily water, high-speed centrifugal separation, de-oiling and deodorization by coke adsorption, and open nature cooling. However, because of water and volatile evaporation loss, it is not suitable to process high-sulphur heavy oil using open treatments. This paper proposed a closed-cycling process in order to solve the wastewater treatment problem. The process is based on the characteristics of coke-cooling water, such as rapid parametric variation, oil-water-coke emulsification and steam-water mixing. The paper discussed the material characteristics and general idea of the study. The process of closed-cycle separation and utilization process of coke-cooling water was presented along with a process flow diagram. Several applications were presented, including a picture of hydrocyclones for pollution separation and a picture of equipments of pollution separation and components regeneration. The results showed good effect had been achieved since the coke-cooling water system was put into production in 2004. The recycling ratios for the components of the coke-cooling water were 100 per cent, and air quality in the operating area reached the requirements of the national operating site circumstance and the health standards. Calibration results of the demonstration unit were presented. It was concluded that since the devices went into operation, the function of production has been normal and stable. The operation was simple, flexible, adjustable and reliable, with significant economic efficiency and environmental benefits. 10 refs., 2 tabs., 3 figs

The effect of ash elements in petroleum coke on hearth furnace heat recovery system performance

Energy Technology Data Exchange (ETDEWEB)

Akhmetov, M M

1981-01-01

Difficulties encountered in the operation of the heat recovery system of a calcination plant at Krasnovodsk Refinery caused by ash element deposits blocking the fire box are described. Deposits and coke ash composition are given. The main cause of blocking was found to be the removal of sea water salt elements which get on the coke surface when the retarded coking plant is discharged with a water-jet borer. Switching over to fresh water and air-blasting of heat recovery pipes decreased blocking considerably.

Fissure formation in coke. 2: Effect of heating rate, shrinkage and coke strength

Energy Technology Data Exchange (ETDEWEB)

D.R. Jenkins; M.R. Mahoney [CSIRO, North Ryde, NSW (Australia). Mathematical and Information Sciences

2010-07-15

We investigate the effects of the heating rate, coke shrinkage and coke breakage strength upon the fissure pattern developed in a coke oven charge during carbonisation. This is done principally using a mechanistic model of the formation of fissures, which considers them to be an array of equally spaced fissures, whose depth follows a 'period doubling' pattern based upon the time history of the fissures. The model results are compared with pilot scale coke oven experiments. The results show that the effect of heating rate on the fissure pattern is different to the effect of coke shrinkage, while the effect of coke breakage strength on the pattern is less pronounced. The results can be seen in both the shape and size of resulting coke lumps after stabilisation. The approach gives the opportunity to consider means of controlling the carbonisation process in order to tune the size of the coke lumps produced. 7 refs., 18 figs., 4 tabs.

Mineral matter reactions in cokes

Energy Technology Data Exchange (ETDEWEB)

D. French; R. Sakurovs; M. Grigore [CSIRO Energy Technology (Australia)

2009-07-15

Some cokes appear to be particularly susceptible to weakening in the blast furnace. A mechanism which has been postulated to explain this is silica reduction by coke. Thus this project was initiated to ascertain the behaviour of quartz and silicates in coke with an emphasis on the role of the clay minerals. It is now possible to obtain quantitative mineralogical data and, the case of coal, to also obtain quantitative data on mineral grain size, shape and association through the use of automated electron beam image analysis techniques. This new ability can allow relationships between the amount of minerals in a coke and its reactivity to be established for the first time. Samples of five Australian coking coals were selected based upon quartz and clay mineral contents, mineral grain size and association. Samples were also provided by BlueScope Steel of coal, feed coke, and tuyere coke samples from the bosh, deadman and raceway regions of the blast furnace. The analytical work program conducted was as follows: Preparation of cokes by CSIRO; Petrography of starting coals and cokes; QEMSCAN of coals; LTA and XRD of starting coals and cokes; Coke reactivity tests (NSC and small scale); Petrography, LTA and XRD of reacted cokes; Petrographic and XRD examination of heat treated cokes. This study indicates that the NSC reactivity test does not adequately reflect the behaviour of coke in the lower part of the blast furnace. Further investigation of the behaviour of coke in the lower part of the blast furnace is required.

Achievements and research programs of the Institute for Chemical Coal Processing in the field of conventional coking

Energy Technology Data Exchange (ETDEWEB)

Cieslar, R.; Kaziszyn, I.; Zawistowksi, J.

1986-11-01

This paper describes research programs of the Institute for Chemical Coal Processing in Zabrze on black coal coking and coke use in metallurgy from 1955 to 1990. In 1955-1970 the programs concentrated on coal mixture composition (selective crushing), optimization of coking conditions, mechanical coke treatment. In 1971-1980 research concentrated on coal preparation prior to coking and new coking systems for the Katowice steel plant (heat treatments, design of large coke ovens). The following research programs were implemented in 1981-1985: partial coal charge briquetting, production of foundry coke, coal charge preheating, production of blast furnace coke from black coal from Dobiensko, reducing coke consumption of blast furnaces. In 1986-1990 the Institute will concentrate on the following research programs: coal preparation schemes and coking schemes for coking low-quality weakly caking coals, optimization of coke oven design (e.g. use of packed charge), reducing coke consumption in metallurgy and heating systems, reducing air pollution from coking.

New and revised standards for coke production

Energy Technology Data Exchange (ETDEWEB)

G.A. Kotsyuba; M.I. Alpatov; Y.G. Shapoval [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15

The need for new and revised standards for coke production in Ukraine and Russia is outlined. Such standards should address improvements in plant operation, working conditions, environmental protection, energy conservation, fire and explosion safety, and economic indices.

Coke retorts

Energy Technology Data Exchange (ETDEWEB)

Jones, S; MacDonald, J D

1916-07-15

To charge vertical coke retorts while preventing escape of gases the coal is fed by a revolving drum to an archimedean screw at the base of the retort, the coke being discharged at the top through a water seal. The feed pockets of the drum which revolves between plates, deliver coal from the hopper to the revolving screw. The coke is forced under the hood to the water seal and is removed by rake conveyor, the gases escaping through the pipe to the main.

Recycling of rubber tires in electric arc furnace steelmaking: simultaneous combustion of metallurgical coke and rubber tyres blends

Energy Technology Data Exchange (ETDEWEB)

Magdalena Zaharia; Veena Sahajwalla; Byong-Chul Kim; Rita Khanna; N. Saha-Chaudhury; Paul O' Kane; Jonathan Dicker; Catherine Skidmore; David Knights [University of New South Wales, Sydney, NSW (Australia). School of Materials Science and Engineering

2009-05-15

The present study investigates the effect of addition of waste rubber tires on the combustion behavior of its blends with coke for carbon injection in electric arc furnace steelmaking. Waste rubber tires were mixed in different proportions with metallurgical coke (MC) (10:90, 20:80, 30:70) for combustion and pyrolysis at 1473 K in a drop tube furnace (DTF) and thermogravimetric analyzer (TGA), respectively. Under experimental conditions most of the rubber blends indicated higher combustion efficiencies compared to those of the constituent coke. In the early stage of combustion the weight loss rate of the blends is much faster compared to that of the raw coke due to the higher volatile yield of rubber. The presence of rubber in the blends may have had an impact upon the structure during the release and combustion of their high volatile matter (VM) and hence increased char burnout. Measurements of micropore surface area and bulk density of the chars collected after combustion support the higher combustion efficiency of the blends in comparison to coke alone. The surface morphology of the 30% rubber blend revealed pores in the residual char that might be attributed to volatile evolution during high temperature reaction in oxygen atmosphere. Physical properties and VM appear to have a major effect upon the measured combustion efficiency of rubber blends. The study demonstrates that waste rubber tires can be successfully co-injected with metallurgical coke in electric arc furnace steelmaking process to provide additional energy from combustion. 44 refs., 11 figs., 2 tabs.

80. special meeting on coke

Energy Technology Data Exchange (ETDEWEB)

1986-01-01

There were 12 papers presented at the special meeting on coke. These have the following headings: relationship between coal properties and optical anisotropic textures of coke; development of optical texture of chemically modified low rank coal; relationship between fluid and swelling properties of Akabira coal; estimation of coal fluidity; present state and future of robotics; on the thermal stress during the carbonisation process of coals; development of estimation model for coke porosity distribution in the coke oven using X-ray CT; carbonization reaction of coke oven; relationship between qualities of coke and width of coke oven; development of carbonization model in coke ovens - estimation of growing clearance between heating wall and charge; development of automatic transparency analyzer for activated sludge process.

Characterization of norm sources in petroleum coke calcining processes - 16314

International Nuclear Information System (INIS)

Hamilton, Ian S.; Halter, Donald A.; Fruchtnicht, Erich H.; Arno, Matthew G.; Haumann, Donald F

2009-01-01

Petroleum coke, or 'petcoke', is a waste by-product of the oil refining industry. The majority of petcoke consumption is in energy applications; catalyst coke is used as refinery fuel, anode coke for electricity conduction, and marketable coke for heating cement kilns. Roskill has predicted that long-term growth in petroleum coke production will be maintained, and may continue to increase slightly through 2012. Petcoke must first be calcined to drive off any undesirable petroleum by-products that would shorten the coke product life cycle. As an example, the calcining process can take place in large, rotary kilns heated to maximum temperatures as high as approximately 1400-1540 deg. C. The kilns and combustion/settling chambers, as well as some cooler units, are insulated with refractory bricks and other, interstitial materials, e.g., castable refractory materials, to improve the efficiency of the calcining process. The bricks are typically made of 70-85-percent bauxite, and are slowly worn away by the calcining process; bricks used to line the combustion chambers wear away, as well, but at a slower rate. It has been recognized that the refractory materials contain slight amounts of naturally occurring radioactive materials (NORM) from the uranium- and thorium-decay series. Similarly, low levels of NORM could be present in the petcoke feed stock given the nature of its origin. Neither the petcoke nor the refractory bricks represent appreciable sources of radiation or radioactive waste. However, some of the demolished bricks that have been removed from service because of the aforementioned wearing process have caused portal alarms to activate at municipal disposal facilities. This has lead to the current investigation into whether there is a NORM concentrating mechanism facilitated by the presence of the slightly radioactive feed stock in the presence of the slightly radioactive refractory materials, at calcining-zone temperatures. Research conducted to date has been

46 CFR 148.04-15 - Petroleum coke, uncalcined; petroleum coke, uncalcined and calcined (mixture).

Science.gov (United States)

2010-10-01

... 46 Shipping 5 2010-10-01 2010-10-01 false Petroleum coke, uncalcined; petroleum coke, uncalcined and calcined (mixture). 148.04-15 Section 148.04-15 Shipping COAST GUARD, DEPARTMENT OF HOMELAND... Requirements for Certain Material § 148.04-15 Petroleum coke, uncalcined; petroleum coke, uncalcined and...

Significance and development of the utilization of brown coal high temperature coke in the economy of the GDR for the period 1964 to 1974

Energy Technology Data Exchange (ETDEWEB)

Klose, E.; Heschel, W.

1979-01-01

Brown coal high temperature coke production in GDR in the years since 1964 is described. In 1969 the second large brown coal high temperature coking plant, Schwarze Pumpe, went into operation, increasing the total brown coal high temperature coke production to 2 million tons annually. Utilization of the coke size classes in mm from 0-3.15, 3.15-20, 20-31.5, 31.5-45 and greater than 45 mm in the metallurgical, chemical, and energy industries as well as for household heating is shown with figures from 1964, 1970 and 1974. The increasing use of coke in households partly as briquet substitution is also shown (in 1970 42% of the coke was used in households). The substitution of black coal coke by brown coal coke in additional fields of industrial production was also further advanced. Coke production at the Schwarze Pumpe plant is scheduled to increase to 1.6 million tons by 1985 by means of the application of improved coking technologies. Investigations for future industrial solutions to the following coking problems are being conducted: processing coke fines (which make up 10 to 12% of the total produced coke) by briquetting with binders into formed coke, firing coke fines in blast furnaces and power plants, mixed briquetting of coke fines with limestone for carbide production and mixed briquetting of coke and ore fines for metallurgical purposes. (8 refs.) (In German)

Coke

Energy Technology Data Exchange (ETDEWEB)

Trumble, M J

1925-07-02

Coke is obtained from coal, lignite, peat, or wood by heating the material in a retort and distilling off the volatiles by the passage of superheated steam or hot vapors, the hot porous residue being treated with a liquid hydrocarbon and the temperature being so maintained the latter is cracked and carbon deposited on the coke. The vapors or light oils are condensed and the incondensable gases are used as fuel.

Producing metallurgic coke

Energy Technology Data Exchange (ETDEWEB)

Abe, T.; Isida, K.; Vada, Y.

1982-11-18

A mixture of power producing coals with coal briquets of varying composition is proposed for coking in horizontal chamber furnaces. The briquets are produced from petroleum coke, coal fines or semicoke, which make up less than 27 percent of the mixture to be briquetted and coals with a standard coking output of volatile substances and coals with high maximal Gizeler fluidity. The ratio of these coals in the mixture is 0.6 to 2.1 or 18 to 32 percent, respectively. Noncaking or poorly caking coals are used as the power producing coals. The hardness of the obtained coke is DJ15-30 = 90.5 to 92.7 percent.

Pace studying worldwide coke production

International Nuclear Information System (INIS)

Anon.

1993-01-01

Pace Consultants Inc., Houston, has started a multiclient study of world-wide petroleum coke production, examining environmental initiatives and eventually forecasting prices of fuel grade coke. Pace expects coker expansions, increased operating severity, and reduced cycle times to boost coke supply to more than 50 million metric tons/year in 2000, compared with 39.7 million metric tons in 1992. Increased supply and tightened environmental rules in countries consuming large amounts of petroleum coke will be the main factors affecting coke markets. The paper discusses coke quality and the Japanese market

Developing new technology of coal coking

Energy Technology Data Exchange (ETDEWEB)

Erkin, L.I.; Nefedov, P.Ya.

1981-03-01

This paper characterizes types of coke (grain size, compression strength, abrasion, porosity) used by: blast furnaces, shaft furnaces, ferroalloys and phosphorus production, and ore agglomeration. Development of formed metallurgical coke production on the basis of technologies worked out by the Eastern Research Scientific Institute for Coal Chemistry is analyzed. The following phases in the investigations are stressed: optimization of coal blends (increasing proportion of coals with poor caking properties, pressing briquets, carbonization, temperature distribution and temperature control, using heat emitted by hot coke for coal preheating (heat consumption of coking is reduced to 200 kcal/kg). On the basis of technology developed and tested by VUKhIN formed coke consisting of 60% G6 coal and 40% 2SS coal has been produced. Using the coke in blast furnaces increases furnace capacity by 5% and reduces coke consumption in a furnace by 2.6%. It is suggested that wide use of the proposed technology of formed metallurgical coke production in the Kuzbass (using coals with poor caking properties from surface mines) would increase coke production of the region to 50 Mt for a year. technology of producing formed foundry coke from: 80 to 86% anthracites, semianthracites and coals with poor caking properties, 5 to 10% coking coal, and 8% binder is evaluated. Formed foundry coke produced from the blend reduces coke consumption in a foundry by 25 to 30% and increases cast iron temperature by 20 to 50/sup 0/C. Technologies of producing coke for phosphorus industry by continuous coking of coals difficult to coke in vertical coke ovens and production of coke for ore agglomeration are also discussed. (In Russian)

Investigations on high temperature coking of lignite with the help of radionuclide techniques

International Nuclear Information System (INIS)

Koennecke, H.G.; Luther, D.; Abendroth, H.C.

1986-01-01

The time characteristics and the varying flow characteristics of fine-grained briquettes during the high temperature coking of lignite according to Rammler and Bilkenroth were studied with the help of radionuclide technique. The process parameters (tsub(V), zsub(R), etc.) refer to the different zones of the coke furnace (bunker/dryer, coker/cooler). The different time charakteristics of the coke-grain fractions formed during the BHT-process enables a correlation of the retention time and the quality factors of the coke. The results obtained would enable a better operation of the individual furnaces in the plant and offer the basis for further process developments. (orig.) [de

Relationship between coal and coke microstructure and the high temperature properties of coke. [Temperature dependence

Energy Technology Data Exchange (ETDEWEB)

Tsuyuguchi, K; Yamaji, M; Sugimoto, Y

1980-02-01

This paper considers the relationship of the properties of coke and parent coal with the high temperature properties, including reactivity, of coke. Aspects considered include coke texture and grade, and the optical reflectivity of coal and coke. (8 refs.) (In Japanese)

Split and collectorless flotation to medium coking coal fines for multi-product zero waste concept

Energy Technology Data Exchange (ETDEWEB)

Dey, Shobhana; Bhattacharyya, K.K. [Mineral Processing Division, National Metallurgical Laboratory, Jamshedpur-831007 (India)

2007-06-15

The medium coking coal fines of - 0.5 mm from Jharia coal field were taken for this investigation. The release analysis of the composite coal reveals that yield is very low at 10.0% ash, about 25% at 14% ash and 50% at 17% ash level. The low yield is caused by the presence of high ash finer fraction. The size-wise ash analysis of - 0.5 mm coal indicated that - 0.5 + 0.15 mm fraction contains less ash than - 0.15 mm fraction. Thus, the composite feed was split into - 0.5 + 0.15 mm and - 0.15 mm fractions and subjected to flotation separately. The low ash bearing fraction (- 0.5 + 0.15 mm) was subjected to two stages collectorless flotation to achieve the concentrate with 10% ash. The cleaner concentrate (18.9%) with 10% ash was recovered which has an application in metallurgical industries. The concentrate of 30.2% yield with 12.5% ash could be achieved in one stage collectorless flotation which is suitable for use in coke making as sweetener. As the - 0.15 mm fraction contains relatively high ash, collector aided flotation using sodium silicate was performed to get a concentrate of 23.6% yield with about 17% ash. The blending of this product with cleaner tail obtained from - 0.5 + 0.15 mm produces about 35.0% yield with 17% ash and that can be utilized for coke making. The reject from the two fractions can be used for conventional thermal power plant or cement industries using a 23.5% ash after one stage collector aided flotation and the final tailings produced content ash of 61.6% can be used for fluidization combustion bed (FBC). This eventually leads to complete utilization of coal. (author)

Solar thermochemical production of syngas from petroleum coke: feasibility study for injection of coke slurries

International Nuclear Information System (INIS)

Vidal, A.; Romero, M.; Kritter F; Steinfeld A

2006-01-01

The steam-gasification of pet-coke using concentrated solar radiation is proposed as a viable alternative to solar hydrogen production. Pet-coke is major solid byproduct from the processing of heavy and extra-heavy oils using delay-coking technology. This report summarizes the major accomplishments to develop a cheap and efficient feeding of petroleum coke by coke water slurries without the need of a carrier gas. The samples were Delayed coke of different grain sizes, in particular from 1,8 to 200 mm (as received). In order to analyse the flow properties of the slurries, some tests were conducted to measure the viscosity of the samples. Then, the pet-coke water slurries were injected into the reactor to study the gasification process. In these experiments, some operational parameters were: molar ratio from 2 to 3 (water/coke), temperature up to 1000 C, residence times from 5 to 9 s. In those conditions, the coke is converted primarily to CO, H 2 , CO 2 and small amounts of methane. Concentration of outlet gases of about 30-50 of H 2 ; 15-20 of CO, 10-15 CO 2 , 1-2% CH 4 were obtained with X coke ∼ 65 to 85%. (authors)

Carbon dioxide emission in hydrogen production technology from coke oven gas with life cycle approach

Directory of Open Access Journals (Sweden)

Burmistrz Piotr

2016-01-01

Full Text Available The analysis of Carbon Footprint (CF for technology of hydrogen production from cleaned coke oven gas was performed. On the basis of real data and simulation calculations of the production process of hydrogen from coke gas, emission indicators of carbon dioxide (CF were calculated. These indicators are associated with net production of electricity and thermal energy and direct emission of carbon dioxide throughout a whole product life cycle. Product life cycle includes: coal extraction and its transportation to a coking plant, the process of coking coal, purification and reforming of coke oven gas, carbon capture and storage. The values were related to 1 Mg of coking blend and to 1 Mg of the hydrogen produced. The calculation is based on the configuration of hydrogen production from coke oven gas for coking technology available on a commercial scale that uses a technology of coke dry quenching (CDQ. The calculations were made using ChemCAD v.6.0.2 simulator for a steady state of technological process. The analysis of carbon footprint was conducted in accordance with the Life Cycle Assessment (LCA.

China's coke industry: Recent policies, technology shift, and implication for energy and the environment

International Nuclear Information System (INIS)

Huo, Hong; Lei, Yu; Zhang, Qiang; Zhao, Lijian; He, Kebin

2012-01-01

China is the largest coke producer in the world, accounting for over 60% of the world coke production, which makes the coke industry in China a significant coal consumer and air pollutant emitter. Recently, China has taken a series of measures to improve energy efficiency and reduce emissions from the coke industry, including eliminating old and low energy-efficiency coking technologies, promoting advanced technologies, and strengthening energy and environmental requirements on coking processes. As a consequence, China's coke industry is experiencing an unprecedented technology shift, which was characterized by the elimination of old, inefficient, and polluting indigenous ovens and small machinery ones within 10 years. This study examines the policies and the prompt technology shift in China's coke industry, as well as the associated energy and environmental effects, and discusses the implications with respect to the development of the coke industry in China towards a more efficient and clean future. As China sets stricter requirements on energy efficiency and the ambient environment, a more significant change focusing on technologies of energy saving and emission reduction is urgently needed at present. Those mature technologies, including coke dry quenching, coke oven gas recycle, fine particle removal, etc., should be enforced in the near future. - Highlights: ► With 60% of world coke output, China's coke making has big energy/pollution issues. ► Actions were taken to improve energy and environmental performance of coke plants. ► China's coke industry is experiencing an unprecedented technology shift. ► Another shift, focusing on technologies of energy and emission saving, is needed. ► More measurement studies on coking emissions are needed given the importance.

Basic characteristics of new shape formed coke in burden distribution; Shingata seikei cokes no sonyu bunpu tokusei

Energy Technology Data Exchange (ETDEWEB)

Ichida, M; Yamamoto, T; Komaki, I; Oda, H; Matsunaga, S; Matsuzaki, S; Deno, T; Konno, N [Nippon Steel Corp., Tokyo (Japan)

1996-12-01

Basic characteristics in burden distribution and charging pattern of new shape formed coke developed in order to improve the properties of small size and low void fraction that pillow-type formed coke h s were conducted by 1/3 scale charging model and mathematical model of blast furnace. Basic characteristics, those are, inclination angle, coke-collapse and trajectory of new shape formed coke are almost the same as those of conventional coke. In the case of wall charging of new shape formed coke, until 60% of total charged coke, new shape formed coke is able to be charged without it`s rolling to the center. It is possible to apply RABIT model to new shape formed coke charging without it`s major modification. In the case of new shape formed coke wall charging, the fluctuation in furnace is supposed to be smaller than that in the case of pillow-type formed coke wall charging. Moreover, it`s center charging is supposed to be applied to actual blast furnace. More accurate estimation of in-furnace phenomena by mathematical model considering coke reactivity, is a subject to be worked out in future. 11 refs., 9 figs., 5 tabs.

Cooperation with COMECON members in coke chemistry

Energy Technology Data Exchange (ETDEWEB)

Medricky. Z

1987-05-01

Discusses activities of the coking industry division of the standing committee for iron metallurgy of the COMECON. The following cooperation fields are analyzed: raw material basis for coking industry, coal charge preparation and methods for reducing proportion of coking coal in a coal charge (heat treatments, formed coke processes, partial briquetting, pelletizing, increasing coking temperature, packing etc.), coking technology, coke quenching, screening, chemical processing of coal gas, environmental protection in the coking industry, environmental effects of coking, pitch coke production, methods for increasing labor productivity. Research programs coordinated by member countries are reviewed. Programs in which Czechoslovakia participates are discussed.

Repair of walls of coke ovens with a volume of 41. 6 m/sup 3/

Energy Technology Data Exchange (ETDEWEB)

Pyatnitsa, V.A.; Bulyga, N.I.

1988-11-01

Discusses repair of coke oven walls and the heating system of a battery with coke ovens 7.0 m high in the Avdeevka plant. The following problems are evaluated: types of wall deformation and wear, distribution of wear zones, zones with maximum wear, coke oven repair without cooling and with cooling, repair of cracks in oven walls, effects of wall temperature (in schemes without cooling) on repair, behavior of walls in zones of temperature differences, sequence of repair operations, repair of heating channels, specific problems of wall repair at the machine side and at the pusher side of a coke oven battery, methods for reducing repair time, materials used for coke oven repair.

Coking oven for continuous coke production

Energy Technology Data Exchange (ETDEWEB)

Vabrousek, R

1979-07-15

The coking oven has a vertical rectangular chamber with lateral heating walls to which heat exchangers are attached. The roof from the face of the chamber is a hermetic chute, whose vertical walls are connected to the lateral walls of the chamber and which has the feed conveyor with an unloading and evening device; to the upper wall of which a hermetic loading funnel for coal is attached and a lead-off for gas. The bottom of the chamber consists of segmented locks that are taken up by the hermetic chute. The chute's vertical walls are connected to the vertical walls of the chamber and its horizontal wall has a hermetic unloading funnel with a conveyor for coke removal. Height and width of the chamber are similar to standard chambers; their length reaches 100 to 200 m and longer. Length depends on coke preparation time and speed with which the unloading device can transfer coal. For normal operation, the conveyor belt must function properly in conjunction with the unloading device and segmented locks that form the bottom of the chamber.

Intensifying waste water clarification in heavy and mining industries for sanitation of rivers in the Katowice district

Energy Technology Data Exchange (ETDEWEB)

Paluch, J.; Twardowska, I.

1976-01-01

This article presents a detailed account of the state of water pollution in the main and tributary rivers of the heavily populated and industrialized district of Katowice, Poland: Results of surveys in the years 1969 to 1972 are given. Several tables and maps show the degree of water pollution in rivers, the amount to which the values exceed pollution standards, percentage of treated and untreated industrial waste water entering the rivers, the classification of river sections according to their content of suspensions, phenols and salt. Further figures show the effectiveness of water cleaning flocculating agents and of waste water treatment at coking plants. Black coal mining and processing contributes the greater part to pollution of the rivers. Only 54% of mining industry waste water is cleaned mechanically and 3% chemically. The amount of 3,300 t/d of chlorite and sulfate salts is led into the rivers primarily from the Rybnik coal mining area. The clarification of waste water resulting from hydraulic stowing and from flotation processes is described as most problematic. Research efforts are being made at economic desalination and suspension flocculation. In the coking industry waste water is treated in 88% of the plants, but dephenolization takes place in only 50% of the plants. (29 refs.) (In German)

Waste incinerating plant

Energy Technology Data Exchange (ETDEWEB)

1972-12-01

This plant is provided with a NKK-Ferunst type reciprocating stage fire lattice which has a good ventilating effect and a proper stirring and loosening effect, achieving a high combustion rate, and has also a gas flow system by which gas can flow in the reverse direction to adjust its flow for seasonal variations in the quality of waste. Also, a room in which the exhaust gas is mixed is provided in this plant as a help for the complete neutralization and combustion of acid gas such as hydrogen chloride and imperfect combustion gas from plastic waste contained in wastes. In this system, waste can accept a sufficient radiant heat from the combustion gas, the furnace wall, and the ceiling; even on the post combustion fire lattice the ashes are given heat enough to complete the post combustion, so that it can be completely reduced to ashes. For these reasons, this type of incinerator is suitable for the combustion of low-calorie wastes such as city wastes. The harmful gases resulting from the combustion of wastes are treated completely by desulfurization equipment which can remove the oxides of sulfur. This type of plant also can dispose of a wide variety of wastes, and is available in several capacities from 30 tons per 8 hr to 1,200 tons per 24 hr.

The year-book of the Coke Oven Managers' Association 2008

Energy Technology Data Exchange (ETDEWEB)

NONE

2008-07-01

The 89th volume of the Year Book outlines activities of the Coke Oven Managers' Association throughout 2008 and reproduces transactions presented to the industry through its various sections. It includes lists of Council and Committee members and representation on committees and past presidents, and a full list of members. Reports of Council 2006-7 and of the annual general meeting 2007 are included. The Presidential address by A. Moore is about his experiences at Redcar Coke Ovens. Carbonisation and briquetting works in the United Kingdom, Koppers carbon materials and chemical works in the UK and Europe, European coking plants, their addresses and managers are listed. Six transactions are abstracted separately on the Coal Abstracts database.

Results of tuyere coke sampling with regard to application of appropriate coke strength after reaction (CSR for a blast furnace

Directory of Open Access Journals (Sweden)

Shiau J-S.

2017-01-01

Full Text Available Raising pulverized coal injection (PCI will decrease coke rate, but increase the residence time of coke and abrasion in the blast furnace (BF. Thus, insufficient coke strength will generate more coke fines in the lower BF and result in lower permeability and production of hot metal (HM. For understanding the behavior of coke at various HM productivities, a tuyere coke sampler was used to collect the coke samples for measuring the coke strength. Firstly, the difference of sampled coke under the conditions of various HM productivities was explored. Secondly, the BF operating conditions and causes of generating more coke fines was correlated by testing the coke reaction rate after reaction. Finally, according to the above analysis results, the relative regression equations had been obtained for sampling coke properties, BF operation conditions and BF permeability. Furthermore, the coke strength after reaction (CSR quantitative target and its online system at various blast conditions were set to provide some reference for coke and HM production.

Assessment of PAH-exposure among coke oven workers

Energy Technology Data Exchange (ETDEWEB)

Vahakangas, K. [and others] [Oulu University, Oulu (Finland)

1992-12-31

Levels of BaP diol epoxide - DNA adducts in urine and blood were monitored for workers at the Raahe coking plant, Finland, and other relevant information was collected. All adduct values were low, but oven battery workers had slightly higher values than matched controls. Antibodies to these adducts increased somewhat after work at the plant started, no differences between smokers and non-smokers were found.

Municipal solid waste disposal by using metallurgical technologies and equipments

Energy Technology Data Exchange (ETDEWEB)

Cai, Jiuju; Sun, Wenqiang [State Environmental Protection Key Laboratory of Eco-industry, Institute of Thermal and Environmental Engineering, Northeastern University, Shenyang 110819 (China)

2012-07-01

Pyrolysis of municipal solid waste can take full advantage of energy and resource and avoid producing hazardous material during this period. In combination with mature metallurgical technologies of coking by coke oven, regenerative flame furnace technology and melting by electric arc furnace, technologies of regenerative fixed bed pyrolysis technology for household waste, co-coking technology for waste plastic and blend coal, and incineration ash melting technology by electric arc technology for medical waste were respectively developed to improve current unsatisfied sorting status of waste. The investigation results of laboratory experiments, semi-industrial experiments and industrial experiments as well as their economic benefits and environmental benefits for related technologies were separately presented.

Substitutes for metallurgical coke in pyrometallurgical processes

Energy Technology Data Exchange (ETDEWEB)

Koshkarov, V.Ya.

1982-08-01

A briquetting process using sulphurous petroleum coke and a bituminous binder is described. The characteristics of briquettes made of petroleum coke, blends of coal and petroleum coke, and coal and metallurgical coke are compared. The prospect of replacing 25 to 50% of the metallurgical coke used in lime kilns with non-calcined petroleum coke briquettes is described. (4 refs.)

Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process

Science.gov (United States)

Shi, Junjun; Guan, Jianyu; Guo, Dawei; Zhang, Jiushun; France, Liam John; Wang, Lefu; Li, Xuehui

2016-06-01

Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed during TPD for the first time, and they arise from decomposition of aliphatic carbons and aromatic carbons. Three types of N species, pyrrolic N, pyridinic N and quaternary N are identified in the FCC coke, the former one is unstable and tends to be decomposed into pyridinic and quaternary N. Mechanisms of NO, CO and CO2 evolution during TPD are proposed and lattice oxygen is suggested to be an important oxygen resource. Regeneration process indicates that coke-C tends to preferentially oxidise compared with coke-N. Hence, new technology for promoting nitrogen-containing compounds conversion will benefit the in-situ reduction of NO by CO during FCC regeneration.

Process and plant for obtaining generator gas from mainly treated non-fossil waste products. Verfahren und Anlage zur Gewinnung von Generatorgas aus vorwiegend aufbereiteten nicht fossilen Abfallprodukten

Energy Technology Data Exchange (ETDEWEB)

Schmid, K

1984-05-03

A processs for obtaining generator gas from mainly non-fossil waste materials proposes first that these waste products should be changed to pyrolysis coke after being mechanically reduced in size and only then should this coke be introduced into the actual gas reactor. In order to carry out this process, a pyrolysis tube separate from the reactor is used, with a gas-heated double jacket, gas guide pockets in the tube crossection and a mechanical infeed device for the granulate to be pyrolysed in the form of a push rod with a connected supply duct and a guide part for the pyrolysis coke into the reactor.

Thermal expansion of coking coals

Energy Technology Data Exchange (ETDEWEB)

Orlik, M.; Klimek, J. (Vyzkumny a Zkusebni Ustav Nova Hut, Ostrava (Czechoslovakia))

1992-12-01

Analyzes expansion of coal mixtures in coke ovens during coking. Methods for measuring coal expansion on both a laboratory and pilot plant scale are comparatively evaluated. The method, developed, tested and patented in Poland by the Institute for Chemical Coal Processing in Zabrze (Polish standard PN-73/G-04522), is discussed. A laboratory device developed by the Institute for measuring coal expansion is characterized. Expansion of black coal from 10 underground mines in the Ostrava-Karvina coal district and from 9 coal mines in the Upper Silesia basin in Poland is comparatively evaluated. Investigations show that coal expansion reaches a maximum for coal types with a volatile matter ranging from 20 to 25%. With increasing volatile matter in coal, its expansion decreases. Coal expansion increases with increasing swelling index. Coal expansion corresponds with coal dilatation. With increasing coal density its expansion increases. Coal mixtures should be selected in such a way that their expansion does not cause a pressure exceeding 40 MPa. 11 refs.

Hanford Waste Vitrification Plant Dangerous Waste Permit Application

International Nuclear Information System (INIS)

1991-10-01

The Hanford Facility currently stores mixed waste, resulting from various processing operations, in underground storage tanks. The Hanford Waste Vitrification Plant will be constructed and operated to process the high-activity fraction of mixed waste stored in these underground tanks. The Hanford Waste Vitrification Plant will solidify pretreated tank waste into a glass product that will be packaged for disposal in a national repository. This Vitrification Plant Dangerous Waste Permit Application, Revision 2, consists of both a Part A and a Part B permit application. An explanation of the Part A revisions, including Revision 4 submitted with this application, is provided at the beginning of the Part A section. The Part B consists of 15 chapters addressing the organization and content of the Part B Checklist prepared by the Washington State Department of Ecology (Ecology 1987)

Emission characteristics and size distribution of polycyclic aromatic hydrocarbons from coke production in China

Science.gov (United States)

Mu, Ling; Peng, Lin; Liu, Xiaofeng; He, Qiusheng; Bai, Huiling; Yan, Yulong; Li, Yinghui

2017-11-01

Coking is regarded as a major source of atmospheric polycyclic aromatic hydrocarbons (PAHs), but few researches have been conducted on the emission characteristics of PAHs from coke production. In this study, emissions of size-segregated particulate matter (PM) and particle-bound PAHs emitted from charging of coal (CC) and pushing of coke (PC) in four typical coke plants were determined. The emission factors on average, sums of CC and PC, were 4.65 mg/kg, 5.96 mg/kg, 19.18 μg/kg and 20.69 μg/kg of coal charged for PM2.1 (≤ 2.1 μm), PM, PAHs in PM2.1 and total-PAHs, respectively. PM and PAHs emission from plants using stamp charging were significantly more than those using top charging. The profile of PAHs in PM with size ≤ 1.4 μm (PM1.4) emitted from CC process were similar with that from PC, however, it revealed obviously different tendency for PAHs in PM with size > 1.4 μm, indicating the different formation mechanism for coarse particles emitted from CC and PC. Size distributions of PM and PAHs indicated that they were primarily connected with PM1.4, and the contributions of PM1.4 to PM and PAHs emitted from the plants using stamp charging were higher than those using top charging. Some improved technology in air-pollution control devices should be considered in coke production in future based on the considerable impacts of PM1.4 and PAHs on human health and ambient air quality.

The year-book of the Coke Oven Managers' Association 2006

Energy Technology Data Exchange (ETDEWEB)

NONE

2006-07-01

The 87th volume of the Year Book outlines activities of the Coke Oven Managers' Association throughout 2006 and reproduces transactions presented to the industry through its various sections. It includes lists of Council and Committee members and representation on committees and past presidents, and a full list of members. Reports of Council 2004-5 and of the annual general meeting 2005 are included. The Presidential address by M. Gore is on the last five years of Monckton Coke and Chemical Company. Carbonisation and briquetting works in the United Kingdom, Koppers carbon materials and chemical works in the UK and Europe, European coking plants, their addresses and managers are listed. Seven transactions are abstracted separately on the Coal Abstracts database.

