WorldWideScience

Sample records for active biogas process

  1. Biogas processing

    Kudláč, Adam

    2010-01-01

    The diploma thesis includes proposals suitable for usage of the technologies for clearing the biogas into a quality of substitute natural gas (SNG). The most suitable technology is chosen for the clearing the biogas out of the septic tanks of the laboratory for biologically decomposable waste treatment at Institute of process and environmental engineering. There is a calculation , a proposal and a realisation of the experimental unit for clearing the biogas performed.

  2. Effect of temperature and active biogas process on passive separation of digested manure

    Kaparaju, Prasad Laxmi-Narasimha; Angelidaki, Irini

    2008-01-01

    outside mechanical or chemical action was used, within the reactor was studied in three vertical settling columns (100 cm deep). Variations in solids and microbial distribution at top, middle and bottom layers of column were assessed over a 15 day settling period. Results showed that best solids...... solids separation was noticed 24 h after settling in column incubated at 55 degrees C, with active biogas process. Microbiological analyses revealed that proportion of Archaea and Bacteria, absent in the autoclaved material, varied with incubation temperature, time and sampling depth. Short rod shaped...... reactor can be used effectively as an operating strategy to optimize biogas production by increasing the solids and biomass retention times. A minimum of 1-2 h "non-stirring" period appears to be optimal time before effluent removal in plants where extraction is batch-wise 2-4 times a day....

  3. Process control in biogas plants

    Holm-Nielsen, Jens Bo; Oleskowicz-Popiel, Piotr

    2013-01-01

    Efficient monitoring and control of anaerobic digestion (AD) processes are necessary in order to enhance biogas plant performance. The aim of monitoring and controlling the biological processes is to stabilise and optimise the production of biogas. The principles of process analytical technology...

  4. Monitoring and controlling the biogas process

    Ahring, B.K.; Angelidaki, I. [The Technical Univ. of Denmark, Dept. of Environmental Science and Engineering, Lyngby (Denmark)

    1997-08-01

    Many modern large-scale biogas plants have been constructed recently, increasing the demand for proper monitoring and control of these large reactor systems. For monitoring the biogas process, an easy to measure and reliable indicator is required, which reflects the metabolic state and the activity of the bacterial populations in the reactor. In this paper, we discuss existing indicators as well as indicators under development which can potentially be used to monitor the state of the biogas process in a reactor. Furthermore, data are presented from two large scale thermophilic biogas plants, subjected to temperature changes and where the concentration of volatile fatty acids was monitored. The results clearly demonstrated that significant changes in the concentration of the individual VFA occurred although the biogas production was not significantly changed. Especially the concentrations of butyrate, isobutyrate and isovalerate showed significant changes. Future improvements of process control could therefore be based on monitoring of the concentration of specific VFA`s together with information about the bacterial populations in the reactor. The last information could be supplied by the use of modern molecular techniques. (au) 51 refs.

  5. A new combined process for biological desulphurisation of biogas; Neue Verfahrenskombination zur biologischen Entschwefelung von Biogas

    Sayder, Bettina; Strauch, Sabine; Krassowski, Joachim; Kabasci, Stephan; Genzowsky, Kristoffer [Fraunhofer-Institut fuer Umwelt-, Sicherheits- und Energietechnik UMSICHT, Oberhausen (Germany)

    2010-07-01

    A new process developed by Fraunhofer UMSICHT is presented. The process comprises a gas purification stage in which the fermentation residue of the biogas plant is utilized. The fermentation residue is then regenerated in a downstream activation pond.

  6. Processing biogas; Biogas-Aufbereitung. Methanverlust von 1%: technisch moeglich

    Judex, J.

    2009-07-01

    This article takes a look at the results of a study made at the Institute of Bio-technology at the Zurich University of Applied Sciences and the Paul Scherrer Institute PSI. The study was made at the wastewater treatment plant in Emmen, Switzerland, on methane losses in the processing of biogas to give it natural gas quality. The avoidance of methane losses - methane is a greenhouse gas - is discussed and various technologies used in the processing of biogas generated from organic waste digestion are examined. The installations at the wastewater treatment plant in Emmen are commented on and the measurement concept and equipment used are described. The results and observations made are also presented in graphical form.

  7. Influence of temperature and pH value on enzyme activity in the biogas process; Einfluss der Temperatur und des pH-Wertes auf die Aktivitaet von Enzymen im Biogasprozess

    Vintiloiu, Anca; Brule, Mathieu; Lemmer, Andreas; Oechsner, Hans [Hohenheim Univ. (Germany). Landesanstalt fuer Landwirtschaftliches Maschinen- und Bauwesen; Jungbluth, Thomas [Hohenheim Univ. (Germany). Fachgebiet Verfahrenstechnik der Tierhaltungssysteme; Jurcoane, Stefana [Bucharest Univ. (Romania). Microbial Biotechnological Centers; Israel-Roming, Florentina [Center of Research for Applied Biochemistry and Biotechnology, Bucharest (Romania)

    2009-07-01

    Enzyme supplementation is often used in agricultural biogas plants to accelerate degradation of crop fibre (e.g. cellulose and hemi-cellulose) and thus increase biogas yield. However, the efficacy of such enzyme supplementation has been insufficiently tested under laboratory conditions. In order to systematically investigate factors influencing enzyme activity, enzymatic hydrolysis experiments were conducted on maize straw at the University of Hohenheim to test the efficacy of commercial enzyme supplementation under controlled conditions outwith the biogas production process. (orig.)

  8. Biogas desulfurization using autotrophic denitrification process.

    Bayrakdar, Alper; Tilahun, Ebrahim; Calli, Baris

    2016-01-01

    The aim of this study was to evaluate the performance of an autotrophic denitrification process for desulfurization of biogas produced from a chicken manure digester. A laboratory scale upflow fixed bed reactor (UFBR) was operated for 105 days and fed with sodium sulfide or H2S scrubbed from the biogas and nitrate as electron donor and acceptor, respectively. The S/N ratio (2.5 mol/mol) of the feed solution was kept constant throughout the study. When the UFBR was fed with sodium sulfide solution with an influent pH of 7.7, about 95 % sulfide and 90 % nitrate removal efficiencies were achieved. However, the inlet of the UFBR was clogged several times due to the accumulation of biologically produced elemental sulfur particles and the clogging resulted in operational problems. When the UFBR was fed with the H2S absorbed from the biogas and operated with an influent pH of 8-9, around 98 % sulfide and 97 % nitrate removal efficiencies were obtained. In this way, above 95 % of the H2S in the biogas was removed as elemental sulfur and the reactor effluent was reused as scrubbing liquid without any clogging problem. PMID:26428238

  9. Conversion of Agricultural Wastes to Biogas using as Inoculum Cattle Manure and Activated Sludge

    Simina Neo; Teodor Vintilă; Marian Bura

    2012-01-01

    Agricultural wastes represent a large unexploited energy potential that could be converted into biogas by anaerobic digestion. In the present study there has been analysed the way in which agricultural wastes are converted into biogas by using as inoculum cattle manure as compared with activated sludge. To carry out this experiment on small scale there have been designed 5 batch bottles. For the batch process all substrate was put into the bottles at start. The biogas process was initiated af...

  10. Improvement of the Biogas Production Process : Explorative project (EP1)

    Karlsson, Anna; Björn, Annika; Sepehr, Shakeri Yekta; Svensson, Bo

    2014-01-01

    There are several ways to improve biogas production in anaerobic digestion processes and a number of strategies may be chosen. Increased organic loading in existing plants will in most cases demand the introduction of new substrate types. However, to substantially increase the Swedish biogas production new, large-scale biogas plants digesting new substrate types need to be established. Better utilization of existing digester volumes can be linked to:  Increase of organic loading rates and/or ...

  11. Biogas reforming process investigation for SOFC application

    Highlights: • Mathematical model of fuel processor and experimental validation was made. • Simulations made to find syngas composition varying fuel processor operating conditions. • Experimental tests were carried out on SOFC mono-cell to obtain polarization curves. • The best conditions for SOFC/fuel processor integrated systems were defined. - Abstract: In recent years, research efforts on fuel cells have been addressed on the development of multifuel reformers with particular emphasis toward the potential use of non-traditional fuels. Among these, biogas is considered very promising to be used as syngas source for fuel cell system applications. The interest on this hydrogen source is focused mainly to supply high temperature fuel cells (HTFC). This paper reports a wide experimental research investigation on SOFC device supplied by syngas produced with different biogas reforming processes (steam reforming, autothermal reforming and partial oxidation). Thermodynamic simulations have been performed to determine the reformed gas composition varying process, reaction temperature and steam to carbon – oxygen to carbon ratios. Syngas mixtures obtained were experimentally tested in order to evaluate the performance of a SOFC mono-cell. Furthermore, an analysis of the combination: fuel processor with a SOFC stack has been determined in order to assess the total energy efficiency

  12. biogas

    2015-01-01

    Functions for working with biogas data. Both low- and high-level functions are included for carrying out common tasks for analysis of biogas and related data. Molar mass and calculated oxygen demand (COD') can be determined from a chemical formula. Measured gas volume can be corrected for water...... vapor and to (possibly user-defined) standard temperature and pressure. Gas composition, cumulative production, or other variables can be interpolated to a specified time. Cumulative biogas and methane production (and rates) can be calculated using volumetric, manometric, or gravimetric methods for any...... be summarized in several different ways (e.g., omitting normalization) using the same function. Lastly, biogas and methane production can be predicted from substrate composition and additional, optional data....

  13. Analysis of problems with dry fermentation process for biogas production

    Pilát, Peter; Patsch, Marek; Jandačka, Jozef

    2012-04-01

    The technology of dry anaerobic fermentation is still meeting with some scepticism, and therefore in most biogas plants are used wet fermentation technology. Fermentation process would be not complete without an optimal controlled condition: dry matter content, density, pH, and in particular the reaction temperature. If is distrust of dry fermentation eligible it was on the workplace of the Department of Power Engineering at University of Zilina built an experimental small-scale biogas station that allows analysis of optimal parameters of the dry anaerobic fermentation, in particular, however, affect the reaction temperature on yield and quality of biogas.

  14. Analysis of problems with dry fermentation process for biogas production

    Jandačka Jozef; Patsch Marek; Pilát Peter

    2012-01-01

    The technology of dry anaerobic fermentation is still meeting with some scepticism, and therefore in most biogas plants are used wet fermentation technology. Fermentation process would be not complete without an optimal controlled condition: dry matter content, density, pH, and in particular the reaction temperature. If is distrust of dry fermentation eligible it was on the workplace of the Department of Power Engineering at University of Zilina built an experimental small-scale biogas statio...

  15. Conversion of Agricultural Wastes to Biogas using as Inoculum Cattle Manure and Activated Sludge

    Simina Neo

    2012-05-01

    Full Text Available Agricultural wastes represent a large unexploited energy potential that could be converted into biogas by anaerobic digestion. In the present study there has been analysed the way in which agricultural wastes are converted into biogas by using as inoculum cattle manure as compared with activated sludge. To carry out this experiment on small scale there have been designed 5 batch bottles. For the batch process all substrate was put into the bottles at start. The biogas process was initiated after closing the bottles, and the biogas was collected during the process until the biogas production ended. During the 33 days of experiment the batch bottles were held at constant temperature (370C in a water bath. The biomass used in the experiment was wheat straw and corn stalks. Before being used in the experiment the biomass was milled using a kitchen mixer. After that the biomass was subjected to a combination of thermal and chemical pretreatments. The volume of biogas produces was measured every seven days during the experiment period. The biogas production measurements were done by using a BlueSens measuring equipment.

  16. Practical application of the microbial activity analysis on the monitoring of the process biological stability of biogas plants; Praktische Anwendung der mikrobiellen Aktivitaetsanalyse zur Ueberwachung der prozessbiologischen Stabilitaet von Biogasanlagen

    Neumann, Lukas; Tietjen, Carsten [MT-Energie GmbH, Zeven (Germany). Forschung und Entwicklung; Rilling, Norbert [MT-Energie GmbH und Co. KG, Rockstedt (Germany)

    2013-10-01

    As extension for the classical fluorescence microscopic analysis of the microbial population in a biogas fermenter the cell counts and frequency of the different methanogenic organisms was used to generate the plant specific stability indicator called MT-Factor. This factor describes the optimal composition of the microbial population for the current process conditions and could be used for the biological process consulting. A study of the MT-Energie laboratory showed that the combination of the microbial cell counts determination and the plant specific stability factor shifts during a process instability or failure of a biogas fermenter. This analysis of the methane-forming microorganisms as well as their cell count and importance for the entire anaerobic biology of the biogas plant can be used for clearly visualizing and tracking the vitality of the digestion process. The evaluation of the microbial activity of different liquid manure samples could show the influence of inhibitors like disinfectant or cleaning agents directly without time consuming cultivation tests. By determining the MT-Factor and analyzing the activity of the methane formers, an impending influence of inhibitors can be detected in liquid manure before the manure enters the digester. This way, a negative influence on the gas yield can be avoided. (orig.)

  17. Methane losses in biogas processing; Methanverluste bei der Biogasaufbereitung

    Baum, S.; Baier, U. [ZHAW, Zuercher Hochschule fuer Angewandte Wissenschaften, IBT Institut fuer Biotechnologie, Fachgruppe Umweltbiotechnologie, Waedenswil (Switzerland); Judex, J.; Biollaz, S.; Schneebeli, J. [PSI, Paul Scherrer Institut, Villigen (Switzerland)

    2008-11-15

    This report for the Swiss Federal Office of Energy (SFOE) by the Paul Scherrer Institute PSI and the Zurich University of Applied Sciences, Switzerland, presents the results of a study made on methane losses that occur during the processing of biogas to provide natural gas quality. Such losses are considered as possibly compromising the environmental advantages offered by the feeding-in of processed biogas into the national gas mains. This processing involves the removal of carbon dioxide from the biogas. The state-of-the-art in this area is discussed, relevant factors and analysis methods are looked at. An overview of methods used to prevent methane losses is presented. The results of investigations made at an installation in Lucerne, Switzerland, are presented and discussed.

  18. Analysis of different substrates for processing into biogas

    B. Mursec

    2009-12-01

    Full Text Available Purpose: The main target is to produce as much biogas as possible with highest possible biomethane content from crops representing the principal fuel for driving the gas motors and electric generators and, consequently, production of electricity.Design/methodology/approach: The biogas production was measured by a mini digester according to the German standard DIN 38414, Part 8. It was effected in the mesophilic temperature range. The biogas production from six different energy crops and pig slurry was measured in the laboratory of the Faculty of Agriculture and Life Sciences. In six trial fields the monocultures such as maize, sorghum, amaranth, sunflower, Jerusalem artichoke and sugar beet were grown.Findings: The highest biomethane production was achieved with the sunflower substrate (283 Nl/kgVS, followed by the sorghum substrate (188 Nl/kgVS and maize (187 Nl/kgVS. The amaranth substrate produced 225 Nl/kgVS and the Jerusalem artichoke 115 Nl/kgVS. The least amount of biomethane was produced from the sugar beet (95 Nl/kgVS.Research limitations/implications: The basic structure of the laboratory device is welded from stainless steel (inox and is limited by the following dimensions: 2500 mm length, 1000 mm height and 350 mm width. The device consists of twelve units of fermentors ensuring four tests simultaneously with three replications and assuring high accuracy of results.Practical implications: The test fermentors serve to test the biogas production from different energy crops and other materials of organic origin. The results reached serve to plan the electricity production in the biogas production plant.Originality/value: The mini digesters simulated in laboratory the actual state from the biogas production plant. Anaerobic fermentation was introduced and the biogas to be processed into electricity was produced.

  19. Dynamic biogas upgrading based on the Sabatier process

    Jurgensen, Lars; Ehimen, Ehiazesebhor Augustine; Born, Jens;

    2015-01-01

    This study aimed to investigate the feasibility of substitute natural gas (SNG) generation using biogas from anaerobic digestion and hydrogen from renewable energy systems. Using thermodynamic equilibrium analysis, kinetic reactor modeling and transient simulation, an integrated approach for the...... operation of a biogas-based Sabatier process was put forward, which was then verified using a lab scale heterogenous methanation reactor. The process simulation using a kinetic reactor model demonstrated the feasibility of the production of SNG at gas grid standards using a single reactor setup. The Wobbe...

  20. Online monitoring and control of the biogas process

    Boe, K.

    2006-07-01

    The demand for online monitoring and control of biogas process is increasing, since better monitoring and control system can improve process stability and enhance process performance for better economy of the biogas plants. A number of parameters in both the liquid and the gas phase have been suggested as process indicators. These include gas production, pH, alkalinity, volatile fatty acids (VFA) and hydrogen. Of these, VFA is the most widely recognised as a direct, relevant measure of stability. The individual, rather than collective VFA concentrations are recognised as providing significantly more information for diagnosis. However, classic on-line measurement is based on filtration, which suffers from fouling, especially in particulate or slurry wastes. In this project, a new online VFA monitoring system has been developed using gas-phase VFA extraction to avoid sample filtration. The liquid sample is pumped into a sampling chamber, acidified, added with salt and heated to extract VFA into the gas phase before analysis by GC-FID. This allows easy application to manure. Sample and analysis time of the system varies from 25-40 min. depending on the washing duration. The sampling frequency is fast enough for the dynamic of a manure digester, which is in the range of several hours. This system has been validated over more than 6 months and had shown good agreement with offline VFA measurement. Response from this sensor was compared with other process parameters such as biogas production, pH and dissolved hydrogen during overload situations in a laboratory-scale digester, to investigate the suitability of each measure as a process indicator. VFA was most reliable for indicating process imbalance, and propionate was most persistent. However, when coupling the online VFA monitoring with a simple control for automatic controlling propionate level in a digester, it was found that propionate decreased so slow that the biogas production fluctuated. Therefore, it is more

  1. Comparative study of stability and half-life of enzymes and enzyme aggregates implemented in anaerobic biogas processes

    Binner, Roman; Schmack, Doris; Reuter, Monika [Research and Development Department, Schmack Biogas GmbH, Schwandorf (Germany); Menath, Veronika; Huber, Harald; Thomm, Michael [University of Regensburg, Department of Microbiology, Regensburg (Germany); Bischof, Franz [University of Applied Sciences Amberg-Weiden, Faculty of Mechanical Engineering/Environmental Engineering, Amberg (Germany)

    2011-03-15

    Anaerobic digestion of mainly energy crops gains more and more importance in developing a sustainable energy supply. Therefore, the optimization of gas yield plays a major role in specific research attempts and economical considerations. One possibility to increase natural polymer degradation and concomitantly energy efficiency is the addition of exoenzymes to biogas facilities to enforce the primary degradation steps for biogas production. Therefore, in the present study, the stability and activity of five externally added enzyme mixtures to anaerobic biogas processes were investigated. Protein assays using soluble fractions of different biogas plants incubated together with the enzyme mixtures revealed that, within about 10 min, the externally added enzymes were mostly degraded. This very low stability in biogas reactors makes it unlikely that the addition of enzymes contributes significantly to degradation of macromolecules in the biogas process. Even the addition of protease inhibitors did not protect the added enzyme mixtures from degradation in most experiments. Furthermore, the influence of added enzymes on the viscosity of the biomass was tested. Only a marginal effect was obtained, when applying a tenfold higher concentration of added enzymes as proposed for practical use. The same result was achieved when commercially available enzymes were added to technical-scale fermentations using corn silage as monosubstrate. Therefore, these studies did not provide evidence that the addition of external enzymes into anaerobic degradation systems increases the methane yield in biogas facilities. (orig.)

  2. Energy from whey - comparison of the biogas and bioethanol processes

    This final report for the Swiss Federal Office of Energy (SFOE) presents the results of a project which investigated how energy could be generated from the whey produced in the cheese-making process. The first part of the project aimed to validate a concept for on-site production and use of biogas at a medium-sized cheese factory. The results of the first step, an experimental study carried out using a down-flow fixed-film bio-reactor, are discussed. This allowed the determination of the optimal working parameters as well as providing an estimate of the performance of the process. The second part of the project aimed to compare the bio-ethanol and biogas production processes. It was carried out in collaboration with AlcoSuisse and the Energy Systems Laboratory at the Swiss Federal Institute of Technology (EPFL) in Lausanne. The results of a life-cycle assessment (LCA) are discussed, which compared the two processes from an environmental point of view. Here, two impacts were considered: fossil fuel consumption and greenhouse effect. The replacement of fuel-oil with biogas for heat production and the replacement of conventional petrol with mixture including 5% bio-ethanol were examined. The results are presented that show that there was no significant difference between the two processes. According to the authors, the treatment of one cubic meter of cheese-whey allows savings of more than 20 litres of oil equivalent and 60 kg of CO2 emissions

  3. Biogas desulfurization with doped activated carbon; Feinentschwefelung von Biogas mit dotierter Aktivkohle

    Rossow, Silvana; Goetze, Toralf [AdFiS systems GmbH, Teterow (Germany); Deerberg, Goerge [Fraunhofer Inst. fuer Umwelt-, Sicherheits- und Energietechnik UMSICHT, Oberhausen (Germany); Kanswohl, Norbert [Rostock Univ. (Germany). Lehrstuhl fuer Abfall- und Stoffstromwirtschaft; Nelles, Michael [Rostock Univ. (Germany). Lehrstuhl fuer Technologie und Verfahrenstechniken der umweltgerechten Landbewirtschaftung

    2009-07-01

    Doped activated carbon is a special developed activated carbon for the desulfurization of biogas. Because of its special properties it is able to bond a big amount of hydrogen sulfide. After many laboratory tests it was possible to demonstrate the performance of doped activated carbon for desulfurization in practical use The advantages and the specific functioning of doped activated carbon for desulfurization were here exactly as in previous laboratory studies. Despite fluctuating boundary conditions a continuous complete desulfurization was possible. By using the desulfurization system the concentration of hydrogen sulfide is lowered to less than 1 ppm. The damages or interferences that are often caused by hydrogen sulfide could not be identified. A directly visible positive impact of the full desulfurization is the doubling of oil using time. (orig.)

  4. Gas Permeation Processes in Biogas Upgrading: A Short Review

    Kárászová, M. (Magda); Sedláková, Z.; Izák, P. (Pavel)

    2015-01-01

    Biogas upgrading is a widely studied and discussed topic. Many different technologies have been employed to obtain biomethane from biogas. Methods like water scrubbing or pressure swing adsorption are commonly used and can be declared as well established. Membrane gas permeation found its place among the biogas upgrading methods some years ago. Here, we try to summarize the progress in the implementation of gas permeation in biogas upgrading. Gas permeation has been already accepted as a comm...

  5. Effect of ferrous chloride on biogas production and enzymatic activities during anaerobic fermentation of cow dung and Phragmites straw.

    Zhang, Huayong; Tian, Yonglan; Wang, Lijun; Mi, Xueyue; Chai, Yang

    2016-06-01

    The effect of ferrous (added as FeCl2) on the anaerobic co-digestion of Phragmites straw and cow dung was studied by investigating the biogas properties, pH values, organic matter degradation (COD) and enzyme activities (cellulase, protease and dehydrogenase) at different stages of mesophilic fermentation. The results showed that Fe(2+) addition increased the cumulative biogas yields by 18.1 % by extending the peak period with high daily biogas yields. Meanwhile, the methane (CH4) contents in the Fe(2+) added groups were generally higher than the control group before the 15th day. The pH values were not significantly impacted by Fe(2+) concentrations during the fermentation process. The COD concentrations, cellulase, protease and dehydrogenase activities varied with the added Fe(2+) concentrations and the stages of the fermentation process. At the beginning stage of fermentation (4th day), Fe(2+) addition increased the biogas production by improving the cellulase and dehydrogenase activities which caused a decline in COD. At the peak stage of fermentation (8th day), Fe(2+) addition enhanced the cellulase and protease activities, and resulted in lower COD contents than the control group. When the biogas yields decreased again (13th day), the COD contents varied similar with the protease and dehydrogenase activities, whilst cellulase activities were not sensitive to Fe(2+) concentrations. At the end of fermentation (26th day), Fe(2+) addition decreased the cellulase activities, led to lower COD contents and finally resulted the lower biogas yields than the control group. Taking the whole fermentation process into account, the promoting effect of Fe(2+) addition on biogas yields was mainly attributed to the extension of the gas production peak stage and the improvement of cellulase activities. PMID:26862032

  6. BIOGAS UPGRADING PROCESSES FOR THE PRODUCTION OF NATURAL GAS SUBSTITUTE

    Čekanova, Patricia; Jasminska, Natalia; Brestovič, Tomaš; Schvarzbacherova, Eva

    2011-01-01

    Biogas from anaerobic digestion of biological wastes is a renewable energy resource. It has been used to provide heat, shaft power and electricity. Typical biogas contains 50-65% methane (CH4), 30-45% carbon dioxide (CO2), moisture and traces of hydrogen sulphide (H2S). Presence of CO2 and H2S in biogas affects engine performance adversely. Reducing CO2 and H2S content will significantly improve quality of biogas. In this work, a method for biogas scrubbing and CH4 enrichment is presented. Ch...

  7. EU Agro Biogas Project

    Amon, T.; Mayr, H.; Eder, M.; Hobbs, P.; Rao Ravella, S.; Roth, U.; Niebaum, A.; Doehler, H.; Weiland, P.; Abdoun, E.; Moser, A.; Lyson, M.; Heiermann, M.; Plöchl, M.; Budde, J.; Schattauer, A.; Suarez, T.; Möller, H.; Ward, A.; Hillen, F.; Sulima, P.; Oniszk-Polplawska, A.; Krampe, P.; Pastorek, Z.; Kara, J.; Mazancova, J.; Dooren, van H.J.C.; Wim, C.; Gioelli, F.; Balsari, P.

    2009-01-01

    EU-AGRO-BIOGAS is a European Biogas initiative to improve the yield of agricultural biogas plants in Europe, to optimise biogas technology and processes and to improve the efficiency in all parts of the production chain from feedstock to biogas utilisation. Leading European research institutions and

  8. Mechanism of zeolite activity in biogas co-digestion

    Hansson, Anna

    2011-01-01

    Biogas is a source of renewable energy and is produced at anaerobic conditions. The gas consists mainly of methane (55-70 %) and carbon dioxide (30-45 %). Biogas can be used as vehicle fuel after the gas has been upgraded to a methane content of approximately 97 %. There are several companies in Sweden producing biogas. Svensk biogas AB in Linköping is one of the largest. The company has two biogas production plants; one in Linköping and one in Norrköping. To meet the surge demand for biogas ...

  9. Life cycle assessment of coupling household biogas production to agricultural industry: A case study of biogas-linked persimmon cultivation and processing system

    Biogas plant construction has been boosted in rural China not only due to the immediate merit from biogas production but also the succeeding benefit from by-product utilization in agro-industry, both of which are significant strategies to address energy shortage and global warming issues. However, little work has been done to evaluate the coupling of biogas projects to traditional agrosystems from a life-cycle perspective, which is most important in process and system optimization in different senses. By taking persimmon cultivation and processing with supports from a household biogas plant as a case study, this study conducts a life cycle assessment of coupling biogas production to agro-industry in terms of energy, environmental and economic performance. The results suggest that each production stage following the biogas/digestate utilization chain (biogas operation-persimmon cultivation-product processing) is beneficial across all three aspects. However, a tradeoff only exists in utilizing digestate as top-dressing and employing biogas utilization as engine fuel, while biogas application in fresh-keeping and digestate reuse as base fertilizer fails to increase either energy production or greenhouse gas mitigation. The coupled system can be hopefully optimized through increasing fermentation efficiency and joint operation of biogas digesters. -- Highlights: •Biogas/digestate utilization is overall beneficial in all production stages. •Each bioresource application may not be profitable in all respects. •Tradeoffs in using biogas and digestate vary among different utilization ways. •Multi-user operation and fermentation efficiency elevation optimize system

  10. Analysis of different substrates for processing into biogas

    B. Mursec; P. Vindis; M. Janzekovic; M. Brus; F. Cus

    2009-01-01

    Purpose: The main target is to produce as much biogas as possible with highest possible biomethane content from crops representing the principal fuel for driving the gas motors and electric generators and, consequently, production of electricity.Design/methodology/approach: The biogas production was measured by a mini digester according to the German standard DIN 38414, Part 8. It was effected in the mesophilic temperature range. The biogas production from six different energy crops and pig s...

  11. Process optimization of biogas production at Nemščak biogas plant by pre-treatment of the substrate and combining with waste sludge

    Žitek, Filip

    2015-01-01

    The purpose of this thesis is to increase the amount of biogas produced by pre-treatment of the substrate and combining with waste sludge. For anaerobic digestion of different substrates, we used a pilot reactor to determine the biogas potential at Nemščak biogas plant. The pilot reactor was built in 2009 for the purpose of testing new substrates in the process of biogas production. The pilot reactor has a working volume of 2000 litres; there is a gas tank above it with the volume of 500 litr...

  12. Life cycle assessment of flexibly fed biogas processes for an improved demand-oriented biogas supply.

    Ertem, Funda Cansu; Martínez-Blanco, Julia; Finkbeiner, Matthias; Neubauer, Peter; Junne, Stefan

    2016-11-01

    This paper analyses concepts to facilitate a demand oriented biogas supply at an agricultural biogas plant of a capacity of 500kWhel, operated with the co-digestion of maize, grass, rye silage and chicken manure. In contrast to previous studies, environmental impacts of flexible and the traditional baseload operation are compared. Life Cycle Assessment (LCA) was performed to detect the environmental impacts of: (i) variety of feedstock co-digestion scenarios by substitution of maize and (ii) loading rate scenarios with a focus on flexible feedstock utilization. Demand-driven biogas production is critical for an overall balanced power supply to the electrical grid. It results in lower amounts of emissions; feedstock loading rate scenarios resulted in 48%, 20%, 11% lower global warming (GWP), acidification (AP) and eutrophication potentials, and a 16% higher cumulative energy demand. Substitution of maize with biogenic-waste regarding to feedstock substitution scenarios could create 10% lower GWP and AP. PMID:27522120

  13. EU Agro Biogas Project

    Amon, T.; Mayr, H.; M. Eder; Hobbs, P.; Rao Ravella, S.; Roth, U.; Niebaum, A.; Doehler, H.; Weiland, P.; Abdoun, E.; A. Moser; Lyson, M.; Heiermann, M.; Plöchl, M.; Budde, J.

    2009-01-01

    EU-AGRO-BIOGAS is a European Biogas initiative to improve the yield of agricultural biogas plants in Europe, to optimise biogas technology and processes and to improve the efficiency in all parts of the production chain from feedstock to biogas utilisation. Leading European research institutions and universities are cooperating with key industry partners in order to work towards sustainable biogas production in Europe. Fourteen partners from eight European countries are involved in the EU-AGR...

  14. Biogas utilization

    Moser, M.A. [Resource Conservation Management, Inc., Berkeley, CA (United States)

    1996-01-01

    Options for successfully using biogas depend on project scale. Almost all biogas from anaerobic digesters must first go through a gas handling system that pressurizes, meters, and filters the biogas. Additional treatment, including hydrogen sulfide-mercaptan scrubbing, gas drying, and carbon dioxide removal may be necessary for specialized uses, but these are complex and expensive processes. Thus, they can be justified only for large-scale projects that require high-quality biogas. Small-scale projects (less than 65 cfm) generally use biogas (as produced) as a boiler fuel or for fueling internal combustion engine-generators to produce electricity. If engines or boilers are selected properly, there should be no need to remove hydrogen sulfide. Small-scale combustion turbines, steam turbines, and fuel cells are not used because of their technical complexity and high capital cost. Biogas cleanup to pipeline or transportation fuel specifications is very costly, and energy economics preclude this level of treatment.