Experimental and numerical investigations of coke descending behavior in a coke dry quenching cooling shaft

International Nuclear Information System (INIS)

Feng Yanhui; Zhang Xinxin; Yu Quan; Shi Zhongyin; Liu Zhicheng; Zhang Hu; Liu Huafei

2008-01-01

A viscous flow model based on the Navier-Stokes equation is developed to describe coke descending behavior in the 1/7-scaled-down experimental setup of an actual 75 t/h cooling shaft. It is found that the internal friction due to cokes viscosity significantly influences the descending behavior of cokes in the lower part of the shaft, while the external wall friction dominates the sluggish flow of the cokes in the shaft. An asymptotic friction coefficient expression is proposed for granular mixtures flowing along the shaft wall modified from normal wall tress, and the concept of bulk solid viscosity is introduced to describe the internal friction between coke particles. The results simulated by the present model are compared with those by the potential flow and the kinematic model without friction. The viscous flow model is quite good to simulate the bulk coke flow as the physically important frictions are engaged

Incorporation of petroleum coke into red ceramic; Incorporacao de coque de petroleo em ceramica vermelha

Energy Technology Data Exchange (ETDEWEB)

Freitas, L.A. de; Monteiro, S.N.; Sanchez, R.; Vieira, C.M.F. [Laboratorio de Materiais Avancados - LAMAV, Universidade Estadual do Norte Fluminense Darcy Ribeiro - UENF, Campos dos Goytacazes, RJ (Brazil)], e-mails: sanchez@uenf.br, vieira@uenf.br

2011-04-15

This work has as its objective the evaluation of the effect of incorporation of petroleum coke in the physical and mechanical properties of red ceramic. Compositions were prepared with 0%, 1%, 2% and 4 wt.% of petroleum coke incorporated into a kaolinitic clayey body. Rectangular specimens were formed by extrusion to fire at 850 deg C and 1050 deg C. The determined physical and mechanical properties were flexural rupture strength and water absorption. The microstructure of the fired ceramics was evaluated by optical microscopy. The results show that the petroleum coke waste can significantly contribute to reduce the energy consumption during the firing stage. However, incorporations must be done in amounts around 1 wt.% to avoid deleterious effect on the water absorption of the ceramic. (author)

Waste treatment plant

International Nuclear Information System (INIS)

Adesanmi, C.A

2009-01-01

Waste Treatment Plant (WTP) is designed to provide appropriate systems for processing, immobilization and storage of low and medium radioactive waste arising from the operation of the research facilities of the Nuclear Technology Centre (NTC). It will serve as central collection station processing active waste generated through application of radionuclide in science, medicine and industry in the country. WTP building and structures will house the main waste processing systems and supporting facilities. All facilities will be interconnected. The interim storage building for processed waste drums will be located separately nearby. The separate interim storage building is located near the waste treatment building. Considering the low radiation level of the waste, storage building is large with no solid partitioning walls and with no services or extra facilities other than lighting and smoke alarm sensors. The building will be designed such that drums(200-1)are stacked 3 units high using handling by fork lift truck. To prevent radiation exposure to on-site personnel, the interim storage building will be erected apart from waste treatment plant or other buildings. The interim storage building will also be ready for buffer storage of unconditioned waste waiting for processing or decay and for storage material from the WTP

Determination of electrical resistivity of dry coke beds

Energy Technology Data Exchange (ETDEWEB)

Eidem, P.A.; Tangstad, M.; Bakken, J.A. [NTNU, Trondheim (Norway)

2008-02-15

The electrical resistivity of the coke bed is of great importance when producing FeMn, SiMn, and FeCr in a submerged arc furnace. In these processes, a coke bed is situated below and around the electrode tip and consists of metallurgical coke, slag, gas, and metal droplets. Since the basic mechanisms determining the electrical resistivity of a coke bed is not yet fully understood, this investigation is focused on the resistivity of dry coke beds consisting of different carbonaceous materials, i.e., coke beds containing no slag or metal. A method that reliably compares the electrical bulk resistivity of different metallurgical cokes at 1500{sup o} C to 1600{sup o}C is developed. The apparatus is dimensioned for industrial sized materials, and the electrical resistivity of anthracite, charcoal, petroleum coke, and metallurgical coke has been measured. The resistivity at high temperatures of the Magnitogorsk coke, which has the highest resistivity of the metallurgical cokes investigated, is twice the resistivity of the Corus coke, which has the lowest electrical resistivity. Zdzieszowice and SSAB coke sort in between with decreasing resistivities in the respective order. The electrical resistivity of anthracite, charcoal, and petroleum coke is generally higher than the resistivity of the metallurgical cokes, ranging from about two to about eight times the resistivity of the Corus coke at 1450{sup o}C. The general trend is that the bulk resistivity of carbon materials decreases with increasing temperature and increasing particle size.

Scientific research in the area of coking and coking by-products (based on material from the All-Union Coordinating Conference)

Energy Technology Data Exchange (ETDEWEB)

Rydkevich, M.I.; Tselik, M.P.; Belkina, T.V.

1985-06-01

Subjects covered in the all-union coordinating conference on coking and chemical by-products of coking, which took place on 13-15 July 1984, are discussed. One hundred forty eight on-going and new research themes accepted as research projects for 1985-86 were discussed. Areas of research include coals from the eastern deposits and Pechora basin as raw materials for coking; coals from the southern deposits as coking raw materials; technology of coal preparation for coking; technology for producing blast furnace coke and methods of assessing its quality; technology for producing other kinds of coke and carbon graphite materials; methods for extraction processing and producing chemical products from coking.

Partial briquetting of coal charges as a means of utilizing lower-grade coal for coke making

Energy Technology Data Exchange (ETDEWEB)

Pieters, B.J. (Iscor Limited, Newcastle (South Africa))

1991-08-01

The paper describes the difficulties experienced with inferior coking coals as Iscor began using larger blast furnaces for the production of liquid iron. Research conducted at Iscor from 1977 to 1979 showed that benefits could be gained from the use of partially briquetted charges, and it was decided to install briquetting plants at the Vanderbijlpark and Newcastle Works. Details are given of the latter plant, which was supplied by a consortium consisting of Voest Alpine, Didier Engineering, and Sumitomo Metal Industries. Sumitomo also supplied information on the optimization of coke quality along the lines of their Sumicoal System. The results have been a marked improvement in coke quality, much better blast-furnace operation, and increased productivity. 11 figs., 3 tabs.

The year-book of the Coke Oven Managers' Association 2007

Energy Technology Data Exchange (ETDEWEB)

NONE

2007-07-01

The 88th volume of the Year Book outlines activities of the Coke Oven Managers' Association throughout 2007 and reproduces transactions presented to the industry through its various sections. It includes lists of Council and committee members and representation on committees and past presidents, and a full list of members. Reports of Council 2005-6 and of the annual general meeting 2005 are included. The Presidential address by R.G.W. Sargent looks at the situation faced by coke oven managers through the decades with some predictions for the future. Carbonisation and briquetting works in the United Kingdom, Koppers carbon materials and chemical works in the UK and Europe, European coking plants, their addresses and managers are listed. Nine transactions are abstracted separately on the Coal Abstracts database.

Coke quality requirements in POSCO

Energy Technology Data Exchange (ETDEWEB)

Song, J.; Yi, J.; Wang, H. [POSCO (Republic of Korea). Cokemaking Dept.

2001-07-01

The 26 overheads describes coke quality requirements in POSCO, Republic of Korea. It is concluded that it is necessary to develop new coal and to prompt technical development in order to produce high quality coke. To improve coke quality. Posco had applied DMAIC (define, measurement, analysis, improvement, control) technique which is part of Six-Sigma activity.

Cocaine (Coke, Crack) Facts

Science.gov (United States)

... That People Abuse » Cocaine (Coke, Crack) Facts Cocaine (Coke, Crack) Facts Listen Cocaine is a white ... 69 KB) "My life was built around getting cocaine and getting high." ©istock.com/ Marjot Stacey is ...

Isotopic ratio based source apportionment of children's blood lead around coking plant area.

Science.gov (United States)

Cao, Suzhen; Duan, Xiaoli; Zhao, Xiuge; Wang, Beibei; Ma, Jin; Fan, Delong; Sun, Chengye; He, Bin; Wei, Fusheng; Jiang, Guibin

2014-12-01

Lead exposure in the environment is a major hazard affecting human health, particularly for children. The blood lead levels in the local children living around the largest coking area in China were measured, and the source of blood lead and the main pathways of lead exposure were investigated based on lead isotopic ratios ((207)Pb/(206)Pb and (208)Pb/(206)Pb) in blood and in a variety of media, including food, airborne particulate matter, soil, dust and drinking water. The children's blood lead level was 5.25 (1.59 to 34.36 as range) μg dL(-1), lower than the threshold in the current criteria of China defined by the US Centers for Disease Control (10 μg dL(-1)). The isotopic ratios in the blood were 2.111±0.018 for (208)Pb/(206)Pb and 0.864±0.005 for (207)Pb/(206)Pb, similar to those of vegetables, wheat, drinking water, airborne particulate matter, but different from those of vehicle emission and soil/dust, suggesting that the formers were the main pathway of lead exposure among the children. The exposure pathway analysis based on the isotopic ratios and the human health risk assessment showed that dietary intake of food and drinking water contributed 93.67% of total exposed lead. The study further indicated that the coal used in the coking plant is the dominant pollution source of lead in children's blood. Copyright © 2014 Elsevier Ltd. All rights reserved.

The impact of liquid-liquid-vapour phase behaviour on coke formation from model coke precusors

Energy Technology Data Exchange (ETDEWEB)

Minicucci, D.; Shaw, J.M. [Univ. of Toronto, Dept. of Chemical Engineering and Applied Chemistry, Toronto, ON (Canada)

2000-08-01

Catalysts used in the hydroprocessing of heavy feedstocks deactivate due to coke deposition. Although the mechanism for coke formation is not fully understood, condensation reactions of polynuclear aromatic compounds present in the feeds are a key aspect. The effect of coke deposition on catalyst performance is typically modelled using accelerated aging agents comprising model coke precursors. Mixtures employed in such studies polynuclear aromatic compounds such as anthracene as the coke precursor, and long chain alkanes such as hexadecane as a diluent. We show in this paper that binary and pseudo binary mixtures of polynuclear aromatic compounds and n-alkanes present TYPE II, TYPE IV, or TYPE III phase behaviour according to the van Konynenburg and Scott (1980) phase projection nomenclature, Incubation periods and the apparent autocatalytic effects associated with coke deposition in such systems are explained through a combination of high temperature phase equilibrium experiments and computations with the model systems n-alkane + anthracene + hydrogen, n-alkane + pyrene + hydrogen, and n-alkane + dibenzo[a,k]chrysene + hydrogen. (au)

Hygiene of work in main shops of modern coking by-product industry. [USSR

Energy Technology Data Exchange (ETDEWEB)

Kapitul' skii, V B

1984-07-01

The hygiene of working conditions is evaluated and compared for coking by-product industry shops using modern technology and machines with those using obsolete equipment and methods. Most basic factors in contamination of atmosphere of coking, pitch-coking and metal-refining shops are coal and coke dust, carbon monoxide and polycyclic aromatic hydrocarbons, especially carcinogenic benzpyrene. Contamination of air of working zone is determined by details of technology: periodicity or continuity of industrial processes, use of improved equipment for smokeless injection of charge into stoves and of hermetic pipes to remove gas with hydraulically operated caps, position of machines in shops and in coal tar distillation removal of carcinogenic benzpyrene by sulfonation and aeration. In modernized shops of coking by-product industry, illness and loss of work capacity are significantly lower than in plants using obsolete methods and equipment. Measures are presented for hygienic improvement of working conditions; both methods to further increase efficiency of technological processes and methods to protect individual worker on job such as use of respirators, protective clothing, plexiglass shields, shampoos and skin creams. 14 references.

A Study on the Waste Water Treatment Technology for Steel Industry: Recycle And Reuse.

OpenAIRE

Sanjeev Kumar Sinha; Vikas Kumar Sinha; Samir Kr. Pandey; Anup Tiwari

2016-01-01

The steel industry is one of the most important and vital Industry of the present and the future. It is the asset of a nation. Steel plants use a tremendous amount of water for waste transfer, cooling and dust control. The steel plants have sintering mills, coke plants, blast furnaces, chemical byproducts and chemical processes, water cooled rolls, pumps, extrusion experiment, transfer lines for sludges and slurries. All these plants use a tremendous amount of water to cool the pr...

Prospects for the use of coke-works gas in the manufacture of sponge iron

Energy Technology Data Exchange (ETDEWEB)

Hatarascu, O; Orosz, R

1978-01-01

This paper presents the results of tests conducted in the laboratory of the I.C.E.M. (National research institute for the mining industry) at Hunedoara; these investigations dealt with the reduction of iron oxide by gas from coking plant. The direct application of coke-works gas for the direct reduction of iron ores represents a new move towards the profitable utilization of this gas which, owing to its high content of hydrogen and CH4, can be transformed into CO and H2 using current conversion techniques (water-vapour or CO2 methods). The article presents a diagram of the 'MIDREX' reduction plant. Also includes a study of the variation in the specific coke-gas consumption as a function of the reducer-gas throughput together with an analysis of the reduction process for recycled and regenerated gas at a temperature of 900 C.

Polyphasic bacterial community analysis of an aerobic activated sludge removing phenols and thiocyanate from coke plant effluent

Energy Technology Data Exchange (ETDEWEB)

Felfoldi, T.; Szekely, A.J.; Goral, R.; Barkacs, K.; Scheirich, G.; Andras, J.; Racz, A.; Marialigeti, K. [Eotvos Lorand University, Budapest (Hungary). Dept. of Microbiology

2010-05-15

Biological purification processes are effective tools in the treatment of hazardous wastes such as toxic compounds produced in coal coking. In this study, the microbial community of a lab-scale activated sludge system treating coking effluent was assessed by cultivation-based (strain isolation and identification, biodegradation tests) and culture-independent techniques (sequence-aided T-RFLP, taxon-specific PCR). The results of the applied polyphasic approach showed a simple microbial community dominated by easily culturable heterotrophic bacteria. Comamonas badia was identified as the key microbe of the system, since it was the predominant member of the bacterial community, and its phenol degradation capacity was also proved. Metabolism of phenol, even at elevated concentrations (up to 1500 mg/L), was also presented for many other dominant (Pseudomonas, Rhodanobacter, Oligella) and minor (Alcaligenes, Castellaniella, Microbacterium) groups, while some activated sludge bacteria (Sphingomonas, Rhodopseudomonas) did not tolerate it even in lower concentrations (250 mg/L). In some cases, closely related strains showed different tolerance and degradation properties. Members of the genus Thiobacillus were detected in the activated sludge, and were supposedly responsible for the intensive thiocyanate biodegradation observed in the system. Additionally, some identified bacteria (e.g. C. badia and the Ottowia-related strains) might also have had a significant impact on the structure of the activated sludge due to their floc-forming abilities.

Behavior of coke in large blast furnaces

Energy Technology Data Exchange (ETDEWEB)

Nakamura, N

1978-01-01

Three blast furnaces were quenched in operation and the contents were examined; the temperature distribution was also measured, using Tempil pellets. The furnaces examined included a low productivity one, which was examined to see what was wrong. Changes in the quality of coke as it descends in the furnace, and coke behavior in the raceway and hearth are reported. The functions required of coke, and the effects of poor coke quality, are explained, together with the coke quality required in large blast furnaces. A theoretical study of the role of coke in large blast furnaces is included.

A new method for manufacturing ICEM form coke and its coking in slanted furnaces. Part II. Obtaining ICEM form coke in slanted furnaces

Energy Technology Data Exchange (ETDEWEB)

Barbu, I; Coposescu, V; Kost, J; Manolescu, A; Michailidis, N; Solceriu, R; Stoicoi, A

1978-01-01

An engineering scheme of the process is given, together with the characteristics of the chamber furnaces with an inclined hearth and the quality of the coke obtained in the industrial assembly at a gas factory. The assembly consists of 56 chamber furnaces with a volume up to 10 cubic meters. The height of the chambers is 4000 mm on one side and 4295 mm on the other with a length of 7500 mm and a width of 360-480 mm. The heating temperature is 1200/sup 0/, and the coking time is 22-24 hours. The annual production of the batteries for metallurgical coke is 90 thousand tons, and the average strength of the coke is M40-66.0; M10-15.51.

The effect of high and low dissolved oxygen on the toxicity of oil sands coke and its leachate to Chironomus tentans

International Nuclear Information System (INIS)

Squires, A.J.; Liber, K.

2003-01-01

A study was conducted to assess the effect of low dissolved oxygen on the long-term leaching potential of the toxic constituents found in coke. Coke is one of the waste products produced during the oil sand upgrading process used at Syncrude Canada Ltd. and Suncor Energy Inc. Coke is contaminated by metals and organic compounds which can leach into the environment. In this study, coke from both companies was exposed to reconstituted water and high dissolved oxygen for a period of 30 days, during which time the overlying water containing the leachate and the coke pore-water was chemically analyzed. The benthic macroinvertebrate, Chironomus tentans, was exposed to the aged coke and the overlying leachate after the 30 day period. The study did not reveal any major difference in the survival or growth between the dissolved oxygen treatments or any of the leachate treatments. The macroinvertebrate in the aged Syncrude grew significantly while the Suncor coke strongly inhibited both survival and growth of the macroinvertebrate. The study demonstrates that coke has the potential to negatively affect benthic organisms if it is used uncovered in an aquatic reclamation effort

Research and development in production of special coke types

Energy Technology Data Exchange (ETDEWEB)

Nefedov, P.Ya.; Unterberger, O.G.; Strakhov, V.M. (Vostochnyi Nauchno-Issledovatel' skii Uglekhimicheskii Institut (USSR))

1991-03-01

Discusses methods for increasing quality of foundry coke and quality of special coke types used in non-ferrous metallurgy. Types of coal from various coal basins for production of foundry coke, types of petroleum and coal-derived additives improving caking and coking properties of the standard coal mixtures and effects of partial coal charge briquetting are discussed. Three types of partial coal charge briquetting are comparatively evaluated: continuous coking of the briquetted mixtures of weakly caking lean coal types, anthracites and coking coal mixed with thermosoftening binders; continuous coking of identical mixtures briquetted with non-thermosoftening binders; coking coke dust mixed with thermoreactive binders and briquetted at 200-300 C. Coking conditions, the final coking temperature, binder consumption rates, dimensions of coal briquets, ash content, sulfur content and coke mechanical properties (compression strength and wear) are comparatively evaluated.

Production of blast furnace coke from soft brown coal

Energy Technology Data Exchange (ETDEWEB)

Scholz, G.; Wundes, H.; Schkommodau, F.; Zinke, H.-G. (VEB Gaskombinat Schwarze Pumpe (German Democratic Republic))

1988-01-01

Reviews experimental production and utilization of high quality brown coal coke in the GDR during 1985 and 1986. The technology of briquetting and coking brown coal dust is described; the superior parameters of produced coke quality are listed in comparison to those of regular industrial coke made from brown and black coal. Dust emission from high quality brown coal coke was suppressed by coke surface treatment with dispersion foam. About 4,200 t of this coke were employed in black coal coke substitution tests in a blast furnace. Substitution rate was 11%, blast furnace operation was positive, a substitution factor of 0.7 t black coal coke per 1 t of brown coal coke was calculated. Technology development of high quality brown coal coke production is regarded as complete; blast furnace coke utilization, however, requires further study. 8 refs.

Urinary 1-hydroxypyrene concentrations in Chinese coke oven workers relative to job category, respirator usage, and cigarette smoking

Energy Technology Data Exchange (ETDEWEB)

Bo Chen; Yunping Hu; Lixing Zheng; Qiangyi Wang; Yuanfen Zhou; Taiyi Jin [Fudan University, Shanghai (China). School of Public Health

2007-09-15

1-Hydroxypyrene (1-OHP) is a biomarker of recent exposure to polycyclic aromatic hydrocarbons (PAHs). We investigated whether urinary 1-OHP concentrations in Chinese coke oven workers (COWs) are modulated by job category, respirator usage, and cigarette smoking. The present cross-sectional study measured urinary 1-OHP concentrations in 197 COWs from Coking plant I and 250 COWs from Coking plant II, as well as 220 unexposed referents from Control plant I and 56 referents from Control plant II. Urinary 1-OHP concentrations (geometric mean, {mu}mol/mol creatinine) were 5.18 and 4.21 in workers from Coking plants I and II, respectively. The highest 1-OHP levels in urine were found among topside workers including lidmen, tar chasers, and whistlers. Benchmen had higher 1-OHP levels than other workers at the sideoven. Above 75% of the COWs exceeded the recommended occupational exposure limit of 2.3 {mu}mol/mol creatinine. Respirator usage and increased body mass index (BMI) slightly reduced 1-OHP levels in COWs. Cigarette smoking significantly increased urinary 1-OHP levels in unexposed referents but had no effect in COWs. Chinese COWs, especially topside workers and benchmen, are exposed to high levels of PAHs. Urinary 1-OHP concentrations appear to be modulated by respirator usage and BMI in COWs, as well as by smoking in unexposed referents.

Prediction of operating parameters range for ammonia removal unit in coke making by-products

Science.gov (United States)

Tiwari, Hari Prakash; Kumar, Rajesh; Bhattacharjee, Arunabh; Lingam, Ravi Kumar; Roy, Abhijit; Tiwary, Shambhu

2018-02-01

Coke oven gas treatment plants are well equipped with distributed control systems (DCS) and therefore recording the vast amount of operational data efficiently. Analyzing the stored information manually from historians is practically impossible. In this study, data mining technique was examined for lowering the ammonia concentration in clean coke oven gas. Results confirm that concentration of ammonia in clean coke oven gas depends on the average PCDC temperature; gas scrubber temperatures stripped liquor flow, stripped liquor concentration and stripped liquor temperature. The optimum operating ranges of the above dependent parameters using data mining technique for lowering the concentration of ammonia is described in this paper.

Numerical analysis of macro-crack formation behavior within the lump coke; Cokes sonai kiretsu shinten kiko no kaiseki

Energy Technology Data Exchange (ETDEWEB)

Aoki, H; Sato, H; Miura, T [Tohoku University, Sendai (Japan). Faculty of Engineering

1995-03-15

The thermal stress analysis within lump coke was studied in order to investigate macro-crack formation and deformation behavior which strongly influence heat and mass transfer in a coke oven chamber. The dilatation of plastic layer, heating rate dependence of thermophysical and mechanical properties of coal/coke, creep in the plastic and semi-coke layers, macro-crack propagation and radiative heat transfer within the macro-crack were considered in an analytical model. The macro-crack propagation was determined from the estimated crack tip stress intensity factor, K{sub I}, at the macro-crack tip compared with the plane strain fracture toughness, K{sub IC}, through the unsteady-state calculation. Calculated results on crack formation and deformation behavior of lump coke were in good agreement with experimental observations in a laboratory-scale oven chamber. The analytical model could predict micro-crack formation within the lump coke normal to the heated wall and the coke surface close to the heated wall. 12 refs., 13 figs.

Coking of residue hydroprocessing catalysts

Energy Technology Data Exchange (ETDEWEB)

Gray, M.R.; Zhao, Y.X. [Alberta Univ., Edmonton, AB (Canada). Dept. of Chemical Engineering; McKnight, C.A. [Syncrude Canada Ltd., Edmonton, AB (Canada); Komar, D.A.; Carruthers, J.D. [Cytec Industries Inc., Stamford, CT (United States)

1997-11-01

One of the major causes of deactivation of Ni/Mo and Co/Mo sulfide catalysts for hydroprocessing of heavy petroleum and bitumen fractions is coke deposition. The composition and amount of coke deposited on residue hydroprocessing catalysts depends on the composition of the liquid phase of the reactor. In the Athabasca bitumen, the high molecular weight components encourage coke deposition at temperatures of 430 to 440 degrees C and at pressures of 10 to 20 MPa hydrogen pressure. A study was conducted to determine which components in the heavy residual oil fraction were responsible for coking of catalysts. Seven samples of Athabasca vacuum residue were prepared by supercritical fluid extraction with pentane before being placed in the reactor. Carbon content and hydrodesulfurization activity was measured. It was concluded that the deposition of coke depended on the presence of asphaltenes and not on other compositional variables such as content of nitrogen, aromatic carbon or vanadium.

Hanford Waste Vitrification Plant: Preliminary description of waste form and canister

International Nuclear Information System (INIS)

Mitchell, D.E.

1986-01-01

In July 1985, the US Department of Energy's Office of Civilian Radioactive Waste Management established the Waste Acceptance Process as the means by which defense high-level waste producers, such as the Hanford Waste Vitrification Plant, will develop waste acceptance requirements with the candidate geologic repositories. A complete description of the Waste Acceptance Process is contained in the Preliminary Hanford Waste Vitrification Plant Waste Form Qualification Plan. The Waste Acceptance Process defines three documents that high-level waste producers must prepare as a part of the process of assuming that a high-level waste product will be acceptable for disposal in a geologic repository. These documents are the Description of Waste Form and Canister, Waste Compliance Plan, and Waste Qualification Report. This document is the Hanford Waste Vitrification Plant Preliminary Description of Waste Form and Canister for disposal of Neutralized Current Acid Waste. The Waste Acceptance Specifications for the Hanford Waste Vitrification Plant have not yet been developed, therefore, this document has been structured to corresponds to the Waste Acceptance Preliminary Specifications for the Defense Waste Processing Facility High-Level Waste Form. Not all of the information required by these specifications is appropriate for inclusion in this Preliminary Description of Waste Form and Canister. Rather, this description is limited to information that describes the physical and chemical characteristics of the expected high-level waste form. The content of the document covers three major areas: waste form characteristics, canister characteristics, and canistered waste form characteristics. This information will be used by the candidate geologic repository projects as the basis for preliminary repository design activities and waste form testing. Periodic revisions are expected as the Waste Acceptance Process progresses

Petroleum coke as energy source: an update

International Nuclear Information System (INIS)

Pinelli, G.

2008-01-01

A previous review presented a critical evaluation of the use of petroleum coke as energy source. After some years, with reference to increased petroleum coke production, that paper is revised. In particular, the attention is now focused on world petroleum coke market trends and, in regard to petroleum coke used as fuel, on new Italian environment laws. [it

Dependence of microhardness of coke on carbon content and final coking temperature

Energy Technology Data Exchange (ETDEWEB)

Kaloc, M.; Dvorak, P.

1995-12-31

At present time is important the coke-quality, tested by various methods again. The new methods of evaluation of coke quality as e.g. CSR, CRI, ACRI etc. demonstrate, that the mechanical stability parameters are in connection of microstructure of coke mass. The purpose of present paper is to investigate the dependence of microhardness on the carbon content and the final carbonisation temperature in the coal-coke series. The samples prepared experimentally in more series from different coal blends from 20{degrees}C to 1100{degrees}C were investigated both mega- and microscopically. The tests of microhardness are based on the use of the Hanemann microhardness tester. Principally this method consists in impressing the diamond pyramid into the surface of the sample. The data on the pressure applied are subtracted on the scale of load. An important factor influencing the results is the choice of the points from which the sample is to be withdrawn. The choice is dependent on the aim to be achieved. For the determination of an average microhardness it is sufficient to take sample from the middle part of the coke block representing the half width of the coking chamber. The choice of the point is also of great importance. In strong and homogeneous walls, sharply bounded, impressions can be found with a distinct diagonal cross. In thin walls the impressions are distinguished by distinct boundaries, the middle part, however, not being distinct as the pyramidal point did not penetrate the wall. Impressions providing accurate values are those distinctly bounded by a distinct diagonal cross. The walls not having been chosen correctly, the errors reveal themselves as the scattering of the points in the diagrams of microhardness.

Benzole still reflux system - Dawes Lane Coke Ovens

Energy Technology Data Exchange (ETDEWEB)

Hardwick, J.

2005-07-01

The paper describes a project carried out at Dawes Lane coking plant (in Scunthorpe, UK) to access current performance of the batch reflux system with respect to the operation of personnel and to recommend a solution to eliminate naphthalene blockage and problems previously caused by the use of hot debenzolised oil (DBO) as make-up. A successful solution was found and implemented. The benzole product now being produced is within specification and regularly achieves the composition produced by the previous hot reflux system (83% benzole, 7% naphthalene) with an addition reduction in wash oil usage of 20%. Problems of naphthalene blockages in reflux pipework have been cured. The expenses on the project were small. The paper was presented at a COMA meeting at Monckton Coke Ovens on 19 May 2005. 6 figs.

Research and development of SCOPE21 (super coke oven for productivity and environment enhancement towards the 21st century)

Energy Technology Data Exchange (ETDEWEB)

Oshima, H.; Otsuka, J.; Nishioka, K.; Kamijo, T. [Japan Iron and Steel Federation, Tokyo (Japan)

2000-07-01

Coke ovens in Japan have 28 years of service on the average and the supply of coke is foreseen to suffer a shortage at the early years of the 21st century. Furthermore, the existing cokemaking process entails a lot of issues such as an effective use of coal resources, an adverse effect on environment. Thus, the Japan Iron and Steel Federation has launched a 9 year research programme called SCOPE 21 in collaboration with the Center for Coal Utilization, Japan in 1994. The programme pursues the following targets. The use ratio of poor coking coal increases from 20-50% with the improvement of coking property of coal by rapid heating and the increase of bulk density by mixing the briquetted coal. The coking time is reduced by rapid heating to 350 to 400{degree}C at the preheater, coking up to 750-850{degree}C at oven chamber, and reheating up to 1000{degree}C at the upgrading chamber, thus trebling productivity. The environment of coke oven is improved by emission free system and by improving the heating system of coke oven to reduce NOx in oven exhaust gas. After two years of preliminary feasible study the programme has advanced to basic research and to a bench scale test. It is in a stage of the construction of a pilot plant. This report describes the outline of the programme and the results obtained through the basic research and the bench scale plant tests. 2 refs., 17 figs., 5 tabs.

Briquetting of Coke-Brown Coal Mixture

Directory of Open Access Journals (Sweden)

Ïurove Juraj

1998-09-01

Full Text Available The paper presents the results of the research of briquetting a coke-brown coal composite The operation consists of the feeding crushed coal and coke to moulds and pressing into briquettes which have been made in the Laboratories at the Mining Faculty of Technical University of Košice (Slovakia. In this research, all demands will be analyzed including the different aspects of the mechanical quality of briquettes, the proportion of fine pulverulent coal and coke in bricks, the requirements for briquetting the coke-brown coal materials.

Making coke

Energy Technology Data Exchange (ETDEWEB)

Wodehouse-Temple, C G

1929-07-12

Semi-coke is produced by mixing low-value absorbent solid carbonaceous material such as coal dust, slack, gas-works coke, lignite, torbanite, raphilite, cannel, or shale with not more than 20% of a carbonaceous binding material such as petroleum distillation residue, tarry residues, pitch bitumen, Trinidad asphalt, Manjak or the substance known under the registered Trade Mark Gilsonite and subjecting the mixture without briquetting to a temperature not exceeding 550/sup 0/C. According to the first Provisional Specification, the mixture may if desired be briquetted before being heated and the second constituent may be present to the extent of 30%.

REDUCING POWER PRODUCTION COSTS BY UTILIZING PETROLEUM COKE

Energy Technology Data Exchange (ETDEWEB)

Kevin C. Galbreath; Donald L. Toman; Christopher J. Zygarlicke

1999-09-01

Petroleum coke, a byproduct of the petroleum-refining process, is an attractive primary or supplemental fuel for power production primarily because of a progressive and predictable increase in the production volumes of petroleum coke (1, 2). Petroleum coke is most commonly blended with coal in proportions suitable to meet sulfur emission compliance. Petroleum coke is generally less reactive than coal; therefore, the cofiring of petroleum coke with coal typically improves ignition, flame stability, and carbon loss relative to the combustion of petroleum coke alone. Although petroleum coke is a desirable fuel for producing relatively inexpensive electrical power, concerns about the effects of petroleum coke blending on combustion and pollution control processes exist in the coal-fired utility industry (3). The Energy & Environmental Research Center (EERC) completed a 2-year technical assessment of petroleum coke as a supplemental fuel. A survey questionnaire was sent to seven electric utility companies that are currently cofiring coal and petroleum coke in an effort to solicit specific suggestions on research needs and fuel selections. An example of the letter and survey questionnaire is presented in Appendix A. Interest was expressed by most utilities in evaluating the effects of petroleum coke blending on grindability, combustion reactivity, fouling, slagging, and fly ash emissions control. Unexpectedly, concern over corrosion was not expressed by the utilities contacted. Although all seven utilities responded to the question, only two utilities, Northern States Power Company (NSP) and Ameren, sent fuels to the EERC for evaluation. Both utilities sent subbituminous coals from the Power River Basin and petroleum shot coke samples. Petroleum shot coke is produced unintentionally during operational upsets in the petroleum refining process. This report evaluates the effects of petroleum shot coke blending on grindability, fuel reactivity, fouling/slagging, and

Gasification reactivities of cokes derived from Athabasca bitumen

Energy Technology Data Exchange (ETDEWEB)

Furimsky, E.

1985-10-01

Gasification reactivities of cokes obtained from Athabasca bitumen by delayed coking and fluid coking were compared in fixed and fluidized bed systems. In both systems the C + O/sub 2/ reaction accounted for the most of converted carbon. The C + H/sub 2/O reaction proceeded to a smaller extent. The bulk reactivity of the fluid coke was higher than that of delayed coke, when comparing -20 to +60 mesh particles in fluidized bed and -14 to +20 mesh particles in fixed bed, respectively. However, the reactivity of the delayed coke expressed per unit of surface area was markedly higher than that of the fluid coke. 9 figs., 7 tabs., 6 refs. (A.V.)

Microwave-assisted grinding of metallurgical coke

International Nuclear Information System (INIS)

Ruisanchez, E.; Juarez-Perez, E. J.; Arenillas, A.; Bermudez, J. M.; Menendez, J. A.

2014-01-01

Metallurgical cokes are composed of graphitic carbon (s2p2) and different inorganic compounds with very different capacities to absorb microwave radiation. Moreover, due to the electric conductivity shown by the metallurgical cokes, microwave radiation produces electric arcs or microplasmas, which gives rise to hot spots. Therefore, when these cokes are irradiated with microwaves some parts of the particle experiment a rapid heating, while some others do not heat at all. As a result of the different expansion and stress caused by thermal the shock, small cracks and micro-fissures are produced in the particle. The weakening of the coke particles, and therefore an improvement of its grind ability, is produced. This paper studies the microwave-assisted grinding of metallurgical coke and evaluates the grinding improvement and energy saving. (Author)

Fine coke production from brown coal (Report on ECSC contract 6220-72/1/102)

Energy Technology Data Exchange (ETDEWEB)

1977-01-01

The possibility of producing a dry brown coal suitable for the production of fine coke and the development of a suitable carbonization process were studied. To prepare the coal it should be screened at 1 mm with the oversize going to fine coke production and the undersize going to briquette production. To increase fine coke production it is necessary to screen the raw smalls less than 2 mm and to pelletize, dry and carbonize them with the coarser constituents. The planning and construction of a hearth oven furnace plant was begun and this is now in operation. A fluidized bed can be used to preheat the coal to improve the oven performance. (In German)

Preparation of briquettes on the basis of desintegrated phyto-materials and the admixture of fine-grained coal and coke

Directory of Open Access Journals (Sweden)

Jakabský Štefan

2002-03-01

Full Text Available The contribution deals with the preparation of small-diameter briquettes on the basis of desintegrated phyto-materials and the admixture of coal and coke. The phyto-materials are classified as a dry biomass that can be, on the one hand, the wastes from wood-working industry,(sawdust, chips, bark, etc. or dried mass from the plant production and, on the other hand, the mass of quick-growing plants cultivated on special plantations. In present time this renewable energy resource attracts attention by its heating value ranging from 10 to 16 MJ.kg-1 (EkoWATT, 2001, a low ash content of 0.5 – 6.5 % and by a low sulphur content in a water free sample of 0.05 –0.12 %.As a phyto-material the spruce sawdusts having a grain size of –2 mm were used. The admixture of brown coal, hard coal and coke with a grain size of 0.040 mm was added to the sawdust and in such way prepared mixtures were subjected to briquetting with the aim to obtain small-diameter briquettes. The influence of admixtures amount on the density, and the suitable briquetting press have been studied. A saleability of briquettes on the basis of phyto-materials is conditioned by their density that must be higher than 1,000 kg.m-3. Thus, an adding of denser material with a relatively high calorific value would enable to attain the required density as well as to retain and/or to improve the main utility properties, i.e. calorific value and ash content.The adding evinces itself in an enhancement of briquetting press, but also density of obtained briquettes is often much higher that required by the market. It was showed that in the case of clear spruce sawdust the density of 1,059 kg.m-3 under the briquetting press of 250 MPa can be attained. According to other results, an admixture of brown coal is not very favourable because briquetting press exceeds the value of 300 MPa. As to hard coal adding, the presses under 250 MPa were achieved at the content of 25 – 30 %. The density of these

Waste Immobilisation Plant (WIP), Trombay

International Nuclear Information System (INIS)

Kaushik, C.P.; Agarwal, K.