  15. Near-infrared spectroscopy for process and substrate supervision of a full-scale biogas plant

    Jacobi, Hans Fabian

    2012-07-01

    Aim of this study was to investigate the possible use of near-infrared spectroscopy in the supervision of the biogas production process or parts thereof. It was examined, whether the surveillance of (a) the process and (b) substrate was feasible. The following tasks were accomplished to this end: 1. Development, construction and assembly of suitable NIRS-metrology, development of proper control-software as well as of strategies for data acquisition and data handling, 2. calculation and validation of regression models on the basis of acquired spectra and reference data for (a) suitable parameters of the biogas process, (b) composition and biogas potential of the substrate, 3. calculation of continuous time series of all parameters in order to prove the possibility of continuous surveillance, 4. integrated processing of continuously calculated biogas potentials together with plant data for the prediction of the biogas production behavior of the biogas plant. A near-infrared spectrometer was installed and equipped with NIR-measuring heads of own design and construction on a full-scale agricultural biogas plant. For 500 days spectra were continuously logged at (a) a pipe flowed through by fermenter slurry and (b) the feeding station, where silage passed. Based on regularly withdrawn reference samples and the corresponding spectra regression models were calibrated for the several constituents. Continuously logged spectra were used to calculate time series with the aid of the regression models for each constituent. Models and time series were established for the following parameters: (a) process parameters: volatile fatty acids, acetic acid, propionic acid, dry matter, volatile solids; (b) substrate parameters: dry matter, volatile solids, crude fiber, crude fat, crude protein, nitrogen-free extracts, experimentally assessed biogas potential, theoretically assessed biogas potential. Despite the partially low quality of the models it was possible to follow the course of

  16. Causes for inhibitions of biogas process; Aarsager til haemning af biogasprocessen

    NONE

    2001-11-01

    It is the aim of the project to map reasons to inhibition of the biogas process. Inhibition of Danish common biogas plants in the last 5 years will be investigated in order to try to find the exact reason to the interruption of the process. Scientific literature will be investigated to describe the different reason for inhibition. The results of the project will be published in a report, an article and a popularized paper. (EHS)

  17. Processing biogas plant digestates into value-added products - BIOVIRTA

    Paavola, T. (MTT Agrifood Research Finland, Jokioinen (Finland)), e-mail: teija.paavola@mtt.fi; Torniainen, M. (Finnish Food Safety Authority, EVIRA, Helsinki (Finland)), e-mail: merja.torniainen@evira.fi; Kaparaju, P. (Jyvaeskylae Univ. (Finland)), e-mail: prasad.kaparaju@jyu.fi (and others)

    2011-11-15

    The objective of BIOVIRTA project is to develop technologies and practices with which digestates, originating from anaerobic digestion of different organic wastes and by-products can be refined to value-added and safe products for various end-uses. It is expected that the operational preconditions for biogas plants will be significantly enhanced when the end-products are proven safe and applicable. Selection of the raw materials for anaerobic co-digestion is the main operational strategy that could influence the nutrient content in the digestate. This has been clearly established in the laboratory and full-scale studies with various digestates originating from different raw materials. The nutrient content in the digestate also affects the opportunities to produce refined digestate products. In this project, the possibilities for several processing technologies, e.g. mechanical separation, stripping, and struvite production have been intensively evaluated for the production of different digestate products. Their mass balances have also been estimated. The feasibility for the use of the digestate products has been assessed based on their chemical and hygienic quality and for various end-uses, including as organic fertiliser and/or soil improver in crop production. The results of these field-experiments showed that the yield of barley fertilised with digestate products was comparable to inorganic fertilisers. (orig.)

  18. Catalytic Effect of Tungsten on Anaerobic Digestion Process for Biogas Production from Fruit and Vegetable Wastes

    Das A; Mondal.C

    2013-01-01

    In the recent years global energy crisis increased at a fast pace. Demand for the use of fossil fuels for cooking and other commercial activities increased along with the increasing population of India. Use of renewable sources of energy viz. biogas for cooking etc can somewhat be an alternative for the excessive demand of fossil fuels like LPG. In this study, the catalytic effect of tungsten for maximizing biogas have been presented. Essentially, anaerobic digesti...

  19. Biogas Production from Sugarcane Waste: Assessment on Kinetic Challenges for Process Designing

    Leandro Janke; Athaydes Leite; Marcell Nikolausz; Thomas Schmidt; Jan Liebetrau; Michael Nelles; Walter Stinner

    2015-01-01

    Biogas production from sugarcane waste has large potential for energy generation, however, to enable the optimization of the anaerobic digestion (AD) process each substrate characteristic should be carefully evaluated. In this study, the kinetic challenges for biogas production from different types of sugarcane waste were assessed. Samples of vinasse, filter cake, bagasse, and straw were analyzed in terms of total and volatile solids, chemical oxygen demand, macronutrients, trace elements, an...

  20. Killing of salmonella in the biogas process; Abtoetung von Salmonellen im Biogasprozess

    Froeschle, Bianca; Lebuhn, Michael

    2012-08-15

    Pathogenic Salmonella are used in ordinances as an indicator for assessing microbial reduction in biogas plants and for the epidemic-hygienic condition of digestate. This brochure presents results of a study that examined the hygienic effect of the biogas process on Salmonella. [German] Krankheitserregende Salmonellen werden in relevanten Rechtsverordnungen als Indikator zur Beurteilung der Keimreduzierung in Biogasanlagen und des seuchenhygienischen Zustands von Gaerresten herangezogen. Die vorliegende Broschuere stellt Ergebnisse einer Studie dar, die die hygienisierende Wirkung des Biogasprozesses auf Salmonellen untersuchte.

  1. The Optimum Mesophilic Temperature of Batch Process Biogas Production from Animal-based Wastes

    Osita Obineche Obiukwu

    2014-10-01

    Full Text Available The optimum mesophilic temperature of biogas production from blends The optimum temperature of biogas production from blends of animal-based wastes was determined under controlled heat supply to the digester in a batch digestion process. Cow Dung (CD and Poultry Droppings (PD were blended in the ratio of CD: PD: 1:3. The digester was operated at average ambient temperature of 30°C as baseline. Biogas production from the waste blends was monitored under the temperatures of 32 to 45°C. Results obtained indicate maximum cumulative gas yield was observed at the temperature of 40°C. The 40°C temperature gave the highest biogas yield of 2685 mL followed by the 35°C temperature with the cumulative yield of 2535 mL. The ambient temperature of 30°C had the least cumulative biogas yield of 185 mL. These results indicate that increased and steady biogas production can be achieved under the optimum mesophilic temperature of 40°C when these animal-based wastes are digested in batch digestion process.

  2. Biogas production from UASB and polyurethane carrier reactors treating sisal processing wastewater

    Rubindamayugi, M.S.T.; Salakana, L.K.P. [Univ. of Dar es Salaam, Faculty of Science, Applied Microbiology Unit (Tanzania, United Republic of)

    1997-12-31

    The fundamental benefits which makes anaerobic digestion technology (ADT) attractive to the poor developing include the low cost and energy production potential of the technology. In this study the potential of using UASB reactor and Polyurethane Carrier Reactor (PCR) as pollution control and energy recovery systems from sisal wastewater were investigated in lab-scale reactors. The PCR demonstrated the shortest startup period, whereas the UASB reactor showed the highest COD removal efficiency 79%, biogas production rate (4.5 l biogas/l/day) and process stability than the PCR under similar HRT of 15 hours and OLR of 8.2 g COD/l/day. Both reactor systems became overloaded at HRT of 6 hours and OLR of 15.7 g COD/l/day, biogas production ceased and reactors acidified to pH levels which are inhibiting to methanogenesis. Based on the combined results on reactor performances, the UASB reactor is recommended as the best reactor for high biogas production and treatment efficiency. It was estimated that a large-scale UASB reactor can be designed under the same loading conditions to produce 2.8 m{sup 3} biogas form 1 m{sup 3} of wastewater of 5.16 kg COD/m{sup 3}. Wastewater from one decortication shift can produce 9,446 m{sup 3} og biogas. The energy equivalent of such fuel energy is indicated. (au)

  3. Eliminating methanogenic activity in hydrogen reactor to improve biogas production in a two-stage anaerobic digestion process co-digesting municipal food waste and sewage sludge.

    Zhu, Heguang; Parker, Wayne; Conidi, Daniela; Basnar, Robert; Seto, Peter

    2011-07-01

    Laboratory scale two-stage anaerobic digestion process model was operated for 280 days to investigate the feasibility to produce both hydrogen and methane from a mixture feedstock (1:1 (v/v)) of municipal food waste and sewage sludge. The maximum hydrogen and methane yields obtained in the two stages were 0.93 and 9.5 mL/mL feedstock. To eliminate methanogenic activity and obtain substantial hydrogen production in the hydrogen reactor, both feedstock and mixed liquor required treatment. The heat treatment (100°C, 10 min) for feedstock and a periodical treatment (every 2-5 weeks, either heating, removal of biomass particles or flushing with air) for mixed liquor were effective in different extent. The methane production in the second stage was significantly improved by the hydrogen production in the first stage. The maximum methane production obtained in the period of high hydrogen production was more than 2-fold of that observed in the low hydrogen production period. PMID:21592783

  4. CONTROL PARAMETERS FOR UNDERSTANDING AND PREVENTING PROCESS IMBALANCES IN BIOGAS PLANTS. EMPHAS IS ON VFA DYNAMICS

    Bangsø Nielsen, Henrik

    control and understanding are necessary. The work of present study was directed towards this challenge. Initially, the response of the anaerobic digestion process to various types of process imbalances was investigated with special focus on volatile fatty acid dynamics (VFA), methane production and p...... indication of process imbalances in biogas plants. At Danish full-scale biogas plants the biogas production is normally the only continuously measured parameter. In order to examine the usability of propionate as control parameter a reactor experiment was constructed in which the reactor operation either was...... carried out on the basis of the methane production or on the basis of fluctuations in the concentration of propionate. The experiment confirmed that propionate is a useful parameter for (1) indication of process imbalances and (2) for regulation and optimization of the anaerobic digestion process in CSTRs...

  5. Microbial Consortium with High Cellulolytic Activity (MCHCA for enhanced biogas production.

    Krzysztof ePoszytek

    2016-03-01

    Full Text Available The use of lignocellulosic biomass as a substrate in agricultural biogas plants is very popular and yields good results. However, the efficiency of anaerobic digestion, and thus biogas production, is not always satisfactory due to the slow or incomplete degradation (hydrolysis of plant matter. To enhance the solubilization of the lignocellulosic biomass various physical, chemical and biological pretreatment methods are used.The aim of this study was to select and characterize cellulose-degrading bacteria, and to construct a microbial consortium, dedicated for degradation of maize silage and enhancing biogas production from this substrate.Over one hundred strains of cellulose-degrading bacteria were isolated from: sewage sludge, hydrolyzer from an agricultural biogas plant, cattle slurry and manure. After physiological characterization of the isolates, sixteen strains (representatives of Bacillus, Providencia and Ochrobactrum genera were chosen for the construction of a Microbial Consortium with High Cellulolytic Activity, called MCHCA. The selected strains had a high endoglucanase activity (exceeding 0.21 IU/mL CMCase activity and a wide range of tolerance to various physical and chemical conditions. Lab-scale simulation of biogas production using the selected strains for degradation of maize silage was carried out in a two-bioreactor system, similar to those used in agricultural biogas plants.The obtained results showed that the constructed MCHCA consortium is capable of efficient hydrolysis of maize silage, and increases biogas production by even 38%, depending on the inoculum used for methane fermentation. The results in this work indicate that the mesophilic Microbial Consortium with High Cellulolytic Activity has a great potential for application on industrial scale in agricultural biogas plants.

  6. Gas Permeation Processes in Biogas Upgrading: A Short Review

    Kárászová, Magda; Sedláková, Zuzana; Izák, Pavel

    2015-01-01

    Roč. 69, č. 10 (2015), s. 1277-1283. ISSN 0366-6352 R&D Projects: GA MŠk(CZ) LD14094; GA MŠk LH14006; GA ČR GA14-12695S Institutional support: RVO:67985858 Keywords : biogas upgrading * memranes * gas permeation Subject RIV: CI - Industrial Chemistry, Chemical Engineering Impact factor: 1.468, year: 2014

  7. Biogas Production from Sugarcane Waste: Assessment on Kinetic Challenges for Process Designing

    Leandro Janke

    2015-08-01

    Full Text Available Biogas production from sugarcane waste has large potential for energy generation, however, to enable the optimization of the anaerobic digestion (AD process each substrate characteristic should be carefully evaluated. In this study, the kinetic challenges for biogas production from different types of sugarcane waste were assessed. Samples of vinasse, filter cake, bagasse, and straw were analyzed in terms of total and volatile solids, chemical oxygen demand, macronutrients, trace elements, and nutritional value. Biochemical methane potential assays were performed to evaluate the energy potential of the substrates according to different types of sugarcane plants. Methane yields varied considerably (5–181 Nm3·tonFM−1, mainly due to the different substrate characteristics and sugar and/or ethanol production processes. Therefore, for the optimization of AD on a large-scale, continuous stirred-tank reactor with long hydraulic retention times (>35 days should be used for biogas production from bagasse and straw, coupled with pre-treatment process to enhance the degradation of the fibrous carbohydrates. Biomass immobilization systems are recommended in case vinasse is used as substrate, due to its low solid content, while filter cake could complement the biogas production from vinasse during the sugarcane offseason, providing a higher utilization of the biogas system during the entire year.

  8. Biogas Production from Sugarcane Waste: Assessment on Kinetic Challenges for Process Designing.

    Janke, Leandro; Leite, Athaydes; Nikolausz, Marcell; Schmidt, Thomas; Liebetrau, Jan; Nelles, Michael; Stinner, Walter

    2015-01-01

    Biogas production from sugarcane waste has large potential for energy generation, however, to enable the optimization of the anaerobic digestion (AD) process each substrate characteristic should be carefully evaluated. In this study, the kinetic challenges for biogas production from different types of sugarcane waste were assessed. Samples of vinasse, filter cake, bagasse, and straw were analyzed in terms of total and volatile solids, chemical oxygen demand, macronutrients, trace elements, and nutritional value. Biochemical methane potential assays were performed to evaluate the energy potential of the substrates according to different types of sugarcane plants. Methane yields varied considerably (5-181 Nm³·tonFM(-1)), mainly due to the different substrate characteristics and sugar and/or ethanol production processes. Therefore, for the optimization of AD on a large-scale, continuous stirred-tank reactor with long hydraulic retention times (>35 days) should be used for biogas production from bagasse and straw, coupled with pre-treatment process to enhance the degradation of the fibrous carbohydrates. Biomass immobilization systems are recommended in case vinasse is used as substrate, due to its low solid content, while filter cake could complement the biogas production from vinasse during the sugarcane offseason, providing a higher utilization of the biogas system during the entire year. PMID:26404248

  9. Microbial Consortium with High Cellulolytic Activity (MCHCA) for Enhanced Biogas Production

    Poszytek, Krzysztof; Ciezkowska, Martyna; Sklodowska, Aleksandra; Drewniak, Lukasz

    2016-01-01

    The use of lignocellulosic biomass as a substrate in agricultural biogas plants is very popular and yields good results. However, the efficiency of anaerobic digestion, and thus biogas production, is not always satisfactory due to the slow or incomplete degradation (hydrolysis) of plant matter. To enhance the solubilization of the lignocellulosic biomass various physical, chemical and biological pretreatment methods are used. The aim of this study was to select and characterize cellulose-degrading bacteria, and to construct a microbial consortium, dedicated for degradation of maize silage and enhancing biogas production from this substrate. Over 100 strains of cellulose-degrading bacteria were isolated from: sewage sludge, hydrolyzer from an agricultural biogas plant, cattle slurry and manure. After physiological characterization of the isolates, 16 strains (representatives of Bacillus, Providencia, and Ochrobactrum genera) were chosen for the construction of a Microbial Consortium with High Cellulolytic Activity, called MCHCA. The selected strains had a high endoglucanase activity (exceeding 0.21 IU/mL CMCase activity) and a wide range of tolerance to various physical and chemical conditions. Lab-scale simulation of biogas production using the selected strains for degradation of maize silage was carried out in a two-bioreactor system, similar to those used in agricultural biogas plants. The obtained results showed that the constructed MCHCA consortium is capable of efficient hydrolysis of maize silage, and increases biogas production by even 38%, depending on the inoculum used for methane fermentation. The results in this work indicate that the mesophilic MCHCA has a great potential for application on industrial scale in agricultural biogas plants. PMID:27014244

  10. Near-infrared spectroscopic online monitoring of process stability in biogas plants

    Stockl, Andrea; Oechsner, Hans [State Institute of Agricultural Engineering and Bioenergy, University of Hohenheim, Stuttgart (Germany)

    2012-06-15

    The conditions laid down in the Renewable Energy Source Act for production of electricity from biogas have led to an enormous expansion of new biogas plants in the recent years in Germany. Through near-infrared reflection spectroscopy (NIRS) process stability of a biogas digester can be monitored online. This study presents the development of NIRS calibrations on acetic acid equivalents, acetic acid, and propionic acid concentrations in the digester substrate. Thereby, differences between thermophilic and mesophilic operations were measured and presented for the first time. Good calibration models were achieved by artificially increasing concentrations of the above-mentioned acids in two 400 L experimental biogas digesters with mesophilic and thermophilic operation and applying support vector regression. The presented values demonstrate that calibration with NIRS is possible. In the thermophilic digester, a calibration model with a ratio of standard deviation and standard error of prediction (RPD) value of 3.21 was achieved for the parameter acetic acid and in the mesophilic digester a RPD of 4.91 for the same acid. For the parameter propionic acid, calibration models with RPD values of 4.23 and 4.78 were achieved for the thermophilic- and mesophilic-operated digesters, respectively. The presented NIRS calibration can be used to develop an early warning system for process stability, which can be used for reliable optimization of biogas production to increase the methane yield. (copyright 2012 WILEY-VCH Verlag GmbH 8 Co. KGaA, Weinheim)

  11. Investigation of Phasic Process of Biogas Yield by Measuring pH, ORP and Electrical Power Changes

    Mohammad Ali Abdoli

    2016-04-01

    Full Text Available Background & Aims of the Study: Studying the phasic process of the biogas yieldis required to optimize the design and operations; it also helps to lower energy production costs by decreasing the capital investment and operational costs. Here we determine the biogas process by measuring pH, ORP, electrical power and make compatibility to the biogas production trend. Materials and Methods: In this research, one 1150 ml single chamber reactor is used. Biogas production trend was precisely followed by a probable compatibleness with pH, Oxidation Reduction Potential (ORP, electrical Power at a temperature of 37+ 0.5˚C with the substrate of cattle manure. The experiment was followed for 120 days approximately. Results: As a result, the phases of biogas yield could be determined by the measuring of pH, ORP and its compatibility to gas production. In the reactor, hydrolytic, acetogenic and methanogenic phases were occurred in the days 1-7, 8-16 and 17-104, respectively. Also the electrical power at first showed to be produced at high range but by increasing, the production of biogas decreased and then by decreasing the biogas production gradually, it increased slightly. Conclusion: Our results indicated that the phases of biogas production can be separated  completely and by diffracting the phases, the efficiency of biogas production could be increased.

  12. Preparing investigations for determining the mechanism in the desulfurization of biogas with a biologic laundry process; Vorbereitende Untersuchungen zur Ermittlung der Mechanismen in der Entschwefelung von Biogas mit einem biologischen Waschverfahren

    Genzowsky, Kristoffer

    2010-05-15

    The author of the contribution under consideration examines an innovative desulfurization process of biogas from agricultural biogas plants. For this purpose, an existing pilot plant was operated at a 200-L experimental biogas digester. It is used to record and classify physical and biological processes in the desulfurization process. The degradation efficiency of the biological desulfurization process is determined. Recommendations for an optimized pilot plant will be given.

  13. Process flow model of solid oxide fuel cell system supplied with sewage biogas

    Van herle, Jan; Favrat, Daniel; Maréchal, François; Bucheli, Olivier; Leuenberger, Sacha; Membrez, Yves

    2004-01-01

    A model for a 1000 kW class solid oxide fuel cell (SOFC) system running on biogas from a sewage sludge digestion plant was implemented in a process flow scheme using external steam reforming. The model stack consisted of planar anode supported cells operated at 800 degreesC displaying state-of- the-art electrochemical performance (0.15 W/cm(2) at 80% fuel utilisation). Real annual data from an existing sewage plant were used as input to the model. From the input of 43 m(3)/h biogas (63% ...

  14. Monitoring and control of the biogas process based on propionate concentration using online VFA measurement

    Boe, Kanokwan; Steyer, J.P.; Angelidaki, Irini

    2008-01-01

    Simple logic control algorithms were tested for automatic control of a lab-scale CSTR manure digester. Using an online VFA monitoring system, propionate concentration in the reactor was used as parameter for control of the biogas process. The propionate concentration was kept below a threshold of...... stress under gradual overload and thus recommended as an alarm in the control algorithm....

  15. Factors affecting process temperature and biogas production in small-scale rural biogas digesters in winter in northern Vietnam

    Cuong, Pham Hung; Vu, C.C.; Sommer, Sven G.;

    2014-01-01

    and 180 cm, biogas production and methane (CH4) concentration in biogas from August to February. In parallel the temperature of the air (100 cm above ground), in the slurry mixing tank and in the soil (10, 100, 140, and 180 cm depth) was measured by thermocouple. The influent amount was measured daily...... and the influent chemical composition was measured monthly during the whole experimental period. Seasonal variations in air temperature significantly affected the temperature in the soil, mixing tank and digester. Consequently, biogas production, which is temperature dependent, was influenced by the...... season. The main factors determining the internal temperature in the digesters were insulation with Styrofoam, air temperature and temperature of slurry in the mixing tank. Biogas production is low due to the cold climate conditions in winter in Northern Vietnam, but the study proved that storing slurry...

  16. Biogas from ley crops

    This report describes the cost of producing biogas from energy crops. Five process systems, sized 0.25-8 MW are studied. The cultivation of biogas-crops is made in three regions in Sweden. Also valued are the positive cultivation effects obtained when cereal dominated crop rotation is broken by biogas crops. 8 refs, 40 figs, 10 tabs

  17. Decomposition of biogas residues in soil and their effects on microbial growth kinetics and enzyme activities

    The rapid development of biogas production will result in increased use of biogas residues as organic fertilizers. However, control of microbial activity by organic fertilizers remains a challenge for modern land use, especially with respect to mitigating greenhouse effects and increasing C sequestration in soil. To address this issue, we compared CO2 emissions, microbial growth and extracellular enzyme activities in agricultural soil amended with biogas residues (BGR) versus maize straw (MST). Over a 21 day incubation period, 6.4% of organic C added was mineralised and evolved as CO2 with BGR and 30% with MST. As shown by the substrate-induced growth respiration approach, BGR and MST significantly decreased the specific microbial growth rate (μ) and increased the microbial biomass C in the soil, indicating a clear shift in the microbial community to slower-growing microorganisms. Because of the reduced availability of C associated with the less labile C and more lignin in biogas residues, observed μ values and microbial biomass C were lower after BGR application than after MST application. After 21 days incubation, BGR had no effect on the activity of three extracellular enzymes: β-glucosidase and cellobiohydrolase, both of which are involved in cellulose decomposition; and xylanase, which is involved in hemicellulose decomposition. In contrast, MST significantly increased the activity of these three enzymes. The application of biogas residues in short-term experiment leads to a 34% increase in soil C content and slower C turnover as compared to common maize residues. -- Highlights: ► Biogas residues (BGR) applied to soil as organic fertilizers were decomposed 2.5 times slower as compared to maize straw. ► BGR application stimulated mainly slow-growing soil microorganisms. ► In contrast to maize straw the BGR did not increase the activity of cellulose-degrading soil enzymes. ► BGR leads to slower C turnover and a 34% increase in C sequestration versus

  18. Enhancing the hydrolysis process of a two-stage biogas technology for the organic fraction of municipal solid waste

    Nasir, Zeeshan; Uellendahl, Hinrich

    2015-01-01

    The Danish company Solum A/S has developed a two-stage dry anaerobic digestion process labelled AIKAN® for the biological conversion of the organic fraction of municipal solid waste (OFMSW) into biogas and compost. In the AIKAN® process design the methanogenic (2nd) stage is separated from...... the hydrolytic (1st) stage, which enables pump-free feeding of the waste into the 1st stage (processing module), and eliminates the risk for blocking of pumps and pipes by pumping only the percolate from the 1st stage into the 2nd stage (biogas reactor tank). The biogas yield of the AIKAN® two-stage process...... stage showed high efficiency. The current project investigates how the efficiency of the hydrolytic process in the first stage can be enhanced to achieve a higher overall biogas yield by the following means: •The influence of the process conditions in the processing module (temperature, pH, retention...

  19. Regulation and optimization of the biogas process: Propionate as a key parameter

    Bangsø Nielsen, Henrik; Uellendahl, Hinrich; Ahring, Birgitte Kiær

    2007-01-01

    The use of volatile fatty acids (VFA) as process indicators in biogas reactors treating manure together with industrial waste was studied. At a full-scale biogas plant, an online VFA sensor was installed in order to study VFA dynamics during stable and unstable operation. During stable operation...... describe the normalizing of the process. In a lab-scale continuously stirred tank reactor experiment, with manure as main substrate, the prospective of using either propionate concentration or methane production as single process indicators was studied. Propionate was found to be the best indicator. Thus......, a process breakdown caused by organic overloading with meat and bone meal and lipids was indicated by changes in propionate concentration 12-18 days before a decrease in methane production was observed. Furthermore, a more efficient and stable utilization of the substrate was observed when...

  20. Biogas production and methanogenic archaeal community in mesophilic and thermophilic anaerobic co-digestion processes.

    Yu, D; Kurola, J M; Lähde, K; Kymäläinen, M; Sinkkonen, A; Romantschuk, M

    2014-10-01

    Over 258 Mt of solid waste are generated annually in Europe, a large fraction of which is biowaste. Sewage sludge is another major waste fraction. In this study, biowaste and sewage sludge were co-digested in an anaerobic digestion reactor (30% and 70% of total wet weight, respectively). The purpose was to investigate the biogas production and methanogenic archaeal community composition in the anaerobic digestion reactor under meso- (35-37 °C) and thermophilic (55-57 °C) processes and an increasing organic loading rate (OLR, 1-10 kg VS m(-3) d(-1)), and also to find a feasible compromise between waste treatment capacity and biogas production without causing process instability. In summary, more biogas was produced with all OLRs by the thermophilic process. Both processes showed a limited diversity of the methanogenic archaeal community which was dominated by Methanobacteriales and Methanosarcinales (e.g. Methanosarcina) in both meso- and thermophilic processes. Methanothermobacter was detected as an additional dominant genus in the thermophilic process. In addition to operating temperatures, the OLRs, the acetate concentration, and the presence of key substrates like propionate also affected the methanogenic archaeal community composition. A bacterial cell count 6.25 times higher than archaeal cell count was observed throughout the thermophilic process, while the cell count ratio varied between 0.2 and 8.5 in the mesophilic process. This suggests that the thermophilic process is more stable, but also that the relative abundance between bacteria and archaea can vary without seriously affecting biogas production. PMID:24837280

  1. ZnCl2-activated biochar from biogas residue facilitates aqueous As(III) removal

    Xia, Dong; Tan, Fen; Zhang, Chuanpan; Jiang, Xiuli; Chen, Zheng; Li, Heng; Zheng, Yanmei; Li, Qingbiao; Wang, Yuanpeng

    2016-07-01

    Biochars prepared from biogas residue using different chemical activators were investigated for their As(III) adsorption properties. The results indicated that the original biochars did not exhibit significant As(III) adsorption. However, ZnCl2-activated biochar, which possessed the largest specific surface area, 516.67 cm2/g, and exhibited a perfectly porous texture, showed excellent performance in a 500 μgL-1 solution of As(III). Fourier transform infrared spectroscopy (FT-IR) and X-ray photoelectron spectroscopy were utilized to identify the mechanism of As(III) adsorption by ZnCl2-activated biochar. Adsorption was found to occur mainly through ligand exchange of the hydroxyl in Zn-OH to form Zn-O-As(III), as well as through porous adsorption. As a low-cost adsorbent, the adsorption process was well fitted using a pseudo-second-order model, with an R2 > 0.993. The adsorption process was fast, requiring nearly 90 min to reach adsorption equilibrium. Batch adsorption experimental results indicated that ZnCl2-activated biochar has a maximum adsorption capacity of 27.67 mg/g at pH 7.0, and the adsorption process followed the Freundlich isotherm model well, with an R2 > 0.994. In addition, the current work demonstrated the efficiency of using ZnCl2-activated biochar adsorbent to treat As(III)-contaminated water.

  2. Investigation of the effects of co-digesting of biodegradable waste and swine manure on the biogas process

    Ojong, Pascal

    2011-01-01

    Biomass and biomass-derived waste are important renewable energy sources which plays a vital role in greenhouse gas reduction from fossil fuel.  Biomass can be degraded in a process known as anaerobic digestion (AD) to produce biogas. Biogas is a mixture of methane and carbon dioxide which is utilized as a renewable source of energy. This project was based on the investigation of AD process in Nordvästra Skånes Renhållnings AB (NSR) a biogas facility in Helsingborg Sweden. A lab simulation of...

  3. Evaluation of silage-fed biogas process performance using microbiological and kinetic methods

    Jarvis, Aa.

    1996-10-01

    In this study, different kinetic and microbiological methods were used to evaluate the growth and activity of key groups of bacteria degrading ley silage in one-phase and two-phase biogas processes. Emphasis was placed on studying the dynamic behaviour of different trophic groups resulting from the initiation of liquid recirculation in the processes. The microbiological methods included microscopy and most probable number (MPN) counts with different substrates. The kinetic methods included measurements of specific methanogenic activity (SMA) with acetate and H{sub 2}/CO{sub 2} as substrates, batch assays with trace element additions and measurement of conversion rates of mannitol and lactate in the digesters. In general, the initiation of liquid recirculation at first promoted the growth and/or activity of several trophic groups of bacteria, such as butyrate and propionate degraders and acetotrophic and hydrogenotrophic methanogens in the liquefaction/acidogenesis reactors of the two-phase processes. This was probably mainly due to the increased pH. However, after some time of liquid recirculation, an inhibition of some bacterial groups occurred, such as propionate degraders and methanogens in the methanogenic reactors of two-phase processes. This was probably due to increased concentrations of salts and free ammonia. The batch assays proved to be valuable tools in process optimization by the addition of trace elements. Here, the addition of cobalt significantly increased methane production from acetate. In this study, a more comprehensive understanding of the process behaviour in response to the initiation of liquid recirculation was achieved which could not have been obtained by only monitoring routine parameters such as pH, methane production and concentrations of organic acids and salts. 120 refs, 4 figs, 1 tab

  4. Mathematic modelling of anaerobic degradation processes in biogas plants; Mathematische Modellierung der anaeroben Abbauprozesse in Biogasanlagen

    Weinrich, Soeren [Rostock Univ. (Germany). Agrar- und Umweltwissenschaftliche Fakultaet; Mauky, Eric [DBFZ - Deutsches BiomasseForschungsZentrum gGmbH, Leipzig (Germany). Fachbereich Biochemische Konversion; Nelles, Michael

    2011-07-01

    In view of the ongoing political discussion on the enhanced utilization of renewable energy sources biogas technologies continue to gain significance. To develop economic plant concepts and guaranty high energy efficiency the knowledge of the dynamic degradation of various substrates at different operating conditions are of crucial importance. Within the field of modelling the dynamic changes in concentration of substantial components (mass balance) are commonly described by known physical laws or empirical observations. On the basis of a dynamic process model by the German Biomass Research Centre (DBFZ) the main functional principles and capabilities of a simulation of a real biogas plant are described exemplarily. Besides the choice of appropriate kinetic and stoichiometric parameters the model output depends significantly on the quality of the (measured) input variables. Thus the implementation of continuous accurate data logging and the development of important process parameters are also major research topics for modelling and parameter identification of the anaerobic digestion process. (orig.)