2017-01-01

Waste Immobilization Plant (WIP), Trombay is designed and constructed for the management of radioactive liquid wastes generated during reprocessing of spent nuclear fuel from research reactors at Bhabha Atomic Research Centre. In common with such facilities elsewhere, the objective here is to manage the wastes in such a way as to protect human health and the environment and to limit any burden on future generations. The plant has several facilities for the handling and treatment of the three classes of waste, viz., high, intermediate and low level, a classification based on their radioactivity content. In keeping with the general objective of radioactive waste management, the focus is on concentration and confinement of radioactivity. Strict adherence to the universal principles of radiation protection during operation of the plant ensures that radiation exposure is always kept as low as reasonably achievable (ALARA) under the prescribed limits

A study of the performance of a reclamation soil cover placed over an oilsands coke deposit

Energy Technology Data Exchange (ETDEWEB)

Fenske, D.S.; Barbour, S.L. [Saskatchewan Univ., Saskatoon, SK (Canada). Dept. of Civil Engineering; Qualizza, C. [Syncrude Canada Ltd., Fort McMurray, AB (Canada)

2006-07-01

Coke is a solid, carbonaceous residue that forms during the cracking of high-boiling point distillates and is one of the by-products of petroleum extraction from oilsands. Coke is known as a possible future energy source and therefore, must be stored within the reclaimed landscape in a form that allows it to be recovered. In addition, it also could be used as a low-density capping material over soft tailings. This paper presented the results of a study that examined the effects of coke in the environment. The study involved construction of two small instrumented watersheds at Syncrude Canada's Mildred Lake Settling Basin. Preliminary field data, highlighting the moisture dynamics within the covers and the underlying coke were discussed. Sand tailings underlie the hydraulically placed coke deposit. Overlying the coke were two different reclamation soil covers constructed of a peat/mineral mix over glacial or glacial lacustrine soils. Placing the finer textured soil cover over coarser grained coke produced a textural or capillary break which enhanced moisture storage for plant use while minimizing deep percolation of infiltrating water. The site has been instrumented with a meteorological station; automated soil stations to monitor suction, water content and temperature through the cover profile; lysimeters to collect net percolation; access tubes for water content monitoring; gas sampling points at depth in the coke; and standpipe piezometers to monitor water chemistry and total head in the coke at depth. 10 refs., 2 tabs., 16 figs.

Power, cement industries shape coke future

International Nuclear Information System (INIS)

Swain, E.J.

1991-01-01

The production of petroleum coke by U.S. refineries is expected to continue to increase in the coming years. Process and market trends also indicate the likelihood of further increases in fuel-grade coke production. In this article, the properties and uses of the various grades of petroleum coke, as well as pricing and market trends, will be discussed

Technology for beneficiation of non-coking coals

Energy Technology Data Exchange (ETDEWEB)

Bose, S.K.

1987-04-01

This article outlines the need for efficient non-coking coal beneficiation plants in India to cope with mass production from opencast coal mines. The existing use of magnetite in heavy medium separation processes is expensive and not very efficient in respect to removing shales from opencast lump coals. Instead a new technique is proposed using a ROMJIG washing plant developed in the Federal Republic of Germany. This provides a very efficient, low cost washing system for the coals and allows the continued integration with the coal blending plants. This simplified technology allows for flexible working hours to meet demand and will allow new developments to continue including fuel slurry pipelines, automated testing of coals and new pulverized boiler fuels.

Production of fine coke from brown coal

Energy Technology Data Exchange (ETDEWEB)

Koenigs, H B

1977-08-01

The coke supply of the iron and steel industry, the design, function, and special features of the open-hearth are described, including coking properties and applications of the culm coke produced from brown coal. (In German)

Blast-furnace coke production in high capacity coke oven batteries from the viewpoint of domestic raw material resources

Energy Technology Data Exchange (ETDEWEB)

Krause, W

1977-05-01

The problem is treated in a complex manner taking into account such technological improvements as: oiling, drying, charge preheating, dry quenching of coke as well as mechanical processing of coke which taken together will give blast furnace coke of the highest quality from domestic coals.

New designs in the reconstruction of coke-sorting systems

Energy Technology Data Exchange (ETDEWEB)

A.S. Larin; V.V. Demenko; V.L. Voitanik [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15

In recent Giprokoks designs for the reconstruction of coke-sorting systems, high-productivity vibrational-inertial screens have been employed. This permits single-stage screening and reduction in capital and especially operating expenditures, without loss of coke quality. In two-stage screening, >80 mm coke (for foundry needs) is additionally separated, with significant improvement in quality of the metallurgical coke (25-80 mm). New designs for the reconstruction of coke-sorting systems employ mechanical treatment of the coke outside the furnace, which offers new scope for stabilization of coke quality and permits considerable improvement in mechanical strength and granulometric composition of the coke by mechanical crushing.

Production of rubbly culm coke from lignite

Energy Technology Data Exchange (ETDEWEB)

Koenigs, H B [Rheinische Braunkohlenwerke A.G., Koeln (Germany, F.R.). Hauptabteilung Kohleverarbeitung; Kurtz, R [Rheinische Braunkohlenwerke A.G., Frechen (Germany, F.R.). Abt. Verkokung und Chemie

1977-08-01

The article deals with the coke supply of the iron and steel industry, the design, function, and special features of the open-hearth, and describes the coking properties and applications of the culm coke produced from lignite.

Fluid coking of heavy hydrocarbons and apparatus therefor

Energy Technology Data Exchange (ETDEWEB)

1956-07-11

A process for the conversion of hydrocarbon oils comprises injecting a plurality of streams of oil into an enlarged coking vessel containing a mass of finely divided solids, thereby, preventing agglutination of the solids, circulating the solids through an external heating zone and back to the coking vessel to maintain the vessel at a coking temperature between 850 and 1,200/sup 0/F, passing gaseous material upwardly through the coking vessel at a superficial velocity of between 0.1 and 5.0 feet per second, controlled to maintain the body of solids in a dense turbulent fluidized state, maintaining the oil within coking the vessel for a period sufficient to convert into vapors and coke, withdrawing vapors from the top of the vessel through an outlet, separating high-boiling ends from vapors, returning at least a portion of the high-boiling ends to the coking vessel for further cracking and withdrawing excess of coke formed in the process.

Deciphering Cyanide-Degrading Potential of Bacterial Community Associated with the Coking Wastewater Treatment Plant with a Novel Draft Genome.

Science.gov (United States)

Wang, Zhiping; Liu, Lili; Guo, Feng; Zhang, Tong

2015-10-01

Biotreatment processes fed with coking wastewater often encounter insufficient removal of pollutants, such as ammonia, phenols, and polycyclic aromatic hydrocarbons (PAHs), especially for cyanides. However, only a limited number of bacterial species in pure cultures have been confirmed to metabolize cyanides, which hinders the improvement of these processes. In this study, a microbial community of activated sludge enriched in a coking wastewater treatment plant was analyzed using 454 pyrosequencing and Illumina sequencing to characterize the potential cyanide-degrading bacteria. According to the classification of these pyro-tags, targeting V3/V4 regions of 16S rRNA gene, half of them were assigned to the family Xanthomonadaceae, implying that Xanthomonadaceae bacteria are well-adapted to coking wastewater. A nearly complete draft genome of the dominant bacterium was reconstructed from metagenome of this community to explore cyanide metabolism based on analysis of the genome. The assembled 16S rRNA gene from this draft genome showed that this bacterium was a novel species of Thermomonas within Xanthomonadaceae, which was further verified by comparative genomics. The annotation using KEGG and Pfam identified genes related to cyanide metabolism, including genes responsible for the iron-harvesting system, cyanide-insensitive terminal oxidase, cyanide hydrolase/nitrilase, and thiosulfate:cyanide transferase. Phylogenetic analysis showed that these genes had homologs in previously identified genomes of bacteria within Xanthomonadaceae and even presented similar gene cassettes, thus implying an inherent cyanide-decomposing potential. The findings of this study expand our knowledge about the bacterial degradation of cyanide compounds and will be helpful in the remediation of cyanides contamination.

Conceptual design of coke-oven gas assisted coal to olefins process for high energy efficiency and low CO2 emission

International Nuclear Information System (INIS)

Man, Yi; Yang, Siyu; Zhang, Jun; Qian, Yu

2014-01-01

Highlights: • A novel coke-oven gas assisted coal to olefins (GaCTO) process is proposed. • GaCTO has higher energy efficiency and emits less CO 2 compared to coal-to-olefins process. • GaCTO proposes an idea of using redundant coke-oven gas for producing value added products. - Abstract: Olefins are one of the most important platform chemicals. Developing coal-to-olefins (CTO) processes is regarded as one of promising alternatives to oil-to-olefins process. However, CTO suffers from high CO 2 emission due to the high carbon contents of coal. In China, there is 7 × 10 10 m 3 coke-oven gas (COG) produced in coke plants annually. However, most of the hydrogen-rich COG is utilized as fuel or discharged directly into the air. Such situation is a waste of precious hydrogen resource and serious economic loss, which causes serious environmental pollution either. This paper proposes a novel co-feed process of COG assist CTO in which CH 4 of COG reacts with CO 2 in a Dry Methane Reforming unit to reduce emissions, while the Steam Methane Reforming unit produces H 2 -rich syngas. H 2 of COG can adjust the H/C ratio of syngas. The analysis shows that the energy efficiency of the co-feed process increases about 10%, while at the same time, life cycle carbon footprint is reduced by around 85% in comparison to the conventional CTO process. The economic sustainability of the co-feed process will be reached when the carbon tax would be higher than 150 CNY/t CO 2

Hanford Waste Vitrification Plant technology progress

International Nuclear Information System (INIS)

Wolfe, B.A.; Scott, J.L.; Allen, C.R.

1989-10-01

The Hanford Waste Vitrification Plant (HWVP) is currently being designed to safely process and temporarily store immobilized defense liquid high-level wastes from the Hanford Site. These wastes will be immobilized in a borosilicate glass waste form in the HWVP and stored onsite until a qualified geologic waste repository is ready for permanent disposal. Because of the diversity of wastes to be disposed of, specific technical issues are being addressed so that the plant can be designed and operated to produce a waste form that meets the requirements for permanent disposal in a geologic repository. This paper reports the progress to date in addressing these issues. 2 figs., 3 tabs

Hydrotreating catalyst deactivation by coke from SRC-II oil

Energy Technology Data Exchange (ETDEWEB)

Yamamoto, Y.; Kumata, F.; Massoth, F.E.

1988-10-01

Samples of a CoMo/Al/sub 2/O/sub 3/ catalyst were partially deactivated with SRC-II feed in an autoclave reactor to give coked samples of 5 to 18% C. The coked catalysts were analyzed for surface area, pore volume, coronene adsorption and diffusivity, and their catalytic activity determined for hydrodesulfurization (HDS), hydrodeoxygenation (HDO) and C-N hydrogenolysis (CNH) using model compounds. All of the above measurements decreased with increase in coke content. Property data indicate that some pores are blocked by coke and diffusivity results show narrowing of pore mouths with increasing coke content. Catalyst deactivation versus coke level was identical for HDS and HDO, but less for CNH. A simple model of coke deactivation was developed to relate activity to coke content. Coke is envisioned as forming wedge-like deposits in the catalyst pores. 11 refs., 5 figs., 3 tabs.

Coke breakage behaviour in relation to its structure

Energy Technology Data Exchange (ETDEWEB)

Peirce, T J; Horton, A E; Tucker, J

1980-06-14

The relationship between coke macrostructure and volumetric (coarse) breakage behaviour, and the manner in which both features are affected by the coal charge composition are discussed. Coke pieces which are extensively fissured fail spontaneously after only a few revolutions in the drum; coke pieces which are less fissured require an extended treatment in the drum and finally fail in a manner consistent with that of fatigue crack growth induced by repeated impact. This heterogeneity in breakage behaviour was demonstrated in terms of an abrupt change in gradient of the Weibull distribution function for the coke. Heterogeneity may be removed by fully stabilising the coke or by the use of a more energetic test method. The role of fatigue crack growth in coke breakage was studied by cutting fissures of defined depth in full stabilised coke and assessing the rate of crack growth as a function of fissure depth and fracture toughness. The form of the results was consistent with that given by the Paris-Erdogan law and the rate of crack growth (for a given stress intensity level) was shown to increase with reducing coke toughness. Explanations are suggested to account for the role of blend additives in modifying the fissured properties and fracture toughness of coke made from high-volatile coal.

Statistical summary of coal mining, coking, and briquetting plants and review of the solid fuels market in 1976

Energy Technology Data Exchange (ETDEWEB)

Medaets, J

1977-05-01

This paper reviews the activities of the Belgian coal and coke industry noting that some of the figures are still provisional. Figures are given for production and stocks of coal; personnel; productivity; working hours; salaries; and the production of coke and briquettes.

Scientific Council on problems on new processes in the coking industry. [Effect on coke consumption of moisture, sulfur and ash; substitution possibility

Energy Technology Data Exchange (ETDEWEB)

Filippov, B.S.

1981-07-01

This paper presents a report on the Coking Section of the Scientific Council held on November 20, 1980 in Moscow. The following problems were discussed: indexes characterizing blast furnace coke (for furnaces with a volume of 5580 M/sup 3/); replacing metallurgical coke with other types of fuels; use of brown coal; liners of coke ovens. Papers delivered during the session are summarized. Reducing moisture content in blast furnace coke permits its consumption to be reduced by 2%. Reducing sulfur content in blast furnace coke by 0.1% permits its consumption to be reduced from 10 to 15 kg for 1 t of pig iron. Increase in ash content of coke by 1% causes coke consumption increase ranging from 1.5 to 2.0%. About 10 Mmt of coke class with grains above 25 mm in USSR is used for purposes other than blast furnaces. Possibilities of substituting coke with lean coal are evaluated (particularly from Kuzbass). A method for briquetting a mixture of black and brown coal is proposed. Briquets are a suitable fuel in metallurgy. A new type of liner, which consists of at least 92% silicon dioxide, is described. Physical and mechanical properties of the liners are discussed.

Trends in the automation of coke production

Energy Technology Data Exchange (ETDEWEB)

R.I. Rudyka; Y.E. Zingerman; K.G. Lavrov [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15

Up-to-date mathematical methods, such as correlation analysis and expert systems, are employed in creating a model of the coking process. Automatic coking-control systems developed by Giprokoks rule out human error. At an existing coke battery, after introducing automatic control, the heating-gas consumption is reduced by {>=}5%.

Fluid coking : a competitive option for heavy feed processing

International Nuclear Information System (INIS)

Hammond, D.G.; Feinberg, A.S.; McCaffrey, D.S.

1997-01-01

Fluid coking is a proven thermal conversion process for converting heavy hydrocarbon feeds to lighter products. Fluid coking was commercialized by Exxon over 40 years ago. A total of 13 units have been built with over 330 years of cumulative operating experience. Fluid coking can process many different feeds at once and is usually insensitive to feed contaminants such as sulfur, nitrogen and metals. New developments in coke utilization and flue gas desulfurization/departiculation have prompted new economic studies. Fluid coking is competitive and is the most attractive option compared to delayed coking, particularly for very heavy feed stocks such as deasphalter bottoms. Viewgraphs describe the fluid coking process, its advantages, utilization, and commercial viability. 7 tabs., 3 figs

Conflicts concerning sites for waste treatment and waste disposal plants

International Nuclear Information System (INIS)

Werbeck, N.

1993-01-01

The erection of waste treatment and waste disposal flants increasingly meets with the disapproval of local residents. This is due to three factors: Firstly, the erection and operation of waste treatment plants is assumed to necessarily entail harmful effects and risks, which may be true or may not. Secondly, these disadvantages are in part considered to be non-compensable. Thirdly, waste treatment plants have a large catchment area, which means that more people enjoy their benefits than have to suffer their disadvantages. If residents in the vicinity of such plants are not compensated for damage sustained or harmed in ways that cannot be compensated for it becomes a rational stance for them, while not objecting to waste treatment and waste disposal plants in principle to object to their being in their own neighbourhood. The book comprehensively describes the subject area from an economic angle. The causes are analysed in detail and an action strategy is pointed, out, which can help to reduce acceptance problems. The individual chapters deal with emissions, risk potentials, optimization calculus considering individual firms or persons and groups of two or more firms or persons, private-economy approaches for the solving of site selection conflicts, collective decision-making. (orig./HSCH) [de

Waste management in MOX fuel fabrication plants

International Nuclear Information System (INIS)

Schneider, V.

1982-01-01

After a short description of a MOX fuel fabrication plant's activities the waste arisings in such a plant are discussed according to nature, composition, Pu-content. Experience has shown that proper recording leads to a reduction of waste arisings by waste awareness. Aspects of the treatment of α-waste are given and a number of treatment processes are reviewed. Finally, the current waste management practice and the α-waste treatment facility under construction at ALKEM are outlined. (orig./RW)

AVLIS production plant waste management plan

International Nuclear Information System (INIS)

1984-01-01

Following the executive summary, this document contains the following: (1) waste management facilities design objectives; (2) AVLIS production plant wastes; (3) waste management design criteria; (4) waste management plan description; and (5) waste management plan implementation. 17 figures, 18 tables

Impact of co-combustion of petroleum coke and coal on fly ash quality: Case study of a Western Kentucky power plant

International Nuclear Information System (INIS)

Hower, James C.; Thomas, Gerald A.; Mardon, Sarah M.; Trimble, Alan S.

2005-01-01

Petroleum coke has been used as a supplement or replacement for coal in pulverized-fuel combustion. At a 444-MW western Kentucky power station, the combustion of nearly 60% petroleum coke with moderate- to high-sulfur Illinois Basin coal produces fly ash with nearly 50% uncombusted petroleum coke and large amounts of V and Ni when compared to fly ash from strictly pulverized coal burns. Partitioning of the V and Ni, known from other studies to be concentrated in petroleum coke, was noted. However, the distribution of V and Ni does not directly correspond to the amount of uncombusted petroleum coke in the fly ash. Vanadium and Ni are preferentially associated with the finer, higher surface area fly ash fractions captured at lower flue gas temperatures. The presence of uncombusted petroleum coke in the fly ash doubles the amount of ash to be disposed, makes the fly ash unmarketable because of the high C content, and would lead to higher than typical (compared to other fly ashes in the region) concentrations of V and Ni in the fly ash even if the petroleum coke C could be beneficiated from the fly ash. Further studies of co-combustion ashes are necessary in order to understand their behavior in disposal

The effect of calcination conditions on the graphitizability of novel synthetic and coal-derived cokes

Science.gov (United States)

Bennett, Barbara Ellen

The effects of calcination heating rate and ultimate calcination temperature upon calcined coke and subsequent graphitic material microstructures were studied for materials prepared from three different precursors. The pitch precursors used were Mitsubishi AR pitch (a synthetic, 100% mesophase pitch), the NMP-extracted portion of a raw coal, and the NMP-extracted fraction of a coal liquefaction residue obtained from an HTI pilot plant. These materials were all green-coked under identical conditions. Optical microscopy confirmed that the Mitsubishi coke was very anisotropic and the HTI coke was nearly as anisotropic. The coke produced from the direct coal extract was very isotropic. Crystalline development during calcination heating was verified by high-temperature x-ray diffraction. Experiments were performed to ascertain the effects of varying calcination heating rate and ultimate temperature. It was determined that calcined coke crystallite size increased with increasing temperature for all three materials but was found to be independent of heating rate. The graphene interplanar spacing decreased with increasing temperature for the isotropic NMP-extract material but increased with increasing temperature for the anisotropic materials---Mitsubishi and HTI cokes. Graphene interplanar spacing was also found to be independent of heating rate. Calcined coke real densities were, likewise, found to be independent of heating rate. The anisotropic cokes (Mitsubishi and HTI) exhibited increasing real density with increasing calcination temperature. The NMP-extract coke increased in density up to 1050°C and then suffered a dramatic reduction in real density when heated to 1250°C. This is indicative of puffing. Since there was no corresponding disruption in the crystalline structure, the puffing phenomena was determined to be intercrystalline rather than intracrystalline. After the calcined cokes were graphitized (under identical conditions), the microstructures were re

Waste Isolation Pilot Plant transuranic wastes experimental characterization program: executive summary

International Nuclear Information System (INIS)

Molecke, M.A.

1978-11-01

A general overview of the Waste Isolation Pilot Plant transuranic wastes experimental characterization program is presented. Objectives and outstanding concerns of this program are discussed. Characteristics of transuranic wastes are also described. Concerns for the terminal isolation of such wastes in a deep bedded salt facility are divided into two phases, those during the short-term operational phase of the facility, and those potentially occurring in the long-term, after decommissioning of the repository. An inclusive summary covering individual studies, their importance to the Waste Isolation Pilot Plant, investigators, general milestones, and comments are presented

Study of the raw material base for a by-product coke plant by the method of thermal degradation of coal in a centrifugal field

Energy Technology Data Exchange (ETDEWEB)

Epimakhov, N.M.; Kardashova, V.F.; Sulimova, E.I.

1982-01-01

Coals from the Donbass and Karaganda basins, being supplied to a Bagley by-product coke plant were studied. A sharp distinction between coals of different degrees of metamorphism in respect to the yield of liquid nonvolatile products was demonstrated. A difference in respect to this index was recognized for individual coals from one and the same technological group from a single basin.

Emission and source characterization of monoaromatic hydrocarbons from coke production

Energy Technology Data Exchange (ETDEWEB)

He, Q.S.; Wang, X.M.; Sheng, G.Y.; Fu, J.M. [Chinese Academy of Sciences, Guangzhou (China). State Key Laboratory of Organic Geochemistry

2005-09-15

Monoaromatic hydrocarbons (MAHs) from indigenous and industrial coking processes are studied in Shanxi province. They are sampled on the top of coke ovens and in the chimneys using stainless steel canister and determined by GC/MSD after preconcentration with liquid nitrogen. Benzene, toluene and xylene are the main components among MAHs emitted from coking processes. Benzene and the total MAHs concentrations were as high as 3421.0 microg/m3 and 4 865.9 microg/m3 in the air from indigenous coking, 548.7 microg/m3 and 1 054.8 microg/m3 in the oventop air from industrial coking, and 1 376.4 microg/m3 and 1 819.4 microg/m3 in stack gas from industrial coking, respectively. The MAHs concentrations vary greatly during the indigenous coking process, which in the prophase (from firing to 10 days) is obviously higher than in the anaphase (10 days to quenching the coke). In industrial coking the MAHs in the oventop air are highest when charging the coal and next when transferring the hot coke, but in stack gas they are highest when charging coal and lowest when transferring the coke. Benzene, toluene, ethylbenzene and xylene (BTEX) in industrial coking samples show good linearity, indicating that MAHs in industrial coking might come predominantly from coal pyrolysis; but BTEX distribute dispersedly in indigenous coking samples, indicating that its emission might be affected by many factors. In all samples BTEX ratios especially high B/E ratio, is unique among MAHs sources, and might be helpful to characterize pollution from coking.

[Emission and source characterization of monoaromatic hydrocarbons from coke production].

Science.gov (United States)

He, Qiu-Sheng; Wang, Xin-Ming; Sheng, Guo-Ying; Fu, Jia-Mo

2005-09-01

Monoaromatic hydrocarbons (MAHs) from indigenous and industrial coking processes are studied in Shanxi province. They are sampled on the top of coke ovens and in the chimneys using stainless steel canister and determined by GC/MSD after preconcentration with liquid nitrogen. Benzene, toluene and xylene are the main components among MAHs emitted from coking processes. Benzene and the total MAHs concentrations were as high as 3421.0 microg/m3 and 4 865.9 microg/m3 in the air from indigenous coking, 548.7 microg/m3 and 1 054.8 microg/m3 in the oventop air from industrial coking, and 1 376.4 microg/m3 and 1 819.4 microg/m3 in stack gas from industrial coking, respectively. The MAHs concentrations vary greatly during the indigenous coking process, which in the prophase (from firing to 10 days) is obviously higher than in the anaphase (10 days to quenching the coke). In industrial coking the MAHs in the oventop air are highest when charging the coal and next when transferring the hot coke, but in stack gas they are highest when charging coal and lowest when transferring the coke. Benzene, toluene, ethylbenzene and xylene (BTEX) in industrial coking samples show good linearity, indicating that MAHs in industrial coking might come predominantly from coal pyrolysis; but BTEX distribute dispersedly in indigenous coking samples, indicating that its emission might be affected by many factors. In all samples BTEX ratios especially high B/E ratio, is unique among MAHs sources, and might be helpful to characterize pollution from coking.

Major growth in coke production takes place

International Nuclear Information System (INIS)

Swain, E.J.

1991-01-01

U.S. petroleum coke production has increased 64% during the 10-year period from 1980 to 1990. This dramatic rise makes it timely to discuss the history and future of U.S. coking capacity, production, and processing. The article covers the properties and uses of the various grades of petroleum coke, as well as pricing and market trends

Effect of oxide film of heat resistant alloy on coke formation during naphtha pyrolysis

International Nuclear Information System (INIS)

Shiratori, Nobuo; Hosoya, Keizo

2002-01-01

The coking of cracking furnace tubes has been an important subject of ethylene plants. The coke formations rate on the heat resistant alloys of 20Cr-4.5Al-0.5Y 2 O 3 covered with Al 2 O 3 oxide film and 25Cr-35Ni covered with Cr 2 O 3 oxide film during the thermal cracking of naphtha was quantitatively evaluated at temperatures ranging from 810 to 930 .deg. C. The experimental results showed that the coke formation rate on 20Cr-4.5Al-0.5Y 2 O 3 was lower than that on 25Cr-35Ni because of the difference of a catalytic activity to coke formation, especially in the case of a pre-carburized condition. Namely, the Al 2 O 3 formed on 20Cr-4.5Al-0.5Y 2 O 3 was stable even after carburization treatment and inert for catalytic coke formation, while coke formation on 25Cr-35Ni was under the control of catalytic coke formation, and carburization of 25Cr-35Ni accelerated catalytic coke formation. The stability of Al 2 O 3 and Cr 2 O 3 in a hydrocarbon with steam environment was thermodynamically calculated in 0.1mol of steam, 0.2mol of ethylene and 0.1mol of methane at 1,100 .deg. C. The simulation result shows that Al 2 O 3 is exceedingly stable while Cr 2 O 3 could be decomposed partially into chromium carbide. Therefore, it is concluded that Al 2 O 3 on 20Cr-4.5Al-0.5Y 2 O 3 is more stable than Cr 2 O 3 on 25Cr-35Ni, and 20Cr-4.5Al-0.5Y 2 O 3 is more resistant to coke formation and carburization than 25Cr-35Ni in a hydrocarbon with steam environment at high temperature

Cancer mortality among coke oven workers.

OpenAIRE

Redmond, C K

1983-01-01

The OSHA standard for coke oven emissions, which went into effect in January 1977, sets a permissible exposure limit to coke oven emissions of 150 micrograms/m3 benzene-soluble fraction of total particulate matter (BSFTPM). Review of the epidemiologic evidence for the standard indicates an excess relative risk for lung cancer as high as 16-fold in topside coke oven workers with 15 years of exposure or more. There is also evidence for a consistent dose-response relationship in lung cancer mort...

Waste Isolation Pilot Plant Overview

Energy Technology Data Exchange (ETDEWEB)

Weaver, Douglas James [Los Alamos National Lab. (LANL), Los Alamos, NM (United States)

2017-03-27

The mission of Waste Isolation Pilot Plant (WIPP) is to demonstrate the safe, environmentally sound, cost effective, permanent disposal of Transuranic (TRU) waste left from production of nuclear weapons.

Characterisation of coking activity during supercritical hydrocarbon pyrolysis

Energy Technology Data Exchange (ETDEWEB)

Gascoin, Nicolas; Gillard, Philippe; Bernard, Stephane [Laboratoire Energetique, Explosion, Structure, UPRES-EA 1205, 63, avenue de Lattre de Tassigny, 18020 Bourges Cedex (France); Bouchez, Marc [MBDA France, 8, rue Le Brix, 18000 Bourges (France)

2008-12-15

The active cooling of the Supersonic Combustion Ramjet engine, for hypersonic flight purpose, is ensured thanks to fuel, n-dodecane for the present study. The endothermic fuel pyrolysis, starting above 800 K, could generate an unwanted coke formation. Experimental tests up to 1125 K and between 1 MPa and 6 MPa have been performed on the hydrocarbon fuel pyrolysis to evaluate the coking activity. 316L stainless steel, low carbon steel and titanium reactors have been considered. A witness of the coke formation, based on its thermal insulation and pressure loss effects, has been found. A correlation between methane production and coke deposit was found. The coke has been studied with Scanning Electron Microscope (SEM), Energy Dispersion Spectroscopy (EDS), X-ray diffractometer and Fourier Transform Infrared (FTIR) spectroscopy. The porosity, the density and the permeability of the coke have been estimated. (author)

Waste from decommissioning of nuclear power plants

International Nuclear Information System (INIS)

Nielsen, P.O.

1992-05-01

This report is based on the assumption that all twelve nuclear power plants will be shut down no later than A.D. 2010, as was decided by the parliament after the referendum on the future of nuclear power in Sweden. The recent 'Party agreement on the energy policy' of January 15, 1991 does, indeed, leave the door open for an extension of the operational period for the nuclear reactors. This will, however, not change the recommendations and conclusions drawn in this report. The report consists of two parts. Part 1 discusses classification of waste from decommissioning and makes comparisons with the waste arising from reactor operation. Part 2 discusses the documentation required for decommissioning waste. Also this part of the report draws parallels with the documentation required by the authorities for the radioactive waste arising from operation of the nuclear power plants. To some extent these subjects depend on the future use of the nuclear power plant sites after decommissioning of the plants. The options for future site use are briefly discussed in an appendix to the report. There are many similarities between the waste from reactor operations and the waste arising from dismantling and removal of decommissioned nuclear power plants. Hence it seems natural to apply the same criteria and recommendations to decommissioning waste as those presently applicable to reactor waste. This is certainly true also with respect to documentation, and it is strongly recommended that the documentation requirements on decommissioning waste are made identical, or at least similar, to the documentation requirements for reactor waste in force today. (au)

Genesis of natural cokes: Some Indian examples

Energy Technology Data Exchange (ETDEWEB)

Singh, Ashok K.; Sharma, Mamta [Central Institute of Mining and Fuel Research, Dhanbad, PIN-828108 (India); Singh, Mahendra P. [Banaras Hindu University, Varanasi, PIN-221005 (India)

2008-06-13

In Indian coalfields huge amounts of natural coke have been produced due to magmatic intrusions. Jharia Coalfield in eastern part of India alone contains approximately 2000 Mt of baked coking coal as a consequence of these intrusions in the form of discordant and concordant bodies. This paper is an effort to investigate the effect of carbonization in two intrusion affected coal seams of Ena (seam XIII) and Alkusa (seam XIV) collieries of Jharia Coalfield. Natural coke is derived from coking coal under in-situ conditions due to intense magmatic induced heat and overburden pressure. Natural coke is characterized by the presence of low volatile matter and high ash contents and organic constituents showing isotropy and anisotropy. Through physical, petrographic and chemical properties of natural coke or 'jhama' as determined by various methods it has been established that the reactives in the unaltered coals (vitrinite, liptinite, pseudovitrinite, reactive semifusinite, etc.) are < 25.0 vol.%, moisture < 2.5%, volatile matter < 15.0% and hydrogen < 4.0%. The temperatures attained in the coal seams have been deciphered using some standard models, which indicate that a temperature {proportional_to} 1000 C was attained. This produced huge amount of anisotropic and deposited carbons. An attempt has been made to understand the factors that influence the genesis of natural coke and heat altered maceral products in coals in Indian coalfields. (author)

Scientific and technical problems in the production of coke

Energy Technology Data Exchange (ETDEWEB)

Glushchenko, I M

1979-05-01

This paper lists several scientific and technological problems facing the producers of coke in the future. The demand for coke on the world market is steadily increasing despite the efforts of metallurgists to find non-coke methods of ore smelting. The major problems are held to be the gap between very successful results of research and the lack of their application to industry, unsatisfactory coke oven construction, problems in quenching and imperfections in the formed coke process. (In Russian)

ORNL process waste treatment plant modifications

International Nuclear Information System (INIS)

Bell, J.P.

1982-01-01

The ORNL Process Waste Treatment Plant removes low levels of radionuclides (primarily Cs-137 and Sr-90) from process waste water prior to discharge. The previous plant operation used a scavenging precipitaton - ion exchange process which produced a radioactive sludge. In order to eliminate the environmental problems associated with sludge disposal, the plant is being converted to a new ion exchange process without the precipitation process

Y-12 Plant waste minimization strategy

International Nuclear Information System (INIS)

Kane, M.A.

1987-01-01

The 1984 Amendments to the Resource Conservation and Recovery Act (RCRA) mandate that waste minimization be a major element of hazardous waste management. In response to this mandate and the increasing costs for waste treatment, storage, and disposal, the Oak Ridge Y-12 Plant developed a waste minimization program to encompass all types of wastes. Thus, waste minimization has become an integral part of the overall waste management program. Unlike traditional approaches, waste minimization focuses on controlling waste at the beginning of production instead of the end. This approach includes: (1) substituting nonhazardous process materials for hazardous ones, (2) recycling or reusing waste effluents, (3) segregating nonhazardous waste from hazardous and radioactive waste, and (4) modifying processes to generate less waste or less toxic waste. An effective waste minimization program must provide the appropriate incentives for generators to reduce their waste and provide the necessary support mechanisms to identify opportunities for waste minimization. This presentation focuses on the Y-12 Plant's strategy to implement a comprehensive waste minimization program. This approach consists of four major program elements: (1) promotional campaign, (2) process evaluation for waste minimization opportunities, (3) waste generation tracking system, and (4) information exchange network. The presentation also examines some of the accomplishments of the program and issues which need to be resolved

Bacterial community compositions of coking wastewater treatment plants in steel industry revealed by Illumina high-throughput sequencing.

Science.gov (United States)

Ma, Qiao; Qu, Yuanyuan; Shen, Wenli; Zhang, Zhaojing; Wang, Jingwei; Liu, Ziyan; Li, Duanxing; Li, Huijie; Zhou, Jiti

2015-03-01

In this study, Illumina high-throughput sequencing was used to reveal the community structures of nine coking wastewater treatment plants (CWWTPs) in China for the first time. The sludge systems exhibited a similar community composition at each taxonomic level. Compared to previous studies, some of the core genera in municipal wastewater treatment plants such as Zoogloea, Prosthecobacter and Gp6 were detected as minor species. Thiobacillus (20.83%), Comamonas (6.58%), Thauera (4.02%), Azoarcus (7.78%) and Rhodoplanes (1.42%) were the dominant genera shared by at least six CWWTPs. The percentages of autotrophic ammonia-oxidizing bacteria and nitrite-oxidizing bacteria were unexpectedly low, which were verified by both real-time PCR and fluorescence in situ hybridization analyses. Hierarchical clustering and canonical correspondence analysis indicated that operation mode, flow rate and temperature might be the key factors in community formation. This study provides new insights into our understanding of microbial community compositions and structures of CWWTPs. Copyright © 2014 Elsevier Ltd. All rights reserved.

ORGANIC WASTE USED IN AGRICULTURAL BIOGAS PLANTS

OpenAIRE

Joanna Kazimierowicz

2014-01-01

Treatment of organic waste is an ecological and economical problem. Searching method for disposal of these wastes, interest is methane fermentation. The use of this process in agricultural biogas plants allows disposal of hazardous waste, obtaining valuable fertilizer, while the production of ecologically clean fuel – biogas. The article presents the characteristics of organic waste from various industries, which make them suitable for use as substrates in agricultural biogas plants.

Coke fouling monitoring by electrical resistivity

Energy Technology Data Exchange (ETDEWEB)

Bombardelli, Clovis; Mari, Livia Assis; Kalinowski, Hypolito Jose [Universidade Tecnologica Federal do Parana (UTFPR), Curitiba, PR (Brazil). Programa de Pos-Graduacao em Engenharia Eletrica e Informatica Industrial (CPGEI)

2008-07-01

An experimental method to simulate the growth of the coke fouling that occurs in the oil processing is proposed relating the thickness of the encrusted coke to its electrical resistivity. The authors suggest the use of the fouling electrical resistivity as a transducer element for determining its thickness. The sensor is basically two electrodes in an electrically isolated device where the inlay can happen in order to compose a purely resistive transducer. Such devices can be easily constructed in a simple and robust form with features capable to face the high temperatures and pressures found in relevant industrial processes. For validation, however, it is needed a relationship between the electrical resistivity and the fouling thickness, information not yet found in the literature. The present work experimentally simulates the growth of a layer of coke on an electrically insulating surface, equipped with electrodes at two extremities to measure the electrical resistivity during thermal cracking essays. The method is realized with a series of consecutive runs. The results correlate the mass of coke deposited and its electrical resistivity, and it can be used to validate the coke depositions monitoring employing the resistivity as a control parameter. (author)

Development of waste water reuse water system for power plants

Energy Technology Data Exchange (ETDEWEB)

Park, K K; Kim, D H; Weon, D Y; Yoon, S W; Song, H R [Korea Electric Power Research Institute, Taejeon (Korea, Republic of)

1998-12-31

1. Status of waste water discharge at power plants 2. Present status of waste water reuse at power plants 3. Scheme of waste water reuse at power plants 4. Standardization of optimum system for waste water reuse at power plants 5. Establishment of low cost zero discharge system for waste water 6. Waste water treatment technology of chemical cleaning. (author). 132 figs., 72 tabs.

Development of waste water reuse water system for power plants

Energy Technology Data Exchange (ETDEWEB)

Park, K.K.; Kim, D.H.; Weon, D.Y.; Yoon, S.W.; Song, H.R. [Korea Electric Power Research Institute, Taejeon (Korea, Republic of)

1997-12-31

1. Status of waste water discharge at power plants 2. Present status of waste water reuse at power plants 3. Scheme of waste water reuse at power plants 4. Standardization of optimum system for waste water reuse at power plants 5. Establishment of low cost zero discharge system for waste water 6. Waste water treatment technology of chemical cleaning. (author). 132 figs., 72 tabs.