  5. Learning as the Construction and Re-Mediation of Activity Systems: Environmental Management in Biogas Production

    Pereira Querol, Marco A.; Suutari, Timo; Seppanen, Laura

    2010-01-01

    The purpose of this paper is to present theoretical tools for understanding the dynamics of change and learning during the emergence and development of environmental management activities. The methodology consists of a historical analysis of a case of biogas production that took place in the Southwest region of Finland. The theoretical tools used…

  6. Supplying the energy demand in the chicken meat processing poultry with biogas

    A. H. Ferrarez

    2016-04-01

    Full Text Available The main use of electrical energy in the chicken meat processing unit is refrigeration. About 70% of the electricity is consumed in the compressors for the refrigeration system. Through this study, the energetic viability of using biogas from poultry litter in supplying the demand for the refrigeration process was found. The meat processing unit studied has the potential to process about a hundred and sixty thousand chickens a day. The potential biogas production from poultry litter is 60,754,298.91 m3.year-1. There will be a surplus of approximately 8,103MWh per month of electric energy generated from biogas. An economic analysis was performed considering a planning horizon of 20 years and the discount rate of 12% per year. The economic analysis was performed considering scenario 1: sale of all electricity generated by the thermoelectric facility, and scenario 2: sale of the surplus electricity generated after complying with the demands of the refrigeration process and all other electrical energy and thermal energy use. Economic indicators obtained for scenarios 1 and 2 were favorable for the project implementation.

  7. Supplying the energy demand in the chicken meat processing poultry with biogas

    Adriano Henrique Ferrarez

    2016-04-01

    Full Text Available The main use of electrical energy in the chicken meat processing unit is refrigeration. About 70% of the electricity is consumed in the compressors for the refrigeration system. Through this study, the energetic viability of using biogas from poultry litter in supplying the demand for the refrigeration process was found. The meat processing unit studied has the potential to process about a hundred and sixty thousand chickens a day. The potential biogas production from poultry litter is 60,754,298.91 m3.year-1. There will be a surplus of approximately 8,103MWh per month of electric energy generated from biogas. An economic analysis was performed considering a planning horizon of 20 years and the discount rate of 12% per year. The economic analysis was performed considering scenario 1: sale of all electricity generated by the thermoelectric facility, and scenario 2: sale of the surplus electricity generated after complying with the demands of the refrigeration process and all other electrical energy and thermal energy use. Economic indicators obtained for scenarios 1 and 2 were favorable for the project implementation.

  8. Profiling of the metabolically active community from a production-scale biogas plant by means of high-throughput metatranscriptome sequencing

    Zakrzewski, Martha; Goesmann, Alexander; Jaenicke, Sebastian;

    2012-01-01

    Structural composition and gene content of a biogas-producing microbial community from a production-scale biogas plant fed with renewable primary products was recently analyzed by means of a metagenome sequencing approach. To determine the transcriptionally active part of the same biogas communit...

  9. An Analysis of Biogas Reforming Process on Ni/YSZ and Ni/SDC Catalysts

    Janusz Szmyd

    2012-02-01

    Full Text Available The conversion of biogas to electricity presents an attractive niche application for fuel cells. Thus attempts have been made to use biogas as a fuel for high temperature fuel cell systems such as SOFC. Biogas can be converted to hydrogen-rich fuel in a reforming process. For hydrocarbon-based fuel, three types of fuel conversion can be considered in reforming reactions: an external reforming system, an indirect internal reforming system and a direct internal reforming system. High-temperature SOFC eliminates the need for an expensive external reforming system. The possibility of using internal reforming is one of the characteristics of high temperature fuel cells like SOFC. However, for high-temperature operation, thermal management of the SOFC system becomes an important issue. To properly carry out thermal management, both detailed modeling and numerical analyses of the phenomena occurring inside the SOFC system is required. In the present work, the process of reforming biogas on a Ni/YSZ and a Ni/SDC catalyst has been numerically and experimentally investigated. Measurements including different thermal boundary conditions, steam-to-carbon ratios and several different fuel compositions were taken. A numerical model containing methane/steam reforming reaction, dry reforming reaction and shift reaction has been proposed to predict the gas mixture composition at the outlet of the reformer. The results of the numerical computation were compared with experimental data and good agreement has been found. The results indicate the importance of combined, numerical and experimental studies in the design of SOFC reformers. The combined approach used leads to the successful prediction of the outlet gas composition for different modelling conditions.

  10. Biogas Tinja Manusia dalam Perspektif Fiqih-Kimia

    Wawan Juandi Muhyiddin Khatib Ummi Khoiriyah

    2014-01-01

    Energy is one of the most important factors to global prosperity. The dependence on fossil fuels as primary energy source has led to global climate change, environmental degradation, and human health problems. In order to reduce dependence on commercial energy, steps have been taken to develop an alternative source, such as biogas. Biogas was a gas produced from biological activities in anaerobic fermentation processes and as a renewable energy. Biogas is one form of the alternative energy. I...

  11. Process flow model of solid oxide fuel cell system supplied with sewage biogas

    Van herle, J.; Maréchal, F.; Leuenberger, S.; Membrez, Y.; Bucheli, O.; Favrat, D.

    A model for a 100 kW class solid oxide fuel cell (SOFC) system running on biogas from a sewage sludge digestion plant was implemented in a process flow scheme using external steam reforming. The model stack consisted of planar anode supported cells operated at 800 °C displaying state-of-the-art electrochemical performance (0.15 W/cm 2 at 80% fuel utilisation). Real annual data from an existing sewage plant were used as input to the model. From the input of 43 m 3/h biogas (63% CH 4), equivalent to 269 kW (higher heating value, HHV), the SOFC stack was calculated to deliver 131 kW el electricity (48.7%) using a steam-to-carbon ratio of 0.5. This would allow the sewage site to more than cover its own electrical needs, hence to depollute the waste stream at negative energy cost. In its current exploitation using a low efficient gas engine (130 kW), the site is only ≈50% self-sufficient. Special attention was given to the thermal balance of the stack. The stack developed heat (143 kW) could be balanced by endothermal reforming (78 kW) and by cathode excess air λ (=3), allowing a temperature difference between stack inlet and outlet of 200 K. The case was compared to other fuel scenarios. Steam-added biogas behaves basically identically to steam-reformed methane. For partial oxidation of biogas or pure hydrogen feeding, electrical efficiency drops to under 43% while λ needs to be raised to 4.5 to maintain the 200 K thermal gradient over the stack.

  12. New steady-state microbial community compositions and process performances in biogas reactors induced by temperature disturbances

    Luo, Gang; De Francisci, Davide; Kougias, Panagiotis;

    2015-01-01

    . Although three different temperature disturbances were applied to each biogas reactor, the increased methane yields (around 10% higher) and decreased volatile fatty acids (VFAs) concentrations at steady state were found in all three reactors after the temperature disturbances. After the temperature......Background The microbial community in a biogas reactor greatly influences the process performance. However, only the effects of deterministic factors (such as temperature and hydraulic retention time (HRT)) on the microbial community and performance have been investigated in biogas reactors. Little...... is known about the manner in which stochastic factors (for example, stochastic birth, death, colonization, and extinction) and disturbance affect the stable-state microbial community and reactor performances. Results In the present study, three replicate biogas reactors treating cattle manure were...

  13. Enhanced biogas recovery by applying post-digestion in large-scale centralized biogas plants

    Angelidaki, Irini; Hejnfelt, Anette; Ellegaard, L.

    2006-01-01

    The main objective of this study was to investigate the degradation efficiency of centralized biogas plants and provide guidance for the design of more efficient digester and post-digestion systems. These centralized biogas plants in Denmark digest manure together with organic waste from the food...... industry to generate biogas, which is used for electricity and thermal energy. A total of 20 such plants are currently active in Denmark, most of which were included in the investigation. From the plants, samples were obtained from various steps of the process. Samples were analysed and the residual biogas...... potential determined by batch post-digestion at various temperature levels. Results were correlated with plant characteristics and production statistics in order to judge the efficiency of various digestion concepts. A simplified model based on a two-step biogas production process was developed...

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

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

    2016-02-01

    Compression and upgrading of biogas to vehicle fuel generates process water, which to varying degrees contains volatile organic compounds (VOCs) originating from the biogas. The compostion of this process water has not yet been studied and scientifically published and there is currently an uncertainty regarding content of VOCs and how the process water should be managed to minimise the impact on health and the environment. The aim of the study was to give an overview about general levels of VOCs in the process water. Characterisation of process water from amine and water scrubbers at plants digesting waste, sewage sludge or agricultural residues showed that both the average concentration and composition of particular VOCs varied depending on the substrate used at the biogas plant, but the divergence was high and the differences for total concentrations from the different substrate groups were only significant for samples from plants using waste compared to residues from agriculture. The characterisation also showed that the content of VOCs varied greatly between different sampling points for same main substrate and between sampling occasions at the same sampling point, indicating that site-specific conditions are important for the results which also indicates that a number of analyses at different times are required in order to make an more exact characterisation with low uncertainty. Inhibition of VOCs in the anaerobic digestion (AD) process was studied in biomethane potential tests, but no inhibition was observed during addition of synthetic process water at concentrations of 11.6 mg and 238 mg VOC/L. PMID:26694791

  15. BIOGAS TECHNOLOGY

    D.B. SALUNKHE

    2012-12-01

    Full Text Available Due to scarcity of petroleum and coal it threatens supply of fuel throughout the world also problem of their combustion leads to research in different corners to get access the new sources of energy, like renewable energy resources. Solar energy, wind energy, different thermal and hydro sources of energy, biogas are all renewable energy resources. But, biogas is distinct from other renewable energies because of its characteristics of using, controlling and collecting organic wastes and at the same time producing fertilizer and water for use in agricultural irrigation. Biogas does not have any geographical limitations nor does it require advanced technology for producing energy, also it is very simple to use and apply. Anaerobic digestion is controlled biological degradation process which allows efficient capturing & utilization of biogas (approximately 60% methane and 40% carbon dioxide for energy generation. Anaerobic digestion of food waste is achievable but different types, composition of food waste results in varying degrees of methane yields, and thus the effects of mixing various types of food waste and their proportions should be determined on case by case basis.

  16. Microbiologic handbook for biogas plants; Mikrobiologisk handbok foer biogasanlaeggningar

    Jarvis, Aasa; Schnuerer, Anna

    2009-05-15

    There is today great interest in the biogas process. The reason for interest is that this process offers an opportunity to stabilize and reduce various types of organic waste, while also generating clean renewable energy in the form of biogas. Purified biogas is a good alternative to gasoline and diesel as motor fuel and can also be used for heating and electricity production. Behind efficient biogas production lies a complex microbiological process. For biogas to be formed many different species of microorganisms have to be active. A disturbance of this teamwork leads to a reduction in biogas production or in the worst case that the process stops. In order to operate a biogas process in an efficient manner, it is necessary to have knowledge of the underlying microbiology and how microorganisms function. Today Swedish biogas plants have personnel with great technical knowledge, while the biological knowledge often is more limited. It has been difficult to find appropriate Swedish language literature in the field. This handbook aims to increase the microbiological expertise of staff at the biogas plants and thus to facilitate the stable operation and optimization of gas production

  17. Biogas charging and dissipating process and its accumulation in the Sebei gasfield,Qaidam Basin,China

    2008-01-01

    The Sebei gasfield is the largest biogas accumulation found in China and many reservoirs and seal rocks superposed on a syndepositional anticline in Quaternary.The biogas charging and dissipating process and its distribution have been a research focus for many years.The authors suggest a diffusing and accumulating model for the biogas,as they find that the shallower the gas producer,the more methane in the biogas,and the lighter stable carbon isotope composition of methane.Based on the diffusing model,diffused biogas is quantitatively estimated for each potential sandy reservoir in the gasfield,and the gas charging quantity for the sandy reservoir is also calculated by the diffused gas quantity plus gas reserve in-place.A ratio of diffusing quantity to charging quantity is postulated to describe biogas accumulating state in a sandy reservoir,if the ratio is less than 0.6,the reservoir forms a good gas-pool and high-production layer in the gasfield,which often occurs in the reservoirs deeper than 900 m;if the ratio is greater than 0.6,a few gas accumulated in the reservoir,which frequently exists in the reservoirs shallower than 900 m.Therefore,a biogas accumulation model is built up as lateral direct charging from gas source for the sands deeper than 900 m and indirect charging from lower gas-bearing sands by diffusion at depth shallower than 900 m.With this charging and diffusion quantitative model,the authors conducted re-evaluation on each wildcat in the central area of the Qaidam Basin,and found many commercial biogas layers.

  18. INCREASING ADSORPTION OF ACTIVATED CARBON FROM PALM OIL SHELL FOR ADSORB H2S FROM BIOGAS PRODUCTION BY IMPREGNATION

    Wasan Phooratsamee

    2014-01-01

    Full Text Available Biogas is the combustible gas produced through a biological process, known as anaerobic digestion which is the process operated at low-temperature and without air. Biogas consists of 55-80% CH4, 20-45% CO2 with trace amount of H2S and other impurities. Common H2S removal technologies from biogas fall into one of adsorption on a solid such as iron oxide based materials, activated carbon or impregnated activated carbon. Conventionally, activated carbon is produced from biomass residues and agricultural residues such as palm oil shell which promising approach for the production of cheap. It is so due to the palm oil shell carries a large amount of carbon content which it is the main composition of activated carbon. Therefore, it is usable as raw material for producing impregnated activated carbon and used as adsorbents. The aim of this study is a produce the activated carbon from palm oil shells by chemical activation using ZnCl2 and optimal conditions after impregnated them with NaOH, KI and K2CO3 for H2S absorption from biogas product. In this research, production of activated carbon involved three stages; (i carbonization of raw material in an inert atmosphere which was carbonized in a muffle furnace at 600°C for 1 h; (ii secondly activation of char product from the first stages at fixed bed reactor (stainless steel with 54.1 mm internal diameter and 320 mm length which was studied to observe the effect of char product: Chemical agent ratio (ZnCl2, 1:1 to 1:3, which there are activated at 700°C activation temperature for 2 h; and (iii finally alkali impregnated activated carbon which were immersed 1:3 ratio in 500 mL of 1 N NaOH, KI and K2CO3 solutions and stirred for 30 min. The result showed that the surface area and the pore volume increased progressively with increasing the char product: Chemical agent ratio. The maximum

  19. Energy recovering and biogas

    In spite of the advantages of the methanation and the biogas valorization, the France is one of the european countries where these energy recovery techniques have less developed. Liquid industrial effluents, sewage sludges, waste waters, oils or vinification residues can be processed to produce biogas. In this innovative context biogas combustion installations will have to anticipate the regulations on CO2 emissions. (A.L.B.)

  20. Methanogenesis in Thermophilic Biogas Reactors

    Ahring, Birgitte Kiær

    1995-01-01

    Methanogenesis in thermophilic biogas reactors fed with different wastes is examined. The specific methanogenic activity with acetate or hydrogen as substrate reflected the organic loading of the specific reactor examined. Increasing the loading of thermophilic reactors stabilized the process...... as indicated by a lower concentration of volatile fatty acids in the effluent from the reactors. The specific methanogenic activity in a thermophilic pilot-plant biogas reactor fed with a mixture of cow and pig manure reflected the stability of the reactor. The numbers of methanogens counted by the most...... against Methanothrix soehngenii or Methanothrix CALS-I in any of the thermophilic biogas reactors examined. Studies using 2-14C-labeled acetate showed that at high concentrations (more than approx. 1 mM) acetate was metabolized via the aceticlastic pathway, transforming the methyl-group of acetate...

  1. Optimization of the digestion process of Scenedesmus sp. and Opuntia maxima for biogas production

    Highlights: • Scenedesmus biomass showed low biodegradability and biogas production. • Methane yield and kinetics of the batch process were improved by co-digestion. • Scenedesmus and Opuntia maxima were successfully co-digested in CSTR. • High biogas yields were obtained and no inhibition by ammonia was observed. - Abstract: Scenedesmus biomass is not an adequate substrate for anaerobic digestion due to its low biodegradability and low biogas yield. This study aims to evaluate the anaerobic co-digestion of Scenedesmus microalgal biomass and Opuntia maxima cladodes, the latter added in order to improve the digestion process. Batch assays were conducted to evaluate possible synergistic effects in different mixtures of both substrates. Mixture with highest methane yield was digested in semi-continuous mode at different VS concentrations. Feedstock composed of 75% O.maxima and 25% Scenedesmus (VS basis) showed the highest methane yield increasing 66.4% and 63.9% that of Scenedesmus and O.maxima, respectively. In semi-continuous mode, ideal organic loading rate (OLR) with 6%VS feed concentration was 4 gVS L−1 d−1, which yielded 292 ± 39 LCH4 kgVS−1 (15 days HRT). In the case of 8%VS feed concentration ideal OLR was 5.33 gVS L−1 d−1, which yielded 308 ± 22 LCH4 kgVS−1 (15 days HRT). The co-digestion of O.maxima and Scenedesmus biomass enhanced the anaerobic digestion process and avoided inhibition caused by low C/N ratio of microalgae

  2. Biogas production from mono-digestion of maize silage-long-term process stability and requirements.

    Lebuhn, M; Liu, F; Heuwinkel, H; Gronauer, A

    2008-01-01

    Biogas production from mono-digestion of maize silage was studied for more than one year in six continuously stirred, daily fed 36 L fermenters. Chemical and microbiological parameters were analysed concomitantly. The reactors acidified already after 8 months of operation at a low organic loading rate (OLR) of 2 g VS*(L*d)(-1). The TVA/TAC ratio was the most reliable parameter to indicate early process instabilities leading to acidification. A TVA/TAC threshold of 0.5 should not be exceeded. After acidification and recovery of the fermenters, propionic acid was no reliable parameter anymore to indicate process failure, since values far below the threshold of 1 g*L(-1) were obtained although the process had collapsed.The acidified reactors recovered better, showed greatly improved stability and allowed a higher OLR when a trace element (TE) cocktail was supplemented. Hydrolysis was obviously not process-limiting, results indicated that methanogens were affected. The most limiting element in long-term mono-digestion of maize silage turned out to be cobalt, but data obtained suggest that molybdenum and selenium should also be provided. TE supplementation should be designed specifically in order to meet the actual needs. TE availability for the biocenosis appears to be a key issue in biogas production, not only in mono-but also in co-digestion processes. PMID:19001720

  3. Terpenes removal from biogas; Terpenenverwijdering uit biogas

    Schulze, P.; Holstein, J.; De Haan, HR.; Vlap, H. [DNV KEMA, Arnhem (Netherlands)

    2013-06-15

    Biogas may contain unwanted and harmful components, including aromatic hydrocarbons such as terpenes. These terpenes (organic oils) are mainly present in citrus peel and plant residues; that is why especially raw biogas from organic waste digestion plants contains high concentrations of terpenes. If terpenes end up in the gas grid (with the injected biomethane) there is a risk that plastics (PE pipes) lose their mechanical properties by absorbing liquids or extracting ethereal plasticizers. This can lead to embrittlement greatly lowering the reliability of the piping. In addition, soft components are als o affected (gaskets and rubber O-rings). Besides the impact on the integrity of the gas grid, terpenes also mask the odor of natural gas odorants such as THT. This impedes the detection of gas leaks which is a significant security risk. Furthermore, the presence of terpenes in biogas leads to fouling of equipment used for the drying of biomethane, as well as contamination of adsorption liquids and membranes used in the upgrading process. Currently, terpenes are removed by activated carbon filters. The tool life of such a filter can be relatively short if terpene concentrations are high in the biogas; this results in a significant increase of the operational costs, due to the replacement of the carbon. This study looked at alternative techniques for removing much of the terpenes from biogas in a simple, efficient and cheap way. In a workshop with stakeholders two techniques were chosen to be tested on laboratory scale in order to demonstrate the proof of principle. These techniques are photo-oxydation and a gas scrubbing. Of all investigated techniques for the removal of limonene the application of UV radiation seems to be the most promising option because of the simplicity of the process, the high efficiency (up to 94%), the comparable operational costs with activated carbon (6.7 to 9.5 euro/kg limonene removed, compared to 10 euro/kg limonene removed for activated

  4. Integrated biogas systems

    Amaratunga, M.

    1980-01-01

    Integrated biogas systems as alternatives to fossil fuels in Sri Lanka are considered from standpoints of population growth, land availability, and employment opportunities. Agricultural practices would be improved by use of chemical fertilizers, and health/nutrition problems be alleviated by using biogas systems. Fuel for cooking and rural industries will become more easily available; water weeds, such as water hyacinth and salvinia which pose a threat to waterways and rice paddy lands could be used for the production of biogas and fertilizers. A concept of an integrated biogas system comprising photosynthesis and anaerobic degradation processes to produce food and energy is presented.

  5. What does the hydrolysis perform in the fermentation of biogas? Biogas, hydrolysis, fermenter biology, multistage process operation; Was kann die Hydrolyse bei der Biogasvergaerung leisten? Biogas, Hydrolyse, Fermenterbiologie, mehrphasige Prozessfuehrung

    Oechsner, H.; Lemmer, A. [Landesanstalt fuer Agrartechnik und Bioenergie, Univ. Hohenheim, Stuttgart (Germany)

    2009-07-01

    Nowadays renewable primary products are normally favored for fermentation in agricultural biogas plants. Since this substrate has to be cultivated for biogas fermentation in particular and hence causes production costs, the energy content of the material should be dissipated in biogas completely. For this the fermentation process has to run as efficient as possible. In case of one-phase process management with high space loading there is a risk of imbalance and maybe even collapse of process biology in the fermenter. In case of high space loading and short retention time the substrate won't be fermented completely. The aim is to create good conditions for microorganism participating in the process by a two-phase process management which integrates a stage of hydrolysis. In the stage of hydrolysis the microorganisms and enzymes metabolize the organic matter into readily biodegradable carbonic acids, which can be supplied targeted in the following methanisation as substrate for methanogenic bacteria. The hydrolysis proceeds under various terms and conditions (aerobic/anaerobic, different pH-value, different temperature level). This necessitates a safe control of operation and process parameters, which is often difficult to ensure in practice. In a malfunctioning hydrolysis also methane can be produced, that causes energy losses and environmental damage when emitted in atmosphere. Hydrogen can be produced in the hydrolysis as well what can involve a safety risk. Urgent need for research exists concerning the two-phase fermentation of renewable primary products. By systematic laboratory analysis the knowledge should be expanded, to improve the planning reliability in this field. (orig.)

  6. Process for increased biogas production and energy efficient hygienisation of sludge; Process foer oekad biogasproduktion och energieffektiv hygienisering av slam

    Rogstrand, Gustav; Olsson, Henrik; Andersson Chan, Anneli; Johansson, Niklas; Edstroem, Mats

    2012-07-01

    In Sweden there is a need to increase biogas production to meet the rising demand for biomethane as vehicle fuel but the amount of domestically available biomass to digest is limited. One way to help meet current and future demand for methane is to enhance the digestion of the substrates that are currently utilized. Vaexjoe municipality in southern Sweden is in the process of upgrading their facilities for biogas production at the Sundet waste water treatment plant. Their aim is to produce more biogas in order to meet the demand from an increasing methane-based local transit fleet. This is the backdrop to a joint project between JTI and Vaexjoe municipality where JTI's mobile pilot plant was used to study the possibility of extracting more biogas from the existing sewage sludge. In the future, Vaexjoe municipality also plans to co-digest source separated municipal organics with the sewage sludge, which will likely result in stricter demands in terms of hygienization of all utilized substrates. The goal of the project at hand was to demonstrate the possibility to produce more than enough additional biogas from existing sewage sludge to yield a net energy profit even with the added energy demand of ensuring the hygienic quality of the digestate through conventional pasteurization. Although the project was focused on the conditions at Sundet waste water treatment plant, the issues dealt with are general and the results are relevant to many waste water treatment plants in Sweden. The research, conducted between June 2011 and January 2012 were divided into two trials. The two trials, described schematically in Figure 1, represented two possible process configurations designed to reach the goal stated above. The key component of both process configurations is the addition of a post-digestion step to the existing single-step digestion process. In trial 1 the additional feature of dewatering between the two digestion steps served to reduce energy demand for

  7. Biogas Production Potential from Waste in Timis County

    Teodor Vintila

    2012-05-01

    Full Text Available This work is a study of biogas production potential using as substrate the residues generated in the agricultural activities and the organic fraction from municipal wastes collected in Timis County. Data available in regional and national statistics have been reported to Timis County and used to calculate the potential quantity of biogas to be produced by anaerobic fermentation using as fermentable substrate residues generated in various human activities. To estimate the electric and thermal energy potential of the biogas, we considered the productivity of an average biogas plant couplet with a CHP unit with an efficiency of 40% net electric and 40% net thermal output and functioning 7500 hours per year. Processing data for the biogas production potential from livestock manure in Romania, we found that over 500 GWh of energy from biogas can be provided in one year. It is estimated that only half of the theoretical energy potential is technically usable by biogas investments. As for the crops residues, has been shown that the theoretical biogas potential is over 2900 GWh/year. Wastewater sludge can be converted in around 1700MWh/year, and the organic wastes available from municipal wastes can provide over 137 GWh/year. Another potential for renewable energy production in Timis County is the arable land uncultivated yearly, which can be used to cultivate energy crops, as raw material for biogas providing over 2800 GWh/year. All this quantity of biogas can be converted in numerous CHP biogas plants totaling an installed power of over 340 MWel. This potential can contribute to reach the target for 2020 in Romania to build biogas plants totaling at least 195 MWel. installed power, with an output of 950 GW electric power. 

  8. An innovative bioelectrochemical-anaerobic digestion-coupled system for in-situ ammonia recovery and biogas enhancement: process performance and microbial ecology

    Zhang, Yifeng; Angelidaki, Irini

    Ammonia (NH4+/NH3) inhibition during anaerobic digestion process is one of the most frequent problems existing in biogas plants, resulting in unstable process and reduced biogas production. In this study, we developed a novel hybrid system, consisted of a submersed microbial resource recovery cell...

  9. Codigestion of manure and industrial organic waste at centralized biogas plants: process imbalances and limitations

    Bangsø Nielsen, Henrik; Angelidaki, Irini

    2008-01-01

    The present study focuses on process imbalances in Danish centralized biogas plants treating manure in combination with industrial waste. Collection of process data from various full-scale plants along with a number of interviews showed that imbalances occur frequently. High concentrations of...... conditions) and high fractions of industrial waste in the feedstock was also observed. The process imbalances and suboptimal conditions are mainly allowed to occur due to 1) inadequate knowledge about the waste composition, 2) inadequate knowledge about the waste degradation characteristics, 3) inadequate...... process surveillance, especially with regard to volatile fatty acids, and 4) insufficient pre-storage capacity causing inexpedient mixing and hindering exact dosing of the different waste products....

  10. Early warning of disturbances in a laboratory-scale MSW biogas process.

    Hansson, M; Nordberg, A; Sundh, I; Mathisen, B

    2002-01-01

    The use of near-infrared spectroscopy (NIR) to monitorthe dynamics of a biogas process was evaluated using multivariate data analysis. The digester was a completely stirred 8 I tank reactor fed with the organic fraction of source-sorted MSW. Intermittently the digester was overloaded with feed. Before and after overload on-line monitoring of NIR spectra and off-line analysis in the liquid and the gas phase of traditional chemical variables and microbial biomass, determined as total concentration of phospholipid fatty acids (PLFA and PLEL), were done. The dynamics that occurred due to overloading could be followed using principal component analysis of the obtained NIR-spectra. In addition, the response to changes in the digester fluid was reproducible and could be detected within five minutes, which can be considered as real-time monitoring. Selected wavelengths in the region 800-2,000 nm were used to make a PLS1 -regression with propionate. The regression resulted in a good correlation for propionate (R= 0.94 and RMSEP of 0.21 g/l in the range of 0.3-3 g/l). The results indicate the possibility to develop an early warning biogas control system based on near-infrared spectroscopy monitoring of propionate. PMID:12188554

  11. Farm Biogas Handbook; Gaardsbiogashandbok

    Christensson, Kjell; Bjoernsson, Lovisa; Dahlgren, Stefan; Eriksson, Peter; Lantz, Mikael; Lindstroem, Johanna; Mickelaaker, Maria

    2009-04-15

    A very large share of the total raw material potential for biogas production will be found within the agriculture. The raw material potential of manure in Sweden amounts to 4 - 6 TWh. Within the agriculture there is moreover a big potential in the form of residues from plant cultivation and non-food crops (approximately 7 TWh) that can to be used for biogas production. The potential for biogas production from only residues and manure is around 8-10 TWh. An increased biogas production within the agriculture would give significant environmental effects. Among other things manure, that today is leaking methane gas to the atmosphere, can be fermented, and trough this process the methane losses will be reduced. When the produced biogas replaces fossil fuel, an overall environmental effect will be reached, that is highly significant. This manual deals with biogas plants for agriculture and such plants that do not have extensive transports of different raw materials, as manure, wastes etc. One of the starting points for this manual's set-up is a course plan that Biogas Syd made for the courses they give to farmers, advisors and others. The manual illustrates important aspects in planning and construction of biogas plants, from raw material and technology to dimensioning of plant, use of biogas and planning of local gas grids. We also think it is important to illustrate the legislation that encompasses construction work and operation of a biogas plant. Investment costs are also illustrated, but the book does not give any extensive economic calculations, since we believe that such calculations need their own manual in the form of calculation examples, based on various conditions. The final section is called 'Biogas on farm - from idea to reality' where the entire process from analysis and pre-planning to monitoring and control of plant during operation is briefly described

  12. Development of a complete bio-NGV production process based on agricultural biogas at farm scale

    Sarperi, Laura

    2014-01-01

    Bio-NGV (bio- Natural Gas for Vehicles) is a bio-fuel based on the biogas in which components such as CO2and H2S are removed. But the economical feasibility of available and commercial technologies to perform these removals is limited to 80 Nm3/h of treated biogas. Regarding farm scale biogas plant, fuel needs of 1 fill-upper day would represent the treatment of only 1 Nm3/hof raw biogas. The aim of our work was to develop a solution economically adapted to farm scale to produce bio-NGV from ...

  13. Analysis of the Value Chain for Biogas in Tanzania Northern Zone (Tanga, Kilimanjaro, Arusha, Manyara)

    Nyagabona, N.T.

    2009-12-15

    This study aimed at exploring weaknesses in the biogas value chain that hinder wider dissemination of the technology in Tanzania. The research included assessment of processes and activities carried out by the players, the influencers and business supporters of the biogas value chain. The methodology used is holistic, combining literature review with focus group discussions and interviews with actors and observations of processes across the value chain in Arusha and Kilimanjaro regions, where biogas has the longest history in Tanzania.