Fundamentals of Delayed Coking Joint Industry Project

Energy Technology Data Exchange (ETDEWEB)

Michael Volk; Keith Wisecarver

2003-09-26

Delayed coking evolved steadily over the early to mid 1900s to enable refiners to convert high boiling, residual petroleum fractions to light products such as gasoline. Pound for pound, coking is the most energy intensive of any operation in a modern refinery. Large amounts of energy are required to heat the thick, poor-quality petroleum residuum to the 900 to 950 degrees F required to crack the heavy hydrocarbon molecules into lighter, more valuable products. One common misconception of delayed coking is that the product coke is a disadvantage. Although coke is a low valued (near zero economic value) byproduct, compared to transportation fuels, there is a significant worldwide trade and demand for coke as it is an economical fuel. Coke production has increased steadily over the last ten years, with further increases forecast for the foreseeable future. Current domestic production is near 111,000 tons per day. A major driving force behind this increase is the steady decline in crude quality available to refiners. Crude slates are expected to grow heavier with higher sulfur contents while environmental restrictions are expected to significantly reduce the demand for high-sulfur residual fuel oil. Light sweet crudes will continue to be available and in even greater demand than they are today. Refiners will be faced with the choice of purchasing light sweet crudes at a premium price, or adding bottom of the barrel upgrading capability, through additional new investments, to reduce the production of high-sulfur residual fuel oil and increase the production of low-sulfur distillate fuels. A second disadvantage is that liquid products from cokers frequently are unstable, i.e., they rapidly form gum and sediments. Because of intermediate investment and operating costs, delayed coking has increased in popularity among refiners worldwide. Based on the 2000 Worldwide Refining Survey published in the Oil and Gas, the delayed coking capacity for 101 refineries around the world

Hanford Waste Vitrification Plant Quality Assurance Program description for high-level waste form development and qualification

International Nuclear Information System (INIS)

1993-08-01

The Hanford Waste Vitrification Plant Project has been established to convert the high-level radioactive waste associated with nuclear defense production at the Hanford Site into a waste form suitable for disposal in a deep geologic repository. The Hanford Waste Vitrification Plant will mix processed radioactive waste with borosilicate material, then heat the mixture to its melting point (vitrification) to forin a glass-like substance that traps the radionuclides in the glass matrix upon cooling. The Hanford Waste Vitrification Plant Quality Assurance Program has been established to support the mission of the Hanford Waste Vitrification Plant. This Quality Assurance Program Description has been written to document the Hanford Waste Vitrification Plant Quality Assurance Program

Coke Formation During Hydrocarbons Pyrolysis. Part One: Steam Cracking Formation de coke pendant la pyrolise des hydrocarbures. Première partie : vapocraquage

Directory of Open Access Journals (Sweden)

Weill J.

2006-11-01

Full Text Available Thermal cracking is always accompanied by coke formation, which becomes deposited on the wall and limits heat transfers in the reactor while increasing pressure drops and possibly even plugging up the reactor. This review article covers undesirable coking operations in steam craking reactors. These coking reactions may take place in the gas phase and/or on the surface of the reactor, with coke being produced during pyrolysis by a complex mechanism that breaks down into a catalytic sequence and a noncatalytic sequence. After a brief description of different experimental set-ups used to measure the coke deposition, on the basis of research described in the literature, the different factors and their importance for coke formation are listed. In particular, we describe the effects of surface properties of stainless-steel and quartz reactors as well as the influence of the cracked feedstock, of temperature, of dilution, of residence time and of the conversion on coke deposition. Some findings about the morphology of coke are described and linked to formation mechanisms. To illustrate this review, some particularly interesting research is referred to concerning models developed to assess coke formation during propane steam cracking. Le craquage thermique est toujours accompagné de la formation de coke qui, en se déposant à la paroi, limite les transferts de chaleur au réacteur, augmente les pertes de charges et même peut boucher celui-ci. Cet article fait le point sur les réactions indésirables de cokage dans les réacteurs de vapocraquage. Ces réactions de cokage peuvent avoir lieu en phase gazeuse et/ou sur la surface du réacteur, le coke étant produit pendant la pyrolyse par un mécanisme complexe qui se décompose en une séquence catalytique et une séquence non catalytique. Après une brève présentation des différents montages expérimentaux utilisés pour mesurer le dépôt de coke, il est mentionné, à partir de travaux de la

ORGANIC WASTE USED IN AGRICULTURAL BIOGAS PLANTS

Directory of Open Access Journals (Sweden)

Joanna Kazimierowicz

2014-04-01

Full Text Available Treatment of organic waste is an ecological and economical problem. Searching method for disposal of these wastes, interest is methane fermentation. The use of this process in agricultural biogas plants allows disposal of hazardous waste, obtaining valuable fertilizer, while the production of ecologically clean fuel – biogas. The article presents the characteristics of organic waste from various industries, which make them suitable for use as substrates in agricultural biogas plants.

Clean utilization of high sulphur petroleum coke by circulating fluidized bed combustion (CFBC) in Romania

International Nuclear Information System (INIS)

Dragos, L.; Flueraru, C.; Girjoaba, M.

1996-01-01

The economic and environmental problems caused by inefficient utilization of residual high-sulphur petroleum coke resulted from oil cracking in Romania is discussed. A special research programme applying CFBC technology has been carried out in the Institute for Power Equipment, Bucharest. The results from both laboratory facilities and pilot plant are presented. The main operating conditions and parameters are pointed out. Data on quality and composition of petroleum coke, combustion efficiency, temperature range in different zones and flue gas composition at distinct operating loads are given. The results obtained will be used for innovative design of CFBC boilers based on petroleum coke. A project for implementing a CFBC boiler in one of the Romanian oil refineries is being developed. An analysis of technical and economic advantages of these boilers for energy generation is presented

Safety in waste management plants: An Indian perspective

International Nuclear Information System (INIS)

Shekhar, P.; Ozarde, P.D.; Gandhi, P.M.

2000-01-01

Assurance of safety of public and plant workers and protection of the environment are prime objectives in the design and construction of Waste Management Plants. In India, waste management principles and strategies have been evolved in accordance with national and international regulations and standards for radiation protection. The regulations governing radiation protection have a far-reaching impact on the management of the radioactive waste. The wastes arise at each stages of the fuel cycle with varying chemical nature, generation rate and specific activity levels depending upon the type of the facility. Segregation of waste based on its chemical nature and specific activity levels is an essential feature, as its aids in selection of treatment and conditioning process. Selection of the process, equipment and materials in the plant, are governed by safety consideration alongside factors like efficiency and simplicity. The plant design considerations like physical separation, general arrangement, ventilation zoning, access control, remote handling, process piping routing, decontamination etc. have major role in realizing waste safety. Stringent quality control measures during all stages of construction have helped in achieving the design intended safety. These aspects together with operating experience gained form basis for the improved safety features in the design and construction of waste management plants. The comprehensive safety is derived from adoption of waste management strategies and appropriate plant design considerations. The paper briefly brings safety in waste management programme in India, in its current perspective. (author)

Rapid production of metallurgical coke by a pressurized hot-briquetting method. Netsukan kaatsu seikei ni yoru cokes no jinsoku seizo no kokoromi

Energy Technology Data Exchange (ETDEWEB)

Miura, K.; Hayashi, J.; Noguchi, N. (Kyoto University, Kyoto (Japan). Research Laboratory of Carbonaceous Resources Conversion Technology); Hashimoto, K. (Kyoto University, Kyoto (Japan). Faculty of Engineering)

1993-09-20

Rapid production of metallurgical coke from non- and slightly coking coals was studied by pressurized hot-briquetting method. Coal specimens were filled into the mold after pulverizing, and heated at a constant temperature rise rate up to caking temperature under loading pressure to obtain caked coal specimens. Such specimens were then carbonized in nitrogen gas at 800[degree]C. As a result, the coke obtained was superior in compressive strength as compared with commercial cokes, however, its CO2 reactivity was very high requiring heating up to 1,000[degree]C to decrease it, while the reactivity was strongly dependent on coal kind. The optimum processing conditions for slightly coking coal were as follows; loading pressure: 10 [times] 10[sup 5] Pa or more, temperature range under loading pressure: 300-450[degree]C, temperature rise rate: 2-100[degree]C/min, and caking temperature: nearly 500[degree]C. No coke could be produced from coking coals because no volatile matter could be removed from it in a short time under pressure. 13 refs., 8 figs., 1 tab.

WIPP: Waste Isolation Pilot Plant

International Nuclear Information System (INIS)

1984-01-01

The following aspects of the Waste Isolation Pilot Plant are discussed briefly: history and site selection; salt as a disposal medium; transporting waste materials; early key events; impacts on New Mexico; project organization; and site certification profile

The world coke market. Problems and outlook

International Nuclear Information System (INIS)

Anon.

1998-01-01

Outlooks to the world coke market are considered with regard to supply and demand as well as the current state of capacities for its production in some countries of Asia, Western and Eastern Europe, USA. In experts opinion increase of coke import from China, increase in service life of currently operating coke furnaces, as well as more extensive use of PCI coal mixture are among the most feasible opportunities for its Western consumers [ru

Coke industry and steel metallurgy as the source of soil contamination by technogenic magnetic particles, heavy metals and polycyclic aromatic hydrocarbons.

Science.gov (United States)

Rachwał, Marzena; Magiera, Tadeusz; Wawer, Małgorzata

2015-11-01

Application of integrated magnetic, geochemical and mineralogical methods for qualitative and quantitative assessment of forest topsoils exposed to the industrial emissions was the objective of this manuscript. Volume magnetic susceptibility (κ) in three areas of southern Poland close to the coke and metallurgical plants was measured directly in the field. Representative topsoil samples were collected for further chemical and mineralogical analyses. Topsoil magnetic susceptibility in the studied areas depended mainly on the content of technogenic magnetic particles (TMPs) and decreased downwind at increasing distance from the emitters. In the vicinity of coking plants a high amount of polycyclic aromatic hydrocarbons (PAHs) was observed, especially the most carcinogenic ones with four- and five-member rings. No significant concentration of TMPs (estimated on the base of κ values) and heavy metals (HM) was observed in area where the coke plant was the only pollution source. In areas with both coke and metallurgical industry, higher amounts of TMPs, PAHs and HM were detected. Morphological and mineralogical analyses of TMPs separated from contaminated soil samples revealed their high heterogeneity in respect of morphology, grain size, mineral and chemical constitution. Pollution load index and toxicity equivalent concentration of PAHs used for soil quality assessment indicated its high level of pollution. Copyright © 2014 Elsevier Ltd. All rights reserved.

Waste processing system for nuclear power plant

International Nuclear Information System (INIS)

Higashinakagawa, Emiko; Tezuka, Fuminobu; Maesawa, Yukishige; Irie, Hiromitsu; Daibu, Etsuji.

1996-01-01

The present invention concerns a waste processing system of a nuclear power plant, which can reduce the volume of a large amount of plastics without burying them. Among burnable wastes and plastic wastes to be discarded in the power plant located on the sea side, the plastic wastes are heated and converted into oils, and the burnable wastes are burnt using the oils as a fuel. The system is based on the finding that the presence of Na 2 O, K 2 O contained in the wastes catalytically improves the efficiency of thermal decomposition in a heating atmosphere, in the method of heating plastics and converting them into oils. (T.M.)

New formulae for the manufacture of formed coke of the ICEM type and carbonization of this type of coke in oblique ovens

Energy Technology Data Exchange (ETDEWEB)

Barbu, I.; Georgescu, I.

1978-01-01

This paper presents the industrial experiences between 1971 and 1976 which led to the elaboration of new formulae for the manufacture of ICEM type coke briquettes, plus the results of coking the latter in a vertical oven. The possibility of using this type of coke in the chemical industry and in metallurgy instead of ordinary coke was simultaneously examined but this proved unsuccessful. Gives a detailed report of all the tests carried out by the State undertaking, Victoria-Galan.

Evaluation of coke microstructure and its effects on graphite fabrication

International Nuclear Information System (INIS)

Fotourehchian, S.; Ahmadi, S.

2001-01-01

A variety of applications for cokes (metallurgy, petroleum, etc.) have been defined in parallel to the new industrial technology growth. Coke is rich in carbon and has the main role in manufacturing carbonaceous materials such as graphite, steel, silicon carbide, titanium carbide, etc. Among the most important applications of different variety of cokes is their usage for different graphite fabrications. The crystalline structure of graphite (hexagonal with sp 2 hybrid) is based upon the microstructure of coke and it causes anisotropy in properties of produced graphite. Thus, the study of macrostructure and anisotropy degree of cokes is of importance. There are several theoretical and experimental methods to determine the Coke's microstructure and anisotropy. Numerous tests have been conducted on different variety of cokes based on the used method. Here, it is attempted to introduce an applied method to determine the microstructure and anisotropy degree of cokes based upon the kind of application

Study on the Inference Factors of Huangling Coking Coal Pyrolysis

Science.gov (United States)

Du, Meili; Yang, Zongyi; Fan, Jinwen

2018-01-01

In order to reasonably and efficiently utilize Huangling coking coal resource, coal particle, heating rate, holding time, pyrolysis temperature and others factors were dicussed for the influence of those factor on Huangling coking coal pyrolysis products. Several kinds of coal blending for coking experiments were carried out with different kinds of coal such as Huangling coking coal, Xida coal with high ash low sufur, Xinghuo fat coal with hign sulfur, Zhongxingyi coking coal with high sulfur, Hucun lean coal, mixed meager and lean coal. The results shown that the optimal coal particle size distribution was 0.5~1.5mm, the optimal heating rate was 8°C/min, the optimal holding time was 15min, the optimal pyrolysis temperature was 800°C for Huangling coking coal pyrolysis, the tar yield increased from 4.7% to 11.2%. The maximum tar yield of coal blending for coking under the best single factor experiment condition was 10.65% when the proportio of Huangling coking coal was 52%.

Upgrading oil sands bitumen with FLUID COKING and FLEXICOKING technologies

Energy Technology Data Exchange (ETDEWEB)

Kamienski, P.; Phillips, G. [ExxonMobil Research and Engineering Co., Fairfax, VA (United States); McKnight, C.; Rumball, B. [Syncrude Canada Ltd., Calgary, AB (Canada)

2009-07-01

This presentation described EMRE's Fluid Coking and Flexicoking technologies that are well suited for upgrading Alberta's heavy crudes and oil sands bitumen into pipelineable crudes or synthetic crudes, which can be further processed into transportation fuels. The Fluid Coking technology uses a fluidized bed reactor that thermally converts the heavy oils into light gases, liquids and coke. The metals and much of the sulphur are concentrated in the coke. Combustion of the coke provides process heat and the remaining coke is sold or stored on site for later recovery. Syncrude Canada currently operates 3 Fluid Coking units in northern Alberta. Flexicoking extends fluid coking by integrating air gasification to produce a carbon monoxide/hydrogen rich fuel gas that helps meet fuel and energy requirements of bitumen recovery and upgrading. The yields of light gas and liquids are similar to those of the Fluid Coking process. The partial combustion of coke provides the process heat for the thermal conversion and gasification steps. The remaining coke is gasified and desulphurized using Flexsorb technology. At present, there are 5 Flexicoking units in operation around the world. Interest in the technology is growing, particularly in locations with large demand for clean fuel or electricity. It is also suitable for steam assisted gravity drainage (SAGD) operations in Alberta. This presentation outlined the operating principles of the Flexicoking integrated gasification system and compared it with more expensive oxygen gasification processes. tabs., figs.

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.

Hanford Waste Vitrification Plant

International Nuclear Information System (INIS)

Larson, D.E.; Allen, C.R.; Kruger, O.L.; Weber, E.T.

1991-10-01

The Hanford Waste Vitrification Plant (HWVP) is being designed to immobilize pretreated Hanford high-level waste and transuranic waste in borosilicate glass contained in stainless steel canisters. Testing is being conducted in the HWVP Technology Development Project to ensure that adapted technologies are applicable to the candidate Hanford wastes and to generate information for waste form qualification. Empirical modeling is being conducted to define a glass composition range consistent with process and waste form qualification requirements. Laboratory studies are conducted to determine process stream properties, characterize the redox chemistry of the melter feed as a basis for controlling melt foaming and evaluate zeolite sorption materials for process waste treatment. Pilot-scale tests have been performed with simulated melter feed to access filtration for solids removal from process wastes, evaluate vitrification process performance and assess offgas equipment performance. Process equipment construction materials are being selected based on literature review, corrosion testing, and performance in pilot-scale testing. 3 figs., 6 tabs

Hanford Waste Vitrification Plant technical manual

Energy Technology Data Exchange (ETDEWEB)

Larson, D.E. [ed.; Watrous, R.A.; Kruger, O.L. [and others

1996-03-01

A key element of the Hanford waste management strategy is the construction of a new facility, the Hanford Waste Vitrification Plant (HWVP), to vitrify existing and future liquid high-level waste produced by defense activities at the Hanford Site. The HWVP mission is to vitrify pretreated waste in borosilicate glass, cast the glass into stainless steel canisters, and store the canisters at the Hanford Site until they are shipped to a federal geological repository. The HWVP Technical Manual (Manual) documents the technical bases of the current HWVP process and provides a physical description of the related equipment and the plant. The immediate purpose of the document is to provide the technical bases for preparation of project baseline documents that will be used to direct the Title 1 and Title 2 design by the A/E, Fluor. The content of the Manual is organized in the following manner. Chapter 1.0 contains the background and context within which the HWVP was designed. Chapter 2.0 describes the site, plant, equipment and supporting services and provides the context for application of the process information in the Manual. Chapter 3.0 provides plant feed and product requirements, which are primary process bases for plant operation. Chapter 4.0 summarizes the technology for each plant process. Chapter 5.0 describes the engineering principles for designing major types of HWVP equipment. Chapter 6.0 describes the general safety aspects of the plant and process to assist in safe and prudent facility operation. Chapter 7.0 includes a description of the waste form qualification program and data. Chapter 8.0 indicates the current status of quality assurance requirements for the Manual. The Appendices provide data that are too extensive to be placed in the main text, such as extensive tables and sets of figures. The Manual is a revision of the 1987 version.

Hanford Waste Vitrification Plant technical manual

International Nuclear Information System (INIS)

Larson, D.E.; Watrous, R.A.; Kruger, O.L.

1996-03-01

A key element of the Hanford waste management strategy is the construction of a new facility, the Hanford Waste Vitrification Plant (HWVP), to vitrify existing and future liquid high-level waste produced by defense activities at the Hanford Site. The HWVP mission is to vitrify pretreated waste in borosilicate glass, cast the glass into stainless steel canisters, and store the canisters at the Hanford Site until they are shipped to a federal geological repository. The HWVP Technical Manual (Manual) documents the technical bases of the current HWVP process and provides a physical description of the related equipment and the plant. The immediate purpose of the document is to provide the technical bases for preparation of project baseline documents that will be used to direct the Title 1 and Title 2 design by the A/E, Fluor. The content of the Manual is organized in the following manner. Chapter 1.0 contains the background and context within which the HWVP was designed. Chapter 2.0 describes the site, plant, equipment and supporting services and provides the context for application of the process information in the Manual. Chapter 3.0 provides plant feed and product requirements, which are primary process bases for plant operation. Chapter 4.0 summarizes the technology for each plant process. Chapter 5.0 describes the engineering principles for designing major types of HWVP equipment. Chapter 6.0 describes the general safety aspects of the plant and process to assist in safe and prudent facility operation. Chapter 7.0 includes a description of the waste form qualification program and data. Chapter 8.0 indicates the current status of quality assurance requirements for the Manual. The Appendices provide data that are too extensive to be placed in the main text, such as extensive tables and sets of figures. The Manual is a revision of the 1987 version

Operation car for horizontal coke ovens. Bedienungswagen fuer waagrechte Verkokungsoefen

Energy Technology Data Exchange (ETDEWEB)

Kwasnik, H J; Piduch, H G

1981-07-30

An operation car which is driveable on the coke side of a coke oven battery is described. The operation car is equipped with a door lifter, a door and frame cleaner, a coke guiding grid and a collection hood for emissions developed on coke pushing. The car has a portal construction and it is driveable on both sides of the path of the coke receiving car. The operation has a considerable lower weight than usual cars. (HGOE).

Solidification of Savannah River Plant high-level waste

International Nuclear Information System (INIS)

Maher, R.; Shafranek, L.F.; Stevens, W.R. III.

1983-01-01

The Department of Energy, in accord with recommendations from the Du Pont Company, has started construction of a Defense Waste Processing Facility (DWPF) at the Savannah River Plant. The facility should be completed by the end of 1988, and full-scale operation should begin in 1990. This facility will immobilize in borosilicate glass the large quantity of high-level radioactive waste now stored at the plant plus the waste to be generated from continued chemical reprocessing operations. The existing wastes at the Savannah River Plant will be completely converted by about 2010. 21 figures

Utilization of formed coke from HBNPC in the Dunkerque blast furnaces

Energy Technology Data Exchange (ETDEWEB)

Le Scour, C; Capelani, R

1978-01-01

Recalls the aspects involved in the manufacture of formed coke together with the coke characteristics. Describes the features of blast-furnaces No. 1 and No. 2 at Dunkerque. The blend used for producing the ovoids is composed of 70 to 80% non-coking coal and the ovoids are carbonized at 900 C. The first stage of the tests was carried out with 25% formed coke and the second stage with 22%. The formed coke was charged separately. The results were as follows: the coke rate was comparable and the permeability identical; there was no change in the behaviour of the furnace chamber and no problems were experienced at the hearth stage. The replacement of 30% of the conventional coke by HBNPC formed coke seemed a practical proposition.

Process for the preparation of isotropic petroleum coke

International Nuclear Information System (INIS)

Kegler, W.H.; Huyser, M.E.

1975-01-01

A description is given of a process for preparing isotropic coke from oil residue charge. It includes blowing air into the residue until it reaches a softening temperature of around 49 to 116 deg C, the deferred coking of the residue having undergone blowing at a temperature of around 247 to 640 deg C, at a pressure between around 1.38x10 5 and 1.72x10 6 Pa, and the recovery of isotropic coke with a thermal expansion coefficient ratio under 1.5 approximately. The isotropic coke is used for preparing hexagonal graphite bars for nuclear reactor moderators [fr

Reducing dust emissions at OAO Alchevskkoks coke battery 10A

Energy Technology Data Exchange (ETDEWEB)

T.F. Trembach; E.N. Lanina [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15

Coke battery 10A with rammed batch is under construction at OAO Alchevskkoks. The design documentation developed by Giprokoks includes measures for reducing dust emissions to the atmosphere. Aspiration systems with dry dust trapping are employed in the new components of coke battery 10A and in the existing coke-sorting equipment. Two-stage purification of dusty air in cyclones and bag filters is employed for the coke-sorting equipment. This system considerably reduces coke-dust emissions to the atmosphere.

Fundamentals of Delayed Coking Joint Industry Project

Energy Technology Data Exchange (ETDEWEB)

Michael Volk Jr; Keith Wisecarver

2005-10-01

Delayed coking evolved steadily over the early to mid 1900s to enable refiners to convert high boiling, residual petroleum fractions to light products such as gasoline. Pound for pound, coking is the most energy intensive of any operation in a modern refinery. Large amounts of energy are required to heat the thick, poor-quality petroleum residuum to the 900 to 950 degrees F required to crack the heavy hydrocarbon molecules into lighter, more valuable products. One common misconception of delayed coking is that the product coke is a disadvantage. Although coke is a low valued (near zero economic value) byproduct, compared to transportation fuels, there is a significant worldwide trade and demand for coke as it is an economical fuel. Coke production has increased steadily over the last ten years, with further increases forecast for the foreseeable future. Current domestic production is near 111,000 tons per day. A major driving force behind this increase is the steady decline in crude quality available to refiners. Crude slates are expected to grow heavier with higher sulfur contents while environmental restrictions are expected to significantly reduce the demand for high-sulfur residual fuel oil. Light sweet crudes will continue to be available and in even greater demand than they are today. Refiners will be faced with the choice of purchasing light sweet crudes at a premium price, or adding bottom of the barrel upgrading capability, through additional new investments, to reduce the production of high-sulfur residual fuel oil and increase the production of low-sulfur distillate fuels. A second disadvantage is that liquid products from cokers frequently are unstable, i.e., they rapidly form gum and sediments. Because of intermediate investment and operating costs, delayed coking has increased in popularity among refiners worldwide. Based on the 2000 Worldwide Refining Survey published in the Oil and Gas, the delayed coking capacity for 101 refineries around the world

Statistical assessment of coal charge effect on metallurgical coke quality

Directory of Open Access Journals (Sweden)

Pavlína Pustějovská

2016-06-01

Full Text Available The paper studies coke quality. Blast furnace technique has been interested in iron ore charge; meanwhile coke was not studied because, in previous conditions, it seemed to be good enough. Nowadays, requirements for blast furnace coke has risen, especially, requirements for coke reactivity. The level of reactivity parameter is determined primarily by the composition and properties of coal mixtures for coking. The paper deals with a statistical analysis of the tightness and characteristics of the relationship between selected properties of coal mixture and coke reactivity. Software Statgraphic using both simple linear regression and multiple linear regressions was used for the calculations. Obtained regression equations provide a statistically significant prediction of the reactivity of coke, or its strength after reduction of CO2, and, thus, their subsequent management by change in composition and properties of coal mixture. There were determined indexes CSR/CRI for coke. Fifty – four results were acquired in the experimental parts where correlation between index CRI and coal components were studied. For linear regression the determinant was 55.0204%, between parameters CRI – Inertinit 21.5873%. For regression between CRI and coal components it was 31.03%. For multiple linear regression between CRI and 3 feedstock components determinant was 34.0691%. The final correlation has shown the decrease in final coke reactivity for higher ash, higher content of volatile combustible in coal increases the total coke reactivity and higher amount of inertinit in coal increases the reactivity. Generally, coke quality is significantly affected by coal processing, carbonization and maceral content of coal mixture.

The coke drum thermal kinetic effects

Energy Technology Data Exchange (ETDEWEB)

Aldescu, Maria M.; Romero, Sim; Larson, Mel [KBC Advanced Technologies plc, Surrey (United Kingdom)

2012-07-01

The coke drum thermal kinetic dynamics fundamentally affect the coker unit yields as well as the coke product properties and unit reliability. In the drum the thermal cracking and polymerization or condensation reactions take place in a semi-batch environment. Understanding the fundamentals of the foaming kinetics that occur in the coke drums is key to avoiding a foam-over that could result in a unit shutdown for several months. Although the most dynamic changes with time occur during drum filling, other dynamics of the coker process will be discussed as well. KBC has contributed towards uncovering and modelling the complexities of heavy oil thermal dynamics. (author)

A hydraulic device for unloading coke

Energy Technology Data Exchange (ETDEWEB)

Kretinin, M.V.; Abizgildin, U.M.; Kirillov, T.S.; Makarov, M.I.; Prokopov, O.I.; Solov' ev, A.M.

1979-07-15

A hydraulic device for unloading petroleum coke from slow carbonization chambers is characterized by an arrangement whereby in order to increase the output of large size coke by controlling the increment of the cutting line of the coke, the mechanism used to move the rod in the hydraulic cutter is built in the form of a rod rotation rotor; a gear wheel is mounted on the immobile section of this rotor, and on the mobile section a multi-stage regulator is installed. The drive gear of the regulator is engaged with the gear wheel, while the driven gear is connected to the rack, which is fastened to the rod.

Fatigue behaviour of coke drum materials under thermal-mechanical cyclic loading

Directory of Open Access Journals (Sweden)

Jie Chen

2014-01-01

Full Text Available Coke drums are vertical pressure vessels used in the delayed coking process in petroleum refineries. Significant temperature variation during the delayed coking process causes damage in coke drums in the form of bulging and cracking. There were some studies on the fatigue life estimation for the coke drums, but most of them were based on strain-fatigue life curves at constant temperatures, which do not consider simultaneous cyclic temperature and mechanical loading conditions. In this study, a fatigue testing system is successfully developed to allow performing thermal-mechanical fatigue (TMF test similar to the coke drum loading condition. Two commonly used base and one clad materials of coke drums are then experimentally investigated. In addition, a comparative study between isothermal and TMF lives of these materials is conducted. The experimental findings lead to better understanding of the damage mechanisms occurring in coke drums and more accurate prediction of fatigue life of coke drum materials.

Sustainable waste management: Waste to energy plant as an alternative to landfill

International Nuclear Information System (INIS)

Cucchiella, Federica; D’Adamo, Idiano; Gastaldi, Massimo

2017-01-01

Highlights: • WTE plant is a reasonable and sustainable alternative technology to landfill. • A 150 kt plant in the only electrical configuration for Abruzzo region. • The percentage of energy recovery ranges from 21% to 25% in examined scenarios. • Financial Net Present Value is equal to 25.4 € per kiloton of treated waste. • The annual reduction of emissions is equal to 370 kgCO_2eq per ton of treated waste. - Abstract: The management of municipal solid waste (MSW) has been identified as one of the global challenges that must be carefully faced in order to achieve sustainability goals. European Union (EU) has defined as Waste to Energy (WTE) technology is able to create synergies with EU energy and climate policy, without compromising the achievement of higher reuse and recycling rates. The methodology used in this paper is based on two levels. A strategy analysis defines the amount of waste to incinerate with energy recovery considering different approaches based on unsorted waste, landfilled waste and separated collection rate, respectively. Consequently, it is evaluated the sustainability of a WTE plant as an alternative to landfill for a specific area. Two indicators are used: the Reduction of the Emissions of equivalent Carbon Dioxide (ER_C_O_2_e_q) and Financial Net Present Value (FNPV). Furthermore, a social analysis is conducted through interviews to identify the most critical elements determining the aversion toward the WTE realization. The obtained results show the opportunity to realize a 150 kt plant in the only electrical configuration. In fact, the cogenerative configuration reaches better environmental performances, but it is not profitable for this size. Profits are equal to 25.4 € per kiloton of treated waste and 370 kgCO_2eq per ton of treated waste are avoided using a WTE plant as an alternative to landfill. In this way, the percentage of energy recovery ranges from 21% to 25% in examined scenarios and disposal waste is minimised

Report: environmental assessment of Darmstadt (Germany) municipal waste incineration plant.

Science.gov (United States)

Rimaityte, Ingrida; Denafas, Gintaras; Jager, Johannes

2007-04-01

The focus of this study was the emissions from waste incineration plants using Darmstadt (Germany) waste incineration plant as an example. In the study the emissions generated by incineration of the waste were considered using three different approaches. Initially the emissions from the waste incineration plant were assessed as part of the impact of waste management systems on the environment by using a Municipal Solid Waste Management System (MSWMS) assessment tool (also called: LCA-IWM assessment tool). This was followed by a comparison between the optimal waste incineration process and the real situation. Finally a comparison was made between the emissions from the incineration plant and the emissions from a vehicle.

Coking coal outlook from a coal producer's perspective

International Nuclear Information System (INIS)

Thrasher, E.

2008-01-01

Australian mine production is recovering from massive flooding while Canadian coal shipments are limited by mine and rail capacity. Polish, Czech, and Russian coking coal shipments have been reduced and United States coking coal shipments are reaching their maximum capacity. On the demand side, the Chinese government has increased export taxes on metallurgical coal, coking coal, and thermal coal. Customers seem to be purchasing in waves and steel prices are declining. This presentation addressed the global outlook for coal as well as the challenges ahead in terms of supply and demand. Supply challenges include regulatory uncertainty; environmental permitting; labor; and geology of remaining reserves. Demand challenges include global economic uncertainty; foreign exchange values; the effect of customers making direct investments in mining operations; and freight rates. Consolidation of the coal industry continued and several examples were provided. The presentation also discussed other topics such as coking coal production issues; delayed mining permits and environmental issues; coking coal contract negotiations; and stock values of coking coal producers in the United States. It was concluded that consolidation will continue throughout the natural resource sector. tabs., figs

Hanford Waste Vitrification Plant Project Waste Form Qualification Program Plan

International Nuclear Information System (INIS)

Randklev, E.H.

1993-06-01

The US Department of Energy has created a waste acceptance process to help guide the overall program for the disposal of high-level nuclear waste in a federal repository. This Waste Form Qualification Program Plan describes the hierarchy of strategies used by the Hanford Waste Vitrification Plant Project to satisfy the waste form qualification obligations of that waste acceptance process. A description of the functional relationship of the participants contributing to completing this objective is provided. The major activities, products, providers, and associated scheduling for implementing the strategies also are presented

[NH4+-N removal stability of zeolite media packed multistage-biofilm system for coke-plant wastewater treatment].

Science.gov (United States)

Zhao, Wen-Tao; Huang, Xia; He, Miao; Zhang, Peng-Yi; Zuo, Chen-Yan

2009-02-15

The practical ammonia stripping effectiveness of coke-plant wastewater treatment may vary widely, and high NH4+-N shock loading will lead to the fluctuation of residual NH4+-N concentration of biological effluent. A zeolite media packed multistage-biofilm system (ZMBS) was used for coke-plant wastewater treatment for enhancing the NH4+-N treatment ability of the bio-system to shock loading, as well as achieving high COD removal efficiency. Treatment performance during steady-state and shock loading and transformation of organic pollutants in the system were investigated systematically. The experiment results indicated that when the system was operated at NH4+-N loading 0.21 kg/(m3 x d) and COD loading NH4+-N and COD concentrations were (2.2 +/- 1.2) mg/L, (228 +/- 60) mg/L with average removal efficiencies of (99.1 +/- 0.5)% and (86.0 +/- 2.6)%. During the twice NH4+-N shock loadings [0.03 kg/(m3 x d) and 0.06 kg/(m3 x d)], ZMBS showed a strong resisting ability with average removal efficiencies of 99.0% and 92.9% higher than those of a compared system's 96.8% and 89.3%. By monitoring the change of water quality along the length of the ZMBS's cells, two function zones for different pollutant removal were found to exist, named as decarbonization/nitrification (C/N) zone and nitrification (N) zone, and the NH4+-N removal rate in N zone was 2-8 times as that in C/N zone. TOC concentrations of organic matters with relative molecular weight 1 x 10(4), were 227.6, 104.8 and 35.0 mg/L in raw wastewater, and 31.2, 22.9 and 31.5 mg/L in the effluent, respectively. Organic matters with relative molecular weight 1x 10(3) were the main remained substances in the effluent.

Recovery and removal of uranium by using plant wastes

International Nuclear Information System (INIS)

Nakajima, Akira; Sakaguchi, Takashi

1990-01-01

The uranium-adsorbing abilities of seven plant wastes were investigated. High abilities to adsorb uranium from non-saline water containing 10 mg dm -3 of uranium were observed with a number of plant wastes tested. However, with seawater supplemented with 10 mg dm -3 of uranium, similar results were found only with chestnut residues. When the plant wastes were immobilized with formaldehyde, their ability to adsorb uranium was increased. Uranium and copper ions were more readily adsorbed by all plant wastes tested than other metal ions from a solution containing a mixture of seven different heavy metals. The selective adsorption of heavy metal ions differs with different species of plant wastes. The immobilization of peanut inner skin, orange peel and grapefruit peel increased the selectivity for uranium. (author)

Renewable energy in Switzerland - Potential of waste-water treatment plants, waste-incineration plants and drinking water supply systems - Strategical decisions in politics

International Nuclear Information System (INIS)

Kernen, M.

2006-01-01

This article discusses how waste-water treatment plants, waste-incineration plants and drinking water supply systems make an important contribution to the production of renewable energy in Switzerland. Financing by the 'Climate-Cent' programme, which finances projects involving the use of renewable energy, is discussed. Figures are quoted on the electrical energy produced in waste-water treatment plants, waste-incineration plants and combined heat and power generation plant. Eco-balances of the various systems are discussed. Political efforts being made in Switzerland, including the 'Climate Cent', are looked at and promotion provided by new energy legislation is discussed. Eco-power and the processing of sewage gas to meet natural gas quality standards are discussed, as are energy analysis, co-operation between various research institutions and external costs

Analysis of industrial coke samples by activation with cyclotron protons

International Nuclear Information System (INIS)

Chaudhri, M.A.; Lee, M.M.; Spicer, B.M.

1982-01-01

A Melbourne Petrochemical Company was experiencing excessive coke formation in its ''cracking furnaces'', which was causing unnecessary stoppage of production and wastage of energy due to additional insulation. In order to investigate the possible causes of this excessive coke formation, we analyzed various coke samples and other coke-like materials obtained from these furnaces by activation with cyclotron-protons. Our results showed that, out of the two suspected coke promoters As and Sb whose small concentration in feed would produce greatly accelerated coke formation, As could not be detected in any of the eight samples investigated, while Sb was present in only one sample. However, we did observe Ca, Cr and Fe in all the samples, with surprisingly high concentrations in some of them. It has, therefore, been suggested that Ca, and perhaps Cr and Fe, but not As or Sb, could have been responsible for the excessive coke formation in the ''cracking furnaces''

Radioactive waste management for German nuclear power plants

International Nuclear Information System (INIS)

Weh, R.; Methling, D.; Sappok, M.