  14. DEVELOPMENT TRENDS OF BIOGAS

    Mariana DUMITRU

    2015-04-01

    Full Text Available All over the world, researches are made in order to improve the technologies, the operational and process stability and performance of biogas plants, because the world markets for biogas increased considerably in Europe and all over the world. In this paper we studied the most important parameters related to a biogas plant, starting from the ecologic landfill of Cristian, Sibiu, a landfill which storages industrial and household waste. In this respect, we studied operational parameters, such as organic load and hydraulic retention time, and parameters for evaluation of a biogas plant. Also, we made a case study concerning the evaluation of used waters in the landfill described above under the aspect of pollution sources, way of treatment and evacuation mode of used waters. The existing biomass resources everywhere in the world can give us an idea of the global potential of biogas production, which is not exploited to its capacity, especially in our country.

  15. Separation of H2S and NH3 gases from tofu waste water-based biogas using activated carbon adsorption

    Harihastuti, Nani; Purwanto, P.; Istadi, I.

    2015-12-01

    Research on the separation of H2S and NH3 gases from tofu waste water-based biogas has been conducted to improve the content of CH4 of biogas in order to increase calorific value. Biogas from tofu waste water contained many kinds of gases such as: CH4 of 53-64%, CO2 of 36-45%, H2S of 3,724-5,880 mg/Nm3, NH3 of 0.19-70.36 mg/Nm3, and H2O of 33,800-19,770,000 mg/Nm3. In fact, CO2, H2S, NH3, and moisture are impurities that have disturbance to human and environment, so that they are necessary to be separated from biogas. Particularly, H2S and NH3 have high toxicity to people, particularly the workers in the tofu industry. Therefore, separation of H2S and NH3 from biogas to increase calorific value is the focus of this research. The method used in this research is by adsorption of H2S and NH3 gases using activated carbon as adsorbent. It also used condensation as pretreatment to remove moisture content in biogas. Biogas was flowed to adsorption column (70 cm height and 9 cm diameter containing activated carbon as much as 500 g) so that the H2S and NH3 gases were adsorbed. This research was conducted by varying flow rate and flow time of biogas. From this experiment, it was found that the optimum adsorption conditions were flow rate of 3.5 l/min and 4 hours flow time. This condition could reach 99.95% adsorption efficiency of H2S from 5,879.50 mg/Nm3 to 0.67 mg/Nm3, and 74.96% adsorption efficiency of NH3 from 2.93 mg/Nm3 to 0.73 mg/Nm3. The concentration of CH4 increased from 63.88% to 76.24% in the biogas.

  16. Use of the Sabatier Process for Dynamic Biogas Upgrading in Northern Germany

    Jurgensen, Lars; Ehimen, Ehiazesebhor Augustine; Born, Jens; Holm-Nielsen, Jens Bo

    Approximately 8000 farm scale biogas plants are present in Germany which produce electricity (mainly using energy crops as substrates) . The potential role of biogas plants in energy systems penetrated by high amounts of fluctuating renewable energy production is discussed in this paper. Today th...... scheme in northernmost four counties of Germany. In these four counties, 529 mostly farm scaled biogas plants could potentially produce up to 100 · 106 m3/a SNG using surplus electricity from wind and solar power generation systems availavble from 1600 h/a.......Approximately 8000 farm scale biogas plants are present in Germany which produce electricity (mainly using energy crops as substrates) . The potential role of biogas plants in energy systems penetrated by high amounts of fluctuating renewable energy production is discussed in this paper. Today the...

  17. Natural attenuation of biogas in landfill covers

    In the risk evaluation of uncontrolled biogas emissions from landfills, the process of natural attenuation in landfill covers assumes a very important role. The capacity of biogas oxidation in the cover soils seems to be the most important control to mitigate the biogas emission during the aftercare period when the biogas collection system might fail. In the present paper laboratory experiences on lab columns to study the biogas oxidation are discussed

  18. Biogas processing procedure in the research and technology; Nachhaltige Entwicklung und Klimaschutz. Ertuechtigung von Biogasanlagen aus Sicht des EEG 2012

    NONE

    2011-07-01

    Within the Hohen Luckow bioenergy workshop at 8th September 2011 in Hohen Luckow (Federal Republic of Germany), the following lectures were held: (1) Sustainability from the view of the amendment of EEG 2012 (H. Ludley); (2) The gas formation rate of culm crops and corn crops in the production of biogas (F. Weissbach); (3) Experiences in the cultivation of sorghum in Germany as well as actual questions on the evaluation of the substrate properties (H.-J. Schleusner); (4) Digestion procedure for the energetic utilization of lignocellulose in the agriculture (D. da Rocha); (5) Practical experiences on the thermo-mechanical digestion with extruder technology (C. Knitter); (6) Biogas processing procedure in the research and technology (G, Mann); (7) Progress report on the supply of biogas into the natural gas distribution system from the view of the producer (R. Boback); (8) Biogas container - mobile plant concept for the decentralized power generation (J. Warncke); (9) Upgrading of biomass conversion plants by means of an optimized management (H. Ludley); (10) The spectrum of fermentation acids as a means for the process control (A. Arndt).

  19. Design and scale-up of an oxidative scrubbing process for the selective removal of hydrogen sulfide from biogas.

    Krischan, J; Makaruk, A; Harasek, M

    2012-05-15

    Reliable and selective removal of hydrogen sulfide (H(2)S) is an essential part of the biogas upgrading procedure in order to obtain a marketable and competitive natural gas substitute for flexible utilization. A promising biogas desulfurization technology has to ensure high separation efficiency regardless of process conditions or H(2)S load without the use or production of toxic or ecologically harmful substances. Alkaline oxidative scrubbing is an interesting alternative to existing desulfurization technologies and is investigated in this work. In experiments on a stirred tank reactor and a continuous scrubbing column in laboratory-scale, H(2)S was absorbed from a gas stream containing large amounts of carbon dioxide (CO(2)) into an aqueous solution prepared from sodium hydroxide (NaOH), sodium bicarbonate (NaHCO(3)) and hydrogen peroxide (H(2)O(2)). The influence of pH, redox potential and solution aging on the absorption efficiency and the consumption of chemicals was investigated. Because of the irreversible oxidation reactions of dissolved H(2)S with H(2)O(2), high H(2)S removal efficiencies were achieved while the CO(2) absorption was kept low. At an existing biogas upgrading plant an industrial-scale pilot scrubber was constructed, which efficiently desulfurizes 180m(3)/h of raw biogas with an average removal efficiency of 97%, even at relatively high and strongly fluctuating H(2)S contents in the crude gas. PMID:22440540

  20. Identical full-scale biogas-lift reactors (Blrs) with anaerobic granular sludge and residual activated sludge for brewery wastewater treatment and kinetic modeling.

    Xu, Fu; Huang, Zhenxing; Miao, Hengfeng; Ren, Hongyan; Zhao, Mingxing; Ruan, Wenquan

    2013-10-01

    Two identical full-scale biogas-lift reactors treating brewery wastewater were inoculated with different types of sludge to compare their operational conditions, sludge characteristics, and kinetic models at a mesophilic temperature. One reactor (R1) started up with anaerobic granular sludge in 12 weeks and obtained a continuously average organic loading rate (OLR) of 7.4 kg chemical oxygen demand (COD)/(m3 x day), COD removal efficiency of 80%, and effluent COD of 450 mg/L. The other reactor (R2) started up with residual activated sludge in 30 weeks and granulation accomplished when the reactor reached an average OLR of 8.3 kg COD/(m3 x day), COD removal efficiency of 90%, and effluent COD of 240 mg/L. Differences in sludge characteristics, biogas compositions, and biogas-lift processes may be accounted for the superior efficiency of the treatment performance of R2 over R1. Grau second-order and modified StoverKincannon models based on influent and effluent concentrations as well as hydraulic retention time were successfully used to develop kinetic parameters of the experimental data with high correlation coefficients (R2 > 0.95), which further showed that R2 had higher treatment performance than R1. These results demonstrated that residual activated sludge could be used effectively instead of anaerobic granular sludge despite the need for a longer time. PMID:24494489

  1. Design and scale-up of an oxidative scrubbing process for the selective removal of hydrogen sulfide from biogas

    Highlights: ► Alkaline oxidative scrubbing proved for biogas desulfurization ► Effect of operating conditions on hydrogen sulfide removal efficiency. ► Minimization of caustic and oxidant consumption. ► Process control via pH, redox potential and conductivity measurement. ► Investigation of long-term behavior of pilot plant operation. - Abstract: Reliable and selective removal of hydrogen sulfide (H2S) is an essential part of the biogas upgrading procedure in order to obtain a marketable and competitive natural gas substitute for flexible utilization. A promising biogas desulfurization technology has to ensure high separation efficiency regardless of process conditions or H2S load without the use or production of toxic or ecologically harmful substances. Alkaline oxidative scrubbing is an interesting alternative to existing desulfurization technologies and is investigated in this work. In experiments on a stirred tank reactor and a continuous scrubbing column in laboratory-scale, H2S was absorbed from a gas stream containing large amounts of carbon dioxide (CO2) into an aqueous solution prepared from sodium hydroxide (NaOH), sodium bicarbonate (NaHCO3) and hydrogen peroxide (H2O2). The influence of pH, redox potential and solution aging on the absorption efficiency and the consumption of chemicals was investigated. Because of the irreversible oxidation reactions of dissolved H2S with H2O2, high H2S removal efficiencies were achieved while the CO2 absorption was kept low. At an existing biogas upgrading plant an industrial-scale pilot scrubber was constructed, which efficiently desulfurizes 180 m3/h of raw biogas with an average removal efficiency of 97%, even at relatively high and strongly fluctuating H2S contents in the crude gas.

  2. Biogas barometer

    The energy recovery of biogas has kept on increasing in the European Union in 2013: +10.2%. Almost 13.4 million tep (tonnes of oil equivalent) of biogas primary energy was produced but the growth of the biogas sector is decreasing (it was 16.9% between 2011 and 2012). The growth for the coming years is expected to fall further because of political decisions in some countries to limit the use of land for farming purposes and to manage the biogas sector more efficiently. Germany ranks first for the production of biogas primary energy with 6717 ktep followed by United Kingdom with 1824 ktep. 2 tables give the production of electricity and heat from biogas in the E.U. member states in 2012 and 2013. The total production of electricity and heat from biogas in the E.U. in 2013 reached 53327 GWh and 432 ktep respectively. A list reviews the most significant companies working in Europe in the sector of methanation, 10 companies are listed among which 2 are Italian: AB Energy (Gruppo AB), BTS Italia and 8 are German: MT Energie, Envitec Biogas AG, Biogas Weser-Ems, Planet Biogastechnik, Schmack Biogas GmbH, Weltec Biopower GmbH, UTS Biogastechnik (Anaergia Group), Bioconstruct and BTS Italia. (A.C.)

  3. Influence of Ce-precursor and fuel on structure and catalytic activity of combustion synthesized Ni/CeO{sub 2} catalysts for biogas oxidative steam reforming

    Vita, Antonio, E-mail: antonio.vita@itae.cnr.it; Italiano, Cristina; Fabiano, Concetto; Laganà, Massimo; Pino, Lidia

    2015-08-01

    A series of nanosized Ni/CeO{sub 2} catalysts were prepared by Solution Combustion Synthesis (SCS) varying the fuel (oxalyldihydrazide, urea, carbohydrazide and glycerol), the cerium precursor (cerium nitrate and cerium ammonium nitrate) and the nickel loading (ranging between 3.1 and 15.6 wt%). The obtained powders were characterized by X-ray Diffraction (XRD), N{sub 2}-physisorption, CO-chemisorption, Temperature Programmed Reduction (H{sub 2}-TPR) and Scanning Electron Microscopy (SEM). The catalytic activity towards the Oxy Steam Reforming (OSR) of biogas was assessed. The selected operating variables have a strong influence on the nature of combustion and, in turn, on the morphological and structural properties of the synthesized catalysts. Particularly, the use of urea allows to improve nickel dispersion, surface area, particle size and reducibility of the catalysts, affecting positively the biogas OSR performances. - Highlights: • Synthesis of Ni/CeO{sub 2} nanopowders by quick and easy solution combustion synthesis. • The fuel and precursor drive the structural and morphological properties of the catalysts. • The use of urea as fuel allows to improve nickel dispersion, surface area and particle size. • Ni/CeO{sub 2} (7.8 wt% of Ni loading) powders synthesized by urea route exhibits high performances for the biogas OSR process.

  4. Effects of steam pretreatment and co-production with ethanol on the energy efficiency and process economics of combined biogas, heat and electricity production from industrial hemp

    Barta, Zsolt; Kreuger, Emma; Björnsson, Lovisa

    2013-01-01

    Background The study presented here has used the commercial flow sheeting program Aspen Plus™ to evaluate techno-economic aspects of large-scale hemp-based processes for producing transportation fuels. The co-production of biogas, district heat and power from chopped and steam-pretreated hemp, and the co-production of ethanol, biogas, heat and power from steam-pretreated hemp were analysed. The analyses include assessments of heat demand, energy efficiency and process economics in terms of an...

  5. Drying characteristics and nitrogen loss of biogas digestate during drying process

    Maurer, C.; Muller, J. [Hohenheim Univ., Stuttgart (Germany). Inst. of Agricultural Engineering, Tropical and Subtropical Group

    2010-07-01

    The cost of transporting biogas digestate can be decreased by reducing its water content. However, the digestate emits volatile compounds during drying. This study investigated the drying behaviour and the change of digestate composition. Drying took place in a hybrid solar/waste-heat dryer that used solar energy as well as waste heat from a combined heat and power unit (CHP) and the exhaust air of a microturbine. The experiment involved the use of 60 t of liquid digestate. Climatic conditions were measured inside and outside the drying hall. Dry matter (DM) and organic dry matter (ODM) were also measured on a daily basis. In addition, the energy consumption of waste and solar heat were recorded and related to the quantity of dried feedstock. The total nitrogen, ammonium, phosphate, potassium oxide, magnesium oxide and calcium oxide in the digestate were subjected to chemical analysis before and after the drying process. Losses of nitrogen were calculated. Specific energy consumption depended on the climatic condition. Most of the energy consumption was covered by the waste heat of the CHP. A considerable amount of nitrogen was lost during the drying process.

  6. A combined process to treat lemon industry wastewater and produce biogas

    Navarro, A.R.; Rubio, M.C.; Maldonado, M.C. [Quimica y Farmacia, Universidad Nacional de Tucuman, Instituto de Biotecnologia, Facultad de Bioquimica, Ayacucho, Tucuman (Argentina)

    2012-02-15

    We studied a process employed for treating lemon industry effluents, using the macrophyte Eishhornia crassipes (water hyacinth) in a phytoremediation tank with a 6000-L workload. The diluted effluents BOD and COD were reduced to 70 and 61%, respectively, working with a 1.5-h hydraulic residence time (HRT). We investigated the effect of adding every 12 h an inoculum consisting of a consortium of microorganisms isolated from the macrophyte roots and recirculating 30% of the outflow. In this way, we achieved a volumetric removal rate (VRR) of BOD = 354 g/m{sup 3} day. Plants were daily harvested from the tank to maintain growth rate and the density originally planted. We studied their use for biogas production in an anaerobic digester working with 12 and 16 days of hydraulic residence time. The yield obtained was 0.87 L/g and productivity 0.87 L/L day with a loading rate of 5 g/L day. Integrating both processes on an industrial scale would solve the effluent pollution problem and generate an energy source that could be used by the industry itself to lower its production costs. (orig.)

  7. Evaluation of biogas quality from home biogas pits installed in central Vietnam

    Štěpánek, Pavel

    2013-01-01

    Abstract Biomass or biogas, they are an essential component of the energy sources used in the conditions of the Vietnamese countryside due to its availability and relatively low investment costs. This thesis is focused on the quality and quantity of biogas produced from home biogas plants installed in Central Vietnam. In this thesis is shown the description of the fermentation process, its final product is biogas. The thesis describes the types of home biogas digesters, which are used ...

  8. Increasing biogas production from sewage sludge anaerobic co-digestion process by adding crude glycerol from biodiesel industry.

    Nartker, Steven; Ammerman, Michelle; Aurandt, Jennifer; Stogsdil, Michael; Hayden, Olivia; Antle, Chad

    2014-12-01

    In an effort to convert waste streams to energy in a green process, glycerol from biodiesel manufacturing has been used to increase the gas production and methane content of biogas within a mesophilic anaerobic co-digestion process using primary sewage sludge. Glycerol was systematically added to the primary digester from 0% to 60% of the organic loading rate (OLR). The optimum glycerol loading range was from 25% to 60% OLR. This resulted in an 82-280% improvement in specific gas production. Following the feeding schedule described, the digesters remained balanced and healthy until inhibition was achieved at 70% glycerol OLR. This suggests that high glycerol loadings are possible if slow additions are upheld in order to allow the bacterial community to adjust properly. Waste water treatment plant operators with anaerobic digesters can use the data to increase loadings and boost biogas production to enhance energy conversion. This process provides a safe, environmentally friendly method to convert a typical waste stream to an energy stream of biogas. PMID:25249492

  9. Biogas Filter Based on Local Natural Zeolite Materials

    Satriyo Krido Wahono; Wahyu Anggo Rizal

    2014-01-01

    UPT BPPTK LIPI has created a biogas filter tool to improve the purity of methane in the biogas. The device shaped cylindrical tube containing absorbent materials which based on local natural zeolite of Indonesia. The absorbent has been activated and modified with other materials. This absorbtion material has multi-adsorption capacity for almost impurities gas of biogas. The biogas  filter increase methane content of biogas for 5-20%. The biogas filter improve the biogas’s performance such as ...

  10. Biogas process parameters--energetics and kinetics of secondary fermentations in methanogenic biomass degradation.

    Montag, Dominik; Schink, Bernhard

    2016-01-01

    Pool sizes of short-chain fatty acids (formate, acetate, propionate, and butyrate), hydrogen, and carbon monoxide were assayed in digesting sludge from four different methanogenic reactors degrading either sewage sludge or agricultural products and wastes at pH 8.0 and 40 or 47 °C. Free reaction energies were calculated for the respective degradation reactions involved, indicating that acetate, propionate, and butyrate degradation all supplied sufficient energy (-10 to -30 kJ per mol reaction) to sustain the microbial communities involved in the respective processes. Pools of formate and hydrogen were energetically equivalent as electron carriers. In the sewage sludge reactor, homoacetogenic acetate formation from H2 and CO2 was energetically feasible whereas syntrophic acetate oxidation appeared to be possible in two biogas reactors, one operating at enhanced ammonia content (4.5 g NH4 (+)-N per l) and the other one at enhanced temperature (47 °C). Maximum capacities for production of methanogenic substrates did not exceed the consumption capacities by hydrogenotrophic and aceticlastic methanogens. Nonetheless, the capacity for acetate degradation appeared to be a limiting factor especially in the reactor operating at enhanced ammonia concentration. PMID:26515561

  11. Anaerobic digestion of fines from recovered paper processing - Influence of fiber source, lignin and ash content on biogas potential.

    Steffen, Friedrich; Requejo, Ana; Ewald, Christian; Janzon, Ron; Saake, Bodo

    2016-01-01

    Fines concentration harms paper machine runability and output quality in recovered paper processing, hence, their extraction would be fundamentally beneficial. In this study, separated fines from an industrial recycled fiber pulp (RFP) were characterized and evaluated for their potential biogas yields with a focus on understanding the role of varying lignin and ash contents. Further, these results were compared with biogas yields from conventional chemical and mechanical pulps. Overall, methane yields of fines from mechanical pulps (21-28mL/gVS) and RFP (127mL/gVS) are relatively low compared to the high methane yields of 375mL/gVS from the chemical pulp fines. However, it was shown that the high ash content in RFP fines (up to 50%) did not negatively influence overall yield, rather, it was the presence of slowly biodegrading lignin-rich fiber fines. PMID:26520490

  12. Biogas energy development in Slovenia

    Bojnec, Štefan; Papler, Drago

    2013-01-01

    This paper analyses the development of the biogas energy production and use in Slovenia. The major concern is given to ecological, economic and technical determinants in decision making process for selection among alternative biogas energy production plants and use of energy for heating and electricity. The investments into the biogas plants have reduced ecological problems from large environmental polluters in urban and rural areas. Among them are sewage systems, food wastes, wastes from lar...

  13. Biogas in Burkina Faso. Influential factors of biogas projects in rural areas of Burkina Faso

    Aschaber, Andreas

    2010-07-01

    Full text: Burkina Faso is among the poorest countries in the world. The energy situation in Burkina Faso is among the most critical issues which need to be addressed in the country. The electrical power grid is insufficient and only available in urban centers. Consequently wood and charcoal is used in order to meet the basic needs for heating, cooking, and lightning by the majority of the population. The resulting overuse of natural energy resources in Burkina Faso has been causing massive deforestation and desertification on the one hand and on the other hand scarcity in fuel wood availability. According to a recent feasibility study of the GTZ, biogas is thought to be one of the most sustainable solutions for developing energy self sufficiency in rural areas of Burkina Faso. Biogas is not a new concept in Burkina Faso, as the first biogas plants were already installed in the 70's. Recently a national biogas program and the activity of various NGOs lead to a rejuvenation of attempts to establish biogas in Burkina Faso. Although biogas has a long history in Burkina Faso, no significant breakthrough of this technology has happened so far. None of the biogas plants built during the last 40 years have been operational for a long time. This contribution presents a study aimed to analyze the partial success and failures of the attempts to install biogas plants so far. The study was conducted in May 2009 as part of a project for a model application of the technology in the frame of University cooperation between Austria (University of Innsbruck) and Burkina Faso (Universite Polytechnique du Bobo Dioulasso). During the field study four sites of existing biogas plants were visited, five interviews with experts conducted and two focus groups with potential users in a rural setting were conducted. The systemic approach, including technical as well as socioeconomic aspects, yielded a wealth of factors which can potentially influence the success of biogas projects in

  14. Design and scale-up of an oxidative scrubbing process for the selective removal of hydrogen sulfide from biogas

    Krischan, J., E-mail: jutta_krischan@hotmail.com [Vienna University of Technology, Institute of Chemical Engineering, Getreidemarkt 9/166, 1060 Vienna (Austria); Makaruk, A., E-mail: aleksander.makaruk@tuwien.ac.at [Vienna University of Technology, Institute of Chemical Engineering, Getreidemarkt 9/166, 1060 Vienna (Austria); Harasek, M., E-mail: michael.harasek@tuwien.ac.at [Vienna University of Technology, Institute of Chemical Engineering, Getreidemarkt 9/166, 1060 Vienna (Austria)

    2012-05-15

    Highlights: Black-Right-Pointing-Pointer Alkaline oxidative scrubbing proved for biogas desulfurization Black-Right-Pointing-Pointer Effect of operating conditions on hydrogen sulfide removal efficiency. Black-Right-Pointing-Pointer Minimization of caustic and oxidant consumption. Black-Right-Pointing-Pointer Process control via pH, redox potential and conductivity measurement. Black-Right-Pointing-Pointer Investigation of long-term behavior of pilot plant operation. - Abstract: Reliable and selective removal of hydrogen sulfide (H{sub 2}S) is an essential part of the biogas upgrading procedure in order to obtain a marketable and competitive natural gas substitute for flexible utilization. A promising biogas desulfurization technology has to ensure high separation efficiency regardless of process conditions or H{sub 2}S load without the use or production of toxic or ecologically harmful substances. Alkaline oxidative scrubbing is an interesting alternative to existing desulfurization technologies and is investigated in this work. In experiments on a stirred tank reactor and a continuous scrubbing column in laboratory-scale, H{sub 2}S was absorbed from a gas stream containing large amounts of carbon dioxide (CO{sub 2}) into an aqueous solution prepared from sodium hydroxide (NaOH), sodium bicarbonate (NaHCO{sub 3}) and hydrogen peroxide (H{sub 2}O{sub 2}). The influence of pH, redox potential and solution aging on the absorption efficiency and the consumption of chemicals was investigated. Because of the irreversible oxidation reactions of dissolved H{sub 2}S with H{sub 2}O{sub 2}, high H{sub 2}S removal efficiencies were achieved while the CO{sub 2} absorption was kept low. At an existing biogas upgrading plant an industrial-scale pilot scrubber was constructed, which efficiently desulfurizes 180 m{sup 3}/h of raw biogas with an average removal efficiency of 97%, even at relatively high and strongly fluctuating H{sub 2}S contents in the crude gas.

  15. Robust on-line monitoring of biogas processes; Robusta maettekniker on-line foer optimerad biogasproduktion

    Nordberg, Aake; Hansson, Mikael; Kanerot, Mija; Krozer, Anatol; Loefving, Bjoern; Sahlin, Eskil

    2010-03-15

    project showed that pH-adjustment with Na{sub 3}PO{sub 4} can be a way of compensating for the losses of volatile compounds (up to 20% of VS), which occurs when standardized reference methods are used. This is a fundamental problem and requires further research. Monitoring of a laboratory-scale anaerobic digester with NIR showed that a previously developed multivariate model could predict propionate concentrations (R2= 0,92; RMSEP 0,39 g/L) in the interval 0-5 g/L, which is a relevant interval for inhibition (limit ca 3 g/L). A commercial FT-NIR instrument was subsequently installed at the production plant. However, the organic loading was decreased during the evaluation period due to process disturbances, at which the dynamic of the process was not in the range needed for prediction of e.g. propionate. Measurements and evaluation will continue during normal conditions after the completion of this project. Evaluation of a potentiometric sensor for ammonia with potential for on-line application showed low stability and a need for daily calibration, which therefore did not fulfill the requested demand. The project has demonstrated technologies with significant potential for on-line monitoring at production scale facilities, thus improving the knowledge base for making important decisions. Knowledge about on-line implementation has increased, and important insights into the limitations of standardized reference methods and substrate characteristics have been achieved. Instrument suppliers have in general a limited insight in the conditions at a biogas plant, which suggests that this type of WR-financed project is important for development in the area

  16. Biogas production from food-processing industrial wastes by anaerobic digestion

    Fang, Cheng

    Konfronteret med energikrise og klimaforandringer, har verden brug for grønne, effektive og kulstofneutrale energikilder, som kan erstatte fossile brændstoffer. Biogas, som dannes ved anaerob nedbrydning af organisk materiale, er en bæredygtig, pålidelig og vedvarende energikilde. Der er stor...

  17. Quantification of syntrophic acetate-oxidizing microbial communities in biogas processes.

    Westerholm, Maria; Dolfing, Jan; Sherry, Angela; Gray, Neil D; Head, Ian M; Schnürer, Anna

    2011-08-01

    Changes in communities of syntrophic acetate-oxidizing bacteria (SAOB) and methanogens caused by elevated ammonia levels were quantified in laboratory-scale methanogenic biogas reactors operating at moderate temperature (37°C) using quantitative polymerase chain reaction (qPCR). The experimental reactor was subjected to gradually increasing ammonia levels (0.8-6.9 g NH4 (+) -N l(-1) ), whereas the level of ammonia in the control reactor was kept low (0.65-0.90 g NH4 (+) -N l(-1) ) during the entire period of operation (660 days). Acetate oxidation in the experimental reactor, indicated by increased production of (14) CO2 from acetate labelled in the methyl carbon, occurred when ammonia levels reached 5.5 and 6.9 g NH4 (+) -N l(-1) . Syntrophic acetate oxidizers targeted by newly designed qPCR primers were Thermacetogenium phaeum, Clostridium ultunense, Syntrophaceticus schinkii and Tepidanaerobacter acetatoxydans. The results showed a significant increase in abundance of all these bacteria except T. phaeum in the ammonia-stressed reactor, coincident with the shift to syntrophic acetate oxidation. As the abundance of the bacteria increased, a simultaneous decrease was observed in the abundance of aceticlastic methanogens from the families Methanosaetaceae and Methanosarcinaceae. qPCR analyses of sludge from two additional high ammonia processes, in which methane production from acetate proceeded through syntrophic acetate oxidation (reactor SB) or through aceticlastic degradation (reactor DVX), demonstrated that SAOB were significantly more abundant in the SB reactor than in the DVX reactor. PMID:23761313

  18. Biogas production from a systems analytical perspective

    Berglund, Maria

    2006-01-01

    Anaerobic digestion and the production of biogas can provide an efficient means of meeting several objectives concerning energy, environmental and waste management policy. Interest in biogas is increasing, and new facilities are being built. There is a wide range of potential raw material, and both the biogas and digestates produced can be used in many different applications. The variation in raw materials and digestion processes contributes to the flexibility of biogas production systems, bu...

  19. BIOGAS-ECONOMICAL SIGNIFICANCE AND GENERATION THEREOF

    Kazimierz Brodowicz

    1983-01-01

    The paper presents a review of worldwide and domestic knowledge in the field of biogas generation techniques. To this there are discussed the basic fermentation processes being resonsible for biogas generation and actually used typical systems therefor presented.Particular attention has been paid to energetic aspects of the biogas. The generalization of biogas production would render possible large scale utilization of the biomass which is useless for other purposes but still renewable as a s...

  20. Utilization of auxiliary means for the enhancement of the efficiency and stability of the biogas process; Einsatz von Hilfsmitteln zur Steigerung der Effizienz und Stabilitaet des Biogasprozesses

    NONE

    2011-07-01

    Within the Guelzow expert discussions at 29th September 2010 in Guelzow (Federal Republic of Germany) the following lectures were held: (1) State of the promotional work of the FNR on the subject auxiliary means - open questions (Petra Schuesseler); (2) Utilization of auxiliary means in the biogas production - Survey and experiences from laboratory and practice (Konrad Koch); (3) ORGA - test: Development of a test procedure for the practical evaluation of the fermentation biology of NaWaRo biogas plants (Nils Engler); (3) Investigations for the utilization of minerals in biogas plants - Significance of minerals for anaerobic microorganisms and causes for concentration differences in biogas fermentation plants (Andreas Lemmer); (4) Quantification of the efficiency of mineral biogas additives at the fermentation of renewable raw materials and their verification in the practice (Dirk Wagner); (5) Optimization of processes by means of enzymes in biogas plants (Monika Heiermann); (6) Utilization of microorganisms for the enhancement of the gas yield (Doris Schmack); (7) Results of the discussion and summary (Petra Schuesseler).

  1. Bioenergy, protein and fibres from grass - biogas process monitoring; Bioenergie, Protein und Fasern aus Gras - Monitoring des Biogasprozesses

    Baier, U.; Delavy, P.