1996-01-01

In Germany, back-end fuel cycle provisions must be made for the twenty nuclear power plants currently run by utilities with an aggregate installed power of 23.4 GWe, and the four nuclear power plants already shut down. In addition, there are the shut down nuclear power plants of the former German Democratic Republic, and a variety of decommissioned prototype nuclear power plants built with the participation of the federal government and by firms other than utilities. The nuclear power plants operated by utilities contribute roughly one third of the total electricity generation in public power plants, thus greatly ensuring a stable energy supply in Germany. The public debate in Germany, however, focuses less on the good economic performance of these plants, and the positive acceptance at their respective sites, but rather on their spent fuel and waste management which, allegedly, is not safe enough. The spent fuel and waste management of German nuclear power plants is planned on a long-term basis, and executed in a responsible way by proven technical means, in the light of the provisions of the Atomic Act. Each of the necessary steps of the back end of the fuel cycle is planned and licensed in accordance with German nuclear law provisions. The respective facilities are built, commissioned, and monitored in operation with the dedicated assistance of expert consultants and licensing authorities. Stable boundary conditions are a prerequisite in ensuring the necessary stability in planning and running waste management schemes. As producers of waste, nuclear power plants are responsible for safe waste management and remain the owners of that waste until it has been accepted by a federal repository. (orig./DG) [de

Microstructures and microtextures of natural cokes: A case study of heat-affected coking coals from the Jharia coalfield, India

Energy Technology Data Exchange (ETDEWEB)

Singh, Ashok K. [Central Fuel Research Institute, CSIR, Dhanbad-828108 (India); Singh, Mahendra P. [Department of Geology, Banaras Hindu University, Varanasi-221005 (India); Sharma, Mamta; Srivastava, Sunil K.

2007-07-02

In Jharia coalfield, nearly 1250 Mt of coking coal has been devolatilized due to igneous intrusives and {proportional_to} 1900 Mt due to mine fires. This paper is an effort to investigate the effect of carbonization in two intrusive affected coal seams of Ena (seam XIII) and Alkusa (seam XIV) collieries of this coalfield. Through petrographic studies by microscopy, characterization of normal and heat-affected coals was carried out. The microstructures and microtextures produced due to extraneous heat have been related to nature and extent of heat, location of heating source, and quality and quantity of natural coke produced. Based on the results of this study and earlier studies, an effort has been made to study the classification scheme for microtextures of natural cokes generated through in-situ carbonization of the coal seams. It has been observed that in case of such heat effects under overburden pressure, the anisotropy is much more pronounced as compared to laboratory-carbonized cokes. In the mildly carbonized coals (pre-plastic phase, < 300 C) the vitrinite attained higher reflectance than normal vitrinite, liptinite started disappearing, and inertinite remained unaffected. In the moderately affected coals (plastic phase, 300-500 C), mesophase spheres and fused natural cokes were generated from the reactives (vitrinite and liptinite maceral groups), the liptinites disappeared, and structurally, the inertinites remained almost unchanged with slight increase in the reflectance value. In the severely heat-affected coals (post plastic phase, > 500 C) the identified microtextures were mesophase spheres, different shapes and sizes of natural cokes, graphitic sphaeroliths, pyrolytic carbons, inerts with morpho-structural changes and slightly higher reflectance values, and altered and unaltered mineral matters. A gradual change in the heat-affected coals with increasing temperature was observed with respect to location of intrusive body. It has been concluded that

Waste-to-energy plants - a solution for a cleaner future

International Nuclear Information System (INIS)

Pfeiffer, J.

2007-01-01

Waste-to-energy plants reduce the municipal solid waste volume by about 80% and convert it into residue. The residue quality naturally depends on the burned waste quality and also on the combustion parameters. Hence, tighter control of the plant can improve the residue quality. The generated combustion energy is regarded as renewable energy and is typically used to feed a turbine to generate electricity. Waste-to-energy furnaces react slowly on changing waste charge, so they are not used for peak load generation. The generated electrical power is a plant by product and is sold as base load generation. Usually the waste is burned on a grate which limits the plant size to about 160,000 tons of waste per year or 20 tons of waste per hour or about 28 MW. More recent technology utilizes fluidized bed combustion, which allows larger plant sizes up to 50 MW. Due to the unknown waste composition and stringent environmental standards involved, waste-to-energy plants employ sophisticated flue gas cleaning devices for emission control. ABB's Performance Monitoring continuously compares actual plant and equipment performance to expected performance. This includes the on-line calculation of the waste calorific heat allowing operator decision support and automated control system responses. Dedicated reports offer detailed data on operations, maintenance and emissions to plant management staff. ABB combustion optimization solutions use model based predictive control techniques to reliably find the most suitable set-points for improving the heat rate and reducing emissions like NO x . (author)

Waste management at the Ardennes power plant

International Nuclear Information System (INIS)

Abraham, J.P.

1979-01-01

In 1976, the SENA (with the participation of EDF, CEA and CEC in the framework of a research program on the management and storage of radioactive wastes) has developed an industrial pilot plant for the encapsulation of wastes in thermosetting polyester resins. The industrial putting in operation of the plant will enable most of the wastes from the nuclear station to be processed. The quality of products will be improved and the volume and processing cost reduced

Waste management in reprocessing plants

International Nuclear Information System (INIS)

Mortreuil, M.

1982-01-01

This lecture will give a survey of the French policy for the management of wastes in reprocessing plants. In consideration of their radioactivity, they must be immobilized in matrix in such a manner that they are stored under optimal safety conditions. A general review on the nature, nucleide content and quantity of the various wastes arising from thermal nuclear fuel reprocessing is given in the light of the French plants UP1 at Marcoule and UP2 at La Hague. The procedures of treatment of such wastes and their conditioning into inert packages suitable for temporary or terminal storage are presented, especially concerning the continuous vitrification process carried out for fission product solutions. The requirements of each option are discussed and possible alternative solutions are exposed. (orig./RW)

Disposal of radioactive wastes from Czechoslovak nuclear power plants

International Nuclear Information System (INIS)

Neumann, L.

In gaseous radioactive waste disposal, aerosol particles are filtered and gaseous wastes are discharged in the environment. The filters and filter materials used are stored on solid radioactive waste storage sites in the individual power plants. Liquid radioactive wastes are concentrated and the concentrates are stored. Distillates and low-level radioactive waste water are discharged into the hydrosphere. Solid radioactive wastes are stored without treatment in power plant bunkers. Bituminization and cementation of liquid radioactive wastes are discussed. (H.S.)

Processing and solidification of Savannah River Plant high-level waste

International Nuclear Information System (INIS)

Kelley, J.A.

1981-01-01

The entire flowsheet for processing and solidification of Savannah River Plant (SRP) high-level wastes has been demonstrated. A new small-scale integrated pilot plant is operating with actual radioactive wastes, and large-scale equipment is being demonstrated with nonradioactive simulated wastes. Design of a full-scale waste solidification plant is in progress. Plant construction is expected to begin in 1983, and startup is anticipated in 1988. The plant will poduce about 500 cans of glass per year with each can containing about 1.5 tons of glass

Calcinating petroleum coke in a furnace with a rotating hearth

Energy Technology Data Exchange (ETDEWEB)

Akhmetov, M M; Ezhov, B M; Galeeva, Z G; Goriunov, V S; Karpinskaia, N N; Zaitseva, S A

1980-01-01

A scheme is described for an industrial device with a bottom furnace for calcinating coke from slow coking. The consumption and operational indicators of the process during the calcination of standard and needle cokes are given, together with data on the quality of dry and calcinated cokes under different conditions. The basic drawbacks in the operation of the device are described, and measures are proposed for increasing its operational effectiveness.

Effects of heat treatments of coal on coke destruction under blast furnace conditions

Energy Technology Data Exchange (ETDEWEB)

Shkoller, M.B.; Dinel' t, V.M.; Korchuganova, G.S.; Petrov, V.B.

1983-09-01

This paper discusses results of investigations on effects of chemical reactions in a blast furnace on coke disintegration and destruction. The investigations were carried out by the VUKhIN Institute branch in Kuznetsk. Effects of silicates and carbonates of sodium, potassium and zinc on mechanical coke properties were investigated under laboratory conditions. Coke samples were placed in a reactor and were treated by vapors of metal compounds. Coke produced from a coal mixture with conventional moisture content and from preheated coal mixture was used. Coal properties are given in a table. Design of laboratory equipment used for tests is shown in 2 schemes. Heat treatments influenced coke porosity and its structural strength. Proportion of large pores accessible to sodium and potassium in coke from preheated coal was 4.5 times lower than in coke from a conventional mixture. Adsorption of sodium and potassium on coke from preheated charge was lower (from 0.22% to 0.24%) than on coke from a conventional mixture (from 2.5% to 2.9%). Adsorption of alkali metals on coke reduced its structural strength and increased coke oxidation rate by carbon dioxide. Use of heat treatments of coal for coking reduced adsorption of alkali metals on coke in a blast furnace, increased coke structural strength and reduced coke oxidation rate by carbon dioxide. (16 refs.) (In Russian)

Fissure formation in coke. 1: The mechanism of fissuring

Energy Technology Data Exchange (ETDEWEB)

D.R. Jenkins; M.R. Mahoney; J.C. Keating [CSIRO Mathematical and Information Sciences, North Ryde, NSW (Australia)

2010-07-15

Pilot scale coke oven experiments, in which carbonisation has been arrested after 2 and 4 h, have been used to identify key aspects of the initial formation and propagation of fissuring in coke. The experiments show that the primary fissure network is formed within the first few hours of coking and the fissures propagate towards the centre of the oven as coking progresses. They also show that some of the initially formed fissures stop propagating, thus increasing the effective fissure spacing as coking continues. A model for the propagation of regular crack arrays has been used to identify the cause of the initial formation of the fissure network, evaluate the fissure spacing and explain the fissure coarsening effect. The coarsening is shown to be due to an instability, in the form of every second fissure stopping. The formation of lateral fissures is shown to be due to tensile stress formation near the tips of stopped fissures and also to increased shrinkage due to a maximum in the coke contraction coefficient at around 700{sup o}C. 45 refs., 11 figs., 1 tab.

Hanford Waste Vitrification Plant applied technology plan

International Nuclear Information System (INIS)

Kruger, O.L.

1990-09-01

This Applied Technology Plan describes the process development, verification testing, equipment adaptation, and waste form qualification technical issues and plans for resolution to support the design, permitting, and operation of the Hanford Waste Vitrification Plant. The scope of this Plan includes work to be performed by the research and development contractor, Pacific Northwest Laboratory, other organizations within Westinghouse Hanford Company, universities and companies with glass technology expertise, and other US Department of Energy sites. All work described in this Plan is funded by the Hanford Waste Vitrification Plant Project and the relationship of this Plan to other waste management documents and issues is provided for background information. Work to performed under this Plan is divided into major areas that establish a reference process, develop an acceptable glass composition envelope, and demonstrate feed processing and glass production for the range of Hanford Waste Vitrification Plant feeds. Included in this work is the evaluation and verification testing of equipment and technology obtained from the Defense Waste Processing Facility, the West Valley Demonstration Project, foreign countries, and the Hanford Site. Development and verification of product and process models and other data needed for waste form qualification documentation are also included in this Plan. 21 refs., 4 figs., 33 tabs

Steel Industry Wastes.

Science.gov (United States)

Schmidtke, N. W.; Averill, D. W.

1978-01-01

Presents a literature review of wastes from steel industry, covering publications of 1976-77. This review covers: (1) coke production; (2) iron and steel production; (3) rolling operations; and (4) surface treatment. A list of 133 references is also presented. (NM)

Coke degradation by surface breakage in a modified tumble drum

Energy Technology Data Exchange (ETDEWEB)

Litster, J D

1987-01-01

The surface breakage rate constant for three Australian battery cokes was measured in a specially modified tumble drum using a previously developed technique. The effect of experimental test parameters - coke size, sample mass, drum speed, lifter height and lifter number - on the surface breakage rate constant was examined. The motion of coke particles within a tumble drum was filmed in a simulation experiment with a 0.31 m diameter drum. Particles were raised on the lifters, fell and collided with the bottom of the drum. These collisions were the main source of fines (minus 1 mm) production rather than true abrasion as depicted by a rubbing, rolling action. Hence the term 'surface breakage' is more appropriate than 'abrasion' to describe the breakage process. By measuring the volume of coke carried by each lifter and the height of fall of the coke, the effect of drum speed, sample mass, lifter height and number on the rate of surface breakage was successfully explained. The surface breakage rate constant was found to be proportional to particle size to the power 0.33 for the three cokes studied. A normalized surface breakage rate constant was derived which allowed comparison of cokes with different size distributions. This parameter characterises the coke surface breakage resistance.

Management of radioactive waste from reprocessing plants

International Nuclear Information System (INIS)

Kanwar Raj

2010-01-01

Reprocessing and recycling of both fissile and fertile components back into appropriate reactor systems is an integral part of three stage nuclear energy programme of India. Different steps involved in processing of spent nuclear fuel (SNF) are decladding, dissolution and recovery of fissile and fertile materials. Reprocessing of SNF is a complex process involving handling of large quantity of radioactive materials and processing chemicals. There are three reprocessing plants in operation in the country at Trombay, Tarapur and Kalpakkam. Out of these plants, Trombay reprocessing plant is engaged in reprocessing of SNF from research reactors and other two plants are processing of SNF from PHWRs. A facility is being built for reprocessing of thorium based spent fuel at BARC, Trombay based on the experience of pilot plant scale. Like other industrial activities of nuclear fuel cycle, fuel reprocessing facilities too generate various types of radioactive waste streams. These are generated in all the three physical forms namely solid, liquid and gas. These waste streams are primarily categorized on the basis of concentration of radionuclides, their half lives and toxicity. Management of these wastes aims at (a) recovery and recycle of useful materials, (b) concentration and confinement of radioactivity in inert and stable matrices, (c) minimization of final waste volume for disposal, (d) decontamination of effluents following ALARA principle and (e) minimization of radioactive discharge to the environment. The present paper outlines the salient features of management of different types of radioactive waste generated in reprocessing plants handling SNF from research reactors and PHWR

Solid Waste from the Operation and Decommissioning of Power Plants

Energy Technology Data Exchange (ETDEWEB)

Brown, Marilyn Ann [Georgia Inst. of Technology, Atlanta, GA (United States); D' Arcy, Daniel [Georgia Inst. of Technology, Atlanta, GA (United States); Lapsa, Melissa Voss [Oak Ridge National Lab. (ORNL), Oak Ridge, TN (United States); Sharma, Isha [Oak Ridge National Lab. (ORNL), Oak Ridge, TN (United States); Li, Yufei [Georgia Inst. of Technology, Atlanta, GA (United States)

2017-01-05

This baseline report examines the solid waste generated by the U.S. electric power industry, including both waste streams resulting from electricity generation and wastes resulting from the decommissioning of power plants. Coal and nuclear plants produce large volumes of waste during electricity generation, and this report describes the policies and procedures for handling these materials. Natural gas and oil-fired power plants face similar waste challenges. Renewables considered in this baseline report include hydropower, wind and solar.

Quantification of mineral matter in commercial cokes and their parent coals

Energy Technology Data Exchange (ETDEWEB)

Sakurovs, Richard; French, David; Grigore, Mihaela [CRC for Coal in Sustainable Development, CSIRO Energy Technology, PO Box 330 Newcastle 2300 (Australia)

2007-10-01

The nature of mineral matter in coke is an important factor in determining the behaviour of coke in the blast furnace. However, there have been few quantitative determinations of the types of mineral matter in coke and the feed coal. Here we use a technique of quantitative X-ray diffraction - SIROQUANT trademark - to determine the nature and quantity of mineral matter in eleven cokes and their parent materials, using samples of coals and their cokes utilised commercially in blast furnaces around the world. In some of these coals a considerable proportion of the phosphorus was present as goyazite, an aluminium phosphate. In the cokes, most of the iron was incorporated into amorphous aluminosilicate material; metallic iron accounted for about 15% of the iron present, and a similar amount was present as sulfides. Potassium and sodium were largely present as amorphous aluminosilicate material. Most of the quartz in the coal was unaffected by the coking, but a small fraction was transformed into other minerals. Quartz is not completely inert during coking. The amount of the catalytic forms of iron in the coke - iron, iron oxides and iron sulfides - was not related to the amount of pyrite and siderite in the starting coal, indicating that estimation of catalytic iron requires investigation of the mineral matter in coke directly and cannot be estimated from the minerals in the coal. (author)

Mean-term forecast of coke production in the world

International Nuclear Information System (INIS)

Ukhmylova, G.S.

1996-01-01

The causes of decrease in consumption of metallurgical coke in the world in the ninetieth and at the present time are analyzed. Reduction of reliable coke supply sources to the world market is noted. The data on the coke import and export in the world in 1990-1994 are presented and corresponding forecasts for 2000 and 2005 are given

A comparative economic assessment of hydrogen production from coke oven gas, water electrolysis and steam reforming of natural gas

International Nuclear Information System (INIS)

Nguyen, Y.V.; Ngo, Y.A.; Tinkler, M.J.; Cowan, N.

2003-01-01

This paper presents the comparative economics of producing hydrogen for the hydrogen economy by recovering it from waste gases from the steel industry, by water electrolysis and by conventional steam reforming of natural gas. Steel makers produce coke for their blast furnace operation by baking coal at high temperature in a reduced environment in their coke ovens. These ovens produce a coke oven gas from the volatiles in the coal. The gas, containing up to 60% hydrogen, is commonly used for its heating value with some of it being flared. The feasibility of recovering this hydrogen from the gas will be presented. A comparison of this opportunity with that of hydrogen from water electrolysis using low cost off-peak electricity from nuclear energy will be made. The impact of higher daily average electricity rate in Ontario will be discussed. The benefits of these opportunities compared with those from conventional steam reforming of natural gas will be highlighted. (author)

Acceptable knowledge document for INEEL stored transuranic waste - Rocky Flats Plant waste. Revision 2

International Nuclear Information System (INIS)

1998-01-01

This document and supporting documentation provide a consistent, defensible, and auditable record of acceptable knowledge for waste generated at the Rocky Flats Plant which is currently in the accessible storage inventory at the Idaho National Engineering and Environmental Laboratory. The inventory consists of transuranic (TRU) waste generated from 1972 through 1989. Regulations authorize waste generators and treatment, storage, and disposal facilities to use acceptable knowledge in appropriate circumstances to make hazardous waste determinations. Acceptable knowledge includes information relating to plant history, process operations, and waste management, in addition to waste-specific data generated prior to the effective date of the RCRA regulations. This document is organized to provide the reader a comprehensive presentation of the TRU waste inventory ranging from descriptions of the historical plant operations that generated and managed the waste to specific information about the composition of each waste group. Section 2 lists the requirements that dictate and direct TRU waste characterization and authorize the use of the acceptable knowledge approach. In addition to defining the TRU waste inventory, Section 3 summarizes the historical operations, waste management, characterization, and certification activities associated with the inventory. Sections 5.0 through 26.0 describe the waste groups in the inventory including waste generation, waste packaging, and waste characterization. This document includes an expanded discussion for each waste group of potential radionuclide contaminants, in addition to other physical properties and interferences that could potentially impact radioassay systems

Acceptable knowledge document for INEEL stored transuranic waste -- Rocky Flats Plant waste. Revision 2

Energy Technology Data Exchange (ETDEWEB)

NONE

1998-01-23

This document and supporting documentation provide a consistent, defensible, and auditable record of acceptable knowledge for waste generated at the Rocky Flats Plant which is currently in the accessible storage inventory at the Idaho National Engineering and Environmental Laboratory. The inventory consists of transuranic (TRU) waste generated from 1972 through 1989. Regulations authorize waste generators and treatment, storage, and disposal facilities to use acceptable knowledge in appropriate circumstances to make hazardous waste determinations. Acceptable knowledge includes information relating to plant history, process operations, and waste management, in addition to waste-specific data generated prior to the effective date of the RCRA regulations. This document is organized to provide the reader a comprehensive presentation of the TRU waste inventory ranging from descriptions of the historical plant operations that generated and managed the waste to specific information about the composition of each waste group. Section 2 lists the requirements that dictate and direct TRU waste characterization and authorize the use of the acceptable knowledge approach. In addition to defining the TRU waste inventory, Section 3 summarizes the historical operations, waste management, characterization, and certification activities associated with the inventory. Sections 5.0 through 26.0 describe the waste groups in the inventory including waste generation, waste packaging, and waste characterization. This document includes an expanded discussion for each waste group of potential radionuclide contaminants, in addition to other physical properties and interferences that could potentially impact radioassay systems.

Biogas plants: Utilization of microorganisms for waste management

Energy Technology Data Exchange (ETDEWEB)

Stadlbauer, E A; Trieu, C

1984-05-01

The continuous realisation of the basic principles of environmental conservation and compatability demands concern about the problems of eliminating wastes in an industrialised society. Biogas- and therefore technical plants for methane generation by anaerobic fermentation have promoted to effective means of environmental protection and sources of alternate energy from organic wastes. Methane fermentation has been employed for the stabilisation of sludges at municipal waste treatment plants for decades. However, the anaerobic digestion process shows promising applications both for industrial effluents and agricultural wastes as well as municipal solid wastes and covered waste deposits. In view of the advances achieved interdisciplinary cooperation the actual potential and perspective of methane fermentation technology with respect to the solution of the increasing problems of waste management and energy supply is discussed.

Study of variation grain size in desulfurization process of calcined petroleum coke

Science.gov (United States)

Pintowantoro, Sungging; Setiawan, Muhammad Arif; Abdul, Fakhreza

2018-04-01

Indonesia is a country with abundant natural resources, such as mineral mining and petroleum. In petroleum processing, crude oil can be processed into a source of fuel energy such as gasoline, diesel, oil, petroleum coke, and others. One of crude oil potentials in Indonesia is petroleum coke. Petroleum coke is a product from oil refining process. Sulfur reducing process in calcined petroleum cokes can be done by desulfurization process. The industries which have potential to become petroleum coke processing consumers are industries of aluminum smelting (anode, graphite block, carbon mortar), iron riser, calcined coke, foundry coke, etc. Sulfur reducing process in calcined petroleum coke can be done by thermal desulfurization process with alkaline substance NaOH. Desulfurization of petroleum coke process can be done in two ways, which are thermal desulfurization and hydrodesulphurization. This study aims to determine the effect of various grain size on sulfur, carbon, and chemical bond which contained by calcined petroleum coke. The raw material use calcined petroleum coke with 0.653% sulfur content. The grain size that used in this research is 50 mesh, then varied to 20 mesh and 100 mesh for each desulfurization process. Desulfurization are tested by ICP, UV-VIS, and FTIR to determine levels of sulfur, carbon, chemical bonding and sulfur dissolved water which contained in the residual washing of calcined petroleum coke. From various grain size that mentioned before, the optimal value is on 100 mesh grain size, where the sulfur content in petroleum coke is 0.24% and carbon content reaches the highest level of 97.8%. Meanwhile for grain size 100 mesh in the desulfurization process is enough to break the chemical bonds of organic sulfur in petroleum coke.

Report on 1979 result of Sunshine Project (detailed design). Part 1. Forty t/day solvolysis coal liquefaction pilot plant; 1979 nendo 40T/nichi solvolysis sekitan pilot plant shosai sekkei. 1

Energy Technology Data Exchange (ETDEWEB)

NONE

1980-03-01

The subject design documents are the compilation of the result of the design operation for the 'detailed design of 40 t/day class solvolysis coal liquefaction pilot plant'. The design of this pilot plant was conducted using, as the fundamental reference, the basic data provided by Kyushu National Industrial Research Institute and Kyushu University and the results of a contract research on '1 t/day class solvolysis coal liquefaction plant'. The subject detailed design was intended for Phase 1 centering on a single stage liquefaction - coal liquefaction (transformation into pitch) by solvolysis liquefaction reaction. The areas covered consists of the pre-treatment process, material mixing process, reaction process, reaction freezing process, coke separation process, SR recovery process, pitch refining process, utility facilities, and waste water treatment facilities. Incidentally, the processes for which the design operation has been completed this year, particularly the reaction process, coke separation process, SR recovery process, etc., are in the field untrodden technologically in the world; therefore, their design method is supposed to be established from the results of the R and D on coal liquefaction, '1 t/day class solvolysis coal liquefaction plant.' (NEDO)

Report on 1979 result of Sunshine Project (detailed design). Part 1. Forty t/day solvolysis coal liquefaction pilot plant; 1979 nendo 40T/nichi solvolysis sekitan pilot plant shosai sekkei. 1

Energy Technology Data Exchange (ETDEWEB)

NONE

1980-03-01

The subject design documents are the compilation of the result of the design operation for the 'detailed design of 40 t/day class solvolysis coal liquefaction pilot plant'. The design of this pilot plant was conducted using, as the fundamental reference, the basic data provided by Kyushu National Industrial Research Institute and Kyushu University and the results of a contract research on '1 t/day class solvolysis coal liquefaction plant'. The subject detailed design was intended for Phase 1 centering on a single stage liquefaction - coal liquefaction (transformation into pitch) by solvolysis liquefaction reaction. The areas covered consists of the pre-treatment process, material mixing process, reaction process, reaction freezing process, coke separation process, SR recovery process, pitch refining process, utility facilities, and waste water treatment facilities. Incidentally, the processes for which the design operation has been completed this year, particularly the reaction process, coke separation process, SR recovery process, etc., are in the field untrodden technologically in the world; therefore, their design method is supposed to be established from the results of the R and D on coal liquefaction, '1 t/day class solvolysis coal liquefaction plant.' (NEDO)

Coke formation on hydrodesulphurization catalysts. [Including effects of different promoters

Energy Technology Data Exchange (ETDEWEB)

Ternan, M.; Furimsky, E.; Parsons, B.I.

1979-02-01

The extent of coke formation was measured on a number of different hydrodesulfurization catalysts, primarily as a function of the catalyst chemical composition. Variations in the concentration of MoO/sub 3/ on the alumina, the type of catalyst promoter, the promoter/MoO/sub 3/ ratio, the presulfiding material and the reaction temperature were made. Increases in the reaction rate caused by either changes in the catalyst composition or by moderate changes in the reaction temperature were compared to the catalyst coke content. It was suggested that two types of coke were present on the catalyst, a reactive coke which is subsequently converted to reaction products and an unreactive coke which blocks catalytic sites.

Granulation of coke breeze fine for using in the sintering process

Directory of Open Access Journals (Sweden)

Mohamed F.M.

2010-01-01

Full Text Available Coke breeze is the main fuel used in the sintering process. The value of -3+1 mm. represents the most favorable particle size for coke breeze in the sintering process. About 20% of total coke fines (-0.5 mm are produced during different steps of preparation. Introducing these fines during the sintering process proves to be very harmful for different operating parameters. Thus ,this study aims at investigating the production of granules resulting from these fines using molasses as organic binder and its application in sintering of an iron ore. The results showed that the granules having the highest mechanical properties were obtained with 14.5 wt % molasses addition. The sintering experiments were performed by using coke breeze in different shapes (-3+1 mm in size, coke breeze without sieving and coke breeze granules -3+1 mm. The reduction experiments, microscopic structure and X-ray analysis for the produced sinter were carried out. The results revealed that, all sinter properties (such as shatter test, productivity of sinter machine and blast furnace, reduction time and chemical composition for produced sinter by using coke breeze with size -3+1 mm and coke breeze granules were almost the same. The iron ore sinter which was produced by using coke breeze without sieving yielded low productivity for both sinter machine and blast furnace. Furthermore, using coke breeze without sieving in sintering of an iron ore decreases the vertical velocity of sinter machine and increases the reduction time.

Study and modelling of deactivation by coke in catalytic reforming of hydrocarbons on Pt-Sn/Al{sub 2}O{sub 3} catalyst; La microbalance inertielle: etude et modelisation cinetique de la desactivation par le coke en reformage catalytique des hydrocarbures sur catalyseur Pt-Sn/Al{sub 2}O{sub 3}

Energy Technology Data Exchange (ETDEWEB)

Mathieu-Deghais, S.

2004-07-01

Catalytic reforming is the refining process that produces gasoline with a high octane number. During a reforming operation, undesired side reactions promote the formation of carbon deposits (coke) on the surface of the catalyst. As the reactions proceed, the coke accumulation leads to a progressive decrease of the catalyst activity and to a change in its selectivity. Getting this phenomenon under control is interesting to optimize the industrial plants. This work aims to improve the comprehension and the modeling of coke formation and its deactivating effect on reforming reactions, while working under conditions chosen within a range as close as possible to the industrial conditions of the regenerative process. The experimental study is carried out with a micro unit that is designed to observe simultaneously the coke formation and its influence on the catalyst activity. A vibrational microbalance reactor (TEOM - Tapered Element Oscillating Microbalance) is used to provide continuous monitoring of coke. On-line gas chromatography is used to observe the catalyst activity and selectivity as a function of the coke content. The coking experiments are performed on a fresh Pt-Sn/alumina catalyst, with mixtures of hydrocarbon molecules of 7 carbon atoms as hydrocarbon feeds. The coking tests permitted to highlight the operating parameters that may affect the amount of coke, and to identify the hydrocarbon molecules that behave as coke intermediate. A kinetic model for coke formation could be developed through the compilation of these results. The catalytic activity analysis permitted to point out the coke effect on both of the active phases of the catalyst, to construct a simplified reforming kinetic model that simulates the catalyst activity under the reforming conditions, and to quantify deactivation via deactivation functions. (author)

40 CFR 63.303 - Standards for nonrecovery coke oven batteries.

Science.gov (United States)

2010-07-01

... batteries. 63.303 Section 63.303 Protection of Environment ENVIRONMENTAL PROTECTION AGENCY (CONTINUED) AIR... National Emission Standards for Coke Oven Batteries § 63.303 Standards for nonrecovery coke oven batteries... existing nonrecovery coke oven battery that exceed any of the following emission limitations or...

Effects of Coke Calcination Level on Pore Structure in Carbon Anodes

Science.gov (United States)

Fang, Ning; Xue, Jilai; Lang, Guanghui; Bao, Chongai; Gao, Shoulei

2016-02-01

Effects of coke calcination levels on pore structure of carbon anodes have been investigated. Bench anodes were prepared by 3 types of cokes with 4 calcination temperatures (800°C, 900°C, 1000°C and 1100°C). The cokes and anodes were characterized using hydrostatic method, air permeability determination, mercury porosimetry, image analysis and confocal microscopy (CSLM). The cokes with different calcination levels are almost the same in LC values (19-20 Å) and real density (1.967-1.985 g/cm3), while the anode containing coke calcined at 900°C has the lowest open porosity and air permeability. Pore size distribution (represented by Anode H sample) can be roughly divided into two ranges: small and medium pores in diameter of 10-400 μm and large pores of 400-580 μm. For the anode containing coke calcined at 800°C, a number of long, narrow pores in the pore size range of 400-580 μm are presented among cokes particles. Formation of these elongated pores may be attributed to coke shrinkages during the anode baking process, which may develop cracking in the anode under cell operations. More small or medium rounded pores with pore size range of 10-400 μm emerge in the anodes with coke calcination temperatures of 900°C, 1000°C and 1100°C, which may be generated due to release of volatiles from the carbon anode during baking. For the anode containing coke calcined at 1100°C, it is found that many rounded pores often closely surround large coke particles, which have potential to form elongated, narrow pores.

Plant trial of a fast neutron and gamma-ray transmission gauge for the on-belt determination of moisture in lump coke

International Nuclear Information System (INIS)

Millen, M.J.; Rafter, P.T.; Sowerby, B.D.; Rainbow, M.T.; Jelenich, L.

1990-01-01

A fast neutron and γ-ray transmission (FNGT) gauge has been used to determine the moisture content of lump coke on the conveyor belt supplying the No. 3 blast furnace at the BHP Newcastle Steelworks. The gauge was operated on-line over the period June 1988-March 1989. Gauge moisture was compared with laboratory moisture, based on 30 increment composite samples taken from the belt, and with moisture determined by a second FNGT gauge on one of the hoppers feeding the conveyor belt. The r.m.s. difference between conveyor gauge moisture and laboratory moisture was 0.24 wt% during the calibration period for two hopper flow on the belt, which is normal plant condition. The accuracy of the conveyor belt gauge was maintained to within 0.37 wt% moisture over the full period of the plant trial. (author)

Contribution to the assessment of sampling data of coke. Beitrag zur Auswertung von Probenahme-ergebnissen von Koks

Energy Technology Data Exchange (ETDEWEB)

Goell, G; Helfricht, R; Mueller, H [Forschungsinstitut fuer Aufbereitung, Freiberg (Germany, F.R.)

1991-03-01

Controlling the quality characteristics of disperse material systems in plants where these are produced and applied, by means of test procedures, assumes that samples are taken from mass flows. In this contribution, a report is presented on research on the clarification of the causes of fluctuations and differences of test results for coke between supplier and customer. It is revealed that for an appraisal, prehistory and material behaviour of the test material as well as analysis of the actual condition of the sampling and processing systems of both plants are to be considered. The magnitude of the individual error in relation to the total sampling error is explored and conclusions are drawn, to rule out differences as well as unfavourable developments in the production, utilization and the appraisal of coke products. 15 refs., 7 figs.

Assessment of thermal efficiency of heat recovery coke making

Science.gov (United States)

Tiwari, H. P.; Saxena, V. K.; Haldar, S. K.; Sriramoju, S. K.

2017-08-01

The heat recovery stamp charge coke making process is quite complicated due to the evolved volatile matter during coking, is partially combusted in oven crown and sole flue in a controlled manner to provide heat for producing metallurgical coke. Therefore, the control and efficient utilization of heat in the oven crown, and sole flue is difficult, which directly affects the operational efficiency. Considering the complexity and importance of thermal efficiency, evolution of different gases, combustion of gasses in oven crown and sole flue, and heating process of coke oven has been studied. A nonlinear regression methodology was used to predict temperature profile of different depth of coal cake during the coking. It was observed that the predicted temperature profile is in good agreement with the actual temperature profile (R2 = 0.98) and is validated with the actual temperature profile of other ovens. A complete study is being done to calculate the material balance, heat balance, and heat losses. This gives an overall understanding of heat flow which affects the heat penetration into the coal cake. The study confirms that 60% heat was utilized during coking.

Polish scenery of coking industry activity

International Nuclear Information System (INIS)

Zielinski, H.

1994-01-01

The cooking industry in Poland and the world depends on conditions of iron and steel industry. Nowadays it is observed depression of this industry. On the other hand it is occurred a strong public pressure to reduce pollution by coking works. It is known that modernizing enterprises need a great deal of funds, but they are necessary, in order to keep coking industry on market. (author). 2 tabs

Pilot incineration plant for solid, combustible, and low-level wastes

International Nuclear Information System (INIS)

Francioni, W.M.

Radioactively contaminated wastes are formed in the handling of radioactive materials at the Federal Institute for Reactor Research (FIRR) and in other facilities, hospitals, sanitoria, industry, and nuclear power plants. A large part of the wastes are combustible and only very slightly radioactive. Incineration of these wastes is obvious. A pilot incineration plant, henceforth called the PIP, for radioactive combustible wastes of the FIRR is surveyed. The plant and its individual components are described. The production costs of the plant and experience gained in operation available at present are reviewed. Solid combustible radioactive waste can be incinerated in the PIP. The maximum possible reduction in volume of these wastes is achieved by incineration. Subsequently the chemically sterile ashes can be consolidated in a stable block suitable for long-term storage mixing with cement

Production of conductive coke for cathodic protection

Energy Technology Data Exchange (ETDEWEB)

Mogollon, E.G.; Henao, L.E.; Pacheco, L.A.; Ortiz, J.L.; Diaz, J.J. [Universidad Nacional de Colombia, Bogota (Colombia). Departamento de Quimica

1999-07-01

The reduction of resistivity of coke by means of the cocarbonization of mixtures of coking coals was studied using coal tar as an additive. Optimum temperature and blending conditions for decreased resistivity were investigated. The effect of particle size on the dependency of coal rank was investigated. 2 refs., 4 figs., 2 tabs.

Aqueous Waste Treatment Plant at Aldermaston

International Nuclear Information System (INIS)

Keene, D.; Fowler, J.; Frier, S.

2006-01-01

For over half a century the Pangbourne Pipeline formed part of AWE's liquid waste management system. Since 1952 the 11.5 mile pipeline carried pre-treated wastewater from the Aldermaston site for safe dispersal in the River Thames. Such discharges were in strict compliance with the exacting conditions demanded by all regulatory authorities, latterly, those of the Environment Agency. In March 2005 AWE plc closed the Pangbourne Pipeline and ceased discharges of treated active aqueous waste to the River Thames via this route. The ability to effectively eliminate active liquid discharges to the environment is thanks to an extensive programme of waste minimization on the Aldermaston site, together with the construction of a new Waste Treatment Plant (WTP). Waste minimization measures have reduced the effluent arisings by over 70% in less than four years. The new WTP has been built using best available technology (evaporation followed by reverse osmosis) to remove trace levels of radioactivity from wastewater to exceptionally stringent standards. Active operation has confirmed early pilot scale trials, with the plant meeting throughput and decontamination performance targets, and final discharges being at or below limits of detection. The performance of the plant allows the treated waste to be discharged safely as normal industrial effluent from the AWE site. Although the project has had a challenging schedule, the project was completed on programme, to budget and with an exemplary safety record (over 280,000 hours in construction with no lost time events) largely due to a pro-active partnering approach between AWE plc and RWE NUKEM and its sub-contractors. (authors)

EPA Administrative Order on Consent (AOC) with ERP Compliant Coke, LLC

Science.gov (United States)

This Administrative Order on Consent with ERP Compliant Coke was effective August 2016. The Walter Coke facility located in North Birmingham was purchased by ERP Compliant Coke, LLC in February 2016 out of bankruptcy proceedings.

Hanford Waste Vitrification Plant quality assurance program description: Overview and applications

International Nuclear Information System (INIS)

Caplinger, W.H.