    2003-07-01

    Starting in Summer 2001 the first full scale Swiss Bio-refinery for grass processing took up operation in Schaffhausen. Grass processing covers the production of technical fibres and protein concentrate as well as anaerobic digestion of residual slops for the production of biogas and 'green' electricity. The refinery is operated by the company Bioenergie Schaffhausen as a P+D (pilot + demonstration) project of the Swiss Federal Office of Energy. Under full load it will deliver 2,000 MWh of 'green' electricity (10% own needs) and 3,000 MWh heat (50% own needs). Prior to start up the Swiss technology holder 2B Biorefineries AG mandated the University of Applied Sciences HSW with lab scale testing of the mesophilic biogas potential and anaerobic degradability of residual grass processing slops. Nutrient limitations and possible inhibition risks were evaluated. During the initial 8 months of full scale operation of the refinery in Schaffhausen an intensive monitoring of the anaerobic digester's performance was carried out. Carbon and nitrogen mass balances have been set up and the development of the granular EGSB sludge was characterised. From operational data a set of performance values was elaborated. The first year of operation was characterised by only partial exploitation of the refinery's grass processing capacity. Furthermore the protein separation and production unit has not yet been incorporated. Consequently, the EGSB biogas reactor showed a significant hydraulic underload when compared to dimensioning basics. Raw residuals were characterised by a higher particulate protein fraction. Operational conditions for the EGSB reactor were worked out to allow stable operation at elevated load conditions and with protein separation in operation. (author)

  2. Biogas : Animal Waste That Can be Alternative Energy Source

    Tuti Haryati

    2006-09-01

    Full Text Available Biogas is a renewable energy which can be used as alternative fuel to replace fossil fuel such as oil and natural gas . Recently, diversification on the use of energy has increasingly become an important issue because the oil sources are depleting . Utilization of agricultural wastes for biogas production can minimize the consumption of commercial energy source such as kerosene as well as the use of firewood . Biogas is generated by the process of organic material digestion by certain anaerobe bacteria activity in aerobic digester . Anaerobic digestion process is basically carried out in three steps i.e. hydrolysis, acidogenic and metanogenic . Digestion process needs certain condition such as C : N ratio, temperature, acidity and also digester design . Most anaerobic digestions perform best at 32 - 35°C or at 50 - 55°C, and pH 6 .8 - 8 . At these temperatures, the digestion process essentially converts organic matter in the present of water into gaseous energy . Generally, biogas consists of methane about 60 - 70% and yield about 1,000 British Thermal Unit/ft 3 or 252 Kcal/0.028 m3 when burned . In several developing countries, as well as in Europe and the United States, biogas has been commonly used as a subtitute environmental friendly energy . Meanwhile, potentially Indonesia has abundant potential of biomass waste, however biogas has not been used maximally .

  3. Lab-scale demonstration of recuperative thickening technology for enhanced biogas production and dewaterability in anaerobic digestion processes.

    Cobbledick, Jeffrey; Aubry, Nicholas; Zhang, Victor; Rollings-Scattergood, Sasha; Latulippe, David R

    2016-05-15

    There is growing interest in the use of high performance anaerobic digestion (AD) processes for the production of biogas at wastewater treatment facilities to offset the energy demands associated with wastewater treatment. Recuperative thickening (RT) is a promising technique which involves recycling a portion of the digested solids back to the incoming feed. In general there exists a significant number of knowledge gaps in the field of RT because the studies that have been conducted to date have almost exclusively occurred in pilot plant or full scale trials; this approach greatly limits the amount of process optimization that can be done in a given trial. In this work, a detailed and comprehensive study of RT was conducted at the lab scale; two custom designed digesters (capacity = 1.5 L) were operated in parallel with one acting as a 'control' digester and the other operating under a semi-batch RT mode. There was no significant change in biogas methane composition for the two digesters, however the RT digester had an average biogas productivity over two times higher than the control one. It was found that the recycling of the polymer flocculant back into the RT digester resulted in a significant improvement in dewatering performance. At the highest polymer concentration tested, the capillary suction time (CST) values for flocculated samples for the RT digester were over 6 times lower than the corresponding values for the control digester. Thus, there exists an opportunity to decrease the overall consumption of polymer flocculants through judicious selection of the dose of polymer flocculant that is used both for the thickening and end-stage dewatering steps in RT processes. PMID:26986495

  4. BIOGAS PROCTION FROM ANAEROBIC CO-DIGESTION OF COW DUNG AND ORGANIC WASTES (NAPIER PAK CHONG I AND FOOD WASTE IN THAILAND: TEMPERATURE EFFECT ON BIOGAS PRODUCT

    Lertluck Saitawee

    2014-01-01

    Full Text Available Biogas production has been attracting increasing attention as a biofuel of the future because biogas technology not only constitutes a biofuel source, but also can be applied in the various environmental pollutants. Anaerobic digestion of high solid slurries (such as food waste and cow dung is typically performed in continuously reactor (by force substrate flow to avoid problems with a thick floating layer or large amounts of sediments. Temperature also seems to have profound influence on the biogas production. The objective of the study was to identify the optimum biogas production for anaerobic co-digestion of cow dung and organic wastes (napierpakchong I and food waste. Influence of temperature (psyhrophilic temperature 25°C and thermoplilic temperature 45°C and active biogas process on single substrate (food waste feed and co-digestion of cow dung and organic wastes (napierpakchong I and food waste was used, within the reactor was studies in 1.80 cm high over a 45 day. Results showed that best digestion was achieved when digested of cow dung, napierpakchong I and food waste on 1:1:1 and thermoplilic temperature. Maximum biogas production (R4, biogas yield, methane content and %VS reduction was found that 70 L/day, 70 L/VS feed, 65 and 80%, respectively. The result showed that the biogas production increased progressively withhigher temperature.The increased in biogas production in thermophilic temperature and psyhrophilic temperature could be up 28.01 and 26%, respectively. The biogas yield increased 12.5% of co-digestion system, which compared to thermophilic temperature and psyhrophilic temperature (R4 and R2. This behavior might be due to the higher degradability. Therefore, temperature of digester can be used effectively as an operating strategy to optimize biogas production.

  5. Experimental validation of hydrogen sulphide removal from biogas using biotrickling process at pilot plant level

    Mesa Garcia, Cristian

    2012-01-01

    Within the framework of sustainable development, and ever-increasing energy costs, wastewater treatment operators focus on developing on-site energy production: the main approach today is via sewage biogas. In most cases, H2S removal is necessary to meet the requirements of the energy conversion equipment inlet requirements (for cogeneration motors around 300 – 500 ppm, but for fuel cells around 1ppm or below). Therefore to optimise the overall energy and economic balance, it i...

  6. Biogas technology in Pakistan

    Although biomethanation is a mature technology its implementation is paradoxically only partly a success in Pakistan. Biogas plants on family farms can be economical but seldom are so in Pakistan. Either the investment cost has been high or satisfactory performance of the process could not be maintained or in some case for a short period of time only. It is, however, concluded that biogas plants, if correctly operated and maintained, may prove to be appropriate to the technical abilities and economic capacity of Pakistani farmers. It can get a change to be disseminated in rural areas. Biogas technology is appropriate to the ecological and economic demands of the future. With the potential from existing cattle population only, 3 to 4 million family size biogas plants may be installed in Pakistan which can substitute of considerable part of rural fuel wood demand for their daily household energy requirements. A large amount of dung is burnt every year by households which if put in the biogas plant, may provide a considerable amount of energy along with organic fertilizer could be saved from being burned at the same time. On the basis of available data from the livestock excluding agriculture residue (50% collectivity-1991), in terms of fuel substitution, this would be equivalent to 1200 million litres of kerosene at worth economic value of 9021 million rupees saving in the form of gas and 821 million rupees as additional fertilizer value annually. (LN)

  7. Dynamic experiment of biogas desulfurization by activated carbon%活性炭脱除模拟沼气中H2S的动态试验

    史风梅; 裴占江; 王粟; 高亚冰; 孙彬; 刘杰

    2016-01-01

    The world suffers the fossil energy crisis, and biogas gains more and more attention for it is a kind of reproducible, clean and environmental-friendly energy. Biogas comes from the anaerobic fermentation of organic materials in agriculture, industry and household waste at certain temperature and pressure. The concentration of H2S in biogas varies from 10 to 2 000 ×10-6 or even more, which is different with the type, concentration of organic materials and the operation of anaerobic digestion process. In order to use biogas safely, the H2S in biogas which is hazardous to the equipment or human health should be removed from the biogas. Purification methods of H2S vary from simple physical or chemical technology to complex process including chemical, physical or biological treatment units, which depended on the use purpose of biogas. Activated carbon is a highly porous material, and known as an efficient media for low-concentration H2S removal by adsorption process. Moreover, activated carbon is easily available and cheap in price, because it is produced from biomass such as agricultural waste, wood, bamboo, coconut shells, and almond shells, which is abundant in China. Currently, most efforts are made in the study on H2S adsorption by modified activated carbon such as impregnated activated carbon with alkali or heavy metal salts. The modified active carbon has the better performances in most cases, but it is proved to have negative effects on the removal of H2S. For example, active carbon’s absorption capacity of H2S will decrease when the crystals of alkali or metal salts block the pores which act as adsorption site. The price of impregnated active carbon is higher than unmodified activated carbon and the corrosion often occurs inevitably. It is necessary to study the most efficient way to improve the performance of unmodified active carbon. Thus, the effects of the inflow rate, the concentration of H2S, the size of unmodified activated carbon and the length of

  8. Microbial community dynamics linked to enhanced substrate availability and biogas production of electrokinetically pre-treated waste activated sludge.

    Westerholm, Maria; Crauwels, Sam; Houtmeyers, Sofie; Meerbergen, Ken; Van Geel, Maarten; Lievens, Bart; Appels, Lise

    2016-10-01

    The restricted hydrolytic degradation rate of complex organic matter presents a considerable challenge in anaerobic digestion of waste activated sludge (WAS). Within this context, application of pre-treatment of digester substrate has potential for improved waste management and enhanced biogas production. Anaerobic degradation of untreated or electrokinetically pre-treated WAS was performed in two pilot-scale digesters for 132days. WAS electrokinetically pre-treated with energy input 0.066kJ/kg sludge was used in a first phase of operation and WAS pre-treated with energy input 0.091kJ/kg sludge was used in a second phase (each phase lasted at least three hydraulic retention times). Substrate characteristics before and after pre-treatment and effects on biogas digester performance were comprehensively analysed. To gain insights into influences of altered substrate characteristics on microbial communities, the dynamics within the bacterial and archaeal communities in the two digesters were investigated using 16S rRNA gene sequencing (pyrosequencing) and quantitative PCR (qPCR). Specific primers targeting dominant operation taxonomic units (OTUs) and members of the candidate phylum Cloacimonetes were designed to further evaluate their abundance and dynamics in the digesters. Electrokinetic pre-treatment significantly improved chemical oxygen demand (COD) and carbohydrate solubility and increased biogas production by 10-11% compared with untreated sludge. Compositional similarity of the bacterial community during initial operation and diversification during later operation indicated gradual adaptation of the community to the higher solubility of organic material in the pre-treated substrate. Further analyses revealed positive correlations between gene abundance of dominant OTUs related to Clostridia and Cloacimonetes and increased substrate availability and biogas production. Among the methanogens, the genus Methanosaeta dominated in both digesters. Overall, the

  9. The Development of Biogas Technology in Denmark: Achievements & Obstacles

    Sannaa, Mohamed Najib

    2004-01-01

    Denmark is one of the most advanced countries in biogas technology. This country added several improvements to the biogas process in order to increase the biogas yield and thereby improve the economical profitability. Consequently, this project studied the developments of biogas technology in Denmark. The study includes a historical progress of biogas plants since 1970s; the different problems interrupted the expansion of this technology and the actions taken to overcome these obstacles. This...

  10. Anaerobic Digestion and Biogas Potential: Simulation of Lab and Industrial-Scale Processes

    Ihsan Hamawand

    2015-01-01

    Full Text Available In this study, a simulation was carried out using BioWin 3.1 to test the capability of the software to predict the biogas potential for two different anaerobic systems. The two scenarios included: (1 a laboratory-scale batch reactor; and (2 an industrial-scale anaerobic continuous lagoon digester. The measured data related to the operating conditions, the reactor design parameters and the chemical properties of influent wastewater were entered into BioWin. A sensitivity analysis was carried out to identify the sensitivity of the most important default parameters in the software’s models. BioWin was then calibrated by matching the predicted data with measured data and used to simulate other parameters that were unmeasured or deemed uncertain. In addition, statistical analyses were carried out using evaluation indices, such as the coefficient of determination (R-squared, the correlation coefficient (r and its significance (p-value, the general standard deviation (SD and the Willmott index of agreement, to evaluate the agreement between the software prediction and the measured data. The results have shown that after calibration, BioWin can be used reliably to simulate both small-scale batch reactors and industrial-scale digesters with a mean absolute percentage error (MAPE of less than 10% and very good values of the indexes. Furthermore, by changing the default parameters in BioWin, which is a way of calibrating the models in the software, as well, this may provide information about the performance of the digester. Furthermore, the results of this study showed there may be an over estimation for biogas generated from industrial-scale digesters. More sophisticated analytical devices may be required for reliable measurements of biogas quality and quantity.

  11. Quantification of syntrophic acetate-oxidizing microbial communities in biogas processes

    Westerholm, Maria; Dolfing, Jan; Sherry, Angela; Gray, Neil D.; Head, Ian M; Schnürer, Anna

    2011-01-01

    Changes in communities of syntrophic acetate-oxidizing bacteria (SAOB) and methanogens caused by elevated ammonia levels were quantified in laboratory-scale methanogenic biogas reactors operating at moderate temperature (37°C) using quantitative polymerase chain reaction (qPCR). The experimental reactor was subjected to gradually increasing ammonia levels (0.8–6.9 g NH4 +-N l−1), whereas the level of ammonia in the control reactor was kept low (0.65–0.90 g NH4 +-N l−1) during the entire perio...

  12. Biogas document; Dossier Biogaz

    Verchin, J.C.; Servais, C. [Club BIOGAZ, 94 - Arcueil (France)

    2002-06-01

    In this document concerning the biogas, the author presents this renewable energy situation in 2001-2002, the concerned actors, the accounting of the industrial methanization installations in France, the three main chains of process for industrial wastes and two examples of methanization implementation in a paper industry and in a dairy. (A.L.B.)

  13. Theoretical analysis of a biogas-fed PEMFC system with different hydrogen purifications: Conventional and membrane-based water gas shift processes

    Highlights: • Thermodynamic analysis of the biogas-fed PEMFC system is performed. • Conventional and membrane-based WGS processes for H2 purification are studied. • A flowsheet model of the PEMFC system is developed. • Effect of key parameters on yields of H2 and carbon in the biogas reformer is shown. • Performance of PEMFC systems with different H2 purification processes is analyzed. - Abstract: This study presents a thermodynamic analysis of biogas reforming and proton electrolyte membrane fuel cell (PEMFC) integrated process with different hydrogen purifications: conventional and membrane-based water gas shift processes. The aim is to determine the optimal reforming process for hydrogen production from biogas in the PEMFC system. The formation of carbon is concerned in the hydrogen production. The simulation results show that increases in the steam-to-methane ratio and reformer temperature can improve the hydrogen yield and reduce the carbon formation. From the performance analysis, it is found that when the PEMFC is operated at high temperature and fuel utilization, the overall system efficiency enhances. The performance of the PEMFC system with the installation of a water gas shift membrane unit in the hydrogen purification step is slightly increased, compared with a conventional process

  14. Trace elements in NaWaRo biogas plants for balancing substrate limited deficiency symptoms and stabilizing the fermentation process; Spurenelemente in NawaRo-Biogasanlagen zum Ausgleich substratbedingter Mangelerscheinungen und zur Stabilisierung des Gaerprozesses

    Oechsner, Hans; Lemmer, Andreas [Hohenheim Univ., Stuttgart (Germany). Landesanstalt fuer Agrartechnik und Bioenergie; Preissler, Daniel

    2011-07-01

    The authors of the contribution under consideration report on trace elements in renewable resource biogas plants in order to compensate for substrate induced deficiency symptoms and to stabilize the fermentation process. The analysis of biological connections in biogas processes showed, that an optimal supply of the microorganisms with trace elements is essential for the course of the four stages of decomposition of the biogas process. Trace elements significantly are involved in the structure of coenzymes or cofactors, reduce the sulfide toxicity and stimulate the growth of methanogens. If the individual items are missing, the biogas process can be disrupted. This can result in a cut-off of the fermenter and in a stopping of the biogas production.

  15. Modeling the water scrubbing process and energy requirements for CO2 capture to upgrade biogas to biomethane

    Nock, William James; Walker, Mark; Kapoor, Rimika; Heaven, Sonia

    2014-01-01

    Water scrubbing is the most widely used technology for removing CO2 from biogas and landfill gas. This work developed a rate-based mass transfer model of the CO2–water system for upgrading biogas in a packed bed absorption column. The simulated results showed good agreement with both a pilot-scale plant operating at 10 bar, and a large-scale biogas upgrading plant operating at atmospheric pressure. The calculated energy requirement for the absorption column to upgrade biogas to 98% CH4 (0.23 ...

  16. Enhancing biogas production from vinasse in sugarcane biorefineries: Effects of urea and trace elements supplementation on process performance and stability.

    Janke, Leandro; Leite, Athaydes F; Batista, Karla; Silva, Witan; Nikolausz, Marcell; Nelles, Michael; Stinner, Walter

    2016-10-01

    In this study, the effects of nitrogen, phosphate and trace elements supplementation were investigated in a semi-continuously operated upflow anaerobic sludge blanket system to enhance process stability and biogas production from sugarcane vinasse. Phosphate in form of KH2PO4 induced volatile fatty acids accumulation possibly due to potassium inhibition of the methanogenesis. Although nitrogen in form of urea increased the reactor's alkalinity, the process was overloaded with an organic loading rate of 6.1gCODL(-1)d(-1) and a hydraulic retention time of 3.6days. However, by supplementing urea and trace elements a stable operation even at an organic loading rate of 9.6gCODL(-1)d(-1) and a hydraulic retention time of 2.5days was possible, resulting in 79% higher methane production rate with a stable specific methane production of 239mLgCOD(-1). PMID:26873284

  17. A membrane based process for the upgrading of biogas to substituted natural gas (SNG) and recovery of carbondioxide for industrial use

    Norddahl, Birgir; dePreez, Jan

    2007-01-01

    A low pressure carbon molecular sieve (CMS) membrane based process to upgrade biogas from anaerobic digestion of agricultural waste to a substitute natural gas (SNG) has been tested on a pilot scale. The data extracted from the pilot plant was used to estimate membrane permeance and ideal selecti...

  18. Monitoring of biogas test plants

    Holm-Nielsen, Jens Bo; Esbensen, Kim H.

    2011-01-01

    Most studies reported in the literature have investigated near infrared spectroscopy (NIR) in laboratory-scale or minor pilot biogas plants only; practically no other studies have examined the potential for meso-scale/full-scale on-line process monitoring. The focus of this study is on a meso......-scale biogas test plant implementation of process analytical technologies (PAT) to develop multivariate calibration/prediction models for anaerobic digestion (AD) processes. A 150 L bioreactor was fitted with a recurrent loop at which NIR spectroscopy and attendant reference sampling were carried out. In all...... realistic bioreactor scales, it is necessary to obtain a fairly constant level of volatile fatty acid (VFA) concentration, which furthers a stable biogas production. Uncontrolled VFA contents have a significant negative impact on biogas production; VFA concentrations should not exceed 5–6000 mg/L lest...

  19. Performance of a biogas upgrading process based on alkali absorption with regeneration using air pollution control residues.

    Baciocchi, Renato; Carnevale, Ennio; Costa, Giulia; Gavasci, Renato; Lombardi, Lidia; Olivieri, Tommaso; Zanchi, Laura; Zingaretti, Daniela

    2013-12-01

    This work analyzes the performance of an innovative biogas upgrading method, Alkali absorption with Regeneration (AwR) that employs industrial residues and allows to permanently store the separated CO2. This process consists in a first stage in which CO2 is removed from the biogas by means of chemical absorption with KOH or NaOH solutions followed by a second stage in which the spent absorption solution is contacted with waste incineration Air Pollution Control (APC) residues. The latter reaction leads to the regeneration of the alkali reagent in the solution and to the precipitation of calcium carbonate and hence allows to reuse the regenerated solution in the absorption process and to permanently store the separated CO2 in solid form. In addition, the final solid product is characterized by an improved environmental behavior compared to the untreated residues. In this paper the results obtained by AwR tests carried out in purposely designed demonstrative units installed in a landfill site are presented and discussed with the aim of verifying the feasibility of this process at pilot-scale and of identifying the conditions that allow to achieve all of the goals targeted by the proposed treatment. Specifically, the CO2 removal efficiency achieved in the absorption stage, the yield of alkali regeneration and CO2 uptake resulting for the regeneration stage, as well as the leaching behavior of the solid product are analyzed as a function of the type and concentration of the alkali reagent employed for the absorption reaction. PMID:24045173

  20. Comparison of VFA titration procedures used for monitoring the biogas process

    Lützhøft, Hans-Christian Holten; Boe, Kanokwan; Fang, Cheng;

    2014-01-01

    titration procedures. Currently, no standardized procedure is used and it is therefore difficult to compare the performance among plants. The aim of this study was to evaluate four titration procedures (for determination of VFA-levels of digested manure samples) and compare results with gas chromatographic...... (GC) analysis. Two of the procedures are commonly used in biogas plants and two are discussed in literature. The results showed that the optimal titration results were obtained when 40mL of four times diluted digested manure was gently stirred (200rpm). Results from samples with different VFA...... concentrations (1-11g/L) showed linear correlation between titration results and GC measurements. However, determination of VFA by titration generally overestimated the VFA contents compared with GC measurements when samples had low VFA concentrations, i.e. around 1g/L. The accuracy of titration increased when...

  1. Research on Anaerobic Digestion: Optimization and Scalability of Mixed High-strength Food Processing Wastes for Renewable Biogas Energy

    Yu, Zhongtang [The Ohio State Univ., Columbus, OH (United States); Hitzhusen, Fredrick [The Ohio State Univ., Columbus, OH (United States)

    2012-12-27

    This research project developed and improved anaerobic digestion technologies, created a comprehensive Inventory of Ohio Biomass and a database of microorganisms of anaerobic digesters, and advanced knowledge and understanding of the underpinning microbiology of the anaerobic digestion process. The results and finding of this research project may be useful for future development and implementation of anaerobic digesters, especially at livestock farms. Policy makers and investors may also find the information on the biomass availability in Ohio and valuation of energy projects useful in policy making and making of investment decisions. The public may benefit from the information on biogas as an energy source and the potential impact of anaerobic digester projects on their neighborhoods.

  2. The effect of anaerobic fermentation processing of cattle waste for biogas as a renewable energy resources on the number of contaminant microorganism

    Kurnani, Tb. Benito A.; Hidayati, Yuli Astuti; Marlina, Eulis Tanti; Harlia, Ellin

    2016-02-01

    Beef cattle waste has a positive potential that can be exploited, as well as a negative potential that must be controlled so as not to pollute the environment. Beef cattle waste can be processed into an alternative energy, namely biogas. Anaerobic treatment of livestock waste to produce gas can be a solution in providing optional energy, while the resulted sludge as the fermentation residue can be used as organic fertilizer for crops. However, this sludge may containt patogenic microorganism that will damage human and environmet healt. Therefor, this study was aimed to know the potency of beef cattle waste to produce biogas and the decrease of the microorganism's number by using fixed dome digester. Beef cattle waste was processed into biogas using fixed dome digester with a capacity of 12 m3. Biogas composition was measured using Gas Cromatografi, will microorganism species was identified using Total plate Count Methode. The result of this study shows that the produced biogas contains of 75.77% Mol (CH4), 13.28% Mol (N), and 6.96% Mol (CO2). Furthermor, this study show that the anaerobic fermrntation process is capable of reducing microorganisms that could potentially pollute the environment. The number of Escherichia coli and Samonella sp. were protozoa can be reduced in order of 94.73%. Protozoa that can be identified in cattle waste before, and after anaerobic fermentation was merely Eimeria sp.. The process also reduced the yeast of 86.11%. The remaining yeast after fermentation was Candida sp. Finally, about 93.7% of endoparasites was reduced by this process. In this case, every trematode and cestoda were 100% reduced, while the nematode only 75%. Reducing some microorganisms that have the potential to pollute the environment signifies sludge anaerobic fermentation residue is safe to be applied as organic fertilizer for crops.

  3. The effect of anaerobic fermentation processing of cattle waste for biogas as a renewable energy resources on the number of contaminant microorganism

    Kurnani, Tb. Benito A.; Hidayati, Yuli Astuti; Marlina, Eulis Tanti; Harlia, Ellin

    2016-02-01

    Beef cattle waste has a positive potential that can be exploited, as well as a negative potential that must be controlled so as not to pollute the environment. Beef cattle waste can be processed into an alternative energy, namely biogas. Anaerobic treatment of livestock waste to produce gas can be a solution in providing optional energy, while the resulted sludge as the fermentation residue can be used as organic fertilizer for crops. However, this sludge may containt patogenic microorganism that will damage human and environmet healt. Therefor, this study was aimed to know the potency of beef cattle waste to produce biogas and the decrease of the microorganism's number by using fixed dome digester. Beef cattle waste was processed into biogas using fixed dome digester with a capacity of 12 m3. Biogas composition was measured using Gas Cromatografi, will microorganism species was identified using Total plate Count Methode. The result of this study shows that the produced biogas contains of 75.77% Mol (CH4), 13.28% Mol (N), and 6.96% Mol (CO2). Furthermor, this study show that the anaerobic fermrntation process is capable of reducing microorganisms that could potentially pollute the environment. The number of Escherichia coli and Samonella sp. were waste before, and after anaerobic fermentation was merely Eimeria sp.. The process also reduced the yeast of 86.11%. The remaining yeast after fermentation was Candida sp. Finally, about 93.7% of endoparasites was reduced by this process. In this case, every trematode and cestoda were 100% reduced, while the nematode only 75%. Reducing some microorganisms that have the potential to pollute the environment signifies sludge anaerobic fermentation residue is safe to be applied as organic fertilizer for crops.

  4. Biogas recovery from waste organic materials: a comparative experimental study

    Full text: Biogas production from organic waste is already traditional method for treatment of agricultural waste with simultaneous energy recovery in the form of biogas. However, biogas can also be produced efficiently treating organic waste from beverage industries and biodiesel production. In the latter case, huge amounts of crude glycerol are released posing severe problems with their treatment. The main obstacle to the efficient waste treatment by anaerobic digestion is the sensitivity of the methanogenic bacteria toward pH variations. When the digester is overloaded, high concentrations of organic acids are produced damping the activity of methanogenes. This problem can be overcome by separating the digester into different compartments, enabling the development of the consecutive processes of hydrolysis, acidogenesis and methanogenesis in different spaces.; In the present study results of biogas production from poultry litter, stillage from ethanol production, and crude glycerol from biodiesel manufacturing are presented. The experiments were carried out in a continuous baffled anaerobic reactor. It was established that the process with glycerol utilization was too sensitive toward the loading because of intensive acid formation as intermediates. The process with stillage as substrate was stable and well steered for months with very high biogas yield (350 I/kg COD) at high production rate, i.e. up to 4 wd'. The microbial profiles, the pH values and the intermediate concentrations along the reactor were determined and correlated with the biogas yield. Different microbial strains and profiles for the different substrates were observed. In the case of glycerol digestion, almost one bacterial genus, i.e. Klebsiella sp., was detected besides the methanogenes, which enables to make speculations about the pathway of competitive intermediate, biogas, and final products formation

  5. Economic assessment of biogas-to-electricity generation system with H2S removal by activated carbon in small pig farm

    This study was conducted to assess the economic feasibility of electricity generation from biogas in small pig farms with and without the H2S removal prior to biogas utilisation. The 2% potassium iodide (KI) impregnated activated carbon selected as H2S adsorbent was introduced to a biogas-to-electricity generation system in a small pig farm in Thailand as a case study. With the average inlet H2S concentration of about 2400 ppm to the adsorption unit, the H2S removal efficiency could reach 100% with the adsorption capacity of 0.062 kg of H2S/kg of adsorbent. Under the reference scenario (i.e., 45% subsidy on digester installation and fixed electricity price at 0.06 Euro/kWh) and based on an assumption that the biogas was fully utilised for electricity generation in the system, the payback period for the system without H2S removal was about 4 years. With H2S removal, the payback period was within the economic life of digester but almost twice that of the case without H2S removal. The impact of electricity price could be clearly seen for the case of treated biogas. At the electricity price fixed at 0.07 Euro/kWh, the payback period for the case of treated biogas was reduced to about 5.5 years, with a trend to decrease at higher electricity prices. For both treated and untreated biogas, the governmental subsidy was the important factor determining the economics of the biogas-to-electricity systems. Without subsidy, the payback period increased to almost 7 years and about 11 years for the case of untreated and treated biogas, respectively, at the reference electricity price. Although the H2S removal added high operation cost to the system, it is still highly recommended not only for preventing engine corrosion but also for the environment benefit in which air pollution by H2S/SO2 emission and impact on human health could be potentially reduced. (author)

  6. Promotion and marketing of the biogas way

    The biological process of anaerobic digestion is used primarily as a tool for waste treatment. It also produces energy in the form of biogas - a feature by which it is often called the biogas technology. This paper outlines special features of this process, together with other advantages and disadvantages of applying the AD or the biogas technology, to satisfy ever increasing regulatory requirements and public concerns over pollution at both global and local levels. The paper then gives suggestions which could be implemented at the Commission, national and regional levels to propagate the implementation of the biogas technology. (au)

  7. Cavitation for improved sludge conversion into biogas

    Stoop, A.H.; Bakker, T.W.; Kramer, H.J.M.

    2015-01-01

    In several studies the beneficial influence of pre-treatment of waste activated sludge with cavitation on the biogas production was demonstrated. It is however, still not fully certain whether this effect should be mainly contributed to an increase in conversion rate of organics into biogas by anaerobic bacteria, and how much cavitation increases the total biogas yield. An increase in yield is only the case if cavitation can further disrupt otherwise inaccessible cell membrane structures and ...

  8. Appraisal of domestic biogas plants in Bangladesh

    Kabir, H.; Palash, M S; Bauer, S

    2012-01-01

    Bangladesh. Biogas activities in Bangladesh have been expanding to meet the needs of alternative energy sources and reduce of the country dependence on biomass energy. Biogas is viewed an innovative and most promising option toward a partial mitigation of the existing energy problems in Bangladesh. This study examined the cost-capacity relationships of biogas plant use while considering the financial and economic feasibility with several decision making tools. Data were collected from 150 sma...

  9. Biogas Filter Based on Local Natural Zeolite Materials

    Satriyo Krido Wahono

    2014-02-01

    Full Text Available UPT BPPTK LIPI has created a biogas filter tool to improve the purity of methane in the biogas. The device shaped cylindrical tube containing absorbent materials which based on local natural zeolite of Indonesia. The absorbent has been activated and modified with other materials. This absorbtion material has multi-adsorption capacity for almost impurities gas of biogas. The biogas  filter increase methane content of biogas for 5-20%. The biogas filter improve the biogas’s performance such as increasing methane contents, increasing heating value, reduction of odors, reduction of corrosion potential, increasing the efficiency and stability of the generator.

  10. Dry-Wet Fermentation for Biogas Production

    Ahlhaus, M; Barz, M; Vogel, T.

    2008-01-01

    At present biogas plants produce biogas mainly from slurry by liquid fermentation. But the low substrate digestation of herbaceous biomass by liquid fermentation permits to use only a low amount of herbaceous biomass. Since April 2007 the collaborative project entitled “Development of a combined dry-wet fermentation process to produce biogas from herbaceous biomass substrates” is conducted at the Laboratory for Integrated Energy Systems of the University of Applied Sciences in ...

  11. Risk assessment of biogas in kitchens

    Leroux, Carole; Modelon, Hugues; Rousselle, Christophe; Bellenfant, Gaël; Ramalho, Olivier; Jaeg, Jean-Paul; Zdanevitch, Isabelle; Naja, Ghinwa M.

    2009-01-01

    The health risk associated with human exposure to pollutants while using biogas for cooking was assessed following the methodology described by the US - National Research Council. Information of hazardous compounds and compositions of several biogas types were extracted from scientific literature. Compositions were dependent on the biogas origin (production process). First, a quantitative approach was conducted to identify substances with a high health risk based on their Human Toxicity Value...

  12. ORGANIC WASTE USED IN AGRICULTURAL BIOGAS PLANTS

    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.

  13. ORGANIC WASTE USED IN AGRICULTURAL BIOGAS PLANTS

    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.

  14. Comparative Studies on Methane Upgradation of Biogas by Removing of Contaminant Gases Using Combined Chemical Methods

    Muhammad Rashed Al Mamun

    2015-07-01

    Full Text Available Biogas, which generated from renewable sources can be used as a sustainable energy to achieve resourceful targets of biofuel for internal combustion engines. This process can be achieved in combined absorption and adsorption chemical way. This method can be employed by aqueous solutions of calcium hydroxide, activated carbon, iron(II chloride, silica gel and sodium sulfate respectively. The presence of CO2, H2S and H2O in the biogas has lowering the calorific value and detrimental corrosion effects on the metal components. Removal of these contaminants from the biogas can therefore significantly improve the gas quality. A comparison study was investigated using combined chemical methods of improving the calorific value of biogas. Experiment results revealed that the aqueous solution used effectively in reacting with CO2 in biogas (over 85-90% removal efficiency, creating CH4 enriched biogas. The removal efficiency was the highest in method 1, where efficiency results were 91.5%, 97.1% and 91.8%, for CO2, H2S, and H2O, respectively. The corresponding CH4 enrichment was 97.5%. These results indicate that the method 1 is more suitable compare to method 2. However, both methane enrichment processes might be useful for cleaning and upgrading methane quality in biogas.

  15. Biogas production from cattle manure by anaerobic digestion

    Full text: In order to deal with the energy shortage problem, we are searching for more alternative energy resources especially renewable or sustainable. Biogas is one of the solutions in dealing with the energy shortage problem. Biogas is a type of energy resources derives from organic matter during the process called anaerobic digestion. The biogas produced is mainly consisting of methane and carbon dioxide. In this research, diluted cattle manure (1:1 ration with water) was inoculated with palm oil mill (POME) activated sludge at the ratio of 1:5 and placed in a 10 liter bioreactor. The temperature and pH in the bioreactor was regulated at 6.95 and 53 degree Celsius, respectively to enhance the anaerobic digestion process. Parameters such as chemical oxygen demand, biochemical oxygen demand, total solid, volatile solid, ammonia nitrogen (NH3-N), methane (CH4) and the volume of biogas generated was monitored for effectiveness of the treatment of cattle manure via anaerobic digestion. The total volume of biogas produced in this study is 80.25 liter in 29 days while being able to treat the COD content up to 52 %. (author)

  16. Biogas from farms will be tomorrow's fuel

    This final report for the Swiss Federal Office of Energy presents the results of a preliminary study on the technical, logistical and economic possibilities of agricultural biogas production for use as motor fuel. The study was made for a geographically limited region in the Swiss Canton of Lucerne. The reason for the choice of this area - which exhibits a high density of cattle and fowl - and its high potential for the production of biogas from animal excrements are discussed. The economic viability of three possible variants of biogas usage are discussed - its use as a fuel for electricity generation, the processing of the biogas and its injection into the natural gas mains and storage of the biogas in compressed-gas cylinders. Also, the relevance of biogas production in terms of environmental protection is emphasised - ammonia emissions from liquid manure poses a serious problem for the region. Further, political and market development aspects are discussed

  17. The commercialization of biogas production

    Currently there are ten large collective biogas plants and ten smaller farm plants operating in Denmark. During the last five years, biogas technology has undergone extensive technological development. The developmental process is supported by a public R and D programme and a follow-up programme for full-scale demonstration plants. Most plants still need considerable income increases before a final conclusion can be reached as to whether it is possible to achieve a profit from a corporate economic viewpoint. All plants have received investment grants. Gas production is in most cases reliable, especially due to the admixture of easily convertible organic waste as a supplement to the slurry supplies. Profitable collective biogas plants are within reach, even without investment grants. The total intake of biomass must be supplemented by 10 to 25 per cent easily convertible organic waste so that the minimum gas production reaches 30 to 35 m3 per m3 of biomass. Plants based solely on animal manure are not profitable. Energy from the biogas has to be sold at prices corresponding to consumer prices, which include Danish energy taxes. Collective biogas plants in Denmark appear to be approaching a commercial breakthrough. The concept of a collective biogas plant has been developed to address the energy-related, environmentally-related and agricultural problems. (AB)

  18. Energy from whey - comparison of the biogas and bioethanol processes; Energie a partir de petit-lait : comparaison des filieres biogaz et bioethanol

    Fruteau de Laclos, H.; Membrez, Y. [Erep SA, Aclens (Switzerland)

    2004-07-01

    This final report for the Swiss Federal Office of Energy (SFOE) presents the results of a project which investigated how energy could be generated from the whey produced in the cheese-making process. The first part of the project aimed to validate a concept for on-site production and use of biogas at a medium-sized cheese factory. The results of the first step, an experimental study carried out using a down-flow fixed-film bio-reactor, are discussed. This allowed the determination of the optimal working parameters as well as providing an estimate of the performance of the process. The second part of the project aimed to compare the bio-ethanol and biogas production processes. It was carried out in collaboration with AlcoSuisse and the Energy Systems Laboratory at the Swiss Federal Institute of Technology (EPFL) in Lausanne. The results of a life-cycle assessment (LCA) are discussed, which compared the two processes from an environmental point of view. Here, two impacts were considered: fossil fuel consumption and greenhouse effect. The replacement of fuel-oil with biogas for heat production and the replacement of conventional petrol with mixture including 5% bio-ethanol were examined. The results are presented that show that there was no significant difference between the two processes. According to the authors, the treatment of one cubic meter of cheese-whey allows savings of more than 20 litres of oil equivalent and 60 kg of CO{sub 2} emissions.

  19. Effects of various LED light wavelengths and intensities on microalgae-based simultaneous biogas upgrading and digestate nutrient reduction process.

    Zhao, Yongjun; Wang, Juan; Zhang, Hui; Yan, Cheng; Zhang, Yuejin

    2013-05-01

    Biogas is a well-known, primary renewable energy source, but its utilizations are possible only after upgrading. The microalgae-based bag photo-bioreactor utilized in this research could effectively upgrade biogas and simultaneously reduce the nutrient content in digestate. Red light was determined as the optimal light wavelength for microalgae growth, biogas upgrading, and digestate nutrient reduction. In the range of moderate light intensities (i.e., 800, 1200, 1600, and 2000 μmol m(-2) s(-1)), higher light intensities achieved higher biogas upgrade and larger digestate nutrient reduction. Methane content attained the highest value of 92.74±3.56% (v/v). The highest chemical oxygen demand, total nitrogen, and total phosphorus reduction efficiency of digestate were 85.35±1.04%, 77.98±1.84%, and 73.03±2.14%, respectively. Considering the reduction and economic efficiencies of the carbon dioxide content of biogas and digestate nutrient as well as the biogas upgrading standard, the optimal light intensity range was determined to be from 1200 to 1600 μmol m(-2) s(-1). PMID:23567717

  20. Biogas barometer; barometre biogaz

    Anon.

    2010-11-15

    The biogas sector has never before aroused so much attention as it does today. Elected officers and investors' interest has been fired by the gradual introduction of regulatory restrictions on the treatment of organic waste and the renewable energy commitments recently made by the European Union Member States. The biogas sector is gradually deserting its core activities of waste cleanup and treatment and getting involved in energy production, with so much enthusiasm that in some countries its scope of action has extended to using energy crops. Across the European Union, the sector's progress is as clear as daylight, as in 2009, primary energy growth leapt by a further 4.3 per cent. (author)

  1. Start-up strategies in manure-fed biogas reactors: Process parameters and methanogenic communities

    Four start-up strategies were assayed in 75 dm3 continuous stirred-tank reactors to select the optimal conditions for the start-up of the demonstration BIO4GAS® plant. Two reactors were completely filled with manure and their temperature increased from 20 to 37 °C at either a slow or fast rate. The other two reactors were started at 37 °C with a seed sludge from a stably operating plant and their load (cattle manure) increased at a low or high rate. Reactor performance was monitored for 35 days. The composition and abundance of the methanogenic communities was determined using a phylogenetic microarray and quantitative PCR. All reactors performed successfully in terms of biogas production and experienced a steady start-up, with pH values above 7.3 and VFA/alkalinity ratios below 0.3, denoting stability. Similar methanogenic loads (averaging 5 × 107 g-1 of 16S rRNA gene copies) were detected in the cattle manure and seed sludge, however the methanogenic diversity was higher in the manure with dominance of Methanosarcina and subdominance of Methanocorpusculum and Methanobrevibacter. Starting-up the reactors with an initial full load of manure and progressively increasing the temperature entailed less changes in the sludge chemical environment and in the dynamics of the dominant methanogens. Using a rate of temperature increase of 0.61 K d−1 proved better than1.21 K d−1 with a methane yield of 103.8 dm3 kg−1 VS and a COD mass removal efficiency of 28.3%. The diverse methanogenic community in the manure easily adapted to reactor upsets due to forced overload conditions. - Highlights: • Cattle manure holds abundant and diverse methanogenic communities. • CSTRs can be started up without seed, but manure and a slow temperature rise. • This warrants a smooth start-up in terms of performance and community dynamics. • Methanogenic communities in such reactors withstand upsets due to overload conditions

  2. Yield and Quality of Biogas from Anaerobic Fermentation of Grass

    Poláček, Jan

    2014-01-01

    Biogas is generally considered as a renewable source of energy. In fact, however, it is biodegradable organic material, that makes this source of energy renewable. Biogas is, then, the final product of anaerobic fermentation of these materials. Because energetically the most valuable component of biogas is methane (CH4) its relative volume stands as the measure of biogas quality. The process of anaerobic fermentation was characterized in the first part of this thesis. Organic materials ar...

  3. The progress and prospects of rural biogas production in China

    Biogas production is an important aspect of China's energy strategy. After decades’ application and research, China biogas has achieved considerable accomplishments. This study presents the progress and prospect of biogas technologies and industry in China. Two biogas patterns exist in China, that is, household-scaled digester for scattered farmers and biogas plant for centralized biogas production. Household-scaled digester which is simple and practical has been widely used and fully developed. Biogas plants have being sprung up with different materials, process and biogas utilization technologies. By the end of 2010, 38.51 million household-scaled digesters, and 27,436 large- and medium-scaled biogas plants for agricultural wastes were built. The calculation result of biogas potential from agricultural wastes shows that those used raw materials account for only 1.90% of the total availability. Chinese government promulgated several laws and policies, and gave financial supports to promote the development of biogas. However, some problems such as inferior equipment technology, imperfect policy incentive hamper its wide application and promotion. With the rapid development of economy and the improvement of rural living condition, China biogas industry is expected to advance toward orientation of scalization, industrialization and commercialization. - Highlights: ► Developing progress of biogas production in China is evaluated comprehensively. ► Status of biogas industrialization is estimated. ► New problems which occurred during rural biogas construction were analyzed. ► Biogas production potentials from agricultural wastes in China were calculated. ► Prospect of China rural biogas is expected.

  4. Biogas plant in Järna

    Schäfer, Winfried; Granstedt, Artur; Evers, Lars

    2005-01-01

    The Biodynamic Research Institute in Järna developed an on-farm biogas plant integrated within the highly self-supporting farm organism, Skilleby-Yttereneby, one of the farms studied in the BERAS project. The biogas plant digests dairy cattle manure and organic residues originating from the farm and the surrounding food processing units.

  5. Parameter estimation and long-term process simulation of a biogas reactor operated under trace elements limitation

    Highlights: • Estimation of ADM1 parameter uncertainty by nonlinear, correlated parameter analysis. • Unbounded confidence regions were obtained for single hydrolysis rate constants. • ADM1 carbohydrates were divided into a slowly and readily degradable part. • Bioavailability of trace metals explained discrepancies between modeled and measured data. - Abstract: The Anaerobic Digestion Model No. 1 (ADM1) was modified to describe the long-term process stability of a two-stage agricultural biogas system operated for 494 days with a mono-substrate. The ADM1 model fraction for carbohydrates was divided into a slowly and readily degradable part. Significant different hydrolysis rate constants were found for proteins and single fractions of carbohydrates in batch experiments. Degradation of starch, xylan (hemicellulose), cellulose and zein (protein) were modeled with first order hydrolysis rate coefficients of 1.20 d−1, 0.70 d−1, 0.18 d−1 and 0.30 d−1, respectively. While the hydrolysis rate coefficients found in batch experiments could be used for predicting continuous process data, the statistically calculated confidence regions (nonlinear parameter estimation) showed that the upper limits were unbounded. Single discrepancies between measured and modeled process data of the two-stage pilot system could be explained by the lack of bioavailability of trace elements. Addition of iron, as Fe(III)Cl3, allowed stable process conditions for an organic loading rate (OLR) up to 2.5 gVS L−1 d−1. Additional supplement of trace elements was necessary for process operation at OLRs above 2.5 gVS L−1 d−1

  6. Informing international UNFCCC technology mechanisms from the ground up: Using biogas technology in South Africa as a case study to evaluate the usefulness of potential elements of an international technology agreement in the UNFCCC negotiations process

    Transfer of low carbon technologies to developing countries is 1 approach for tackling rising global emissions. An international technology transfer mechanism has been proposed under the UNFCCC; however, it remains unclear how this international mechanism would translate into local level technology implementation. This study uses biogas technology in South Africa to obtain empirical data inductively related to technology transfer. Observations and activities specific to the biogas sector in South Africa are put forward based on site visits and stakeholder discussions in South Africa, the UK, Germany and Sweden. This paper presents empirical findings on technology transfer in the biogas sector in South Africa and analyses the role of an international technology mechanism in supporting the uptake of biogas. Many of the barriers to biogas technology in South Africa are national level constraints such as lack of supportive policy environment, financial incentives and information sharing. This case study supports the argument that it will be unrealistic for international technology mechanisms to capture the necessary specificities of individual technologies at a country level. Therefore, as demonstrated through the example of biogas technology in South Africa, there is a need for both effective national and international engagement to support technology implementation. - Highlights: ► The UNFCCC technology mechanism aims to increase low carbon technology deployment. ► The interface of global technology frameworks and national implementation is unclear. ► Biogas is a widely used technology yet its uptake in South Africa (SA) is minimal. ► Empirical data is gathered from biogas sites in SA, UK, Germany and Sweden. ► Findings show biogas uptake in SA requires national and international support

  7. The control of H2S in biogas using iron ores as in situ desulfurizers during anaerobic digestion process.

    Zhou, Qiying; Jiang, Xia; Li, Xi; Jiang, Wenju

    2016-09-01

    In this study, five kinds of iron ores, limonite, hematite, manganese ore, magnetite and lava rock, were used as the in situ desulfurizers in the anaerobic digestion reactors to investigate their effects on controlling H2S in biogas. The results show that the addition of the five iron ores could significantly control the content of H2S in biogas, with the best performance for limonite. As limonite dosages increase (10-60 g/L), the contents of H2S in biogas were evidently decreased in the digesters with different initial sulfate concentrations (0-1000 mg/L). After the anaerobic digestion, the removed sulfur was mostly deposited on the surface of limonite. A possible mechanism of H2S control in biogas by limonite was proposed preliminarily, including adsorption, FeS precipitation, and Fe (III) oxidation. The results demonstrated that limonite was a promising in situ desulfurizer for controlling H2S in biogas with low cost and high efficiency. PMID:27209038

  8. Technical improvements with biogas plants

    Perwanger, A.

    In theory and practice, science aims at smooth operation of biogas plants at a good cost/benefit ratio by improving plant design and introducing more effective process techniques. For several years now, experience gained with the construction and operation of over 40 biogas plants are evaluated at the Landtechnik Weihenstephan in co-operation with manufacturing companies and committed farmers. By means of elementary drawings, 10 differently designed biogas plants are explained in greater detail concerning their technical features (structure, efficiency, function) which comprise, too, a through-flow facility, separate gasometer, mechanical stirrer, construction and refitting of such plants by the user, a rotary reactor floating in a water tank, a small-sized gas cupola and a flexible foil hood. With optimum process technology, there are still some issues left unanswered like e.g. suitable process temperature and intensity of stirrer.

  9. Biogas from by-products; Biogas aus Nebenprodukten

    Mack, Andreas [Eisenmann Anlagenbau GmbH und Co. KG, Boeblingen (Germany)

    2013-01-15

    The Italian sugar producer Co.Pro.B. (Minerbio, Italy) looked for an industrially experienced plant engineer for the biogas process in order to utilize energetically the by-products from the processing of sugar beets. Co.Pro.B. found the German environmental technology specialist Eisenmann Anlagenbau GmbH and Co. KG (Boeblingen, Federal Republic of Germany). After a planning and building period of only six months, even three biogas plants with plug-flow fermentation were brought on line in the provinces Bologna and Padua in autumn 2012.

  10. Biogas desulfurization with a new developed doped activated carbon. 20 month pilot test; Biogasfeinentschwefelung mittels neu entwickelter dotierter Aktivkohle. 20-monatiger Praxistest

    Rossow, Silvana; Deerberg, Goerge; Goetze, Toralf; Kanswohl, Norbert; Nelles, Michael [Univ. Rostock (Germany). Lehrstuhl fuer Abfall- und Stoffstromwirtschaft

    2009-05-15

    Doped activated carbon is a special developed activated carbon for the desulfurization of technical gases. Based on its special adsorption properties, it is able to bond a large amount of hydrogen sulfide. By the special manufacturing method it was possible to optimize further the performance for the desulfurization of gases. In a biogas plant with an installed electric capacity of 2 MW the functionality of the doped activated carbon was proofed in a real biogas stream in a 20 month pilot test. The activated carbon was used in a special adsorption system that was tunes on the requirement of the activated carbon and on the site of installation. Because the biogas plant was in the starting period, all the time there were variable operation conditions. In spite of the variable conditions the doped activated carbon shows a permanent complete desulfurization, as in the executed laboratory experiments. By the use of the desulfurization system the concentration of hydrogen sulfide is decreased less than 1 ppm. The prejudices with are often caused by hydrogen sulphide could not identify until now. A positive evidence of the excellent desulfurization is the doubling of the oil lifetime of the block heating station. (orig.)

  11. Biogas upgrading to biomethane. Proceedings; Biogasaufbereitung zu Biomethan. Tagungsband

    NONE

    2008-12-05

    Within the 6th Hanauer Dialogue 'Biogas upgrading to biomethane' at 21st February, 2008, the following lectures were held: (a) Processing of biogas - an introduction (Michael Beil); (b) The climate protecting targets of the Federal Republic of Germany: Which role will play the upgrading of biogas, and which legal boundary conditions are created by the Federal Government? (Uwe Holzhammer); (c) Future strategy: CH{sub 4} grids (Juergen Schmid); (d) Biogas upgrading and biomethane utilization in Sweden (Anneli Petersson); (e) Biogas upgrading and utilization of bio methane in Switzerland (Arthur Wellinger); (f) Biogas upgrading by means of pressure swing adsorption (Alfons Schulte-Schulze Berndt); (g) Biogas upgrading by means of pressurized water washing (Ulf Richter); (h) Biogas upgrading for feeding in public grids. The case of biogas plant Bruck a.d. Leitha (Michael Harasek); (i) Biogas upgrading by means of chemical absorption according to the LP Cooab process (Jerome van Beek); (j) Practical experiences in unpressurized amine washing MT bio methane (Karsten Wuensche); (k) Biogas upgrading by means of organic physical washing with HAASE biogas amplifiers (Roland Kahn); (l) Upgrading using cryogenic technology; the GPP registered -system (Jeroen de Pater); (m) Micro Gas Distribution Systems: Alternatives to biogas upgrading and grid injection (Michael Beil, Bernd Krautkremer); (n) Feeding of exchange gas. The case of project Straelen and Kerpen (Frank Schaefer); (o) Feeding of biogas from the view of grid operators (Norbert Nordmeyer); BIOGASMAX: Biogas as Vehicle Fuel - Market Expansion to 2020 Air Quality (Michael Beil, Uwe Hoffstede); (p) Study: Feeding of biogas into the natural gas distribution system (Fachagentur Nachwachsende Rohstoffe).

  12. Evaluation of biogas of waste from poultry

    Most of the farms, the waste of agricultural production do not receive adequate treatment for the stabilization of organic matter and reduce its pollution potential. The anaerobic digestion is an alternative for the treatment of waste, as well as allowing the reduction of pollution potential and the health risks of waste to a minimum, promotes the generation of biogas used as a heat source for various uses on the farm. Thus, the aim of this work was to evaluate the biogas production efficiency from the chicken waste. For the supply of biodigesters, adopted the total solids content of 8% and discontinuous supply system. The biogas potential was determined on the basis of their daily production and explosive rate. It was observed that the biogas production started 24 hours after the start of supplying the digesters. The maximum biogas production was approximately 0.87 L after the ninth and the 54th day starting the digestion process. The average daily production of biogas generated from bird manure was 0.022 L, while the cumulative 0.91 L after 72 days of digestion. The explosive rate of biogas generated by poultry origin residues peaked at 51% after 32 days of the start of the digestion process. In this analysis, we found the presence of methane in the biogas produced in all substrates tested after 24 h of digestion, because it’s burning in the presence of an ignition source (Fire). (full text)

  13. Critical evaluation of substitution of natural gas by biogas

    Biogas use in Germany's distribution grid is regulated by the federal integrated energy and climate program. The key measures that influence the biogas feed-in include core regulation; changes to the act grating feed-in preference for electricity generated from renewable energies; regulation for heat supply from renewable energies; and regulations regarding biofuels. A critical evaluation of substitution of natural gas by biogas was presented. Specific topics that were discussed included aims and measures; potential; usage pathways for biogas; efficiency criteria of usage pathways; and location analysis. The presentation also discussed the parameters of raw biogas and regular distribution grid; a process chain for biogas upgrading; and criteria for process evaluation. It was concluded that costs and environmental relevance of biogas-processing can be compared over the complete life cycle for various pathways and configurations. This represented an excellent and very flexible planning tool. Subsidies and related measures could be focussed on the most efficient pathways. tabs., figs.

  14. New Networks for Biogas

    Eekelen, R. van [Kiwa Gas Technology B. V., Apeldoorn (Netherlands)

    2012-06-15

    The study of 'New Networks for Biogas' main goal is to reduce the uncertainties associated with the design choices for biogas network configurations. Supplementary to the objective an overview of the state-of-the-art on the design, operations and maintenance of biogas networks in Europe is given.

  15. Integrated rural industrialization through biogas

    Role of biogas in rural industrialization in India is explained. The Khadi and Village Industries Commission has installed over 2 lakhs (0.2 million) biogas plants during the last 30 years. A 15 cu.m. capacity plant costs Rs. 35,000/-. It produces 65 tons bio-manure worth Rs. 13,000/- in a year and fuel gas equivalent to 3,285 litres of kerosene worth Rs. 9855/-. It provides employment to 300 man days. In addition to serving as a source of energy and manure, it reduces deforestation, solves rural sanitation problem and maintain environmental equilibrium. Industrial activities suitable for rural areas and which can use biogas as a source of power are indicated. (M.G.B.)

  16. Geodetic works in the process of planning and constructing a biogas plant

    Hajdenek, Lidija

    2011-01-01

    Land surveying plays an important role in the process of building constructions. Apart from providing geodetic plans, land surveying also manages procedures that are necessary for the real estate data recording. At the same time the legislation of land survey services needs to be followed, because the changes of legislation consequently play the role in land surveying in the process of building construction. The land surveying works must be carried out with high quality, because they present ...

  17. Study of the Process of Hydraulic Mixing in Anaerobic Digester of Biogas Plant

    Karaeva Julia V.

    2015-03-01

    Full Text Available Two systems of hydraulic mixing in a vertical cylindrical anaerobic digester: standard and modernised are discussed in the paper. Numerical investigations that were carried out are focused on a study of hydrodynamic processes in an aerobic digester using two various systems of hydraulic mixing as well as on analysis of the efficiency of methane fermentation process accomplished under different geometric parameters of an anaerobic digester and systems of hydraulic mixing.

  18. Biogas from lignocellulosic biomass

    Berglund Odhner, Peter; Schabbauer, Anna [Grontmij AB, Stockholm (Sweden); Sarvari Horvath, Ilona; Mohseni Kabir, Maryam [Hoegskolan i Boraas, Boraas (Sweden)

    2012-01-15

    Grontmij AB has cooperated with the University of Boraas to evaluate the technological and economical possibilities for biogas production from substrates containing lignocellulose, such as forest residues, straw and paper. The state of knowledge regarding biogas production from cellulosic biomass has been summarized. The research in the field has been described, especially focusing on pretreatment methods and their results on increased gas yields. An investigation concerning commercially available pretreatment methods and the cost of these technologies has been performed. An economic evaluation of biogas production from lignocellulosic materials has provided answers to questions regarding the profitability of these processes. Pretreatment with steam explosion was economically evaluated for three feedstocks - wood, straw and paper - and a combination of steam explosion and addition of NaOH for paper. The presented costs pertain to costs for the pretreatment step as it, in this study, was assumed that the pretreatment would be added to an existing plant and the lignocellulosic substrates would be part of a co-digestion process. The results of the investigation indicate that it is difficult to provide a positive net result when comparing the cost of pretreatment versus the gas yield (value) for two of the feedstocks - forest residues and straw. This is mainly due to the high cost of the raw material. For forest residues the steam pretreatment cost exceeded the gas yield by over 50 %, mainly due to the high cost of the raw material. For straw, the production cost was similar to the value of the gas. Paper showed the best economic result. The gas yield (value) for paper exceeded the pretreatment cost by 15 %, which makes it interesting to study paper further.

  19. A review of chemical absorption of carbon dioxide for biogas upgrading

    Fouad RH Abdeen; Maizirwan Mel; Mohammed Saedi Jami; Sany Izan Ihsan; Ahmad Faris Ismail

    2016-01-01

    Significant attention has been given to biogas production, purification and upgrading as a renewable and clean fuel supplement. Biogas is a product of an anaerobic digestion process comprising methane, carbon dioxide, and trace amounts of other gases. Biogas purification removes trace gases in biogas for safe utilisation. Biogas upgrading produces methane-rich biogas by removing bulk carbon dioxide from the gas mixture. Several carbon dioxide removal techniques can be applied for biogas upgrading. However, chemical absorption of carbon dioxide for biogas upgrading is of special significance due to its operation at ambient or near ambient temperature and pressure, thus reducing energy consumption. This paper reviews the chemical absorption of carbon dioxide using amine scrubbing, caustic solvent scrubbing, and amino acid salt solution scrubbing. Each of these tech-niques for biogas upgrading is discussed. The paper concludes that an optimised implementation of the chemical absorption techniques for biogas upgrading requires further research.

  20. Investigation of thermal integration between biogas production and upgrading

    Highlights: • Identify thermal characteristics of amine-based biogas upgrading for waste heat recovery. • Identify thermal characteristics of AD biogas production as sink for heat recovery. • Evaluation of thermal integration between biogas production and upgrading to improve overall energy efficiency. • Cost analysis applied for the economic feasibility of the thermal integration. • Using the principles of target design and system integration for connected thermal processes. - Abstract: Thermal integration of anaerobic digestion (AD) biogas production with amine-based chemical absorption biogas upgrading has been studied to improve the overall efficiency of the intergraded system. The thermal characteristics have been investigated for industrial AD raw biogas production and amine-based chemical absorption biogas upgrading. The investigation provides a basic understanding for the possibilities of energy saving through thermal integration. The thermal integration is carried out through well-defined cases based on the thermal characteristics of the biogas production and the biogas upgrading. The following factors are taken into account in the case study: thermal conditions of sub-systems, material and energy balances, cost issues and main benefits. The potential of heat recovery has been evaluated to utilise the waste heat from amine-based upgrading process for the use in the AD biogas production. The results show that the thermal integration has positive effects on improving the overall energy efficiency of the integrated biogas plant. Cost analysis shows that the thermal integration is economically feasible

  1. Integrated extraction and anaerobic digestion process for recovery of nutraceuticals and biogas from pomegranate marcs

    Pomegranate marc (PM), a by-product from pomegranate juice processing, has not been effectively utilized. The objectives of this study were to (1) determine the yields and properties of antioxidants (henceforth referring to total phenolics in terms of tannic acid equivalent) and oil extracted from v...

  2. Process model for ammonia volatilization from anaerobic swine lagoons incorporating varying wind speeds and biogas bubbling

    Ammonia volatilization from treatment lagoons varies widely with the total ammonia concentration, pH, temperature, suspended solids, atmospheric ammonia concentration above the water surface, and wind speed. Ammonia emissions were estimated with a process-based mechanistic model integrating ammonia ...

  3. Numerical investigation of biogas flameless combustion

    Highlights: • Fuel consumption decreases from 3.24 g/s in biogas conventional combustion to 1.07 g/s in flameless mode. • The differences between reactants and products temperature intensifies irreversibility in traditional combustion. • The temperature inside the chamber is uniform in biogas flameless mode and exergy loss decreases in this technique. • Low O2 concentration in the flameless mode confirms a complete and quick combustion process in flameless regime. - Abstract: The purpose of this investigation is to analyze combustion characteristics of biogas flameless mode based on clean technology development strategies. A three dimensional (3D) computational fluid dynamic (CFD) study has been performed to illustrate various priorities of biogas flameless combustion compared to the conventional mode. The effects of preheated temperature and wall temperature, reaction zone and pollutant formation are observed and the impacts of combustion and turbulence models on numerical results are discussed. Although preheated conventional combustion could be effective in terms of fuel consumption reduction, NOx formation increases. It has been found that biogas is not eligible to be applied in furnace heat up due to its low calorific value (LCV) and it is necessary to utilize a high calorific value fuel to preheat the furnace. The required enthalpy for biogas auto-ignition temperature is supplied by enthalpy of preheated oxidizer. In biogas flameless combustion, the mean temperature of the furnace is lower than traditional combustion throughout the chamber. Compared to the biogas flameless combustion with uniform temperature, very high and fluctuated temperatures are recorded in conventional combustion. Since high entropy generation intensifies irreversibility, exergy loss is higher in biogas conventional combustion compared to the biogas flameless regime. Entropy generation minimization in flameless mode is attributed to the uniform temperature inside the chamber

  4. Energy use of biogas hampered by the presence of siloxanes

    Siloxanes are widely used in industrial processes and consumer products. Some of them reach the wastewater. Siloxanes are not decomposed in the activated sludge process and partly concentrate in the sludge. During anaerobic digestion of the sludge, they volatilise into the formed biogas. Combustion of silicon containing gases, e.g., when producing electricity, produces, however, the abrasive microcrystalline silica that has chemical and physical properties similar to those of glass and causes serious damage to gas engines, heat exchangers and catalytic exhaust gas treatment systems. The growing consumption of silicones and siloxanes and the subsequent increased concentration in wastewater, together with the increasing interest in the production of biogas and 'green energy' in sewage treatment plants, has created significant concern about the presence of siloxanes and the related damage (fouling etc.) in the biogas beneficiation equipment. The present paper, therefore, reviews the fundamentals of siloxanes and the current problems of the associated fouling. Moreover, it summarizes the useable methods for siloxane abatement from biogas and makes some recommendations towards preventive actions

  5. Co-digestion of manure and whey for in situ biogas upgrading by the addition of H2: process performance and microbial insights

    Luo, Gang; Angelidaki, Irini

    2013-01-01

    the biogas composition. The best biogas composition (75:6.6:18.4) was obtained at stirring speed 150 rpmand using ceramic diffuser, while the biogas in the control reactor consisted of CH4 and CO2 at a ratio of 55:45. The consumed hydrogen was almost completely converted to CH4, and there was no...