1990-12-01

This document describes the Hanford Waste Vitrification Plant Project Quality Assurance Program. This program is being implemented to ensure the acceptability of high-level radioactive canistered waste forms produced by the Hanford Waste Vitrification Plant for disposal in a licensed federal repository. The Hanford Waste Vitrification Plant Quality Assurance Program is comprised of this Quality Assurance Program Description as well as the associated contractors' quality assurance programs. The objective of this Quality Assurance Program Description is to provide the Hanford Waste Vitrification Plant Project participants with guidance and direction for program implementation while satisfying the US Department of Energy Office of Civilian Radioactive Waste Management needs in repository licensing activities with regard to canistered waste forms. To accomplish this objective, this description will be prepared in three parts: Part 1 - Overview and applications document; Part 2 - Development and qualification of the canistered waste form; Part 3 - Production of canistered waste forms. Part 1 describes the background, strategy, application, and content of the Hanford Waste Vitrification Plant Quality Assurance Program. This Quality Assurance Program Description, when complete, is designed to provide a level of confidence in the integrity of the canistered waste forms. 8 refs

Waste Treatment & Immobilization Plant Project

Data.gov (United States)

Federal Laboratory Consortium — In southeastern Washington State, Bechtel National, Inc. is designing, constructing and commissioning the world's largest radioactive waste treatment plant for the...

Alternative method for assessing coking coal plasticity

Energy Technology Data Exchange (ETDEWEB)

Dzuy Nguyen; Susan Woodhouse; Merrick Mahoney [University of Adelaide (Australia). BHP Billiton Newcastle Technology Centre

2008-07-15

Traditional plasticity measurements for coal have a number of limitations associated with the reproducibility of the tests and their use in predicting coking behaviour. This report reviews alternative rheological methods for characterising the plastic behaviour of coking coals. It reviews the application of more fundamental rheological measurements to the coal system as well as reviewing applications of rheology to other physical systems. These systems may act as potential models for the application of fundamental rheological measurements to cokemaking. The systems considered were polymer melts, coal ash melts, lava, bread making and ice cream. These systems were chosen because they exhibit some physically equivalent processes to the processes occurring during cokemaking, eg, the generation of bubbles within a softened system that then resolidifies. A number of recommendations were made; the steady and oscillatory shear squeeze flow techniques be further investigated to determine if the measured rheology characteristics are related to transformations within the coke oven and the characteristics of resultant coke; modification of Gieseler plastometers for more fundamental rheology measurements not be attempted.

Savannah River Plant Separations Department mixed waste program

International Nuclear Information System (INIS)

Wierzbicki, W.M.

1988-01-01

The Department of Energy's (DOE) Savannah River Plant (SRP) generates radioactive and mixed waste as a result of the manufacture of nuclear material for the national defense program. The radioactive portion of the mixed waste and all nonhazardous radioactive wastes would continue to be regulated by DOE under the Atomic Energy Act. The Separations Department is the largest generator of solid radioactive waste at the Savannah River Plant. Over the last three years, the Separations Department has developed and implemented a program to characterize candidate mixed-waste streams. The program consisted of facility personnel interviews, a waste-generation characterization program and waste testing to determine whether a particular waste form was hazardous. The Separations Department changed waste-handling practices and procedures to meet the requirements of the generator standards. For each Separation Department Facility, staging areas were established, inventory and reporting requirements were developed, operating procedures were revised to ensure proper waste handling, and personnel were provided hazardous waste training. To emphasize the importance of the new requirements, a newsletter was developed and issued to all Separations supervisory personnel

New Mexico waste plant sits idle amid controversy

International Nuclear Information System (INIS)

Lovejoy, L.A. Jr.

1994-01-01

The Department of Energy (DOE) hopes to permanently dispose of radioactive waste from its weapons program at a Waste Isolation Pilot Plant about 26 miles from Carlsbad, New Mexico. The plant has been plagued by problems, according to Lindsay A. Lovejoy, Jr., an assistant attorney general of New Mexico. Among them are cracks in the walls of some of the underground rooms slated for storage of radioactive waste. Meanwhile, above-ground problems involve DOE's struggle toward regulatory compliance. The Environmental Protection Agency (EPA), under the Resource Conservation Recovery Act, has assumed a regulatory role over DOE's radioactive waste-disposal efforts, which is a new role for the agency. Lovejoy proposes that EPA, in its regulation of the New Mexico plant, develop compliance criteria and involve DOE and the public in ongoing open-quotes dialogue aimed at ferreting out any and all problems before a single scrap of radioactive waste is deposited into the earth beneath new Mexico.close quotes

Some aspects of the technology improvement for heat reprocessing of the combustible radioactive wastes and ash residue conditioning

International Nuclear Information System (INIS)

Dmitriev, S.A.; Lifanov, F.A.; Knyazev, I.A.; Buravchenko, N.N.; Sobolev, I.A.; Mamaev, L.A.; Alekseev, A.N.; Simagina, O.S.

1991-01-01

The results of studies devoted to increasing the efficiency of thermal reprocessing (combustion) of organic low- and intermediate-level radioactive wastes are given. The new most efficient three-stage process including: 1) gasification and pyrolysis of an organic material with volatile product release, 2) coke residual combustion, ash and noncombustible materials melting, 3) combustion of volatile products of thermal decomposition is developed on the basis of the analysis of solid radioactive waste combustion schemes, mathematical simulation and laboratory studies. Experimental bed, in which these processes are realized, is created. The results obtained in it have allowed one to begin designing of the pilot-commercial plant with shaft furnace having the capacity up to 200 kg/h for solid wastes

Gasification experience with biomass and wastes

Energy Technology Data Exchange (ETDEWEB)

Schiffer, H P; Adlhoch, W [Rheinbraun AG, Cologne (Germany)

1997-12-31

The HTW process is particularly favourable for the gasification of low-rank feedstocks. During various tests - performed in b-bench- scale, pilot-scale and industrial scale units - consequences with regard to feedstock preparation. Gasification behaviour, corrosion, emission and residual matter were carefully studied for a large number of different feedstocks. Information is now available for optimal utilisation of several types of biomass and waste materials in relation to plant operation, emission and residue utilization. Different types of biomass were tested in bench-scale conditions in an atmospheric HTW process development unit. Industrial-scale experience concerning biomass is available from the Gasification plant at Oulu, Finland, which operated from 1988 to 1991, producing ammonia synthesis gas from dried Finnish peat. During several test campaigns performed at the HTW demonstration plant sewage sludge, loaded coke and used plastics were co-gasified at feeding rates of up to 5 t/h. Operability, conversion efficiency, syngas contaminants, solid residue characteristics and emissions were monitored very carefully. Co-gasification in a dried lignite mixture allows synthesis gas for methanol production to be obtained also from waste materials. Thus, waste is converted into a useful chemical feedstock. For both sewage sludge and loaded coke, conversion efficiency and syngas yield were sufficient. Within the scope of a solid residue characterization various contaminants, including chlorine, sulphur, heavy metals and other trace elements or organic compounds, their formation and/or release were detected. Emissions were well below the limits. However, an increase in the benzene and naphthalene concentrations in the crude gas occurred. Thus, a commercial application requires additional gas treatment. In the next few years, feedstock recycling of mixed plastics household waste from Duales System Deutschland GmbH will call for a plant capacity of 350 000 to 400 000

Gasification experience with biomass and wastes

Energy Technology Data Exchange (ETDEWEB)

Schiffer, H.P.; Adlhoch, W. [Rheinbraun AG, Cologne (Germany)

1996-12-31

The HTW process is particularly favourable for the gasification of low-rank feedstocks. During various tests - performed in b-bench- scale, pilot-scale and industrial scale units - consequences with regard to feedstock preparation. Gasification behaviour, corrosion, emission and residual matter were carefully studied for a large number of different feedstocks. Information is now available for optimal utilisation of several types of biomass and waste materials in relation to plant operation, emission and residue utilization. Different types of biomass were tested in bench-scale conditions in an atmospheric HTW process development unit. Industrial-scale experience concerning biomass is available from the Gasification plant at Oulu, Finland, which operated from 1988 to 1991, producing ammonia synthesis gas from dried Finnish peat. During several test campaigns performed at the HTW demonstration plant sewage sludge, loaded coke and used plastics were co-gasified at feeding rates of up to 5 t/h. Operability, conversion efficiency, syngas contaminants, solid residue characteristics and emissions were monitored very carefully. Co-gasification in a dried lignite mixture allows synthesis gas for methanol production to be obtained also from waste materials. Thus, waste is converted into a useful chemical feedstock. For both sewage sludge and loaded coke, conversion efficiency and syngas yield were sufficient. Within the scope of a solid residue characterization various contaminants, including chlorine, sulphur, heavy metals and other trace elements or organic compounds, their formation and/or release were detected. Emissions were well below the limits. However, an increase in the benzene and naphthalene concentrations in the crude gas occurred. Thus, a commercial application requires additional gas treatment. In the next few years, feedstock recycling of mixed plastics household waste from Duales System Deutschland GmbH will call for a plant capacity of 350 000 to 400 000

Dechlorane Plus (DP) in air and plants at an electronic waste (e-waste) site in South China

Energy Technology Data Exchange (ETDEWEB)

Chen Shejun [State Key Laboratory of Organic Geochemistry, Guangzhou Institute of Geochemistry, Chinese Academy of Sciences, Guangzhou 510640 (China); Tian Mi; Wang Jing; Shi Tian [State Key Laboratory of Organic Geochemistry, Guangzhou Institute of Geochemistry, Chinese Academy of Sciences, Guangzhou 510640 (China); Graduate School, Chinese Academy of Sciences, Beijing 100049 (China); Luo Yong [Guangdong Forestry Survey and Planning Institute, Guangzhou 510520 (China); Luo Xiaojun [State Key Laboratory of Organic Geochemistry, Guangzhou Institute of Geochemistry, Chinese Academy of Sciences, Guangzhou 510640 (China); Mai Bixian, E-mail: nancymai@gig.ac.cn [State Key Laboratory of Organic Geochemistry, Guangzhou Institute of Geochemistry, Chinese Academy of Sciences, Guangzhou 510640 (China)

2011-05-15

Air and foliage samples (Eucalyptus spp. and Pinus massoniana Lamb.) were collected from e-waste and reference sites in South China and analyzed for Dechlorane Plus (DP) and two dechlorinated DPs. DP concentrations in the air were 13.1-1794 pg/m{sup 3} for the e-waste site and 0.47-35.7 pg/m{sup 3} for the reference site, suggesting the recycling of e-waste is an important source of DP to the environment. Plant DP, with concentrations of 0.45-51.9 ng/g dry weight at the e-waste site and 0.09-2.46 ng/g at the reference site, exhibited temporal patterns similar to the air DP except for pine needle at the reference site. The air-plant exchange of DP could be described with the two-compartment model. Anti-Cl{sub 11} DP was measured in most air and plant samples from the e-waste site. The ratios of anti-Cl{sub 11} DP to anti-DP in the air and plants may indicate the preferential uptake of dechlorinated DP by plant compared with DP. - Highlights: > Dechlorane Plus was widely present in the air and plants in South China. > Temporal patterns of the plant DP could be described with the two-compartment model. > Plant uptake can efficiently reduce air DP concentration at the reference site. > Anti-Cl{sub 11} DP was measured in most air and plant samples from the e-waste site. - E-waste recycling in South China results in wide occurrence of DP in the air and plant.

Hanford Waste Vitrification Plant Quality Assurance Program description for high-level waste form development and qualification. Revision 3, Part 2

Energy Technology Data Exchange (ETDEWEB)

1993-08-01

The Hanford Waste Vitrification Plant Project has been established to convert the high-level radioactive waste associated with nuclear defense production at the Hanford Site into a waste form suitable for disposal in a deep geologic repository. The Hanford Waste Vitrification Plant will mix processed radioactive waste with borosilicate material, then heat the mixture to its melting point (vitrification) to forin a glass-like substance that traps the radionuclides in the glass matrix upon cooling. The Hanford Waste Vitrification Plant Quality Assurance Program has been established to support the mission of the Hanford Waste Vitrification Plant. This Quality Assurance Program Description has been written to document the Hanford Waste Vitrification Plant Quality Assurance Program.

Mechanical compaction of Waste Isolation Pilot Plant simulated waste

International Nuclear Information System (INIS)

Butcher, B.M.; Thompson, T.W.; VanBuskirk, R.G.; Patti, N.C.

1991-06-01

The investigation described in this report acquired experimental information about how materials simulating transuranic (TRU) waste compact under axial compressive stress, and used these data to define a model for use in the Waste Isolation Pilot Plant (WIPP) disposal room analyses. The first step was to determine compaction curves for various simultant materials characteristic of TRU waste. Stress-volume compaction curves for various combinations of these materials were than derived to represent the combustible, metallic, and sludge waste categories. Prediction of compaction response in this manner is considered essential for the WIPP program because of the difficulties inherent in working with real (radioactive) waste. Next, full-sized 55-gallon drums of simulated combustible, metallic, and sludge waste were axially compacted. These results provided data that can be directly applied to room consolidation and data for comparison with the predictions obtained in Part 1 of the investigation. Compaction curves, which represent the combustible, metallic, and sludge waste categories, were determined, and a curve for the averaged waste inventory of the entire repository was derived. 9 refs., 31 figs., 12 tabs

Processing of coke oven gas. Primary gas cooling

Energy Technology Data Exchange (ETDEWEB)

Ullrich, H [Otto (C.) und Co. G.m.b.H., Bochum (Germany, F.R.)

1976-11-01

The primary cooler is an indispensable part of all byproduct processing plants. Its purpose is to cool the raw gas from the coke oven battery and to remove the accompanying water vapor. The greater part of the cooling capacity is utilized for the condensation of water vapor and only a small capacity is needed for the gas cooling. Impurities in the gas, like naphthalene, tar and solid particles, necessitate a special design in view of the inclination to dirt accumulation. Standard types of direct and indirect primary gas coolers are described, with a discussion of their advantages and disadvantages.

Defense Waste Processing Facility, Savannah River Plant

International Nuclear Information System (INIS)

After 10 years of research, development, and testing, the US Department of Energy is building a new facility which will prepare high-level radioactive waste for permanent disposal. The Defense Waste Processing Facility, known as the DWPF, will be the first production-scale facility of its kind in the United States. In the DWPF, high-level waste produced by defense activities at the Savannah River Plant will be processed into a solid form, borosilicate glass, suitable for permanent off-site geologic disposal. With construction beginning in the fall of 1983, the DWPT is scheduled to be operational in 1989. By 2005, the DWPF will have immobilized the backlog of high-level waste which has been accumulating in storage tanks at the Savannah River Plant since 1954. Canisters of the immobilized waste will then be ready for permanent disposal deep under the ground, safely isolated from the environment

Managing nuclear waste from power plants

International Nuclear Information System (INIS)

Keeney, R.L.; Winterfeldt, D. von

1994-01-01

National strategies to manage nuclear waste from commercial nuclear power plants are analyzed and compared. The current strategy is to try to operate a repository at Yucca Mountain, Nevada, to dispose storage at a centralized facility or next to nuclear power plants. If either of these is pursued now, the analysis assumes that a repository will be built in 2100 for waste not subsequently put to use. The analysis treats various uncertainties: whether a repository at Yucca Mountain would be licensed, possible theft and misuse of the waste, innovations in repository design and waste management, the potential availability of a cancer cure by 2100, and possible future uses of nuclear waste. The objectives used to compare alternatives include concerns for health and safety, environmental and socioeconomic impacts, and direct economic costs, as well as equity concerns (geographical, intergenerational, and procedural), indirect economic costs, as well as equity concerns (geographical, intergenerational, and procedural), indirect economic costs to electricity ratepayers, federal government responsibility to manage nuclear waste, and implications of theft and misuse of nuclear waste. The analysis shows that currently building an underground repository at Yucca Mountain is inferior to other available strategies by the equivalent of $10,000 million to $50,000 million. This strongly suggests that this policy should be reconsidered. A more detailed analysis using the framework presented would help to define a new national policy to manage nuclear waste. 36 refs., 3 figs., 17 tabs

Improvements of radioactive waste management at WWER nuclear power plants

International Nuclear Information System (INIS)

2006-04-01

This report is part of a systematic IAEA effort to improve waste management practices at WWER plants and to make them consistent with the current requirements and standards for safe and reliable operation of nuclear power plants. The report reviews the wet and dry solid waste management practices at the various types of WWER nuclear power plants (NPP) and describes approaches and recent achievements in waste minimization. Waste minimization practices in use at western PWRs are reviewed and compared, and their applicability at WWER plants is evaluated. Radioactive waste volume reduction issues and waste management practices are reflected in many IAEA publications. However, aspects of waste minimization specific to individual WWER nuclear power plant designs and WWER waste management policies are not addressed extensively in those publications. This report covers the important aspects applicable to the improvement of waste management at WWER NPP, including both plant-level and country-level considerations. It is recognized that most WWER plants are already implementing many of these concepts and recommendations with varying degrees of success; others will benefit from the included considerations. The major issues addressed are: - Review of current waste management policies and practices related to WWERs and western PWRs, including the influence of the original design concepts and significant modifications, liquid waste discharge limits and dry solid waste clearance levels applied in individual countries, national policies and laws, and other relevant aspects affecting the nature and quantities of waste arisings; - Identification of strategies and methods for improving the radioactive waste management generated in normal operation and maintenance at WWERs. This report is a composite (combination) of the two separate initiatives mentioned above. The first draft report was prepared at the meeting 26-30 May 1997 by five consultants. The draft was improved during an

Management of radioactive wastes from nuclear power plants

International Nuclear Information System (INIS)

1985-01-01

This Code of Practice defines the minimum requirements for the design and operation of structures, systems and components important for the management of radioactive wastes from thermal neutron nuclear power plants. The topics covered include design and operation of gaseous, liquid and solid waste systems, waste transport, storage and disposal, decommissioning wastes and wastes from unplanned events

Improving plant performance through efficient nuclear waste management - The French experience

International Nuclear Information System (INIS)

Peterson, C.H.

1986-01-01

This paper discusses high and low level waste management and its effect on Plant Performance. In France, high level waste policy is an improtant factor in plant performance. The LLW section of the paper discusses the role of French Industry organization as well as the benefits of standard plants with standard practices. The regulation of the production of waste and the waste processing by utilities is covered

Preparation and characterization of bi-metallic nanoparticle catalyst having better anti-coking properties using reverse micelle technique

Science.gov (United States)

Zacharia, Thomas

Energy needs are rising on an exponential basis. The mammoth energy sources like coal, natural gas and petroleum are the cause of pollution. The large outcry for an alternate energy source which is environmentally friendly and energy efficient is heard during the past few years. This is where “Clean-Fuel” like hydrogen gained its ground. Hydrogen is mainly produced by steam methane reforming (SMR). An alternate sustainable process which can reduce the cost as well as eliminate the waste products is Tri-reforming. In both these reforming processes nickel is used as catalyst. However as the process goes on the catalyst gets deactivated due to coking on the catalytic surface. This goal of this thesis work was to develop a bi-metallic catalyst which has better anti-coking properties compared to the conventional nickel catalyst. Tin was used to dope nickel. It was found that Ni3Sn complex around a core of Ni is coking resistant compared to pure nickel catalyst. Reverse micelle synthesis of catalyst preparation was used to control the size and shape of catalytic particles. These studies will benefit researches on hydrogen production and catalyst manufactures who work on different bi-metallic combinations.

Enrichment of reactive macerals in coal: its characterization and utilization in coke making

Science.gov (United States)

Nag, Debjani; Kopparthi, P.; Dash, P. S.; Saxena, V. K.; Chandra, S.

2018-01-01

Macerals in coal are of different types: reactive and inert. These macerals are differ in their physical and chemical properties. Column flotation method has been used to separate the reactive macerals in a non-coking coal. The enriched coal is then characterized in order to understand the changes in the coking potential by different techniques. It is then used in making of metallurgical coke by proper blending with other coals. Enriched coal enhance the properties of metallurgical coke. This shows a path of utilization of non-coking coal in metallurgical coke making.

Waste water pilot plant research, development, and demonstration permit application

International Nuclear Information System (INIS)

1993-03-01

This permit application has been prepared to obtain a research, development, and demonstration permit to perform pilot-scale treatability testing on the 242-A Evaporator process condensate waste water effluent stream. It provides the management framework, and controls all the testing conducted in the waste water pilot plant using dangerous waste. It also provides a waste acceptance envelope (upper limits for selected constituents) and details the safety and environmental protection requirements for waste water pilot plant testing. This permit application describes the overall approach to testing and the various components or requirements that are common to all tests. This permit application has been prepared at a sufficient level of detail to establish permit conditions for all waste water pilot plant tests to be conducted

Prediction of coking dynamics for wet coal charge

Directory of Open Access Journals (Sweden)

Kardaś Dariusz

2015-09-01

Full Text Available A one-dimensional transient mathematical model describing thermal and flow phenomena during coal coking in an oven chamber was studied in the paper. It also accounts for heat conduction in the ceramic oven wall when assuming a constant temperature at the heating channel side. The model was solved numerically using partly implicit methods for gas flow and heat transfer problems. The histories of temperature, gas evolution and internal pressure were presented and analysed. The theoretical predictions of temperature change in the centre plane of the coke oven were compared with industrialscale measurements. Both, the experimental data and obtained numerical results show that moisture content determines the coking process dynamics, lagging the temperature increase above the water steam evaporation temperature and in consequence the total coking time. The phenomenon of internal pressure generation in the context of overlapping effects of simultaneously occurring coal transitions - devolatilisation and coal permeability decrease under plastic stage - was also discussed.

The Release of Trace Elements in the Process of Coal Coking

Directory of Open Access Journals (Sweden)

Jan Konieczyński

2012-01-01

Full Text Available In order to assess the penetration of individual trace elements into the air through their release in the coal coking process, it is necessary to determine the loss of these elements by comparing their contents in the charge coal and in coke obtained. The present research covered four coke oven batteries differing in age, technology, and technical equipment. By using mercury analyzer MA-2 and the method of ICP MS As, Be, Cd, Co, Hg, Mn, Ni, Se, Sr, Tl, V, and Zn were determined in samples of charge coal and yielded coke. Basing on the analyses results, the release coefficients of selected elements were determined. Their values ranged from 0.5 to 94%. High volatility of cadmium, mercury, and thallium was confirmed. The tests have shown that although the results refer to the selected case studies, it may be concluded that the air purity is affected by controlled emission occurring when coke oven batteries are fired by crude coke oven gas. Fugitive emission of the trace elements investigated, occurring due to coke oven leaks and openings, is small and, is not a real threat to the environment except mercury.

40 CFR 63.302 - Standards for by-product coke oven batteries.

Science.gov (United States)

2010-07-01

... batteries. 63.302 Section 63.302 Protection of Environment ENVIRONMENTAL PROTECTION AGENCY (CONTINUED) AIR... National Emission Standards for Coke Oven Batteries § 63.302 Standards for by-product coke oven batteries... oven emissions from each affected existing by-product coke oven battery that exceed any of the...

Development of the super coke oven for productivity and environment enhancement toward the 21st century (SCOPE 21); Sekitan kodo tenkan cokes seizo gijutsu no kaihatsu

Energy Technology Data Exchange (ETDEWEB)

Sugiyama, T [Center for Coal Utilization, Japan, Tokyo (Japan); Nakashima, Y; Nishioka, K; Otsuka, J [The Japan Iron and Steel Federation, Tokyo (Japan)

1996-09-01

Serious shortage is predicted on cokes for blast furnaces in the first half of the 21st century. In order to deal flexibly with the fluid world market in the future, it is necessary to have a technology developed, by which coals from coking coal to non-coking dust coal can be used. The Japan Iron and Steel Federation and the Center for Coal Utilization, Japan are working on research and development of a new process with enhanced environmentality and economy (SCOPE 21) as a coke manufacturing process to respond to the requirements arisen from the above situation. The process is assessed basing on basic technological seeds such as rapid coal heating and high-speed carbonization and reformation of middle to low temperature cokes. The organizations are moving forward an eight-year development program which has started in fiscal 1994. This paper reports the summary of the development, and results of investigations and researches performed during fiscals 1994 and 1995. Rapid heating tests, middle to low temperature coke reformation tests, and tests for plug transportation of high-temperature coal have been performed. It has been verified, for example, that rapid coal heating can improve coke strength. The development work is being promoted toward grain size distribution and upscaling problems. 5 refs., 16 figs., 2 tabs.

Management of abnormal radioactive wastes at nuclear power plants

International Nuclear Information System (INIS)

1989-01-01

As with any other industrial activity, a certain level of risk is associated with the operation of nuclear power plants and other nuclear facilities. That is, on occasions nuclear power plants or nuclear facilities may operate under conditions which were not specifically anticipated during the design and construction of the plant. These abnormal conditions and situations may cause the production of abnormal waste, which can differ in character or quantity from waste produced during normal routine operation of nuclear facilities. Abnormal waste can also occur during decontamination programmes, replacement of a reactor component, de-sludging of storage ponds, etc. The management of such kinds of waste involves the need to evaluate existing waste management systems in order to determine how abnormal wastes should best be handled and processed. There are no known publications on this subject, and the IAEA believes that the development and exchange of such information among its Member States would be useful for specialists working in the waste management area. The main objective of this report is to review existing waste management practices which can be applied to abnormal waste and provide assistance in the selection of appropriate technologies and processes that can be used when abnormal situations occur. Naturally, the subject of abnormal waste is complex and this report can only be considered as a guide for the management of abnormal waste. Refs, figs and tabs.

Phase I: the pipeline-gas demonstration plant. Demonstration plant engineering and design. Volume 18. Plant Section 2700 - Waste Water Treatment

Energy Technology Data Exchange (ETDEWEB)

None

1981-05-01

Contract No. EF-77-C-01-2542 between Conoco Inc. and the US Department of Energy provides for the design, construction, and operation of a demonstration plant capable of processing bituminous caking coals into clean pipeline quality gas. The project is currently in the design phase (Phase I). This phase is scheduled to be completed in June 1981. One of the major efforts of Phase I is the process and project engineering design of the Demonstration Plant. The design has been completed and is being reported in 24 volumes. This is Volume 18 which reports the design of Plant Section 2700 - Waste Water Treatment. The objective of the Waste Water Treatment system is to collect and treat all plant liquid effluent streams. The system is designed to permit recycle and reuse of the treated waste water. Plant Section 2700 is composed of primary, secondary, and tertiary waste water treatment methods plus an evaporation system which eliminates liquid discharge from the plant. The Waste Water Treatment Section is designed to produce 130 pounds per hour of sludge that is buried in a landfill on the plant site. The evaporated water is condensed and provides a portion of the make-up water to Plant Section 2400 - Cooling Water.

77 FR 15123 - Foundry Coke From China; Scheduling of an Expedited Five-Year Review

Science.gov (United States)

2012-03-14

... submitted by ABC Coke, Erie Coke, Tonawanda Coke Corporation, and Walter Coke Co. to be individually... Analyst... Cynthia Foreso (205-3348). Attorney Charles St. Charles (205-2782). Supervisory Investigator...

Pyrolisator Coal to be Cokes (Coal Cokes Casting Metal Industry Standard

Directory of Open Access Journals (Sweden)

Sukamto

2016-01-01

Full Text Available Pyrolisis of coal is partial combustion to reduce total moisture, volatile matter and sulfur contens and increase the calorific value of coal. The results of pyrolysis of coal is coke. At the laboratory level studies, pyrolisis done in batch using different calorie, namely 5800, 6000, 6300 kcal/kg and a time of 15-60 minutes and the temperature 400-800°C. Maximum results obtained total moisture (0.44%, fixed carbon (89%, volatile matter (2.4%, sulfur content (undetected and ash (7.2%. Then applied to the scale miniplant with continuous processes using multitube pyrolisator which are designed to operate in the temperature range 400-800°C and a flow rate of 240-730 kg/h, obtained coal cokes that meets industry quality standards, namely TM (0.42%, FC (90.40%, VM (2.16%, S (not detected, Ash (6.8% incalori 6300 kcal/h, a flow rate of 240 kg / h and temperatures between 600-700°C

Radioactive-waste isolation pilot plant

International Nuclear Information System (INIS)

Weart, W.D.

1977-01-01

The objective of the Waste Isolation Pilot Plant (WIPP) program is to demonstrate the suitability of bedded salt, specifically, the bedded salt deposits in the Los Medanos area of southeastern New Mexico, as a disposal medium for radioactive wastes. Our program responsibilities include site selection considerations, all aspects of design and development, technical guidance of facility operation, environmental impact assessment, and technical support to ERDA for developing public understanding of the facility

Emission of Polychlorinated Dibenzo-p-Dioxins (PCDDs and Polychlorinated Dibenzofurans (PCDFs from Underfiring System of Coke Oven Battery

Directory of Open Access Journals (Sweden)

Rafał Bigda

2017-11-01

Full Text Available A coke oven battery is not considered as a significant source of PCDDs/PCDFs emissions; however, due to small amounts of chlorine in coal dioxins, dibenzofurans may be formed. The paper presents the attempts to determine the level of emission of PCDDs/PCDFs from the COB underfiring system and to confront the obtained results with the calculations based on the mass balance of chlorine in the coking process and reactions of both chlorophenols formation and PCDDs and PCDFs formation from mono- and polychlorophenols. There were PCDDs/PCDFs concentrations measured in flue gases from the underfiring system of two COBs at a Polish coking plant. The measurements included both an old and a new battery. The obtained concentrations of PCDDs/PCDFs were lower than reported in the literature (0.5-1.7 ng I-TEQ/tcoke, while the results for old COB were on average 3 times higher than for the new one. It was found that PCDD/F emission from COB underfiring system is insignificant and that PCDDs/PCDFs formation during coal coking should consider the mechanisms of their formation from mono- and polychlorophenols, as well as the influence of process parameters on the synthesis.

Modelling of Coke Layer Collapse during Ore Charging in Ironmaking Blast Furnace by DEM

Science.gov (United States)

Narita, Yoichi; Mio, Hiroshi; Orimoto, Takashi; Nomura, Seiji

2017-06-01

A technical issue in an ironmaking blast furnace operation is to realize the optimum layer thickness and the radial distribution of burden (ore and coke) to enhance its efficiency and productivity. When ore particles are charged onto the already-embedded coke layer, the coke layer-collapse phenomenon occurs. The coke layer-collapse phenomenon has a significant effect on the distribution of ore and coke layer thickness in the radial direction. In this paper, the mechanical properties of coke packed bed under ore charging were investigated by the impact-loading test and the large-scale direct shear test. Experimental results show that the coke particle is broken by the impact force of ore charging, and the particle breakage leads to weaken of coke-layer strength. The expression of contact force for coke in Discrete Element Method (DEM) was modified based on the measured data, and it followed by the 1/3-scaled experiment on coke's collapse phenomena. Comparing a simulation by modified model to the 1/3-scaled experiment, they agreed well in the burden distribution.

Incineration plant for low active waste at Inshass, LAWI

International Nuclear Information System (INIS)

Krug, W.; Thoene, L.; Schmitz, H.J.; Abdelrazek, I.D.

1993-10-01

The LAWI (Low Active Waste Incinerator) prototype incinerating plant was devised and constructed according to the principle of the Juelich thermoprocess and installed at the Egyptian research centre Inshass. In parallel, AEA Cairo devised and constructed their own operations building for this plant with all the features, infrastructural installations and rooms required for operating the plant and handling and treating low-level radioactive wastes. The dimensions of this incinerator were selected so as to be sufficient for the disposal of solid, weakly radioactive combustible wastes from the Inshass Research Centre and the environment (e.g. Cairo hospitals). (orig./DG) [de

Radioactive waste processing method for a nuclear power plant

Energy Technology Data Exchange (ETDEWEB)

Sugimoto, Y; Kuriyama, O

1976-06-04

Object is to subject radioactive liquid waste in a nuclear power plant to reverse permeation process after which it is vaporized and concentrated thereby decreasing the quantity of foam to be used to achieve effective concentration of the liquid waste. Liquid waste containing a radioactive material produced from a nuclear power plant is first applied with pressure in excess of osmotic pressure by a reverse permeation device and is separated into clean water and concentrated liquid by semi-permeable membrane. Next, the thus reverse-permeated and concentrated waste is fed to an evaporator which control foaming by the foam and then further reconcentrated for purification of the liquid waste.

Producing hydrogen from coke-oven gas: the Solmer project. [PSA process

Energy Technology Data Exchange (ETDEWEB)

Bernard, G; Vidal, J

1984-05-01

After presenting the energy situation at the Solmer plant, where coke-oven gas is produced to excess, the authors examine the technical and economic possibilities of utilizing this gas for hydrogen extraction. They describe a project (based on the PSA process) for producing some 65 t/d of hydrogen and present the technical features of the scheme. An evaluation of the energy and financial costs of producing the hydrogen confirms the competitive status of the process.

Obtaining fuel briquets from the solid municipal waste

International Nuclear Information System (INIS)

Armenski, Slave; Kachurkov, Gjorgji; Vasilevski, Goce

1998-01-01

Recycling systems for solid waste materials are designed to reduce the amount of solid waste materials going to land fields. Through the Trash Separation Systems, clean municipal waste are reused in production of fuel pellets. Other waste streams such as coal fines, sawdust, wood chips, coke breeze and agricultural waste can be blended with these pellets along with a high thermal value binder and/or used motor oil to form a quality clean burning alternative fuel. (Author)

Engineering solutions to improve environmental characteristics of coke-chemical industry

Energy Technology Data Exchange (ETDEWEB)

Lavrov, K G; Cherkashina, O I; Pushkarev, G P; Pakhomov, V A; Florinskii, N V; Oleinik, K P; Likhogub, E P; Dorfman, G A; Gorelik, Ya L; Vorona, V K

1979-06-01

In future projects consideration will be given to reduction of air and water pollution. Escape of dust from coke-batteries and coal preparation plants will be stopped by using hermetic enclosures with aspirators. Effluent gases and vapours will be curbed by using more efficient scrubbers and flare systems. Effluent waters will be treated at two-stage flotation stations and recycled to 95% as cooling and utility water. Cooling water consumption will be reduced by the use of air coolers. Pollution monitoring will be improved.

Investigating combined influence of petrology and technological parameters on strength of porous coke body

Energy Technology Data Exchange (ETDEWEB)

Dinel' t, V.M.; Shkoller, M.B.; Stankevich, A.S.; Korchuganova, G.S.

1983-09-01

The VUKhIN branch in Kuznetsk investigated effects of coal petrology and coking conditions on structural strength of coke in blast furnaces. Structural strength of coke produced from black coal from the Kuzbass as well as structural strength of coke partially gasified by carbon dioxide under conditions similar to those in blast furnaces was investigated. Fourteen samples of coal mixtures from the Kuzbass were used. Regression analysis was applied. Equations for forecasting coke properties on the basis of coal petrology and selected parameters characterizing coking were derived. Analyses showed that coke structural strength was decisively influenced by coefficients which characterized the average reflectivity of vitrinite in a coal mixture and its average density. After partial coke gasification by carbon dioxide effects of coefficients which characterized coal mixture nonhomogeneity (fluctuations of vitrinite reflectivity) and coal mixture density increased. Increasing coal density partially compensated negative effects of fluctuations of vitrinite reflectivity on coke structural strength. (10 refs.) (In Russian)

Processing of transuranic waste at the Savannah River Plant

International Nuclear Information System (INIS)

Daugherty, B.A.; Gruber, L.M.; Mentrup, S.J.

1986-01-01

Transuranic wastes at the Savannah River Plant (SRP) have been retrievably stored on concrete pads since early 1972. This waste is stored primarily in 55-gallon drums and large carbon steel boxes. Higher activity drums are placed in concrete culverts. In support of a National Program to consolidate and permanently dispose of this waste, a major project is planned at SRP to retrieve and process this waste. This project, the TRU Waste Facility (TWF), will provide equipment and processes to retrieve TRU waste from 20-year retrievable storage and prepare it for permanent disposal at the Waste Isolation Pilot Plant (WIPP) geological repository in New Mexico. This project is an integral part of the SRP Long Range TRU Waste Management Program to reduce the amount of TRU waste stored at SRP. The TWF is designed to process 15,000 cubic feet of retrieved waste and 6200 cubic feet of newly generated waste each year of operation. This facility is designed to minimize direct personnel contact with the waste using state-of-the-art remotely operated equipment

Development and Testing of the Advanced CHP System Utilizing the Off-Gas from the Innovative Green Coke Calcining Process in Fluidized Bed

Energy Technology Data Exchange (ETDEWEB)

Chudnovsky, Yaroslav [Gas Technology Inst., Des Plaines, IL (United States); Kozlov, Aleksandr [Gas Technology Inst., Des Plaines, IL (United States)

2013-08-15

Green petroleum coke (GPC) is an oil refining byproduct that can be used directly as a solid fuel or as a feedstock for the production of calcined petroleum coke. GPC contains a high amount of volatiles and sulfur. During the calcination process, the GPC is heated to remove the volatiles and sulfur to produce purified calcined coke, which is used in the production of graphite, electrodes, metal carburizers, and other carbon products. Currently, more than 80% of calcined coke is produced in rotary kilns or rotary hearth furnaces. These technologies provide partial heat utilization of the calcined coke to increase efficiency of the calcination process, but they also share some operating disadvantages. However, coke calcination in an electrothermal fluidized bed (EFB) opens up a number of potential benefits for the production enhancement, while reducing the capital and operating costs. The increased usage of heavy crude oil in recent years has resulted in higher sulfur content in green coke produced by oil refinery process, which requires a significant increase in the calcinations temperature and in residence time. The calorific value of the process off-gas is quite substantial and can be effectively utilized as an “opportunity fuel” for combined heat and power (CHP) production to complement the energy demand. Heat recovered from the product cooling can also contribute to the overall economics of the calcination process. Preliminary estimates indicated the decrease in energy consumption by 35-50% as well as a proportional decrease in greenhouse gas emissions. As such, the efficiency improvement of the coke calcinations systems is attracting close attention of the researchers and engineers throughout the world. The developed technology is intended to accomplish the following objectives: - Reduce the energy and carbon intensity of the calcined coke production process. - Increase utilization of opportunity fuels such as industrial waste off-gas from the novel

The ChemChar process for hazardous-waste treatment

International Nuclear Information System (INIS)

McGowin, A.E.

1991-01-01

The ChemChar Reverse-Burn Gasification Process has been studied for application to the thermal destruction of radioactive waste organic ion exchange resins. The resulting char was mixed with cement to form a dry, leach-resistant final disposal product. Successful regeneration of spent granular activated carbons was achieved with reverse-burn gasification. Regeneration parameters such as moisture content and supplemental fuel addition were investigated. The performance of regenerated carbon was evaluated by batch equilibrium and breakthrough assay and was comparable to that of the original. Surface areas were determined by the BET method. The fate of mercury during reverse-burn gasification was investigated. TRB Char adsorbent was used to remove mercury vapor emission from the process. The use of petroleum coke as a substrate for gasification of wastes was studied. Petroleum coke was activated by reverse-burn gasification to produce a highly porous, low surface area solid. Destruction efficiency for hexachlorobenzene on activated coke was considerably lower than on coal char, however, the addition of iron appeared to catalyze hexachlorobenzene gasification

Coke Formation During Hydrocarbons Pyrolysis. Part Two: Methane Thermal Cracking Formation de coke pendant la pyrolyse des hydrocarbures. Deuxième partie : pyrolyse du méthane

Directory of Open Access Journals (Sweden)

Billaud F.

2006-11-01

Full Text Available Part one of this article dealt with coking in a steam cracking furnace. In this process, coke deposition is a very complex phenomenon due to the number of parameters involved. Nevertheless, for this process, coke deposition is a secondary reaction which does not affect steam cracking yields. It is completely different for methane thermal cracking. Coke is one of the main products of this reaction. Part two of this article deals with coke deposition on the walls of the reactors used for methane thermal cracking. After a brief description of the different set-ups used to study coke deposition, the main parameters involved are listed. The importance of temperature, conversion, type of diluent, and hydrocarbon partial pressure will be enhanced. To conclude, two approaches to the mechanism are proposed to explain coke formation during methane thermal cracking. La première partie de cet article faisait le point sur les réactions indésirables de cokage dans les réacteurs de vapocraquage : dans le cadre de ce procédé, la formation de coke est un phénomène complexe du fait du nombre important de paramètres mis en jeu. Toutefois, pour ce procédé, la réaction de formation du coke à la paroi des réacteurs est une réaction secondaire qui n'affecte pas les rendements de vapocraquage. Ceci est complètement différent dans le cas de la pyrolyse thermique du méthane, procédé pour lequel le coke est un produit principal et indésirable de la réaction. La seconde partie de cet article est consacrée plus particulièrement à la formation du coke, lors de la pyrolyse du méthane et présente les principaux résultats expérimentaux décrits dans la littérature. Parmi les différents montages expérimentaux utilisés pour mesurer le dépôt de coke, il est mentionné, à partir des travaux de la littérature, les 2 techniques suivantes : - la technique de la paroi chaude, - la technique du fil chaud. Pour la première technique, les montages exp

Solid municipal waste processing plants: Cost benefit analysis

International Nuclear Information System (INIS)

Gerardi, V.

1992-01-01

This paper performs cost benefit analyses on three solid municipal waste processing alternatives with plants of diverse daily outputs. The different processing schemes include: selected wastes incineration with the production of refuse derived fuels; selected wastes incineration with the production of refuse derived fuels and compost; pyrolysis with energy recovery in the form of electric power. The plant daily outputs range from 100 to 300 tonnes for the refuse derived fuel alternatives, and from 200 to 800 tonnes for the pyrolysis/power generation scheme. The cost analyses consider investment periods of fifteen years in duration and interest rates of 5%

Waste generation comparison: Coal-fired versus nuclear power plants

International Nuclear Information System (INIS)

LaGuardia, T.S.

1998-01-01

Low-level radioactive waste generation and disposal attract a great deal of attention whenever the nuclear industry is scrutinized by concerned parties, be it the media, the public, or political interests. It is therefore important to the nuclear industry that this issue be put into perspective relative to other current forms of energy production. Most of the country's fossil-fueled power comes from coal-fired plants, with oil and gas as other fuel sources. Most of the generated waste also comes from coal plants. This paper, therefore, compares waste quantities generated by a typical (1150-MW(electric)) pressurized water reactor (PWR) to that of a comparably sized coal-fired power plant

Simulation and optimization of a coking wastewater biological treatment process by activated sludge models (ASM).

Science.gov (United States)

Wu, Xiaohui; Yang, Yang; Wu, Gaoming; Mao, Juan; Zhou, Tao

2016-01-01

Applications of activated sludge models (ASM) in simulating industrial biological wastewater treatment plants (WWTPs) are still difficult due to refractory and complex components in influents as well as diversity in activated sludges. In this study, an ASM3 modeling study was conducted to simulate and optimize a practical coking wastewater treatment plant (CWTP). First, respirometric characterizations of the coking wastewater and CWTP biomasses were conducted to determine the specific kinetic and stoichiometric model parameters for the consecutive aeration-anoxic-aeration (O-A/O) biological process. All ASM3 parameters have been further estimated and calibrated, through cross validation by the model dynamic simulation procedure. Consequently, an ASM3 model was successfully established to accurately simulate the CWTP performances in removing COD and NH4-N. An optimized CWTP operation condition could be proposed reducing the operation cost from 6.2 to 5.5 €/m(3) wastewater. This study is expected to provide a useful reference for mathematic simulations of practical industrial WWTPs. Copyright © 2015 Elsevier Ltd. All rights reserved.

Kress indirect dry cooling system, Bethlehem Steel's Coke Plant demonstration at Sparrows Point, Maryland. Volume 2. Appendices G-N. Final report, February 1990-February 1992

International Nuclear Information System (INIS)

Ossman, A.G.

1993-05-01

The report provides an evaluation of the Kress Indirect Dry Cooling (KIDC) process. The KIDC process is an innovative system for the handling and cooling of coke produced from a slot type by-product coke oven battery. The report is based on the test work and demonstration of the system at Bethlehem Steel Corporation's Sparrows Point facility in 1991. The report covers both environmental and operational impacts of the KIDC process. The report, Volume 2, contains appendices G-N. Volume 1, PB93-191302, contains the technical report as well as appendices A-F. Volume 2 contains appendixes on coke quality data, blast furnace balwax model report, KIDC operating cost and maintenance requirements, Kress box thickness readings, KIDC coke discharge temperature, QA/QC program, door leak data, and coal data

GASIFICATION PLANT COST AND PERFORMANCE OPTIMIZATION

Energy Technology Data Exchange (ETDEWEB)

Samuel S. Tam

2002-05-01

The goal of this series of design and estimating efforts was to start from the as-built design and actual operating data from the DOE sponsored Wabash River Coal Gasification Repowering Project and to develop optimized designs for several coal and petroleum coke IGCC power and coproduction projects. First, the team developed a design for a grass-roots plant equivalent to the Wabash River Coal Gasification Repowering Project to provide a starting point and a detailed mid-year 2000 cost estimate based on the actual as-built plant design and subsequent modifications (Subtask 1.1). This unoptimized plant has a thermal efficiency of 38.3% (HHV) and a mid-year 2000 EPC cost of 1,681 $/kW. This design was enlarged and modified to become a Petroleum Coke IGCC Coproduction Plant (Subtask 1.2) that produces hydrogen, industrial grade steam, and fuel gas for an adjacent Gulf Coast petroleum refinery in addition to export power. A structured Value Improving Practices (VIP) approach was applied to reduce costs and improve performance. The base case (Subtask 1.3) Optimized Petroleum Coke IGCC Coproduction Plant increased the power output by 16% and reduced the plant cost by 23%. The study looked at several options for gasifier sparing to enhance availability. Subtask 1.9 produced a detailed report on this availability analyses study. The Subtask 1.3 Next Plant, which retains the preferred spare gasification train approach, only reduced the cost by about 21%, but it has the highest availability (94.6%) and produces power at 30 $/MW-hr (at a 12% ROI). Thus, such a coke-fueled IGCC coproduction plant could fill a near term niche market. In all cases, the emissions performance of these plants is superior to the Wabash River project. Subtasks 1.5A and B developed designs for single-train coal and coke-fueled power plants. This side-by-side comparison of these plants, which contain the Subtask 1.3 VIP enhancements, showed their similarity both in design and cost (1,318 $/kW for the

Radioactive Waste Disposal Pilot Plant concept for a New Mexico site

International Nuclear Information System (INIS)

Weart, W.D.

1976-01-01

Twenty years of investigation have shown that disposal of nuclear wastes in deep salt formations is the surest means of isolating these wastes from the biosphere for the extremely long period of time required. A large scale demonstration of this capability will soon be provided by a Radioactive Waste Disposal Pilot Plant (RWDPP) to be developed in southeastern New Mexico. Initially, the pilot plant will accept only ERDA generated waste; high level waste from the commercial power reactor fuel cycle will eventually be accommodated in the pilot plant and the initial RWDPP design will be compatible with this waste form. Selection of a specific site and salt horizon will be completed in June 1976. Conceptual design of the RWDPP and assessment of its environmental impact will be completed by June 1977. Construction is expected to start in 1978 with first waste accepted in 1982. The present concept develops disposal areas for all nuclear waste types in a single salt horizon about 800 meters deep. This single level can accommodate all low level and high level waste generated in the United States through the year 2010. A major constraint on the RWDPP design is the ERDA requirement that all waste be ''readily'' retrievable during the duration of pilot plant operation

Region 9 NPDES Facilities - Waste Water Treatment Plants

Science.gov (United States)

Point geospatial dataset representing locations of NPDES Waste Water Treatment Plant Facilities. NPDES (National Pollution Discharge Elimination System) is an EPA permit program that regulates direct discharges from facilities that discharge treated waste water into waters of the US. Facilities are issued NPDES permits regulating their discharge as required by the Clean Water Act. A facility may have one or more outfalls (dischargers). The location represents the facility or operating plant.

Radioactive waste treatment technology at Czech nuclear power plants

International Nuclear Information System (INIS)

Kulovany, J.

2001-01-01

This presentation describes the main technologies for the treatment and conditioning of radioactive wastes at Czech nuclear power plants. The main technologies are bituminisation for liquid radioactive wastes and supercompaction for solid radioactive wastes. (author)

Increasing operational efficiency in a radioactive waste processing plant - 16100

International Nuclear Information System (INIS)

Turner, T.W.; Watson, S.N.

2009-01-01

The solid waste plant at Harwell in Oxfordshire, contains a purpose built facility to input, assay, visually inspect and sort remote handled intermediate level radioactive waste (RHILW). The facility includes a suite of remote handling cells, known as the head-end cells (HEC), which waste must pass through in order to be repackaged. Some newly created waste from decommissioning works on site passes through the cells, but the vast majority of waste for processing is historical waste, stored in below ground tube stores. Existing containers are not suitable for long term storage, many are already badly corroded, so the waste must be efficiently processed and repackaged in order to achieve passive safety. The Harwell site is currently being decommissioned and the land is being restored. The site is being progressively de-licensed, and redeveloped as a business park, which can only be completed when all the nuclear liabilities have been removed. The recovery and processing of old waste in the solid waste plant is a key project linked to de-licensing of a section of the site. Increasing the operational efficiency of the waste processing plant could shorten the time needed to clear the site and has the potential to save money for the Nuclear Decommissioning Authority (NDA). The waste processing facility was constructed in the mid 1990's, and commissioned in 1999. Since operations began, the yearly throughput of the cells has increased significantly every year. To achieve targets set out in the lifetime plan (LTP) for the site, throughput must continue to increase. The operations department has measured the overall equipment effectiveness (OEE) of the process for the last few years, and has used continuous improvement techniques to decrease the average cycle time. Philosophies from operational management practices such as 'lean' and 'kaizen' have been employed successfully to drive out losses and increase plant efficiency. This paper will describe how the solid waste plant

Combustion kinetics of the coke on deactivated dehydrogenation catalysts

NARCIS (Netherlands)

Luo, Sha; He, Songbo; Li, XianRu; Li, Jingqiu; Bi, Wenjun; Sun, Chenglin

2015-01-01

The coke combustion kinetics on the deactivated catalysts for long chain paraffin dehydrogenation was studied by the thermogravimetry and differential thermogravimetry (TG–DTG) technique. The amount and H/C mole ratio of the coke were determined by the TG and elemental analysis. And the

Fatigue life estimation on coke drum due to cycle optimization

Science.gov (United States)

Siahaan, Andrey Stephan; Ambarita, Himsar; Kawai, Hideki; Daimaruya, Masashi

2018-04-01

In the last decade, due to the increasing demand of petroleum product, the necessity for converting the heavy oil are increasing. Thus, demand for installing coke drum in whole world will be increase. The coke drum undergoes the cyclic high temperature and suddenly cooling but in fact is not designed to withstand that kind of cycle, thus the operational life of coke drum is much shorter in comparison to other equipment in oil refinery. Various factors determine in order to improve reliability and minimize the down time, and it is found that the cycle optimization due to cycle, temperature, and pressure have an important role. From this research it is found that the fatigue life of the short cycle is decrease by a half compare to the normal cycle. It also found that in the preheating stage, the stress peak is far exceed the yield strength of coke drum material and fall into plastic deformation. This is happened because of the temperature leap in the preheating stage that cause thermal shock in the upper part of the skirt of the coke drum.

Radioactive wastes from reprocessing plants

International Nuclear Information System (INIS)

Huppert, K.L.

1977-01-01

The lecture deals with definition, quantity and type of radioactive waste products occurring in a fuel reprocessing plant. Solid, liquid and gaseous fission and activation products are formed during the dissolution of the fuel and during the extraction process, and they must be separated from the fissionalble uranium and plutonium not spent. The chemical behaviour of these products (Zr, Ru, Np, gaseous substances, radiolysis products), which is sometimes very problematic, necessitates careful process control. However, the lifetime of nuclides is just as important for the conditions of the reprocessing procedure. The types of waste obtained after reprocessing are classified according to their state of aggregation and level of activity and - on the basis of the operational data of a prototype plant - they are quantitatively extrapolated for the operation of a large-scale facility of 1,400 tons of fuel annually. (RB) [de

Development of bitumization plant of radioactive waste

International Nuclear Information System (INIS)

Lee, S.H.; Chun, K.S.; Song, H.Y.; Park, S.H.; Park, W.J.; Ryoo, R.; Cho, W.J.; Wee, K.S.; Lee, J.D.

1981-01-01

This study is to develop the bitumization techniques of radioactive waste concentrates from nuclear power plants (PWR), Cold-run and hot-run bitumization pilot plant were designed and constructed, and testing was carried out. The results show that the range of pH 7 to 8, in which a soluble product could form, is suitable for feeding in the waste and for its incorporation into asphalt, domestic blown asphalt is suitable up to an exposure of 10 8 rad. The estimated viscosity of the asphalt/waste product is about 14 poises at 175 0 C and the asphalt/wastes products in simulated sea-water for three weeks showed no evidence of swelling. The leaching rate from the spent resin/asphalt products in distilled water less than 1/1000 of that from the cement-products. It is considered that the resin content which is suitable for the incorporation of spent resin into asphalt is less than 50 wt%

Component design considerations for gas turbine HTGR waste-heat power plant

International Nuclear Information System (INIS)

McDonald, C.F.; Vrable, D.L.

1976-01-01

Component design considerations are described for the ammonia waste-heat power conversion system of a large helium gas-turbine nuclear power plant under development by General Atomic Company. Initial component design work was done for a reference plant with a 3000-MW(t) High-Temperature Gas-Cooled Reactor (HTGR), and this is discussed. Advanced designs now being evaluated include higher core outlet temperature, higher peak system pressures, improved loop configurations, and twin 4000-MW(t) reactor units. Presented are the design considerations of the major components (turbine, condenser, heat input exchanger, and pump) for a supercritical ammonia Rankine waste heat power plant. The combined cycle (nuclear gas turbine and waste-heated plant) has a projected net plant efficiency of over 50 percent. While specifically directed towards a nuclear closed-cycle helium gas-turbine power plant (GT-HTGR), it is postulated that the bottoming waste-heat cycle component design considerations presented could apply to other low-grade-temperature power conversion systems such as geothermal plants

Waste Isolation Pilot Plant No-migration variance petition

International Nuclear Information System (INIS)

1990-03-01

This report describes various aspects of the Waste Isolation Pilot Plant (WIPP) including design data, waste characterization, dissolution features, ground water hydrology, natural resources, monitoring, general geology, and the gas generation/test program

Effects of thermal desorption on the composition of two coking plant soils: Impact on solvent extractable organic compounds and metal bioavailability

Energy Technology Data Exchange (ETDEWEB)

Biache, Coralie [G2R UMR 7566, Nancy Universite, CNRS, Boulevard des Aiguillettes B.P. 239, F-54506 Vandoeuvre-les-Nancy (France); LIMOS UMR 7137, Nancy Universite, CNRS, Boulevard des Aiguillettes B.P. 239, F-54506 Vandoeuvre-les-Nancy (France)], E-mail: coralie.biache@g2r.uhp-nancy.fr; Mansuy-Huault, Laurence; Faure, Pierre [G2R UMR 7566, Nancy Universite, CNRS, Boulevard des Aiguillettes B.P. 239, F-54506 Vandoeuvre-les-Nancy (France); Munier-Lamy, Colette; Leyval, Corinne [LIMOS UMR 7137, Nancy Universite, CNRS, Boulevard des Aiguillettes B.P. 239, F-54506 Vandoeuvre-les-Nancy (France)

2008-12-15

To evaluate the efficiency and the influence of thermal desorption on the soil organic compartment, contaminated soils from coking plant sites (NM and H) were compared to their counterparts treated with thermodesorption. The extractable organic matter, and the metal content and distribution with soil compartments were studied. In both thermodesorbed soils, PAH (polycyclic aromatic hydrocarbon) degradation exceeded 90%. However, the thermal desorption led not only to a volatilization of the organic compounds but also to the condensation of extractable organic matter. The treatments only affected the Fe and Zn distribution within the more stable fractions, whereas the organic compound degradation did not affect their mobility and availability. - Thermal desorption does not induce a metal mobilization but condensation seems to occur during the treatment.

Fundamentals of Delayed Coking Joint Industry Project

Energy Technology Data Exchange (ETDEWEB)

Volk Jr., Michael; Wisecarver, Keith D.; Sheppard, Charles M.

2003-02-07

The coking test facilities include three reactors (or cokers) and ten utilities. Experiments were conducted using the micro-coker, pilot-coker, and stirred-batch coker. Gas products were analyzed using an on-line gas chromatograph. Liquid properties were analyzed in-house using simulated distillation (HP 5880a), high temperature gas chromatography (6890a), detailed hydrocarbon analysis, and ASTM fractionation. Coke analyses as well as feedstock analyses and some additional liquid analyses (including elemental analyses) were done off-site.

Processing constraints on high-level nuclear waste glasses for Hanford Waste Vitrification Plant

International Nuclear Information System (INIS)

Hrma, P.R.

1993-09-01

The work presented in this paper is a part of a major technology program supported by the U.S. Department of Energy (DOE) in preparation for the planned operation of the Hanford Waste Vitrification Plant (HWVP). Because composition of Hanford waste varies greatly, processability is a major concern for successful vitrification. This paper briefly surveys general aspects of waste glass processability and then discusses their ramifications for specific examples of Hanford waste streams

Characterization of core-drilled cokes in a working blast furnace

Energy Technology Data Exchange (ETDEWEB)

Shanning Dong; Nigel Paterson; Denis R. Dugwell; Rafael Kandiyoti [Imperial College London, London (United Kingdom). Dept. of Chemical Engineering

2007-07-01

A batch of tuyere-level core-drilled cokes, taken from a blast furnace working with coal injection has been characterized using a battery of analytical techniques. These included size exclusion chromatography (SEC), FT-Raman Spectroscopy (FT-RS) and X-ray Powder Diffraction (XRD). SEC tests on NMP-extracts of cokes taken from zones where temperatures were ca. 1500{sup o}C, showed the presence of heavy soot-like material (ca. 107-108 u apparent mass). By contrast, cokes in higher temperature zones (ca. 2000{sup o}C), only gave small amounts of extractable material with up to ca. 105 u apparent mass. The presence of soot-like material indicated the conversion-unfavoured locations at the tuyere-level. FT-Raman spectra of NMP-extracted cokes varied: the area ratios of D (at 1288-1295cm{sup -1}) to G (at ca. 1596cm{sup -1}) bands decreased as the exposure temperature increased. The random (r) fractions decreased with increasing exposure temperature, whereas, the graphitic (G) fractions increased whilst the defect (D) fraction showed a more complex variation with temperature. The latter is a likely indicator of graphitization of tuyere-level cokes in the blast furnace. The Raman spectral results were validated by XRD analyses of the demineralised and NMP-extracted cokes. Raceway coke possessed the largest crystalline dimensions and closest inter-layer spacing because it had encountered highest temperatures as well as iron catalysis. The combination of SEC and Raman spectrometry on core-drill samples has provided information relevant for maintaining stable operation in a blast-furnace operating with coal injection. 13 refs., 7 figs., 6 tabs.

Enhanced specific capacitance of modified needle cokes by controlling oxidation treatment

International Nuclear Information System (INIS)

Yang, Sunhye; Kim, Ick-Jun; Choi, In-Sik; Soo Kim, Hyun; Tack Kim, Yu

2010-01-01

The electric double-layer performance of needle cokes can be affected by the morphology of structures. Hence, we introduce modified needle cokes by using simple oxidation treatment. The degree of graphitization with high specific capacitance is controlled by acid and heat treatment. The active sites of cokes are increased with increasing oxidation time. Dilute nitric acid (HNO 3 ) and sodium chlorate (NaClO 3 ) are used for the activation of cokes. In this case, the interlayer distance is dramatically increased from 3.5 to 8.9 A. The specific capacitances are 33 F g -1 and 30 F ml -1 , respectively, on a two-electrode system with a potential range of 0-2.5 V. The behaviors of double-layer capacitance are demonstrated by the charge-discharge process and the morphologies of modified needle cokes are analyzed by XRD, FE-SEM, BET and elemental analysis.

Waste Isolation Pilot Plant Safety Analysis Report. Volume 5

International Nuclear Information System (INIS)

1986-01-01

This Safety Analysis Report (SAR) has been prepared by the US Department of Energy (DOE) to support the construction and operation of the Waste Isolation Pilot Plant (WIPP) in southeastern New Mexico. The WIPP facility is designed to receive, inspect, emplace, and store unclassified defense-generated transuranic wastes in a retrievable fashion in an underground salt medium and to conduct studies and perform experiments in salt with high-level wastes. Upon the successful completion of these studies and experiments, WIPP is designed to serve as a permanent facility. The first chapter of this report provides a summary of the location and major design features of WIPP. Chapters 2 through 5 describe the site characteristics, design criteria, and design bases used in the design of the plant and the plant operations. Chapter 6 discusses radiation protection; Chapters 7 and 8 present an accident analysis of the plant and an assessment of the long-term waste isolation at WIPP. The conduct of operations and operating controls and limits are discussed in Chapters 9 and 10. The quality assurance programs are described in Chapter 11

Waste Isolation Pilot Plant Safety Analysis Report. Volume 4

International Nuclear Information System (INIS)

1986-01-01

This Safety Analysis Report (SAR) has been prepared by the US Department of Energy (DOE) to support the construction and operation of the Waste Isolation Pilot Plant (WIPP) in southeastern New Mexico. The WIPP facility is designed to receive, inspect, emplace, and store unclassified defense-generated transuranic wastes in a retrievable fashion in an underground salt medium and to conduct studies and perform experiments in salt with high-level wastes. Upon the successful completion of these studies and experiments, WIPP is designed to serve as a permanent facility. The first chapter of this report provides a summary of the location and major design features of WIPP. Chapters 2 through 5 describe the site characteristics, design criteria, and design bases used in the design of the plant and the plant operations. Chapter 6 discusses radiation protection; Chapters 7 and 8 present an accident analysis of the plant and an assessment of the long-term waste isolation at WIPP. The conduct of operations and operating controls and limits are discussed in Chapters 9 and 10. The quality assurance programs are described in Chapter 11

Waste Isolation Pilot Plant Safety Analysis Report. Volume 1

International Nuclear Information System (INIS)

1986-01-01

This Safety Analysis Report (SAR) has been prepared by the US Department of Energy (DOE) to support the construction and operation of the Waste Isolation Pilot Plant (WIPP) in southeastern New Mexico. The WIPP facility is designed to receive, inspect, emplace, and store unclassified defense-generated transuranic wastes in a retrievable fashion in an underground salt medium and to conduct studies and perform experiments in salt with high-level wastes. Upon the successful completion of these studies and experiments, WIPP is designed to serve as a permanent facility. The first chapter of this report provides a summary of the location and major design features of WIPP. Chapters 2 through 5 describe the site characteristics, design criteria, and design bases used in the design of the plant and the plant operations. Chapter 6 discusses radiation protection: Chapters 7 and 8 present an accident analysis of the plant and an assessment of the long-term waste isolation at WIPP. The conduct of operations and operating control and limits are discussed in Chapters 9 and 10. The quality assurance programs are described in Chapter 11

Waste Isolation Pilot Plant Safety Analysis Report. Volume 2

International Nuclear Information System (INIS)

1986-01-01

This Safety Analysis Report (SAR) has been prepared by the US Department of Energy (DOE) to support the construction and operation of the Waste Isolation Pilot Plant (WIPP) in southeastern New Mexico. The WIPP facility is designed to receive, inspect, emplace, and store unclassified defense-generated transuranic wastes in a retrievable fashion in an underground salt medium and to conduct studies and perform experiments in salt with high-level wastes. Upon the successful completion of these studies and experiments, WIPP is designed to serve as a permanent facility. The first chapter of this report provides a summary of the location and major design features of WIPP. Chapters 2 through 5 describe the site characteristics, design criteria, and design bases used in the design of the plant and the plant operations. Chapter 6 discusses radiation protection; Chapters 7 and 8 present an accident analysis of the plant and an assessment of the long-term waste isolation at WIPP. The conduct of operations and operating controls and limits are discussed in Chapters 9 and 10. The quality assurance programs are described in Chapter 11

Retrieval of canistered experimental waste at the waste isolation pilot plant

International Nuclear Information System (INIS)

Stinebaugh, R.E.

1979-07-01

To assess the suitability of bedded salt for nuclear waste disposal, an extensive experimental program will be implemented at the Waste Isolation Pilot Plant. In order to evaluate experimental results, it will be necessary to recover certain of these experiments for postmortem examination and analysis. This document describes the equipment and procedures used to effect recovery of one category of WIPP experiments

Low-level radioactive waste associated with plant life extension

International Nuclear Information System (INIS)

Sciacca, F.; Zigler, G.; Walsh, R.

1992-01-01

Many utilities operating nuclear power plants are expected to seek to extend the useful life of their plants through license renewal. These US Nuclear Regulatory Commission (NRC) licensees are expected to implement enhanced inspection, surveillance, testing, and monitoring (ISTM) as needed to detect and mitigate age-related degradation of important structures, systems, and components (SSCs). In addition, utilities may undertake various refurbishment and upgrade activities at these plants to better assure economic and reliable power generation. These activities performed for safety and/or economic reasons can result in radioactive waste generation, which is incremental to that generated in the original licensing term. Work was performed for the NRC to help define and characterize potential environmental impacts associated with nuclear plant license renewal and plant life extension. As part of this work, projections were made of the types and quantities of low-level radioactive waste (LLRW) likely to be generated by licensee programs. These projections were needed to estimate environmental impacts related to the disposal of such wastes

STORAGE AND RECOVERY OF SECONDARY WASTE COMING FROM MUNICIPAL WASTE INCINERATION PLANTS IN UNDERGROUND MINE

Directory of Open Access Journals (Sweden)

Waldemar Korzeniowski

2016-09-01

Full Text Available Regarding current and planned development of municipal waste incineration plants in Poland there is an important problem of the generated secondary waste management. The experience of West European countries in mining shows that waste can be stored successfully in the underground mines, but especially in salt mines. In Poland there is a possibility to set up the underground storage facility in the Salt Mine “Kłodawa”. The mine today is capable to locate over 3 million cubic meters and in the future it can increase significantly. Two techniques are proposed: 1 – storage of packaged waste, 2 – waste recovery as selfsolidifying paste with mining technology for rooms backfilling. Assuming the processing capacity of the storage facility as 100 000 Mg of waste per year, “Kłodawa” mine will be able to accept around 25 % of currently generated waste coming from the municipal waste incineration plants and the current volume of the storage space is sufficient for more than 20 years. Underground storage and waste recovery in mining techniques are beneficial for the economy and environment.

Waste acceptance criteria for the Waste Isolation Pilot Plant

International Nuclear Information System (INIS)

1996-04-01

The Waste Isolation Pilot Plant (WIPP) Waste Acceptance Criteria (WAC), DOE/WIPP-069, was initially developed by a U.S. Department of Energy (DOE) Steering Committee to provide performance requirements to ensure public health and safety as well as the safe handling of transuranic (TRU) waste at the WIPP. This revision updates the criteria and requirements of previous revisions and deletes those which were applicable only to the test phase. The criteria and requirements in this document must be met by participating DOE TRU Waste Generator/Storage Sites (Sites) prior to shipping contact-handled (CH) and remote-handled (RH) TRU waste forms to the WIPP. The WIPP Project will comply with applicable federal and state regulations and requirements, including those in Titles 10, 40, and 49 of the Code of Federal Regulations (CFR). The WAC, DOE/WIPP-069, serves as the primary directive for assuring the safe handling, transportation, and disposal of TRU wastes in the WIPP and for the certification of these wastes. The WAC identifies strict requirements that must be met by participating Sites before these TRU wastes may be shipped for disposal in the WIPP facility. These criteria and requirements will be reviewed and revised as appropriate, based on new technical or regulatory requirements. The WAC is a controlled document. Revised/changed pages will be supplied to all holders of controlled copies

Occupational health risk assessment of volatile organic compounds emitted from the coke production unit of a steel plant.

Science.gov (United States)

Dehghani, Fateme; Omidi, Fariborz; Heravizadeh, Omidreza; Barati Chamgordani, Saied; Gharibi, Vahid; Sotoudeh Manesh, Akbar

2018-03-27

In this study, cancer and non-cancer risks of exposure to volatile organic compounds in the coke production unit of a steel plant were evaluated. To determine individual exposure to benzene, toluene, xylene and ethylbenzene, personal samples were taken from the breathing zone of workers according to National Institute for Occupational Safety and Health (NIOSH) method 1501. Cancer and non-cancer risk assessment was performed, using US Environmental Protection Agency (US EPA) methods. Samples analysis showed that the concentration of benzene in the energy and biochemistry and the benzol refinement sections was higher than occupational exposure limits. The cancer risk for benzene in all sections was significantly higher than allowable limit; the non-cancer risk for benzene in all sections and toluene in the benzol refinement section was also higher than 1.0. In conclusion, the current control measures are not sufficient and should be improved for efficient control of occupational exposures.

Advanced coking process control at Rautaruukki Steel

Energy Technology Data Exchange (ETDEWEB)

Ritamaki, O.; Luhtaniemi, H. [Rautaruukki Engineering (Finland)

1999-12-01

The paper presents the latest development of the Coking Process Management System (CPMS) at Raahe Steel. The latest third generation system is based on the previous system with the addition of fuzzy logic controllers. (The previous second generation system was based simultaneous feed forward and feedback control.) The system development has resulted in balanced coke oven battery heating, decreased variation in process regulation between shifts and increase of process information for operators. The economic results are very satisfactory. 7 figs.

High coking value pitch

Science.gov (United States)

Miller, Douglas J.; Chang, Ching-Feng; Lewis, Irwin C.; Lewis, Richard T.

2014-06-10

A high coking value pitch prepared from coal tar distillate and has a low softening point and a high carbon value while containing substantially no quinoline insolubles is disclosed. The pitch can be used as an impregnant or binder for producing carbon and graphite articles.

Management of low level wastes at Rokkasho reprocessing plant

International Nuclear Information System (INIS)

Moriya, N.; Ochi, E.

2006-01-01

Full text: At Rokkasho Reprocessing Plant (RRP), after start-up of the commercial operation, radioactive wastes will be generated. Wastes generated from a reprocessing plant generally consist of many kinds of characteristics in view of ''activity level'', ''nuclide composition'', ''chemical properties'', ''physical properties'', and so on. For stable operation of a reprocessing plant, we should t reat , ''condition'' and ''dispose'' these wastes considering these wastes characteristics. To contribute to the nuclear fuel cycle project, it is important to evaluate technologies such as, ''Treatment'', ''Conditioning'' and ''Final Disposal'', not only for technical but also for economical aspects. Considering the final disposal in the future, the basic policy in ''Treatment'' and ''Conditioning'' at RRP is shown below: Recover and reuse chemicals (such as nitric acid and TBP, etc.) in plant; Radioactive waste shall be divided, classified and managed according to activity level, nuclide composition, the radiation level, its physical properties, chemical properties, etc.; Treat them based on ''classification'' management with proper combination; Condition them as intermediate forms in order to keep flexibility in the future disposal method; Original volume of annually generated wastes at RRP is estimated as 5600m3 except highly radioactive vitrified waste, and these wastes shall be treated in the following units, which are now under commisioning, in order to reduce and stabilize wastes. Low-level concentrated liquid waste to be treated with a ''Drying and peptization'' unit; Spent solvent to be treated with a ''Pyrolysis and hydrothermal solidification'' unit; Relatively low-level non-alfa flammable wastes to be treated with a ''Incineration and hydrothermal solidification'' unit; CB/BP (Channel Box and Burnable Poison) to be processed with a ''Cutting'' unit; Other wastes to be kept as their generated state with a ''Intermediate storage''. As a result of these

The influence of calcination on the physical and chemical properties of petroleum and mixed cokes

Energy Technology Data Exchange (ETDEWEB)

Sikora, K; Syrek, H

1980-01-01

Freshly prepared petroleum and coal-petroleum cokes, before utilization for the production of various materials, are subjected to calcining--thermal treatment in a neutral or reducing atmosphere without the admission of air at less than or equal to 1400/sup 0/. During calcining, stabilization of the physical and chemical properties of the cokes takes place. The properties of the obtained coke depend chiefly on the calcining time and temperature. During calcining, volatile substances are removed almost completely from the coke; the coke density is increased, and its structure is put in order; the electrical conductivity is improved; the mechanical strength is increased; and the reactivity of the coke is decreased. Laboratory studies were conducted on calcining mixed coal-petroleum cokes of two grades at 1200, 1250, and 1300/sup 0/ for 2-6 h. In the calcining products the content of volatile substances, the ash content, S content, and density were determined. It was ascertained that calcining of mixed coal-petroleum cokes goes analogously to calcining of pure petroleum cokes. Raising the temperature and increasing the time of calcining has a substantial effect on improvement of coke physical and chemical properties. For high-quality coke, calcining is to be carried out at greater than or equal to 1300/sup 0/ for 4-6 h, for ordinary coke at > 1200/sup 0/ and greater than or equal to 4 h. The results are regarded as starting data for an industrial study of the calcining process.

Effects and mechanistic aspects of absorbing organic compounds by coking coal.

Science.gov (United States)

Ning, Kejia; Wang, Junfeng; Xu, Hongxiang; Sun, Xianfeng; Huang, Gen; Liu, Guowei; Zhou, Lingmei

2017-11-01

Coal is a porous medium and natural absorbent. It can be used for its original purpose after adsorbing organic compounds, its value does not reduce and the pollutants are recycled, and then through systemic circulation of coking wastewater zero emissions can be achieved. Thus, a novel method of industrial organic wastewater treatment using adsorption on coal is introduced. Coking coal was used as an adsorbent in batch adsorption experiments. The quinoline, indole, pyridine and phenol removal efficiencies of coal adsorption were investigated. In addition, several operating parameters which impact removal efficiency such as coking coal consumption, oscillation contact time, initial concentration and pH value were also investigated. The coking coal exhibited properties well-suited for organics' adsorption. The experimental data were fitted to Langmuir and Freundlich isotherms as well as Temkin and Redlich-Peterson (R-P) models. The Freundlich isotherm model provided reasonable models of the adsorption process. Furthermore, the purification mechanism of organic compounds' adsorption on coking coal was analysed.