  6. Diffusion of the technology of the biogas in Colombia: Documentation of the Project. Cali (CO)

    The manual shows the general limits and considerations that should be kept in mind to implement the systems of biogas production in the Colombian rural zones. In this project they participated the Regional Autonomous Corporation of the Cauca C.V.C., the German Society of Technical Cooperation GTZ and the consultant German signature Dekotup; society for Adapted Technologies in Areas in Development Ltda. The importance of the biogas systems like technology adapted by the advantages is shown: they Reduce the danger and the contamination of the residuals payees of germs pathogens, they eliminate the unpleasant scent of the waste, they don't produce imbalance in the ecosystem and eat non by-product an effluent it is obtained with high properties bio fertilizing. Initially it is described the phases of the process of fermentation: hydrolysis, acidification and methanization, the types of biogas plants are described used floating bell, fixed dome and the ball plant; the methods for the planning and the design of the plants as well as the dimensions. It is presented a classic example of the design and construction of a plant. It is included the composition of the biogas and their use forms. The different biogas plants are shown that were built and those that were in project; the use of effluents of gas like bio-fertilizer, the form of determining the activities for the popularization of the biogas technology

  7. ANAEROBIC DIGESTION MODEL ANALYSIS OF THE FERMENTATION PROCESS IN PSYCHROPHILIC AND MESOPHILIC CHAMBER IN ACCORDANCE WITH THE AMOUNT OF BIOGAS SOURCED

    Dariusz Zdebik

    2015-03-01

    Full Text Available The paper presents problems concerning the modelling of anaerobic sludge stabilization, with the additional substrate (waste transported, dairy butchery sewage in psychrophilic fermentation conditions in the range 10–20 °C and mesophilic at 35 °C. Simulation test was conducted in the two digesters. Results of the study allowed to evaluate the effectiveness of conducting these processes in separate chambers, i.e. the psychrophilic and mesophilic chamber. During the simulations, terms of obtaining volatile fatty acids and biogas in conjunction with the operating conditions of the chambers indicated.

  8. Replacing Natural Gas by Biogas — Determining the Bacterial Contamination of Biogas by PCR

    Jiřina Čermáková

    2012-01-01

    Full Text Available A promising way of using biogas is to upgrade it to natural gas, which is referred to as Substitute Natural Gas (SNG or biomethane. Biomethane, or biogas, is produced by biological processes of harnessing the ability of microorganisms to degrade organic material to methane. Some of the microorganisms are aerosolized from the digester into the biogas; afterwards a bio-film is formed that attaches to the surfaces of the distribution pipes, and can find it was to the place where the end use of biogas takes place. This paper deals with the detection of microbial species in biogas, their influenceon corrosion and the potential risk that diseases can be spread via biogas using molecular techniques. Using molecular methods, we found that raw biogas contains about 8 million microorganisms per m3, which is most likely the result of microbial transmission from the anaerobic digestion process. Some bacterial species may contribute to the corrosion of pipelines and equipment; others are opportunistic pathogens that can cause toxic reactions. However, most bacterial species, more than 40 % in biogas, are still unknown, as is their influence on the digestion process and on human health. Further studies are needed to better understand the behavior of microorganisms in anaerobic digestion and to preventmicrobial-influenced corrosion and microbial dissemination.

  9. Mathematical modelization of physical process of biogas migration in sanitary landfills of urban solid wastes; Modelizacion matematica del proceso fisico de migracion del biogas en vertederos controlados de R.S.U

    Maranon Maison, E.; Sastre Andres, H.; Martin Gonzalez, S.

    1997-09-01

    An analysis of the laws that govern the biogas movements inside the landfill is carried out. The mathematical equations needed to resolve the problem are studied. Then, a model is defined and used to calculate the biogas movements in several situations. The results obtained are contrasted with data from the bibliography and with tests carried out at the La Zoreda, Landfill (Asturias Spain). (Author) 11 refs.

  10. Bioelectrochemical treatment of table olive brine processing wastewater for biogas production and phenolic compounds removal.

    Marone, A; Carmona-Martínez, A A; Sire, Y; Meudec, E; Steyer, J P; Bernet, N; Trably, E

    2016-09-01

    Industry of table olives is widely distributed over the Mediterranean countries and generates large volumes of processing wastewaters (TOPWs). TOPWs contain high levels of organic matter, salt, and phenolic compounds that are recalcitrant to microbial degradation. This work aims to evaluate the potential of bioelectrochemical systems to simultaneously treat real TOPWs and recover energy. The experiments were performed in potentiostatically-controlled single-chamber systems fed with real TOPW and using a moderate halophilic consortium as biocatalyst. In conventional anaerobic digestion (AD) treatment, ie. where no potential was applied, no CH4 was produced. In comparison, Bio-Electrochemical Systems (BES) showed a maximum CH4 yield of 701 ± 13 NmL CH4·LTOPW(-1) under a current density of 7.1 ± 0.4 A m(-2) and with a coulombic efficiency of 30%. Interestingly, up to 80% of the phenolic compounds found in the raw TOPW (i.e. hydroxytyrosol and tyrosol) were removed. A new theoretical degradation pathway was proposed after identification of the metabolic by-products. Consistently, microbial community analysis at the anode revealed a clear and specific enrichment in anode-respiring bacteria (ARB) from the genera Desulfuromonas and Geoalkalibacter, supporting the key role of these electroactive microorganisms. As a conclusion, bioelectrochemical systems represent a promising bioprocess alternative for the treatment and energy recovery of recalcitrant TOPWs. PMID:27208920

  11. Biogas from algae, seaweed and seagrass?; Biogas aus Algen, Tang und Seegras?

    Schneider, Holger [Fachhochschule Flensburg (Germany)

    2011-07-01

    Algae, seaweed and sea grass are discussed again and again as alternative sources for raw materials for agricultural biogas plants. The author of the contribution under consideration reports on the identification and optimization of the biogas potential of microalgae, macroalgae and flotsam (mixture of seaweed, seaweed, and so on). Algae, seaweed and sea grass can be fermented into biogas by means of an anaerobic process. The specific yield of biogas is small. The processing of these substrates requires a technical adjustment of the biogas plants. Thus, the effective use of these substrates will continue to fall. The achievable benefit highly depends on the location of the facilities and on the available substrates with the corresponding specific gas yields. The economic efficiency of these substrates in agricultural systems must be examined in each case.

  12. Energy Efficiency Evaluation of two Biogas Plants

    Nordlander, Eva; Holgersson, Jenny; Thorin, Eva; Thomassen, Martin; Yan, Jinyue

    2011-01-01

    Anaerobic digestion for biogas production is a promising renewable energy technology whichcan be used to achieve environmental goals set in the European Union and other regions. Thereare however many improvements that can still be made to the process. Furthermore, there arealternative energy conversion processes that compete for some of the substrates used inanaerobic digestion. Energy efficiency could therefore be a tool for measuring and comparingthe performance of biogas plants. This study...

  13. Influence of trace substances on methanation catalysts used in dynamic biogas upgrading.

    Jürgensen, Lars; Ehimen, Ehiaze Augustine; Born, Jens; Holm-Nielsen, Jens Bo; Rooney, David

    2015-02-01

    The aim of this work was to study the possible deactivation effects of biogas trace ammonia concentrations on methanation catalysts. It was found that small amounts of ammonia led to a slight decrease in the catalyst activity. A decrease in the catalyst deactivation by carbon formation was also observed, with ammonia absorbed on the active catalyst sites. This was via a suppression of the carbon formation and deposition on the catalyst, since it requires a higher number of active sites than for the methanation of carbon oxides. From the paper findings, no special pretreatment for ammonia removal from the biogas fed to a methanation process is required. PMID:25316193

  14. Influence of trace substances on methanation catalysts used in dynamic biogas upgrading

    Jurgensen, Lars; Ehimen, Ehiazesebhor Augustine; Born, Jens;

    2015-01-01

    The aim of this work was to study the possible deactivation effects of biogas trace ammonia concentrations on methanation catalysts. It was found that small amounts of ammonia led to a slight decrease in the catalyst activity. A decrease in the catalyst deactivation by carbon formation was also...... observed, with ammonia absorbed on the active catalyst sites. This was via a suppression of the carbon formation and deposition on the catalyst, since it requires a higher number of active sites than for the methanation of carbon oxides. From the paper findings, no special pretreatment for ammonia removal...... from the biogas fed to a methanation process is required....

  15. BIOGAS STATIONS AND THEIR ENVIRONMENTAL IMPACTS

    Vladimir Lapčik

    2011-12-01

    Full Text Available The article summarizes the authors’ experience with environmental impact assessment in branch of biogas plants. The introductory part of the paper describes legislative obligations of the Czech Republic concerning the fulfilment of the European Union’s limits as for utilization of renewable energy resources. The next parts of the paper deal with an impact analysis of biogas plants on the environment. The final part of the paper deals with experience with implementation of the environmental impact assessment process in the field of biogas plants in the Czech Republic.

  16. Biogas, the renewable energy of territories

    A set of articles outlines the essential role of 'green gas' in energy transition, discusses the emergence of a European bio-methane sector with a standard harmonisation, proposes an interview of the person in charge of strategy and territories for GrDF who addresses the building up of operation rules for the biogas sector, comments various aspects of biogas financing, comments the relationships between heat, electricity and fuel within a rural project in Brittany, describes a project of extraction and use of methane from waste waters, and presents a process of liquefaction developed by Cryostar as a possible valorisation of biogas

  17. Analytical investigation of the thermal optimization of biogas plants

    The economic efficiency of biogas plants is more difficult to display with recent legal regulations than with bonus tariff systems of previous EEG amendments. To enhance efficiency there are different options, often linked with further investments. Direct technical innovations with fast economic yields need exact evaluation of limiting conditions. Within this article the heat sector of agricultural biogas plants is studied. So far scarcely considered, especially the improvement of on-site thermal energy consumption promises a high optimisation. Data basis are feeding protocols and temperature measurements of input substrates, biogas, environment etc., also documentations of on-site thermal consumption over 10 years. Analyzing first results of measurements and primary equilibrations shows, that maintenance of biogas process temperature consumes most thermal energy and therefore has the greatest potential of improvement. Passive and active insulation of feed systems and heat recovery from secondary fermenter liquids are identified as first optimization measures. Depending on amount and temperature raise of input substrates, saving potentials of more than hundred megawatt hours per year were calculated.

  18. Wood ash amendment to biogas reactors as an alternative to landfilling? A preliminary study on changes in process chemistry and biology.

    Podmirseg, Sabine M; Seewald, Martin S A; Knapp, Brigitte A; Bouzid, Ourdia; Biderre-Petit, Corinne; Peyret, Pierre; Insam, Heribert

    2013-08-01

    Wood ash addition to biogas plants represents an alternative to commonly used landfilling by improving the reactor performance, raising the pH and alleviating potential limits of trace elements. This study is the first on the effects of wood ash on reactor conditions and microbial communities in cattle slurry-based biogas reactors. General process parameters [temperature, pH, electrical conductivity, ammonia, volatile fatty acids, carbon/nitrogen (C/N), total solids (TS), volatile solids, and gas quantity and quality] were monitored along with molecular analyses of methanogens by polymerase chain reaction- denaturing gradient gel electrophoresis and modern microarrays (archaea and bacteria). A prompt pH rise was observed, as was an increase in C/N ratio and volatile fatty acids. Biogas production was inhibited, but recovered to even higher production rates and methane concentration after single amendment. High sulphur levels in the wood ash generated hydrogen sulphide and potentially hampered methanogenesis. Methanosarcina was the most dominant methanogen in all reactors; however, diversity was higher in ash-amended reactors. Bacterial groups like Firmicutes, Proteobacteria and Acidobacteria were favoured, which could improve the hydrolytic efficiency of the reactors. We recommend constant monitoring of the chemical composition of the used wood ash and suggest that ash amendment is adequate if added to the substrate at a rate low enough to allow adaptation of the microbiota (e.g. 0.25 g g(-1) TS). It could further help to enrich digestate with important nutrients, for example phosphorus, calcium and magnesium, but further experiments are required for the evaluation of wood ash concentrations that are tolerable for anaerobic digestion. PMID:23831776

  19. Progress in biogas. Biogas production from agricultural biomass and organic residues. Pt. 1 and 2. Proceedings (oral presentations and poster presentations); Fortschritt beim Biogas. Biogas aus landwirtschaftlicher Biomasse and organischen Reststoffen. T. 1 und 2. Tagungsband. Vortraege and Poster

    NONE

    2007-07-01

    Within the International Conference ''Progress in Biogas - Biogas production from agricultural biomass and organic residues'' at the University Hohenheim (Stuttgart, Federal Republic of Germany) from 18th to 21st September, 2007, the following lectures were held: (1) Global relevance and potential of bioenergy for regional development; (2) Biogas electricity for France feed-in tariff and some other things to know before entering French market; (3) Policy drivers and future prospects for on-farm anaerobic digestion in Northern Ireland; (4) Biogas in Belgium, a swot analysis; (5) Status and prospects of biogas energy use in Ukraine; (6) Recent developments in Chinese agricultural biogas production; (7) Opportunities for agricultural based biogas systems in the province of Ontario, Canada; (8) Pre-treatment and digestion of separated collected household waste in Sweden; (9) To the problem of monitoring measures and prophylaxis measures with the utilization of organic residual substances in biological gas facilities from hygienic view; (10) Fermenting residues from biological gas facilities - nutrients and pollutants, possibilities of application in the agriculture; (11) Treatment and utilization of fermentation residues; (12) Potential of residual gas of NaWaRo feeded biogas plants in Baden-Wuerttemberg; (13) Operating analytics of biogas plants to improve efficiency and to ensure process stability; (14) The potential of biogas and electric power production from subproducts in the sugar and alcohol industries by the application of anaerobic digestion; (15) Co-digestion plant in dairy cattle farm in Emilia Romagna region (Italy); (16) Facing operational problems in a biodigeser in Yuvientsa - Amazonian Region of Ecuador; (17) Biogas plant instead of milk cow - payment and occupation with the use of grassilage; (18) Biogas in ecologic agriculture - experiences from 3 years of fermentation of grass-clover ley; (19) Combined solar-biogas basis for the

  20. Improvement of Biogas Production by Bioaugmentation

    K. L. Kovács

    2013-01-01

    Full Text Available Biogas production technologies commonly involve the use of natural anaerobic consortia of microbes. The objective of this study was to elucidate the importance of hydrogen in this complex microbial food chain. Novel laboratory biogas reactor prototypes were designed and constructed. The fates of pure hydrogen-producing cultures of Caldicellulosiruptor saccharolyticus and Enterobacter cloacae were followed in time in thermophilic and mesophilic natural biogas-producing communities, respectively. Molecular biological techniques were applied to study the altered ecosystems. A systematic study in 5-litre CSTR digesters revealed that a key fermentation parameter in the maintenance of an altered population balance is the loading rate of total organic solids. Intensification of the biogas production was observed and the results corroborate that the enhanced biogas productivity is associated with the increased abundance of the hydrogen producers. Fermentation parameters did not indicate signs of failure in the biogas production process. Rational construction of more efficient and sustainable biogas-producing microbial consortia is proposed.

  1. Energy efficiency and sustainability of complex biogas systems: A 3-level emergetic evaluation

    Highlights: • The metabolism of complex biogas system increased from 2000 to 2008. • System renewability has been increased due to biogas utilization. • Electricity, diesels and infrastructure were the most efficient supplies. • All processes were challenged by high transformity and low sustainability. - Abstract: Biogas engineering and the biogas-linked agricultural industries as a whole has been used as both a developmental strategy for rural new emergy and an important part of renewable agriculture revolution in China. In this paper, we proposed a 3-level emergetic evaluation framework to investigate the energy efficiency and sustainability of a complex biogas system (CBS) in South China, comprising agro-industries such as planting, aquaculture, breeding and biogas. The framework is capable of tracking dynamical behaviors of the whole complex system (Level I), transformation processes (Level II) and resource components (Level III) simultaneously. Two new indicators, emergy contribution rate (ECR) and emergy supply efficiency (ESE) were developed to address the contribution and efficiency of resource components within each agro-industrial process. Our findings suggested the metabolism of the CBS were increased from 2000 to 2008, in which planting production was the biggest process in terms of total emergy input, while breeding was the most productive one with its highest total emergy yield. The CBS was under an industry transaction process stimulated by biogas construction, while the traditional agricultural activities still play an important role. For economic input, a trend towards a more renewable regime was found behind the total increase over time. With different preferences for renewable or non-renewable resources, planting and aquaculture production were proved natural donation-reliant, while breeding and biogas were economic input-dependent. Among all the economic inputs, electricity, diesels and infrastructure were the most efficient components

  2. Biogas production for the environment and the economy: Results and experiences of biogas actions of climate investment programmes (Klimp); Biogasproduktion foer miljoe och ekonomi: Resultat och erfarenheter av biogasaatgaerderna inom Klimatinvesteringsprogrammen (Klimp)

    Tamm, Daniel; Fransson, Martin

    2011-07-01

    It has proved difficult to make an economic assessment of the biogas projects. With municipal projects, there is often not a clear demarcation to other activities and financial performance is allocated to different activities within the organization. Private companies are today acting in a competitive market which means that very few are willing to share financial data. So instead of an economic evaluation the report presents some qualitative factors shown important to the success or failure of biogas projects in Sweden: - Identify and understand the value chain for the biogas system - Create a consensus on the value of biogas and clear incentives for all actors in the system - Involve the public actors - Long-term and thoroughly analyzed business concepts - Knowledge of the permit processes and regulations - Work in parallel with several development stages - Choose the relevant technical solutions, depending of the substrate and local conditions - Create a market for the produced bio-fertilizer - Work actively and continuously with quality and process development The report also gives a few general recommendations to policy makers at national, regional and local level, and to plant operators of how the development of the biogas sector in Sweden can be promoted. Overall the evaluation showed that Klimp not only serves as a financial support for biogas projects but also as a 'moral' support that signals that biogas is seen as a desired and preferred technique at a national level. It also shows that Klimp has played an important role in the development of the biogas sector in Sweden

  3. Biogas and biofuels barometer

    European union countries are becoming more and more interested by the characteristics of biogas in terms of environment and energy production and are developing their proper channels of valorization according to their potential. In this way, biogas production reached nearly 5,3 million tons oil equivalent in 2006, representing a 13,6% increase with respect to 2005. Statistical data are provided on the primary energy production of biogas, the electricity production from biogas, gross heat production from biogas, and the representative firms of the biogas sector. In a second part the biofuels barometer is presented. The agricultural environment and landscape of the European Union countries is redefined a little more each year by energy crops for biofuel production. According to the first estimates for 2006, biofuel consumption reached 5,38 Mtoe last year in the EU, corresponding to a 1,8% share of the total consumption of fuels devoted to transport. (A.L.B.)

  4. Methods and apparatus for hydrogen based biogas upgrading

    2013-01-01

    The present invention relates to an anaerobic process for biogas upgrading and hydrogen utilization comprising the use of acidic waste as co-substrate.In this process,H2 and CO2 will be converted to CH4, which will result in lower CO2 content in the biogas. The invention relates to both in situ a...... ex situ methods of biogas upgrading. The invention further relates to a bioreactor comprising hollow fibre membranes....

  5. Testing and optimising biogas plants

    Perwanger, A.

    1984-01-01

    The long-term output of biogas systems studied in practice of an average just under 1 cbm gross of biogas per GV and day is below the forecast levels. Only very few plants showed higher output in the long term. This makes it even more important to show ways of improving process control and reducing building costs for the system. As a result of comparative practical studies in connection with corresponding experiments in the laboratory, it has already been possible to find a number of proposals for improvements. For instance, raising substrate performance with substrate dilution, cost-reducing and functionally safe construction of systems with a gas-dome mounted on top and the possibility of simple biogas production in the final storage unit with low-cost voluminous gas storage at the same time. The latter solution has the advantage of allowing the fermentation substrate to be anaerobically treated all year round, the N-losses would be lower by contrast with open slurry storage, and that any ecologically relevant regulations about odeur control and slurry storage at the farm could be complied with absolutely safely and with the additional use of biogas.

  6. Trace compounds affecting biogas energy utilisation - A review

    Rasi, S., E-mail: saija.rasi@gmail.com [University of Jyvaeskylae, Department of Biological and Environmental Science, P.O. Box 35, FI-40014 (Finland); Laentelae, J.; Rintala, J. [University of Jyvaeskylae, Department of Biological and Environmental Science, P.O. Box 35, FI-40014 (Finland)

    2011-11-15

    Highlights: {yields} In regards to trace compounds, landfill gases are the most studied biogases. {yields} More strict requirements are set for biogas purity with new biogas applications. {yields} With traditional applications, small variations in biogas quality are acceptable. {yields} New requirements set challenges on raw material control and biogas quality. {yields} In this study, variations in analysing methods and biogas quality are discussed. - Abstract: This paper investigates the trace compounds affecting energy utilisation in biogas that come from different production sites. With biogas being more widely used in different energy applications more interest has arisen for the specific composition of biogas. In traditional energy applications, methane and hydrogen sulphide contents have had the most influence when energy utilisation application has been considered. With more advanced processes also the quantity and quality of trace compounds is more important. In regards to trace compounds, it was found that the concentrations and the variations of volatile organic compounds (VOCs) can be high in different landfills, especially, with compounds originating from the biological degradation process (like aromatics and terpenes) as seasonal variations affect the biological degradation. Trace compounds produced by direct volatilisation (halogenated and silicon compounds) show a smaller seasonal variation. Halogenated compounds are rarely present in high concentrations in waste water treatment plant (WWTP) biogas, but the concentrations of organic silicon compounds and their variation is high. Organic silicon compounds are usually detected only in low concentrations in co-digestion plant biogas, when no WWTP sludge is used as a raw material.

  7. Trace compounds affecting biogas energy utilisation - A review

    Highlights: → In regards to trace compounds, landfill gases are the most studied biogases. → More strict requirements are set for biogas purity with new biogas applications. → With traditional applications, small variations in biogas quality are acceptable. → New requirements set challenges on raw material control and biogas quality. → In this study, variations in analysing methods and biogas quality are discussed. - Abstract: This paper investigates the trace compounds affecting energy utilisation in biogas that come from different production sites. With biogas being more widely used in different energy applications more interest has arisen for the specific composition of biogas. In traditional energy applications, methane and hydrogen sulphide contents have had the most influence when energy utilisation application has been considered. With more advanced processes also the quantity and quality of trace compounds is more important. In regards to trace compounds, it was found that the concentrations and the variations of volatile organic compounds (VOCs) can be high in different landfills, especially, with compounds originating from the biological degradation process (like aromatics and terpenes) as seasonal variations affect the biological degradation. Trace compounds produced by direct volatilisation (halogenated and silicon compounds) show a smaller seasonal variation. Halogenated compounds are rarely present in high concentrations in waste water treatment plant (WWTP) biogas, but the concentrations of organic silicon compounds and their variation is high. Organic silicon compounds are usually detected only in low concentrations in co-digestion plant biogas, when no WWTP sludge is used as a raw material.

  8. Basic Data on Biogas

    NONE

    2012-07-01

    Renewable gases such as biogas and biomethane are considered as key energy carrier when the society is replacing fossil fuels with renewable alternatives. In Sweden, almost 80 % of the fossil fuels are used in the transport sector. Therefore, the focus in Sweden has been to use the produced biogas in this sector as vehicle gas. Basic Data on Biogas contains an overview of production, utilisation, climate effects etc. of biogas from a Swedish perspective. The purpose is to give an easy overview of the current situation in Sweden for politicians, decision makers and interested public. 1.4 TWh of biogas is produced annually in Sweden at approximately 230 facilities. The 135 wastewater treatment plants that produce biogas contribute with around half of the production. In order to reduce the sludge volume, biogas has been produced at wastewater treatment plants for decades. New biogas plants are mainly co-digestion plants and farm plants. The land filling of organic waste has been banned since 2005, thus the biogas produced in landfills is decreasing.

  9. Solanum Tuberosum Supplementation for Biogas Production

    Pradip B. Acharya; Prateek Shilpkar

    2015-01-01

    Production of biogas using animal dung is well documented. Nutritional supplement enhances microbial activity and ultimately results in increase biogas production. Solanum tuberosum (potato) is a vegetable crop grown in most parts of world. It is a rich source of carbohydrate starch and many minerals. Present experiment was conducted in 5L capacity glass digester bottles filled with mixture of buffalo dung and water at 5.3% total solids. A total of six sets were prepared, three as control and...

  10. Biodeterioration of cementitious materials in biogas digester

    Voegel, C.; Bertron, A.; Erable, B

    2015-01-01

    In biogas production plants, concrete structures suffer chemical and biological attacks during the anaerobic digestion process. The attack on concrete may be linked to the effects of (i) organic acids; (ii) ammonium and CO2 co-produced by the microorganisms’ metabolisms; and (iii) the bacteria’s ability to form biofilms on the concrete surface. In a context of biogas industry expansion, the mechanisms of concrete deterioration need to be better understood in order to propose innovative, effic...

  11. Increase of Bio-Gas Power Potential

    V. Sednin; О. Kraetskaya; I. Prokoрenia

    2014-01-01

    The paper presents a review of industrial technologies for obtaining gas-synthesis which is applicable for bio-gas enrichment process. Comparative characteristics are given in the paper. The paper thoroughly considers a technology of dry methane conversion as the most expedient variant recommended for the application in this case. The bio-gas enrichment carried out during its production expands possibilities and efficiency of its application.

  12. Techno-Economic Feasibility of Selective CO 2 Capture Processes from Biogas Streams Using Ionic Liquids as Physical Absorbents

    García-Gutiérrez, P.; Jacquemin, J.; McCrellis, C.; Dimitriou, I; Taylor, S.F.R.; Hardacre, C.; Allen, R. W. K.

    2016-01-01

    Biogas from anaerobic digestion of sewage sludge is a renewable resource with high energy content, which is composed mainly of CH4 (40−75 vol %) and CO2 (15−60 vol %). Other components, such as water (H2O, 5−10 vol %) and trace amounts of hydrogen sulfide and siloxanes, can also be present. A CH4-rich stream can be produced by removing the CO2 and other impurities so that the upgraded biomethane can be injected into the natural gas grid or used as a vehicle fuel. The main objectiv...

  13. Techno-Economic Feasibility of Selective CO2 Capture Processes from Biogas Streams Using Ionic Liquids as Physical Absorbents

    García-Gutiérrez, P.; Jacquemin, J.; McCrellis, C.; Dimitriou, I; Taylor, S.F.R.; Hardacre, C.; R. W. Allen

    2016-01-01

    Biogas from anaerobic digestion of sewage sludge is a renewable resource with high energy content, which is composed mainly of CH4 (40–75 vol %) and CO2 (15–60 vol %). Other components, such as water (H2O, 5–10 vol %) and trace amounts of hydrogen sulfide and siloxanes, can also be present. A CH4-rich stream can be produced by removing the CO2 and other impurities so that the upgraded biomethane can be injected into the natural gas grid or used as a vehicle fuel. The main objective of this pa...

  14. Application of a qualitative image analysis on the evaluation of microbial process parameters of biogas plants; Einsatz einer quantitativen Bildanalyse zur Beurteilung mikrobieller Prozessparameter von Biogasanlagen

    Kim, Yong Sung; Scherer, Paul [Hamburg Univ. of Applied Sciences, Hamburg-Bergedorf (Germany). Faculty of Life Sciences

    2013-10-01

    To evaluate efficiency and microbial activity of biogas or anaerobic waste water treatment plants, the number of microorganisms per gram or per milliliter is supposed to be a crucial factor. Since some years ago our research group at HAW-Hamburg has struggled to develop a simple and rapid technique for quantification and classification of environmental microbes with a semi-automatic digital image analysis. For detection of methanogens, the methanogenic fluorescence coenzyme F420 was used, which represents the vitality of methanogens. Furthermore this technique has been supplemented with morphological classification resulting in a Quantitative Microscopic Fingerprinting (QMF). The technique facilitates to find out microbial reasons for some problems of reactor performances. In addition QMF allows differentiating between H{sub 2}-CO{sub 2} and acetate consuming methanogens according to their morphology. At the moment, this study focusses on some relationships between QMF and plant operation parameters. As an example, a thermophilic biogas plant fed by 65% liquid cow manure, maize silage, grass silage and solid cow manure was analyzed for more than 22 weeks. Here some basic background and methodical procedures were presented as well as validation of this technique. (orig.)

  15. Anaerobic co-digestion of vegetal oil and thickened waste-activated sludge: Effects on biogas production and microbial community structure

    Lauwers, Joost; Appels, Lise; Ruyters, Stefan; Busschaert, Pieter; Lievens, Bart; Van Impe, Jan; Dewil, Raf

    2013-01-01

    Thickened waste-activated sludge (tWAS) was co-digested with vegetal oil in a continuous 50 L digester. Compared to a digester fed with only tWAS, the biogas production increased as expected due to the addition of oil: about 60 % for an oil load of 10-15 % of the volatile solids (VS) load and a triplication for an oil load of 37-44%. Using 454 pyrosequencing, the microbial community structure was analyzed and visualised in a non-metric multidimensional scaling. The community of the Bacte...

  16. Cavitation for improved sludge conversion into biogas

    Stoop, A. H.; Bakker, T. W.; Kramer, H. J. M.

    2015-12-01

    In several studies the beneficial influence of pre-treatment of waste activated sludge with cavitation on the biogas production was demonstrated. It is however, still not fully certain whether this effect should be mainly contributed to an increase in conversion rate of organics into biogas by anaerobic bacteria, and how much cavitation increases the total biogas yield. An increase in yield is only the case if cavitation can further disrupt otherwise inaccessible cell membrane structures and long chain organic molecules. In this study the influence of hydrodynamic cavitation on sludge that was already digested for 30 days was investigated. The total biogas yield could indeed be increased. The effect of the backpressure behind the venturi tube on the yield could not yet be established.

  17. Storage of catch crops to produce biogas

    Molinuevo-Salces, Beatriz; Ahring, Birgitte Kiær; Uellendahl, Hinrich

    2014-01-01

    Catch crop biomass is a promising co-substrate for manure-based biogas plants in Denmark since the cultivation of catch crops is mandatory to retain nutrients in the soil, contributing to protect the aquatic environment. In general, the growth period for catch crops is from harvest of the previous...... crop in July-August to the end of the growing season and harvest in late October. Hence, for use of the biomass in biogas production there is a need for storage of the biomass. Storage as silage would guarantee the availability of the feedstock for biogas production during the whole year. A proper...... ensiling process determines the storage loss and the quality of the final silage and, thus, the possible use of it as a substrate for biogas production. Moreover, silage has been considered as a pre-treatment since it partially hydrolyses organic matter improving cellulose convertibility. Since a large...

  18. Socio-economic Analysis of Centralised Biogas Plants

    Nielsen, L.H.; Hjort-Gregersen, K.