Delayed coking studies on Athabasca bitumen and Cold Lake heavy oil

Energy Technology Data Exchange (ETDEWEB)

Govindhakannan, J.; Khulbe, C. [National Centre for Upgrading Technology, Devon, AB (Canada); Natural Resources Canada, Devon, AB (Canada). CanmetENERGY

2009-07-01

This poster highlighted the results of a study that quantified the delayed coking product yields of Athabasca bitumen and Cold Lake heavy oil. It also investigated the effect of operating pressure and feed rates on product yield and quality. The effect of pressure on conversion of sulphur and nitrogen was also examined. Experimental results revealed that the yield of liquid products decreases and the yields of coke and gases increase as the operating pressure increases. Sulphur and nitrogen conversions increase with increasing pressure. In this study, the yield and quality of delayed coking products were not influenced by the variation in feed rates. It was concluded that feed rate changes do not significantly affect the yield and quality of delayed coking products because the residual liquid and coke trapped in the coker drum reside there for a duration that approaches infinity, compared to much smaller average residence time for vapor-phase compounds. tabs., figs.

Proceedings of the Joint Meeting of The Fuel Society of Japan (1991). 28th Coal Science Conference/91st Coke Meeting; (Sha) nenryo kyokai godo taikai happyo ronbunshu (1991). Dai 28 kai sekitan kagaku kaigi dai 91 kai cokes tokubetsukai

Energy Technology Data Exchange (ETDEWEB)

1991-11-07

Relating to coke, studies are made on the rapid coke production method, oven investigation during carbonization, and operational management/control. As to coal science, studies are mainly on the brown coal two-stage liquefaction (BCL) method, and data on the pilot plant and PSU are reported. Concerning bituminous coal liquefaction, PSU data mostly including the NEDOL process, and characteristics of liquefaction residue and its effective utilization by thermal decomposition are reported. Regarding the liquefaction mechanism, an experimentally extensive study on catalyst, solvent and reaction conditions is made using model materials and coal itself on the bench scale and also in the pilot plant. Engineering subjects on residue, solvent deashing, scale attachment and coprocessing are also reported. Relations of decomposition process to coal chemical structure changes and reaction conditions are investigated. As to coal gasification, studies, which are not many, are conducted on material balance, heat balance, and image characteristics of char for gasification and factors controlling reactivity.

Hanford Waste Vitrification Plant quality assurance program description for defense high-level waste form development and qualification

International Nuclear Information System (INIS)

Hand, R.L.

1990-12-01

The US Department of Energy-Office of Civilian Radioactive Waste Management has been designated the national high-level waste repository licensee and the recipient for the canistered waste forms. The Office of Waste Operations executes overall responsibility for producing the canistered waste form. The Hanford Waste Vitrification Plant Project, as part of the waste form producer organization, consists of a vertical relationship. Overall control is provided by the US Department of Energy-Environmental Restoration and Waste Management Headquarters; with the US Department of Energy-Office of Waste Operations; the US Department of Energy- Headquarters/Vitrification Project Branch; the US Department of Energy-Richland Operations Office/Vitrification Project Office; and the Westinghouse Hanford Company, operations and engineering contractor. This document has been prepared in response to direction from the US Department of Energy-Office of Civilian Radioactive Waste Management through the US Department of Energy-Richland Operations Office for a quality assurance program that meets the requirements of the US Department of Energy. This document provides guidance and direction for implementing a quality assurance program that applies to the Hanford Waste Vitrification Plant Project. The Hanford Waste Vitrification Plant Project management commits to implementing the quality assurance program activities; reviewing the program periodically, and revising it as necessary to keep it current and effective. 12 refs., 6 figs., 1 tab

The Stored Waste Examination Pilot Plant program at the INEL

International Nuclear Information System (INIS)

McKinley, K.B.; Anderson, B.C.; Clements, T.L.; Hinckley, J.P.; Mayberry, J.L.; Smith, T.H.

1983-01-01

Since 1970, defense transuranic waste has been placed into 20-year retrievable storage at the Radioactive Waste Management Complex at the Idaho National Engineering Laboratory (INEL). A major objective of the U.S. Department of Energy (DOE) Nuclear Waste Management Program is to remove all retrievably stored transuranic waste from the INEL. The January 1981 DOE Record of Decision on the Waste Isolation Pilot Plant (WIPP) stated, ''The WIPP facility will dispose of defense transuranic waste stored retrievably at the Idaho National Engineering Laboratory.'' After retrieval and before shipment, processing may be necessary to prepare the waste for acceptance, handling, and enhanced long-term isolation in the WIPP. However, some of the waste is certifiable to the WIPP waste acceptance criteria without container opening or waste processing. To minimize costs, the Stored Waste Examination Pilot Plant (SWEPP) is being developed to certify INEL stored transuranic waste without container opening or waste processing. The SWEPP certification concept is based on records assessment, nondestructive examination techniques, assay techniques, health physics examinations, and limited opening of containers at another facility for quality control

Influence of thermal charge preparation on coke comminution under blast-furnace operating conditions

Energy Technology Data Exchange (ETDEWEB)

Shkoller, M.B.; Dinel' t, V.M.; Korchuganova, G.S.; Petrov, V.B.

1983-09-01

Reactions of coke in the blast furnace are determined mainly by the nature of the coke itself which depends on the coal properties, its preparation and the coking conditions. In the blast furnace the coke reacts with alkali and alkaline earth metals in the burden. Preheated coal charges were found to absorb far less sodium and potassium carbonates than a conventional moist charge over an equivalent period, due to the smaller pore volume available.

Polymer solidification of mixed wastes at the Rocky Flats Plant

International Nuclear Information System (INIS)

Faucette, A.M.; Logsdon, B.W.; Lucerna, J.J.; Yudnich, R.J.

1994-01-01

The Rocky Flats Plant is pursuing polymer solidification as a viable treatment option for several mixed waste streams that are subject to land disposal restrictions within the Resource Conservation and Recovery Act provisions. Tests completed to date using both surrogate and actual wastes indicate that polyethylene microencapsulation is a viable treatment option for several mixed wastes at the Rocky Flats Plant, including nitrate salts, sludges, and secondary wastes such as ash. Treatability studies conducted on actual salt waste demonstrated that the process is capable of producing waste forms that comply with all applicable regulatory criteria, including the Toxicity Characteristic Leaching Procedure. Tests have also been conducted to evaluate the feasibility of macroencapsulating certain debris wastes in polymers. Several methods and plastics have been tested for macroencapsulation, including post-consumer recycle and regrind polyethylene

Variation in mineral composition of coal during enrichment and coking

Energy Technology Data Exchange (ETDEWEB)

M.L. Ulanovskii; A.N. Likhenko [Ukrkoks Coke Producers' Association, Dnepropetrovsk (Ukraine)

2009-06-15

The parameters I{sub b} and B{sub b} used in developing an optimal coking-batch composition are determined from data on the chemical composition of the ash in Donetsk Basin and other coal. It is found that, when the ash content is reduced in deeper enrichment of coal with an increased content of fine pyrite, there will be accompanying increase in the Fe{sub 2}O{sub 3} content and decrease in the SiO{sub 2} content of the ash in lighter fractions. This increases I{sub b}. In other words, reducing the ash content of the coal is an unpromising means of increasing CRI and CSR of the coke produced. Three ash-containing elements (silicon, aluminum, and iron) are experimentally proven to transfer from coal to coke. Specific behavior of calcium, magnesium, alkali metals, and sulfur during coking.

Graphitization of Coke and Its Interaction with Slag in the Hearth of a Blast Furnace

Science.gov (United States)

Li, Kejiang; Zhang, Jianliang; Liu, Yanxiang; Barati, Mansoor; Liu, Zhengjian; Zhong, Jianbo; Su, Buxin; Wei, Mengfang; Wang, Guangwei; Yang, Tianjun

2016-04-01

Coke reaction behavior in the blast furnace hearth has yet to be fully understood due to limited access to the high temperature zone. The graphitization of coke and its interaction with slag in the hearth of blast furnace were investigated with samples obtained from the center of the deadman of a blast furnace during its overhaul period. All hearth coke samples from fines to lumps were confirmed to be highly graphitized, and the graphitization of coke in the high temperature zone was convinced to start from the coke surface and lead to the formation of coke fines. It will be essential to perform further comprehensive investigations on graphite formation and its evolution in a coke as well as its multi-effect on blast furnace performance. The porous hearth cokes were found to be filled up with final slag. Further research is required about the capability of coke to fill final slag and the attack of final slag on the hearth bottom refractories since this might be a new degradation mechanism of refractories located in the hearth bottom.

Analysis of Waste Isolation Pilot Plant Samples: Integrated Summary Report

Energy Technology Data Exchange (ETDEWEB)

Britt, Phillip F [ORNL

2015-03-01

Analysis of Waste Isolation Pilot Plant Samples: Integrated Summary Report. Summaries of conclusions, analytical processes, and analytical results. Analysis of samples taken from the Waste Isolation Pilot Plant (WIPP) near Carlsbad, New Mexico in support of the WIPP Technical Assessment Team (TAT) activities to determine to the extent feasible the mechanisms and chemical reactions that may have resulted in the breach of at least one waste drum and release of waste material in WIPP Panel 7 Room 7 on February 14, 2014. This report integrates and summarizes the results contained in three separate reports, described below, and draws conclusions based on those results. Chemical and Radiochemical Analyses of WIPP Samples R-15 C5 SWB and R16 C-4 Lip; PNNL-24003, Pacific Northwest National Laboratory, December 2014 Analysis of Waste Isolation Pilot Plant (WIPP) Underground and MgO Samples by the Savannah River National Laboratory (SRNL); SRNL-STI-2014-00617; Savannah River National Laboratory, December 2014 Report for WIPP UG Sample #3, R15C5 (9/3/14); LLNL-TR-667015; Lawrence Livermore National Laboratory, January 2015 This report is also contained in the Waste Isolation Pilot Plant Technical Assessment Team Report; SRNL-RP-2015-01198; Savannah River National Laboratory, March 17, 2015, as Appendix C: Analysis Integrated Summary Report.

Uptake by plants of radionuclides from FUSRAP waste materials

International Nuclear Information System (INIS)

Knight, M.J.

1983-04-01

Radionuclides from FUSRAP wastes potentially may be taken up by plants during remedial action activities and permanent near-surface burial of contaminated materials. In order to better understand the propensity of radionuclides to accumulate in plant tissue, soil and plant factors influencing the uptake and accumulation of radionuclides by plants are reviewed. In addition, data describing the uptake of the principal radionuclides present in FUSRAP wastes (uranium-238, thorium-230, radium-226, lead-210, and polonium-210) are summarized. All five radionuclides can accumulate in plant root tissue to some extent, and there is potential for the translocation and accumulation of these radionuclides in plant shoot tissue. Of these five radionuclides, radium-226 appears to have the greatest potential for translocation and accumulation in plant shoot tissue. 28 references, 1 figure, 3 tables

Uptake by plants of radionuclides from FUSRAP waste materials

Energy Technology Data Exchange (ETDEWEB)

Knight, M.J.

1983-04-01

Radionuclides from FUSRAP wastes potentially may be taken up by plants during remedial action activities and permanent near-surface burial of contaminated materials. In order to better understand the propensity of radionuclides to accumulate in plant tissue, soil and plant factors influencing the uptake and accumulation of radionuclides by plants are reviewed. In addition, data describing the uptake of the principal radionuclides present in FUSRAP wastes (uranium-238, thorium-230, radium-226, lead-210, and polonium-210) are summarized. All five radionuclides can accumulate in plant root tissue to some extent, and there is potential for the translocation and accumulation of these radionuclides in plant shoot tissue. Of these five radionuclides, radium-226 appears to have the greatest potential for translocation and accumulation in plant shoot tissue. 28 references, 1 figure, 3 tables.

B Plant complex hazardous, mixed and low level waste certification plan

International Nuclear Information System (INIS)

Beam, T.G.

1994-11-01

This plan describes the administrative steps and handling methodology for certification of hazardous waste, mixed waste, and low level waste generated at B Plant Complex. The plan also provides the applicable elements of waste reduction and pollution prevention, including up front minimization and end product reduction of volume and/or toxicity. The plan is written to satisfy requirements for Hanford Site waste generators to have a waste certification program in place at their facility. This plan, as described, applies only to waste which is generated at, or is the responsibility of, B Plant Complex. The scope of this plan is derived from the requirements found in WHC-EP-0063, Hanford Site Solid Waste Acceptance Criteria

B Plant complex hazardous, mixed and low level waste certification plan

Energy Technology Data Exchange (ETDEWEB)

Beam, T.G.

1994-11-01

This plan describes the administrative steps and handling methodology for certification of hazardous waste, mixed waste, and low level waste generated at B Plant Complex. The plan also provides the applicable elements of waste reduction and pollution prevention, including up front minimization and end product reduction of volume and/or toxicity. The plan is written to satisfy requirements for Hanford Site waste generators to have a waste certification program in place at their facility. This plan, as described, applies only to waste which is generated at, or is the responsibility of, B Plant Complex. The scope of this plan is derived from the requirements found in WHC-EP-0063, Hanford Site Solid Waste Acceptance Criteria.

Market forces in municipal and industrial waste-to-energy

International Nuclear Information System (INIS)

Makansi, J.

1991-01-01

The market for municipal and industrial waste-to-energy can be characterized simply as currently soft with continued excellent long-term prospects. But as in all markets large and small, niche opportunities exist now which can be profitable with proper definition and strategy. Economics of several projects have proven marginal, cost overruns are common, and revenue projections are sometimes overstates. Also contributing to poorer economics of late are lower prices for the electric power produced from these plants. New environmental restrictions are adding 10-15% to the capital costs of a given project. On the industrial front, the strength of waste-fuel firing continues to be evident for independent power production. Important fuel-niche markets have sprung up over the last decade including petroleum coke, coal-mining wastes, hospital or redbag wastes, biomass, used tires, and so on. Another fuel niche is hazardous waste incineration. In the municipal arena, realism has not yet hit the recycling and source reduction enthusiasts. Only 25-35% recycling is considered practical by experts. There are also limits to how often material can be recycled. Finally, in spite of the best efforts of the population to control the amount of refuse generated and to recycle that which is, population and economic growth may overtake any new sense of environmental responsibility. And, yes, the additional refuse still has to go somewhere exclamation point The best somewhere option continues to be a waste-to-energy plant. Current market opportunities and two other market forces (international activities and the role of US utilities) are discussed

Q Fever Outbreak among Workers at a Waste-Sorting Plant.

Directory of Open Access Journals (Sweden)

Eva Alonso

Full Text Available An outbreak of Q fever occurred in February-April 2014 among workers at a waste-sorting plant in Bilbao (Spain. The outbreak affected 58.5% of investigated employees, 47.2% as confirmed cases (PCR and/or serology and 11.3% as probable cases (symptoms without laboratory confirmation. Only employees who had no-access to the waste processing areas of the plant were not affected and incidence of infection was significantly higher among workers not using respiratory protection masks. Detection by qPCR of Coxiella burnetii in dust collected from surfaces of the plant facilities confirmed exposure of workers inside the plant. Animal remains sporadically detected among the residues received for waste-sorting were the most probable source of infection. After cleaning and disinfection, all environmental samples tested negative. Personal protection measures were reinforced and made compulsory for the staff and actions were taken to raise farmers' awareness of the biological risk of discharging animal carcasses as urban waste.

Survey of minipower plant for municipal solid waste firing

International Nuclear Information System (INIS)

Merkkiniemi, R.; Hyoety, P.; Saiha, E.

1999-01-01

Dumping of municipal waste to disposal areas has caused environmental problems, and this has led to more sophisticated disposal systems and high prices. That and a general demand to reduce the quantity of waste require new solutions, and a question has been arisen whether combustion could be used to treat waste. This project is concentrating to bum waste in a small-scale power plant. The background is one 10-MW pilot in Tampere city based on smelting furnace and a 0.3-MW pyrolyse furnace. The results of these from the viewpoint of operation and effluent were satisfactory and the burning process used is in line with the latest regulations. The second aspect is the economy of waste handling. The minipower plant is designed for reasonable small municipalities, abt 20 000 inhabitants or 1 - 20 MW heat input. According to several feasibility studies this method is the cheapest way to handle waste. A local heat demand is used to support the economy. The prices of products, heat and power, and cost are of the same level as the market prices. Thus, we expect a economical and environmentally safe operation with the minipower plant and it will also give a hint to solve a higher capacity demand of one unit. (orig.)

Hanford Waste Vitrification Plant capacity increase options

International Nuclear Information System (INIS)

Larson, D.E.

1996-04-01

Studies are being conducted by the Hanford Waste Vitrification Plant (HWVP) Project on ways to increase the waste processing capacity within the current Vitrification Building structural design. The Phase 1 study on remote systems concepts identification and extent of capacity increase was completed. The study concluded that the HWVP capacity could be increased to four times the current capacity with minor design adjustments to the fixed facility design, and the required design changes would not impact the current footprint of the vitrification building. A further increase in production capacity may be achievable but would require some technology development, verification testing, and a more systematic and extensive engineering evaluation. The primary changes included a single advance melter with a higher capacity, new evaporative feed tank, offgas quench collection tank, ejector venturi scrubbers, and additional inner canister closure station,a smear test station, a new close- coupled analytical facility, waste hold capacity of 400,000 gallon, the ability to concentrate out-of-plant HWVP feed to 90 g/L waste oxide concentration, and limited changes to the current base slab construction package

Resource conservation and recovery act draft hazardous waste facility permit: Waste Isolation Pilot Plant (WIPP)

International Nuclear Information System (INIS)

1993-08-01

Volume I contains the following attachments for Module II: waste analysis plan; quality assurance program plan for the Waste Isolation Pilot Plant (WIPP) Experiment Waste Characterization Program(QAPP); WIPP Characterization Sampling and Analysis Guidance Manual (Plan)(SAP); and no migration Determination Requirement Summary (NMD)

Conceptual project of waste treatment plant of CDTN

International Nuclear Information System (INIS)

Gabriel, J.L.; Astolfi, D.

1983-01-01

This paper presents the conceptual project of the waste treatment plant of CDTN. Several areas, such as: process area, material entrance and exit area are studied. The treatment processes are: evaporation, filtration, cementation, cutting and processing of solid wastes. (C.M.)

Recycling Mixed Plastics Waste as Reductant in Ironmaking*

African Journals Online (AJOL)

Michael O. Mensah

2015-12-02

Dec 2, 2015 ... Keywords: Reduction, Metallurgical coke, Mixed plastics waste, Extent of reduction. 1 Introduction. Globally .... reactions in a custom-made horizontal resistance .... emissions arising out of the electrical energy that was used to ...

Radioactive Bench-scale Steam Reformer Demonstration of a Monolithic Steam Reformed Mineralized Waste Form for Hanford Waste Treatment Plant Secondary Waste - 12306

Energy Technology Data Exchange (ETDEWEB)

Evans, Brent; Olson, Arlin; Mason, J. Bradley; Ryan, Kevin [THOR Treatment Technologies, LLC - 106 Newberry St. SW, Aiken, SC 29801 (United States); Jantzen, Carol; Crawford, Charles [Savannah River Nuclear Solutions (SRNL), LLC, Aiken, SC 29808 (United States)

2012-07-01

Hanford currently has 212,000 m{sup 3} (56 million gallons) of highly radioactive mixed waste stored in the Hanford tank farm. This waste will be processed to produce both high-level and low-level activity fractions, both of which are to be vitrified. Supplemental treatment options have been under evaluation for treating portions of the low-activity waste, as well as the liquid secondary waste from the low-activity waste vitrification process. One technology under consideration has been the THOR{sup R} fluidized bed steam reforming process offered by THOR Treatment Technologies, LLC (TTT). As a follow-on effort to TTT's 2008 pilot plant FBSR non-radioactive demonstration for treating low-activity waste and waste treatment plant secondary waste, TTT, in conjunction with Savannah River National Laboratory, has completed a bench scale evaluation of this same technology on a chemically adjusted radioactive surrogate of Hanford's waste treatment plant secondary waste stream. This test generated a granular product that was subsequently formed into monoliths, using a geo-polymer as the binding agent, that were subjected to compressibility testing, the Product Consistency Test and other leachability tests, and chemical composition analyses. This testing has demonstrated that the mineralized waste form, produced by co-processing waste with kaolin clay using the TTT process, is as durable as low-activity waste glass. Testing has shown the resulting monolith waste form is durable, leach resistant, and chemically stable, and has the added benefit of capturing and retaining the majority of Tc-99, I-129, and other target species at high levels. (authors)

Binderless briquetting of some selected South African prime coking, blend coking and weathered bituminous coals and the effect of coal properties on binderless briquetting

Energy Technology Data Exchange (ETDEWEB)

Mangena, S.J. [Division of Mining Technology, CSIR, PO Box 395, Pretoria, 0001 (South Africa); du Cann, V.M. [Coal and Mineral Technologies (Pty) Ltd, SABS, PO Box 73656, Lynnwood Ridge, Pretoria, 0040 (South Africa)

2007-07-02

The binderless briquetting of some selected South African prime coking and blend coking coals, as well as the effects of weathering on the binderless briquetting of some inertinite-rich bituminous coals, were investigated in the laboratory. Selected properties of these coals were determined and the coals were briquetted at various moisture contents and pressures. Based on the results obtained in this study, binderless briquetting was found to be most successful in the cases of the fresh, vitrinite-rich coking and blend coking coals and satisfactory in the fresh inertinite-rich Witbank coals. However, the bonding process seemed to be adversely affected by weathering. The negative impact on bonding could be ameliorated to some extent by the presence of a significant kaolinite content when the percentage ash reports in the order of more than 15% (air-dry basis). It should, however, be noted that kaolinite may reduce the water resistance of the briquettes. (author)

Waste retrieval plan for the Waste Isolation Pilot Plant

International Nuclear Information System (INIS)

1993-03-01

The US DOE has prepared this plan to meet the requirements of Public Law 102579, the Waste Isolation Pilot Plant (WIPP) LWA, The purpose. is to demonstrate readiness to retrieve from the WIPP underground transuranic radioactive waste that will be used for testing should retrieval be needed. The WIPP, a potential geologic repository for transuranic wastes generated in national-defense activities, has been constructed in southeastern New Mexico. Because the transuranic wastes will remain radioactive for a very long time, the WIPP must reasonably ensure safe performance over thousands of years. The DOE therefore decided to develop the facility in phases, to preclude premature decisions and to conduct the performance assessments needed to demonstrate long-term safety. Surface facilities for receiving waste have been built, and considerable underground excavation, 2150 feet below the surface, has been completed. The next step is a test phase, including underground experiments called ''bin tests'' and ''alcove test(s)'' with contact-handled transuranic waste. The objective of these waste tests is to collect relevant data about the gas-generation potential and volatile organic compound (VOC) source term of the waste for developing a basis for demonstrating long term safety by compliance with the applicable disposal regulations (40 CFR 191, 264 and 268). The test phase will end when a decision is made to begin disposal in the WIPP or to terminate the project if regulatory compliance cannot be determined and demonstrated. Authorization to receive transuranic waste at the WIPP for the test phase is given by the WIPP LWA provided certain requirements are met

A small-angle neutron scattering investigation of coke deposits on catalysts

International Nuclear Information System (INIS)

Acharya, D.R.; Hughes, R.; Allen, A.J.

1990-01-01

Small-angle neutron scattering (SANS) has been used to characterize a silica-alumina catalyst before and after coke deposition. The reaction used to deactivate the catalyst was the isomerization of xylenes. The results showed that, while most of the surface area in this type of catalyst resides in the ultrafine pores of diameters less than 1 nm occupying about 7% of the sample volume, there appears to be no coke deposition in these pores. The coke seems to coat the solid structures of 3.3-nm diameter which are of capillary shape. Such structures occupy about 6% of the sample volume. The coke was found to correspond to amonolayer of composition CH 0.3 with a density of 1660 kg/m 3

Hanford Waste Vitrification Plant - the project and process systems

International Nuclear Information System (INIS)

Swenson, L.D.; Miller, W.C.; Smith, R.A.

1990-01-01

The Hanford Waste Vitrification Plant (HWVP) project is scheduled to start construction on the Hanford reservation in southeastern Washington State in 1991. The project will immobilize the liquid high-level defense waste stored there. The HWVP represents the third phase of the U.S. Department of Energy (DOE) activities that are focused on the permanent disposal of high-level radioactive waste, building on the experience of Defense Waste Processing Facility (DWPF) at the Savannah River site, South Carolina, and of the West Valley Demonstration Plant (WVDP), New York. This sequential approach to disposal of the country's commercial and defense high-level radioactive waste allows HWVP to make extensive use of lessons learned from the experience of its predecessors, using mature designs from the earlier facilities to achieve economies in design and construction costs while enhancing operational effectiveness

Hanford Waste Vitrification Plant Clean Air Act permit application

International Nuclear Information System (INIS)

1990-04-01

This document briefly describes the Hanford Site and provides a general overview of the Hanford Waste Vitrification Plant (HWVP). Other topics include sources of emissions, facility operating parameters, facility emissions, pollutant and radionuclide control technology and air quality. The HWVP will convert mixed wastes (high-activity radioactive and hazardous liquid wastes) to a solid vitrified form (borosilicate glass) for disposal. Mixed wastes pretreated in the Hanford Site B Plant will be pumped into double- shell tanks in the 200 East Area for interim storage. This pretreated mixed waste will be batch transferred from interim storage to the HWVP facility, where the waste will be concentrated by evaporation, treated with chemicals, and mixed with glass-forming materials. The mixture will then be continuously fed into an electrically heated glass melter. The molten glass will be poured into canisters that will be cooled, sealed, decontaminated, and stored until the vitrified product can be transferred to a geologic repository. 25 refs., 18 figs., 32 tabs

Automatic combustion control of the ArcelorMittal Tubarao coke oven batteries

Energy Technology Data Exchange (ETDEWEB)

L. Barbosa de Oliveira Mello; C.-H. Sampaio Dandrea; G.-H. Marietto Goncalves; A. Estevao Torres; N.-L. Biccas

2008-05-15

The objective of the automatic combustion control is to guarantee the operational stability of the coke batteries based on the control of the coking time and consequently, minimize the reduction of useful life of the ovens. This control is guided by a mathematical model whose inputs are process variables and raw materials parameters and outputs are combustion parameters. Therefore, this paper will present the evolution of the performance of the burning process, providing a stability of the coking time.

Health Effects of Petroleum Coke

Science.gov (United States)

Significant quantities of fugitive dust from pet coke storage and handling operations present a health risk. EPA’s research suggests that petcoke does not pose a different health risk than similar-sized particulate matter (PM10).

Reuse and activation of petroleum coke to remove metals in water

International Nuclear Information System (INIS)

Cardona, Santiago

2006-01-01

In the investigation I am reused the coke generated in the refinancing of the petroleum. It was proposed to activate al coke with characteristics of a carbon activated commercial and subsequently to use it to remove silver and present mercury in water. The carbon activated produced and the carbon activated commercial, LQ1000, they were characterized with the norms ASTM, indicate of iodine, area superficial al blue of methylene and indicate of blue of methylene and the results were compared. Likewise in the process of adsorption, the process of adsorption itself model with the equations of Freundlich and Langmuir. The activation of the coke I am planned through a design of experiments four factorial. The 16 coals produced were submitted al process of adsorption silver and mercury by duplicate. The study I report al coke activated as better adsorbent than the LQ1000 and with a smaller cost of fabrication but with a smaller one area superficial that the commercial one. The results obtained permit to produce carbon activated from the coke but economic to compete with the commercial coals activate

Surface structure and oxidation reactivity of oil sand coke particles

Energy Technology Data Exchange (ETDEWEB)

Fairbridge, C.; Palmer, A.D.; Ng, S.H.; Furimsky, E.

1987-05-01

Fractions of particles of varying mean diameter were isolated from coke obtained from the fluid coking of Athabasca bitumen. Correlations were established between the rate of oxygen sorption and the apparent surface area as measured by carbon dioxide adsorption. The rate of oxygen sorption, r/sub o/, could be related to particle radius, R, by r/sub o/ varying with R/sup D/ T over a range of particle size where D is the fractal dimension of the coke. The existence of such correlations may be related to the iterative processes which form the particles. 14 refs., 5 figs., 2 tabs.

Precautionary measures in determining volatile matter in natural coke washability fractions

Energy Technology Data Exchange (ETDEWEB)

Ashok K. Singh; N.K. Shukla; S.K. Srivastava; D.D. Haldar; B.N. Roy; Mamta Sharma [Central Institute of Mining and Fuel Research, Dhanbad (India)

2009-01-15

Industrial utilization of heat-altered coal, especially natural coke derived from coking coal, has become a challenge. As such approximately 3,500 million tones (Mt) reserves of baked coals are available in different coalfields of India. In the present investigation, a natural coke sample (03 tone) was collected from a huge dump of seam XIV of Burragarh colliery under leasehold of Bharat Coking Coal Ltd., a subsidiary of Coal India Ltd., situated in Dhanbad district of Jharkhand state. It was observed that the volatile matter in the washability fractions of different size ranges (50 to 0.5 mm) at specific gravity 1.40 to 1.80 showed erratic distribution with respect to ash. To check the abnormality, the subsamples were subjected to microscopic (petrographic) study and chemical analysis including CO{sub 2} determination. The high concentration of CO{sub 2} is related to high concentration of carbonate minerals generated due to igneous intrusions in coal seams. Based on above observations, it was concluded that the volatile matter can be corrected through determined CO{sub 2} content in each fraction. Since efforts are being made to use natural coke in different industries such as steel, power, cement, carbon artifacts, etc., a careful investigation of volatile matter distribution in natural coke washability fractions would be of immense help in planning its bulk use.

Distillation of tar and tar fractions in the presence of surface-active coke

Energy Technology Data Exchange (ETDEWEB)

Jaeppelt, A; Klaus, J

1943-01-01

The tar obtained by low-temperature carbonization of Upper Silesian gas coke and fractions from this tar were distilled in the presence of different grades of coke dust with varying surface activity; the coke had been activated by steam in the course of its production by low-temperature carbonization. The surface activity of the coke dusts was measured by determining the heat of wetting with C/sub 6/H/sub 6/. Tar and coke dust, both anhydrous, were mixed in a kneading machine in such proportions that the capillaries of the dust were saturated and enough ''externally'' bound tar was present to permit briquetting. The briquets were distilled without cracking and with steam as heating medium. The yield and quality of the distillate depended on the magnitude of the internal surface of the coke dust used; a mixture of a very active coke from brown coal and tar yielded a distillate with Conradson carbon residue of 1.34 percent, asphalt content 6.1 percent and eta/sub 20/ 5.4/sup 0/ E. as compared with C residue of 10.95 percent, asphalt content 33.5 percent and eta/sub 20/ 123.6/sup 0/ E. of the distillate obtained in the absence of surface-active coke. Even higher-boiling fractions can be improved by this treatment, although it is preferable to use oils with an initial boiling point below 300/sup 0/. The ratio of oil to adsorbent is not critical, but better results were obtained with higher percentages of added coke dust. The process in its present form is not suited for the conversion of crude creosote to useful phenols.

Outline and operations of benzene plant

Energy Technology Data Exchange (ETDEWEB)

Omori, S; Hirooka, N; Nakamura, M; Goto, T

1983-01-01

An account is given of plant which can process 130,000 tonnes of by-product coke oven gas light oil (GLO) per year (via hydrodesulfurization, extraction and distillation) to produce benzene, toluene and xylene. The flowsheets and component equipment of the various production processes are explained, together with special features such as the production of hydrogen from coke oven gas by the PSA process and the processing of GLO by the ARCO process. Plant operation is outlined and the results of performance tests are noted.

The coke formation during the pyrolysis of 1,2-dichloroethane - results of radiotracer experiments

International Nuclear Information System (INIS)

Kopinke, F.D.; Zychlinski, W.; Rodewald, D.

1990-01-01

The formation of coke-like deposits during the pyrolysis of dichloroethane has been investigated by means of 14 C-labelled compounds. Starting from industrial feedstocks coke is formed from dichloroethane and its primary reaction products as well as from trace impurities with comparable rates. Chloroprene has been revealed as an effective coke precursor. The coke formation from industrial feedstocks can be reduced significantly by suitable purification methods. (author)

Region 9 NPDES Facilities 2012- Waste Water Treatment Plants

Science.gov (United States)

Point geospatial dataset representing locations of NPDES Waste Water Treatment Plant Facilities. NPDES (National Pollution Discharge Elimination System) is an EPA permit program that regulates direct discharges from facilities that discharge treated waste water into waters of the US. Facilities are issued NPDES permits regulating their discharge as required by the Clean Water Act. A facility may have one or more outfalls (dischargers). The location represents the facility or operating plant.

Rock mechanics activities at the Waste Isolation Pilot Plant

International Nuclear Information System (INIS)

Francke, C.; Saeb, S.

1996-01-01

The application of rock mechanics at nuclear waste repositories is a true multidisciplinary effort. A description and historical summary of the Waste Isolation Pilot Plant (WIPP) is presented. Rock mechanics programs at the WIPP are outlined, and the current rock mechanics modeling philosophy of the Westinghouse Waste Isolation Division is discussed

Denitrification of coking wastewater with micro-electrolysis.

Science.gov (United States)

Lv, Yanli; Wang, Yanqiu; Shan, Mingjun; Shen, Xue; Su, Ying

2011-06-01

The denitrification for the coking wastewater was conducted by means of original battery principle with Fe-C micro-electrolysis. Fe-C serves as positive and negative electrodes, by which N02(-)-N and TN were reduced to nitrogen, and then the purpose of denitrifieation for coking wastewater was realized. The influences of pH value, carbon particle size, Fe/C ratio (mass ratio), reaction time and coagulation pH value on removal rate of N02(-)-N and TN were investigated. Coking wastewater originated from Jiamusi Coal Chemistry Engineering Company. The optimum conditions of treatment were as follows: the initial pH was 3.0, the dosage of Fe 73.5 g/L, reaction time 70 min, mass ratio of Fe/C ratio 1.0:1.3, coagulation pH 9.0 and sedimentation time 40 min. Under those conditions, nitrogen removal efficiencies of N02(-)-N and TN were beyond 50% and 45%, respectively. Copyright © 2011 The Research Centre for Eco-Environmental Sciences, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.

A new semi-mobile plant for radiation processing of waste

International Nuclear Information System (INIS)

Iacoboni, V.; Liccione, G.; Schwarz, M.; Tata, A.; Fantini, M.

1998-01-01

A new pilot/demonstrative semi-mobile irradiation plant, named TRIRIS (TRIsaia-RIfiuti-Sterilizzazione, namely ''Trisaia Res. Center - Wastes - Sterilization''), has been designed and erected in order to propose and explore new technological opportunities, based on in ''in-situ'' effective cleaning process. The main general goal is to face increased problems and concerns related to the treatment/disposal of different solid-liquid wastes, particularly with reference to emergency situation (e.g. need of quick environment restoring operation following an accident with groundwater pollution). The project, which was jointly carried out by ENEA and Hitesys Co., an Italian electron accelerators manufacturer, foresees a LINAC type EB-machine (s band) having 4-6 MeV and till 1000 W as beam features. A highly flexible automatic system allows materials (solid or liquid wastes) transporting and handling to be equipped with a belt conveyor and a piping net. Scattered radiation shielding is performed by a water pool surrounding the EB-machine head, filled up before operations. Auxiliary systems, control console and analytical chemical laboratories are hosted in suitable containers near the plant and are easily transportable. The whole plant and annexed systems disassembling and reassembling in a new site can be easily carried out in a short time (few days). The plant, located at ENEA-Trisaia Res. Center (Basilicata, southern Italy), allows a large operative flexibility: groundwater and wastewater decontamination (1800 to 70 kg/h in the 1 to 25 kGy dose range), organic and chlorinated waste streams (25 kg/h at 75 kGy), solid hospital wastes (50 kg/h at 35 kGy) or hazardous wastes like polycyclic aromatic compounds (180 to 35 kg/h in the 10 to 50 kGy dose range). The paper describes and illustrates the plant in details and presents the first available operating results so far performed by the installed plant

Making Plant-Support Structures From Waste Plant Fiber

Science.gov (United States)

Morrow, Robert C.; < oscjmocl. < attjew K/; {ertzbprm. A,amda; Ej (e. Cjad); Hunt, John

2006-01-01

Environmentally benign, biodegradable structures for supporting growing plants can be made in a process based on recycling of such waste plant fiber materials as wheat straw or of such derivative materials as paper and cardboard. Examples of structures that can be made in this way include plant plugs, pots, planter-lining mats, plant fences, and root and shoot barriers. No chemical binders are used in the process. First, the plant material is chopped into smaller particles. The particles are leached with water or steam to remove material that can inhibit plant growth, yielding a fibrous slurry. If the desired structures are plugs or sheets, then the slurry is formed into the desired shapes in a pulp molding subprocess. If the desired structures are root and shoot barriers, pots, or fences, then the slurry is compression-molded to the desired shapes in a heated press. The processed materials in these structures have properties similar to those of commercial pressboard, but unlike pressboard, these materials contain no additives. These structures have been found to withstand one growth cycle, even when wet

Radioactive waste disposal: Waste isolation pilot plants (WIPP). (Latest citations from the NTIS Bibliographic database). Published Search

International Nuclear Information System (INIS)

1993-09-01

The bibliography contains citations concerning the Waste Isolation Pilot Plant (WIPP), a geologic repository located in New Mexico for transuranic wastes generated by the U.S. Government. Articles follow the development of the program from initial site selection and characterization through construction and testing, and examine research programs on environmental impacts, structural design, and radionuclide landfill gases. Existing plants and facilities, pilot plants, migration, rock mechanics, economics, regulations, and transport of wastes to the site are also included. The Salt Repository Project and the Crystalline Repository Project are referenced in separate bibliographies. (Contains a minimum of 228 citations and includes a subject term index and title list.)