    2002-01-01

    The development of biogas technology in Denmark has been widely encouraged by the government over the last 15 years. The overall reasons for the government concern has been the increasing awareness that centralised biogas plants make a significant contribution to solve a range of problems in the fields of energy, agriculture and environment. This has been documented through related monitoring and R & D activities. To achieve a satisfactory evaluation of centralised biogas plants, a thorough s...

  19. Biogas : Animal Waste That Can be Alternative Energy Source

    Tuti Haryati

    2006-01-01

    Biogas is a renewable energy which can be used as alternative fuel to replace fossil fuel such as oil and natural gas . Recently, diversification on the use of energy has increasingly become an important issue because the oil sources are depleting . Utilization of agricultural wastes for biogas production can minimize the consumption of commercial energy source such as kerosene as well as the use of firewood . Biogas is generated by the process of organic material digestion by certain anaerob...

  20. Comparative microbial analysis before and after foaming incidents in biogas reactors

    Kougias, Panagiotis; De Francisci, Davide; Treu, Laura;

    2014-01-01

    /or in the pre-storage feeding tank, resulting in 30-50% biogas production loss (Kougias et al., 2014). In activated sludge systems and in wastewater treatment plants the major causes of foaming are organic overload, the presence of surface active agents, operational parameters (e.g. digester’s shape......Foaming is one of the major problems that occasionally occurring in biogas plants affecting negatively the overall anaerobic digestion (AD) process. According to a recent survey, 15 out of 16 full-scale biogas plants, which were surveyed in Denmark, faced foaming incidents in the main reactor and...... extraction and metagenomic analysis. After sampling, the feedstock composition of each reactor was changed by the addition of gelatine or Na-Oleate or glucose (second experimental period). As a consequence, foam formation was observed in all reactors approximately after one HRT period. Once the daily volume...

  1. Electricity from biogas

    Biogas is a medium-Btu methane and carbon dioxide mix produced by bacterial decomposition of organic matter. Its sources include landfills, waste water sludges, and animal wastes. It can fuel energy applications, of which electricity generation is a frequently-preferred option. The greatest current U.S. biogas recovery and energy use is at landfills, where biogas at about 80 landfill sites fuels a total of approximately 300 MWe. Wastewater treatment plants and confined animal waste management systems support additional electric power production. Generation of electricity from biogas can present difficulties due to the generally small scale of the generating facility, variable energy content of the gas, fluctuating availability, contaminant problems, and often-demanding control needs. However, such difficulties are being successfully addressed and economics for electricity generation are often favorable as biogas can be essentially open-quotes freeclose quotes fuel. Biogas recovery and use has the additional advantage of mitigating a potent greenhouse gas. Biogas from U.S. landfills alone could fuel about 1% of U.S. electrical generation while giving climate change benefit equivalent to reducing CO2 emissions in the electricity sector by more than 10%. Growth in landfill gas use will be facilitated by recent regulations, advances in equipment, and improved management techniques such as open-quotes controlled landfillingclose quotes. The potential for biogas recovery and electricity production from sewage sludges, animal wastes and other organic resources such as agricultural residues is uncertain but probably exceeds the estimate for landfills

  2. Biogas in agriculture. Status and prospects. Proceedings; Biogas in der Landwirtschaft. Stand und Perspektiven. Tagungsband

    NONE

    2011-07-01

    Within the congress of the Agency for Renewable Resources (Guelzow, Federal Republic of Germany) and the Association for Technology and Structures in Agriculture (Darmstadt, Federal Republic of Germany) at 20th-21st September, 2011 in Goettingen (Federal Republic of Germany) the following lectures and posters were presented: (1) Perspectives of using biogas as a part of the German power supply (Stefan Rauh); (2) Development of biogas in Europe (Marc Fleureck); (3) Biology of methanogenic archaea and its significance for the microbial process control in biogas plants (Helmut Koenig); (4) Efficiency and behaviour of enzymes in the biogas process (Monika Heiermann); (5) Trace elements in NaWaRo biogas plants for balancing substrate limited deficiency symptoms and stabilizing the fermentation process (Hans Oechsner); (6) EEG - Actual developments for biogas (Ulrich Keymer); (7) Utilization of thermal energy from cogeneration in the practice - Experiences from the view of an environmental expert (Michael Hub); (8) Innovations in the legal aspects of the production and utilization of biogas (Hartwig von Bredow); (9) Damages and deficiencies at biogas plants (Waldemar Gruber); (10) Learning from accidents, damages and their causes as well as their correctives in the operation of biogas plants - Reports from the practice (Wolfgang Horst Stachowitz); (11) Causes and avoidance of container damages by means of biocorrosion (Jan Kuever); (12) Anaerobic degradation of cellulosic substrates - Bionic implementation of the forestomach sysem of a ruminant (Dirk Weichgrebe); (13) Fermentation of renewable raw materials in the up flow procedure (Jan Mumme); (14) Two-phase pressure fermentation for feeding into natural gas grids (Andreas Lemmer); (15) Requirements and potential of sugar beets for fermentation (Christa Hoffmann); (16) Innovation in the area of power beets (Andreas von Felde); (17) Optimization of manuring with fermentation residues in order to reduce the nitrogen

  3. Biogas Production from Thin Stillage on an Industrial Scale—Experience and Optimisation

    Anna Schnürer

    2013-10-01

    Full Text Available With the increasing demand for renewable energy and sustainable waste treatment, biogas production is expanding. Approximately four billion litres of bio-ethanol are produced annually for vehicle fuel in Europe, resulting in the production of large amounts of stillage residues. This stillage is energy-rich and can be used for biogas production, but is a challenging substrate due to its high levels of nitrogen and sulphate. At the full-scale biogas production plant in Norrköping, Sweden (Svensk Biogas i Linköping AB, thin grain stillage is used as a biogas substrate. This paper describes the plant operation and strategies that have been implemented to digest thin stillage successfully. High ammonia concentrations in the digester have resulted in syntrophic acetate oxidation (SAO becoming the major pathway for acetate degradation. Therefore, a long hydraulic retention time (HRT (40–60 days is used to allow the syntrophic acetate-oxidising bacteria time to grow. The high sulphate levels in thin stillage result in high levels of hydrogen sulphide following degradation of protein and the activity of sulphate-reducing bacteria (SRB, the presence of which has been confirmed by quantitative polymerase chain reaction (qPCR analysis. To optimise biogas production and maintain a stable process, the substrate is diluted with tap water and co-digested with grain residues and glycerine to keep the ammonium nitrogen (NH4-N concentration below 6 g L−1. Combined addition of iron, hydrochloric acid and cobalt successfully precipitates sulphides, reduces ammonia toxicity and supplies microorganisms with trace element. Mesophilic temperature (38 °C is employed to further avoid ammonia toxicity. Together, these measures and doubling the digester volume have made it possible to increase annual biogas production from 27.7 TJ to 69.1 TJ.

  4. Improving the biogas production performance of municipal waste activated sludge via disperser induced microwave disintegration.

    Kavitha, S; Rajesh Banu, J; Vinoth Kumar, J; Rajkumar, M

    2016-10-01

    In this study, the influence of disperser induced microwave pretreatment was investigated to analyze the proficiency of floc disruption on subsequent disintegration and biodegradability process. Initially, the flocs in the sludge was disrupted through disperser at a specific energy input of 25.3kJ/kgTS. The upshot of the microwave disintegration presents that the solids reduction and solubilization of floc disrupted (disperser induced microwave pretreated) sludge was found to be 17.33% and 22% relatively greater than that achieved in microwave pretreated (9.3% and 16%) sludge alone. The biodegradability analysis, affords an evaluation of parameter confidence and correlation determination. The eventual biodegradability of microwave pretreated, and floc disrupted sludges were computed to be 0.15(gCOD/gCOD) and 0.28(gCOD/gCOD), respectively. An economic assessment of this study offers a positive net profit of about 104.8USD/ton of sludge in floc disrupted sample. PMID:26897472

  5. BiogasMotor; BiogasMotor

    Roubaud, A.; Favrat, D.

    2002-07-01

    This final report for the Swiss Federal Office of Energy (SFOE) presents the results of tests made at the Swiss Federal Institute of Technology in Lausanne with an unscavenged prechamber ignition system on a 150 kW co-generation engine fuelled with biogas. The engine's performance in terms of fuel conversion efficiency was observed and the reduction potential for exhaust emissions to a level below the Swiss limits was verified. The tests made, which used natural gas mixed with CO{sub 2} as simulated biogas fuel, are described. The results of the tests, including figures on NO{sub x}, CO and HC emissions, are presented and discussed. The authors conclude that biogas engines with unscavenged prechamber ignition could provide a significant boost in energy conversion efficiency whilst keeping emissions within the tough Swiss limits.

  6. Safety and nutritional evaluation of biogas residue left after the production of biogas from wastewater

    Baoguo Bian; Lvmu Li; Xiongyuan Si; Bin Li; Wenjie Guo; Hua Mu; Xiaoling Ding; Fazhi Xu

    2015-01-01

    We investigated the safety and nutritional value of biogas residue left after the production of biogas from wastewater. In Exp. 1, ninety- six female mice were selected for acute oral toxicity testing and randomly allocated to 4 treatment groups, which received distilled water (control) or the biogas residue solution at 1 g/mL, 5 g/mL, or 15 g/mL. Activity levels and serum biochemical parameters were measured after 24 hours. In Exp. 2, eighty mice were divided into 2 treatment groups for suba...

  7. Solanum Tuberosum Supplementation for Biogas Production

    Pradip B. Acharya

    2015-04-01

    Full Text Available Production of biogas using animal dung is well documented. Nutritional supplement enhances microbial activity and ultimately results in increase biogas production. Solanum tuberosum (potato is a vegetable crop grown in most parts of world. It is a rich source of carbohydrate starch and many minerals. Present experiment was conducted in 5L capacity glass digester bottles filled with mixture of buffalo dung and water at 5.3% total solids. A total of six sets were prepared, three as control and three as test. Control sets were fed daily with buffalo dung water mixture throughout the period of experimentation, i.e. 80 days, whereas in test, from 51st day onward digesters were filled with mixture of dung and boiled potato with water. Feed was added daily in the amount of 120mL upto 80 days from beginning. On first day 12 mL fresh digested biogas slurry from running biogas plant was also added in all the digesters as inoculum. From 41th day onward biogas production was recorded by water displacement method and compared. Results reveal that in test digesters addition of potato shows an immediate and long lasting effect and increases biogas production between 90.48 and 192.86% higher than control sets.

  8. Energy systems analysis of biogas systems; Energianalys av biogassystem

    Berglund, Maria; Boerjesson, Paal

    2003-05-01

    The aim of this study was to calculate the net energy output and energy efficiency, from a life-cycle perspective and for Swedish conditions, in anaerobic digestion of various raw materials. Our calculations are based on literature reviews concerning the total primary energy input required for the production of biogas (i.e. direct and indirect energy inputs, e.g. when producing and distributing diesel fuels, electricity, fertilisers) as well as the biogas yield from various raw materials. Our analyses include handling and transportation of raw materials, operation of the biogas plants, and transportation and spreading of digested residues, as well as the biogas yield from manure, ley crops, tops and leaves of sugar beets, straw, municipal organic waste, slaughter waste, and grease separator sludge. All calculations concern individual raw materials. The net energy input required to run a biogas system (i.e. centralised biogas plant) typically corresponds to approximately 20-40% of the energy content in the produced biogas. Theoretically, the raw materials could be transported for some 200 km (manure) up to 700 km (slaughter waste) before the net energy output becomes negative. The variations in energy efficiency between studied biogas systems depend mainly on the type of raw material studied and the calculation methods used. Raw materials with high water content and low biogas yield (e.g. manure) require rather large energy inputs compared to the amount of biogas produced. Energy demanding handling of the raw materials, such as ley crops, could correspond to as much as approximately 40% of the net energy input. Varying energy efficiency in different parts of the biogas system, but most of all, changes in the biogas yield, could considerably affect the total net energy output. In general, operation of the biogas plant is the most energy demanding process in the biogas systems, corresponding to some 40-80% of the net energy input in the biogas systems. This implies

  9. Distribution forms for biogas and natural gas in Sweden

    Since biogas and natural gas basically have the same characteristics, they can be distributed in the same system. In the parts of the country where there is an extensive natural gas distribution network, the infrastructure for natural gas can be used for distribution of biogas. In order to increase the use of renewable energy, it is a political ambition to increase the share of biogas in the natural gas network, and, in the long run, entirely replace natural gas with biogas. Much of biogas production in the country is, however, not reached by the existing natural gas network, and this is also the case for a large part of the potential for future biogas production. In these areas the gas is transported in more or less extensive local gas distribution networks and by truck in compressed or liquid form. Transport of compressed and liquefied gas is efficient in some cases and development of these systems is an ongoing process. A number of facilities are planned for production of large quantities of biogas, several hundred GWh/year, through digestion and gasification processes. These plants will be located either in conjunction with major gas consumers or in the vicinity of the existing natural gas grid. The potential for biogas production is, however, present throughout the country and in order to meet market demand biogas requires efficient distribution systems

  10. Purification of anaerobic digestion biogas from a wastewater treatment plant for its use as bio fuel

    The first phase of the investigation whose results are presented in this article, consists on the optimization of the biogas desulphurization. In our case this process was made by chemical way. Besides the scrubbing towers, the pilot plant used included filters of activated carbon at the end of the line. The H2S inflow concentrations were quite high. After the carried out rehearsals, the effluent biogas from the scrubbing towers presents a H2S concentration less than 1 ppm and zero or undetectable values of up to fifty eight analyzed trace elements. (Author) 12 refs

  11. Use of biogas in agriculture

    Hejný, František

    2012-01-01

    Biogas results from anaerobic fermentation of organic substances either in oxygen atmosphere or non-oxygen atmosphere, depending on decomposition stage. Composition of Biogas is different, depends mainly on development of fermentation and additional important factors. The most important for Biogas is the maximum contents of methane. Biogas stations exploit Biogas for production of electric energy and heat energy by means of congregational units and there is also possibility to generate c...

  12. Simultaneous enhancement of methane production and methane content in biogas from waste activated sludge and perennial ryegrass anaerobic co-digestion: The effects of pH and C/N ratio.

    Dai, Xiaohu; Li, Xiaoshuai; Zhang, Dong; Chen, Yinguang; Dai, Lingling

    2016-09-01

    It is necessary to find an appropriate strategy to simultaneously enhance the methane production and methane content in biogas from waste activated sludge (WAS) and grass co-digestion. In this study an efficient strategy, i.e., adjusting the initial pH 12 and C/N ratio 17/1, for simultaneous enhancement of methane production and methane content in biogas from WAS and perennial ryegrass co-digestion was reported. Experimental results indicated that the maximal methane production was 310mL/gVSadd at the optimum conditions after 30-d anaerobic digestion, which was, respectively, about 1.5- and 3.8-fold of the sole WAS and sole perennial ryegrass anaerobic digestion. Meanwhile, the methane content in biogas was about 74%, which was much higher than that of sole WAS (64%) or sole perennial ryegrass (54%) anaerobic digestion. PMID:27259187

  13. Effect of thermal pretreatment on the biogas production and microbial communities balance during anaerobic digestion of urban and industrial waste activated sludge.

    Ennouri, Hajer; Miladi, Baligh; Diaz, Soraya Zahedi; Güelfo, Luis Alberto Fernández; Solera, Rosario; Hamdi, Moktar; Bouallagui, Hassib

    2016-08-01

    The effect of thermal pre-treatment on the microbial populations balance and biogas production was studied during anaerobic digestion of waste activated sludge (WAS) coming from urban (US: urban sludge) and industrial (IS: industrial sludge) wastewater treatment plants (WWTP). The highest biogas yields of 0.42l/gvolatile solid (VS) removed and 0.37l/gVS removed were obtained with urban and industrial sludge pre-treated at 120°C, respectively. Fluorescent in situ hybridization (FISH) was used to quantify the major Bacteria and Archaea groups. Compared to control trails without pretreatment, Archaea content increased from 34% to 86% and from 46% to 83% for pretreated IS and US, respectively. In fact, the thermal pre-treatment of WAS enhanced the growth of hydrogen-using methanogens (HUMs), which consume rapidly the H2 generated to allow the acetogenesis. Therefore, the stable and better performance of digesters was observed involving the balance and syntrophic associations between the different microbial populations. PMID:27132226

  14. Biogas purification from anaerobic digestion in a wastewater treatment plant for biofuel production

    Osorio, F. [MITA Research Group, Department of Civil Engineering, University of Granada, Campus de Fuentenueva s/n, 18071 Granada (Spain); Torres, J.C. [EMUASA (Murcia Water Works), Pza. Circular, 9, 30008 Murcia (Spain)

    2009-10-15

    The main objective of this investigation consists in the biogas purification coming from the anaerobic digestion of sludges in a wastewater treatment plant, in order to be used later as biofuel for vehicles. This article consists of the optimization of the biogas desulphurization. In our case, this process was achieved in a chemical way. Besides the scrubbing towers, the pilot plant used included filters of activated carbon at the end of the line. The H{sub 2}S inflow concentrations were quite high. The effluent biogas from the scrubbing towers presented an H{sub 2}S concentration less than 1 ppm and zero or undetectable values were obtained for up to 58 analyzed trace elements. (author)

  15. Mini digester and biogas production from plant biomass

    P. Vindis

    2009-08-01

    Full Text Available Purpose: The aim of the paper is to present the construction of a mini digester for biogas production from different agriculture plant biomass and other organic wastes. The amount of biogas production (methane is observed by the mini digester.Design/methodology/approach: The mini digester consisting of twelve units was built and some measurements with agriculture plant biomass were performed according to DIN 38414 part 8. Four tests simultaneously with three repetitions can be performed.Findings: With the mini digester the amount of biogas production is observed. The parameters such as biogas production and biogas composition from maize and sugar beet silage in certain ratio were measured and calculated. The highest biogas and methane yield was 493 NI kg VS-1 or 289 NI CH4 kg VS-1.Research limitations/implications: The scope of substrates for the anaerobic digestion process is on the increase so the interest in the use of the biogas as a source of a renewable energy is very high. With mini digester it is possible to observe the amount of biogas (methane production and so the most suitable plant giving the maximum methane yield, can be determined.Practical implications: The aim of biogas as renewable source of energy is to replace fossil fuels with sustainable energy production systems and to fulfil the requirements of the Kyoto Protocol. On big farms the liquid manure and different energy crops can be used for biogas production. That can improve the economical efficiency of the farm and reduce the CO2 emissions.Originality/value: Mini digester for biogas production was built as special equipment. The quality of produced biogas is determined with a gas analyser GA 45.

  16. Biologische Entschwefelung von Biogas

    Schneider, Ralf

    2009-01-01

    Ziel dieser Arbeit ist die Erhöhung von Abbauleistung und Stabilität des biologischen Abbaus von Schwefelwasserstoff (H2S) in Biotropfkörpern zur Entschwefelung von Biogas. Für die Nutzung von Biogas ist häufig eine Reduktion des H2S-Gehalts erforderlich. Üblicherweise wird H2S von aeroben Mikroorganismen bei Zugabe von Luft zum Biogas entweder direkt im Biogasreaktor oder in nachgeschalteten Biotropfkörpern zu Schwefel und Schwefelsäure oxidiert. In der Praxis auftretende Schwankungen der H2...

  17. Multifeed biogas reactor for coffee waste water and biomass wastes : performance under highly fluctuating operating conditions

    Chanakya, H.N.; Deepa, G.B.; Vinutha, D. [Indian Inst. of Science, Bangalore (India). Centre for Sustainable Technologies; Modak, J.M. [Indian Inst. of Science, Bangalore (India). Dept. of Chemical Engineering

    2004-07-01

    This study compared different operating conditions used in anaerobic digestion processes that convert coffee effluents into biogas. The effluent from wet coffee processing is rich in saccharide. In India, coffee processing is carried out at small to medium sized plantations which do not have the adequate facilities to treat the effluent for biogas recovery. Rather, the wastewater is treated in anaerobic-aerobic lagoons, but this process releases large quantities of methane to the atmosphere. More efficient alternatives are needed to stabilize the operating conditions, concentrations of wastewater and ambient operating temperatures. This study tested a newly developed multi-feed anaerobic reactor that can covert herbaceous biomass and coffee effluent to biogas and compost. The reactor is fed herbaceous biomass feedstock during the 8 month period when there is no coffee processing. Coffee effluent is fed to the reactor during the 4 month coffee processing season. The effluent flows through partially decomposed biomass beds where methanogenic activities yield a biofilm to facilitate conversion to biogas. The seasonal operation can be transformed into a year round advantage. The method can be applied to similar agro-processing units. 6 refs., 3 tabs., 5 figs.

  18. Biogas Production from Household Wastes : A Quantitative Feasibility Study for Student Apartments in Albano

    Önder, Deniz

    2013-01-01

    Biogas is an environmentally friendly energy source with great importance for sustainable development. The purpose of this study is to determine the feasibility of setting up a biogas plant at the student housing area planned at Albano in Stockholm. The possibility of attaining self-sustainability in Albano is also investigated. After compiling the processes for converting household waste into biogas through a literature study, a quantitative feasibility study of setting up a biogas plant is ...

  19. COMPARISON BETWEEN BIOGAS PRODUCTION FROM MANURE OF LAYING HENERS AND BROILERS

    Srećko Kukić; Branimir Bračun; Davor Kralik; Robert T. Burns; Slavko Rupčić; Daria Jovičić

    2010-01-01

    Biogas plants that process raw materials from agriculture, such as poultry manure,are one of the most significant applications of anaerobic fermentation. In Asiancountries, particularly in China, India, Nepal and Vietnam, there are several millionvery simple, small biogas plants that produce gas for household cooking and lighting.In Europe and North America a number of agricultural biogas plants now, areincreasing daily, a few thousand biogas plants exist, most of which use moderntechnologies...

  20. The contribution of Slovenian biogas plants to the reduction of agricultural sector green house emissions

    Romana MARINŠEK LOGAR; Neža NOVAK; Vodovnik, Maša

    2015-01-01

    Agriculture is a source of emissions of the greenhouse gas methane into the environment. These emissions can be reduced by appropriate storage of animal slurry and manure, with proper fertilization and processing of organic agricultural waste into biogas, where methane is captured and used as an energy source. Biogas is a renewable source of energy that is produced by microbial anaerobic digestion in biogas plants. As a substrate in biogas plants using different types of organic biomass such ...

  1. Anaerobic digestion foaming in full-scale biogas plants: A survey on causes and solutions

    Kougias, Panagiotis; Boe, Kanokwan; O-Thong, Sompong;

    2014-01-01

    Anaerobic digestion foaming is a common operation problem in biogas plants with negative impacts on the biogas plants economy and environment. A survey of 16 Danish full-scale biogas plants on foaming problems revealed that most of them had experienced foaming in their processes up to three times...

  2. Optimization of biogas production from manure

    Kaparaju, Prasad Laxmi-Narasimha; Boe, Kanokwan; Buendia, Inmaculada M.;

    The main objective of the project was to improve biogas production from manures. This objective was addressed by investigating 1) the effect of different reactor configurations, 2) operational procedures, aiming to selectively retain/return degradable material in the reactor and 3) different...... process at 90/10, 80/20, 70/30, 50/50 or 30/70% volume distribution could produce 11-17.8% more biogas compared to single CSTR process under similar operating conditions. The increased biogas production was mainly from the second reactor of the serial process, which accounted for 16-18% of the total...... biogas production. At 13/87 ratio, no significant increase in biogas production was noticed. Both single and serial CSTR processes were stable when operated 90/10, 80/20, 70/30 or 50/50% volume distributions and also during an organic pulse load (19.6 to 65.3 g/l reactor volume). Results from pilot...

  3. Biogas Upgrading Using SOEC with a Ni-ScYSZ Electrode

    Ebbesen, Sune Dalgaard; Bøgild Hansen, John; Mogensen, Mogens Bjerg

    2013-01-01

    Biogas consists mainly of CH4, CO2 and small amounts of H2S. The value of biogas will increase significantly if it is upgraded to pipeline quality by converting CO2 and H2O in the biogas to CO and H2 using a Solid Oxide Electrolysis Cell (SOEC) followed by methanation. The Ni-ScYSZ-cermet electrode...... is, however, active for steam reforming of CH4, but sulphur traces in the biogas reduce the steam reforming activity. It is proven that sulphur stops steam reforming activity whereas the electrochemistry is only affected to a limited degree, showing that up-grading of biogas using SOEC with Ni...

  4. Biogas. Present situation and future potential; Biogas. Nulaege och framtida potential

    Nordberg, Ulf [Swedish Inst. of Agricultural and Environmental Engineering, Uppsala (Sweden)

    2006-12-15

    owners need to be improved increase the understanding of the whole management chain, agricultural production, transport, treatment and handling of biofertilizer. The number of production sites for biogas from landfills is decreasing and the amount of biogas from these is diminishing. The number of biogas plants for agricultural crops is likely to increase. Combination processes will increasingly develop towards extracting several different energy products and towards maximising the energy extraction from substrates.

  5. Combustion of Biogas Released from Palm Oil Mill Effluent and the Effects of Hydrogen Enrichment on the Characteristics of the Biogas Flame

    Seyed Ehsan Hosseini; Ghobad Bagheri; Mostafa Khaleghi; Mazlan Abdul Wahid

    2015-01-01

    Biogas released from palm oil mill effluent (POME) could be a source of air pollution, which has illustrated negative effects on the global warming. To protect the environment from toxic emissions and use the energy of POME biogas, POME is conducted to the closed digestion systems and released biogas is captured. Since POME biogas upgrading is a complicated process, it is not economical and thus new combustion techniques should be examined. In this paper, POME biogas (40% CO2 and 60% CH4) has...

  6. Classification of Commercial Biogas Digester and Comparison with Traditional Process%商品化沼气池分类及与传统沼气池比较分析

    冉毅; 彭德全; 王超; 丁自立; 李晋梅; 陈子爱; 席江; 贺莉; 蒋鸿涛

    2012-01-01

    Commercial biogas digester is classified into five categories according to the material properties, marketing, and combining with the characteristics of rural household biogas construction, i. e. glass liber reinforced plastic, hard plastic, flexible plastic (FBR) , glass fiber reinforced cement (GRC) and steel tank. Advantages and disadvantages were expatiated in this paper. The analysis results showed that traditional process biogas digester is the main process in our country. Commercial biogas digester is of important supplement. Glass fiber reinforced plastic type is relatively appropriate material for the biogas digester, followed by PVC (polyvinyl chloride) , PP (polypropylene) and PE (polyethylene). Commercial biogas digester has advantage of better air tightness, short construction period. And construction quality, standard and the cost are easier to control. Therefore, commercial biogas digester could be developed suiting ones measures to local conditions.%文章根据商品化沼气池材料特性与市场行情,结合农村户用沼气池建设特点,将户用商品化沼气池划分为:玻璃钢,塑料硬体,塑料软体(FBR),增强水泥(GRC)和钢制5大类沼气池,分别阐述其优势和劣势,并将玻璃钢沼气池与传统沼气池比较分析得出:传统水泥沼气池是我国沼气建设的主力军,商品化沼气池可作为重要补充;玻璃钢是相对适宜的建池材料,其次是PVC(聚氯乙烯),PP(聚丙烯)和PE(聚乙烯)塑料;商品化沼气池具有气密性好、建设周期短、建池成本较低,建设质量、标准、成本易于统一控制等优势,但塑料材料抗老化性能有待提高,应因地制宜、循序渐进地推广.

  7. Biogas barometer 2011

    Biogas energy recovery for both electricity and heat application has increased in the European Union in 2011 (compared to 2010): +18% for gross electricity production from biogas and +16% for the gross heat production from biogas. The magnitude of the reduction (-7%) in the primary energy figures between 2010 and 2011 can be played down as it can be explained by a change in reporting method of the main producer country, Germany. Germany has taken the lead by far in the E.U. for the production of primary energy of biogas and its uses for heat or electricity production. Among the 13 most representative firms in the anaerobic digestion (methanization) sector in Europe, 8 are German. New markets are starting to emerge but the economic crisis and regulatory restrictions do not augur well of their expansion

  8. Progress in biogas. Biogas production from agricultural biomass and organic residues. Pt. 1 and 2. Proceedings (oral presentations and poster presentations); Fortschritt beim Biogas. Biogas aus landwirtschaftlicher Biomasse and organischen Reststoffen. T. 1 und 2. Tagungsband. Vortraege and Poster

    NONE

    2007-07-01

    Within the International Conference ''Progress in Biogas - Biogas production from agricultural biomass and organic residues'' at the University Hohenheim (Stuttgart, Federal Republic of Germany) from 18th to 21st September, 2007, the following lectures were held: (1) Global relevance and potential of bioenergy for regional development; (2) Biogas electricity for France feed-in tariff and some other things to know before entering French market; (3) Policy drivers and future prospects for on-farm anaerobic digestion in Northern Ireland; (4) Biogas in Belgium, a swot analysis; (5) Status and prospects of biogas energy use in Ukraine; (6) Recent developments in Chinese agricultural biogas production; (7) Opportunities for agricultural based biogas systems in the province of Ontario, Canada; (8) Pre-treatment and digestion of separated collected household waste in Sweden; (9) To the problem of monitoring measures and prophylaxis measures with the utilization of organic residual substances in biological gas facilities from hygienic view; (10) Fermenting residues from biological gas facilities - nutrients and pollutants, possibilities of application in the agriculture; (11) Treatment and utilization of fermentation residues; (12) Potential of residual gas of NaWaRo feeded biogas plants in Baden-Wuerttemberg; (13) Operating analytics of biogas plants to improve efficiency and to ensure process stability; (14) The potential of biogas and electric power production from subproducts in the sugar and alcohol industries by the application of anaerobic digestion; (15) Co-digestion plant in dairy cattle farm in Emilia Romagna region (Italy); (16) Facing operational problems in a biodigeser in Yuvientsa - Amazonian Region of Ecuador; (17) Biogas plant instead of milk cow - payment and occupation with the use of grassilage; (18) Biogas in ecologic agriculture - experiences from 3 years of fermentation of grass-clover ley; (19) Combined solar-biogas basis for the

  9. Energy crops for biogas

    This investigation aims at describing the effects on cropping systems, containing a.o. leguminosae plant leys for biogas production. Problems treated are effects on soil physics, circulation of crop nutrients, use of chemical pesticides, preceding crop effects, and the possibility of utilizing catch crops for methane production. It is observed that the studied biogas-crop sequences gives positive effects on soil structure, reduced need for artificial fertilizers and chemical pesticides. 26 refs, 28 tabs

  10. Methods for preparing biogas in fuel quality; Verfahren zur Aufbereitung von Biogas in Kraftstoffqualitaet

    Prehn, Sascha [Forschungszentrum Verbrennungsmotoren Thermodynamik Rostock GmbH, Rostock (Germany); Wichmann, Volker; Harndorf, Horst

    2012-07-01

    Biogas is obtained from renewable raw materials. Due to its high methane concentration it is suitable as an alternative fuel. In order to provide biogas as a fuel equivalent to natural gas it must be converted into bio-methane. The quality of bio-methane is subject to high demands which are defined in the paper of DVGW G260 and G262 for feeding it into the public gas grid. Criteria for the use of bio-methane as a fuel in combustion engines are defined in DIN 51621. In addition to the separation of carbondioxide and water, biogas has to comply limited values of hydrogen sulfide and other trace gases. This paper gives an overview of various process steps of biogas treatment considering technical and economical aspects. (orig.)