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Статті в журналах з теми "Anaerobic biofilm reactor"
Suidan, Makram T., Joseph R. V. Flora, Pratim Biswas, and Gregory D. Sayles. "Optimization modelling of anaerobic biofilm reactors." Water Science and Technology 30, no. 12 (December 1, 1994): 347–55. http://dx.doi.org/10.2166/wst.1994.0634.
Повний текст джерелаFahmy, M., E. Heinzle, and O. M. Kut. "Treatment of Bleaching Effluents in Aerobic/Anaerobic Fluidized Biofilm Systems." Water Science and Technology 24, no. 3-4 (August 1, 1991): 179–87. http://dx.doi.org/10.2166/wst.1991.0474.
Повний текст джерелаKennedy, K. J., and R. L. Droste. "Diffusional limitations of anaerobic biofilms." Canadian Journal of Civil Engineering 14, no. 5 (October 1, 1987): 631–37. http://dx.doi.org/10.1139/l87-093.
Повний текст джерелаJahren, Sigrun J., and Hallvard Ødegaard. "Treatment of Thermomechanical Pulping (TMP) Whitewater in Thermophilic (55°C) Anaerobic-Aerobic Moving Bed Biofilm Reactors." Water Science and Technology 40, no. 8 (October 1, 1999): 81–89. http://dx.doi.org/10.2166/wst.1999.0391.
Повний текст джерелаLiang, Qiaochu, Takahiro Yamashita, Norihisa Matsuura, Ryoko Yamamoto-Ikemoto, and Hiroshi Yokoyama. "Community Structure Analyses of Anodic Biofilms in a Bioelectrochemical System Combined with an Aerobic Reactor." Energies 12, no. 19 (September 24, 2019): 3643. http://dx.doi.org/10.3390/en12193643.
Повний текст джерелаBoltz, Joshua P., Barth F. Smets, Bruce E. Rittmann, Mark C. M. van Loosdrecht, Eberhard Morgenroth, and Glen T. Daigger. "From biofilm ecology to reactors: a focused review." Water Science and Technology 75, no. 8 (February 2, 2017): 1753–60. http://dx.doi.org/10.2166/wst.2017.061.
Повний текст джерелаKOZAK, Melike, Serdar GÖÇER, Ahmet DUYAR, İrem AYRANPINAR, Emre Oğuz KÖROĞLU, and Kevser CIRIK. "INVESTIGATION OF BIOFILM FORMATION ON KALDNES K1." Kahramanmaraş Sütçü İmam Üniversitesi Mühendislik Bilimleri Dergisi 25, no. 4 (December 3, 2022): 565–69. http://dx.doi.org/10.17780/ksujes.1137084.
Повний текст джерелаHirata, Akira, Haeng-Seog Lee, Satoshi Tsuneda, and Tomotake Takai. "Treatment of photographic processing wastewater using anaerobic-aerobic biofilm reactor." Water Science and Technology 36, no. 12 (December 1, 1997): 91–99. http://dx.doi.org/10.2166/wst.1997.0435.
Повний текст джерелаGönenç, I. E., D. Orhon, and B. Beler Baykal. "Application of Biofilm Kinetics to Anaerobic Fixed Bed Reactors." Water Science and Technology 23, no. 7-9 (April 1, 1991): 1319–26. http://dx.doi.org/10.2166/wst.1991.0584.
Повний текст джерелаComett, I., S. Gonzalez-Martinez, and P. Wilderer. "Treatment of leachate from the anaerobic fermentation of solid wastes using two biofilm support media." Water Science and Technology 49, no. 11-12 (June 1, 2004): 287–94. http://dx.doi.org/10.2166/wst.2004.0863.
Повний текст джерелаДисертації з теми "Anaerobic biofilm reactor"
di, Biase Alessandro. "Industrial wastewater treatment with anaerobic moving bed biofilm reactor." American society of civil engineers, 2016. http://hdl.handle.net/1993/31706.
Повний текст джерелаOctober 2016
Tran, Nguyen Van Nhi. "Treatment of chitin production wastewater with a combined process of chitosan coagulation and anaerobic-anoxic-oxic biofilm reactors." Thesis, Griffith University, 2021. http://hdl.handle.net/10072/406511.
Повний текст джерелаThesis (PhD Doctorate)
Doctor of Philosophy (PhD)
School of Eng & Built Env
Science, Environment, Engineering and Technology
Full Text
Damiano, Elisabeth dos Santos Gaspar. "Tratamento da vinhaça em reator anaeróbio de leito fluidificado." Universidade de São Paulo, 2005. http://www.teses.usp.br/teses/disponiveis/18/18138/tde-08032016-164604/.
Повний текст джерелаThis work had as objective evaluates the efficiency of a anaerobic fluidized bed reactor for vinasse degradation under mesophilic conditions. Batch tests seeking to evaluate the degradation of the substratum for the anaerobic biomass and obtaining kinetic parameters were accomplished to different concentrations. Diluted vinasse to values of 1984 mg/L, 2827 mg/L, 3800 mg/L, 6354 mg/L, 7395 mg/L, 10705 mg/L and 15872 mg/L of COD was used in the experiments showing reductions of 67% in 192 hours, 75% in 358 hours, 81% in 408 hours, 80% in 480, 72% in 504 hours, 76% in 840 hours and of 71% in 1080, for those concentrations, respectively. The reaction happened in the batch reactors it was analyzed as being of order zero, with medium value of 10,4 mg/L.h for the constant of reaction. Tests with polyamide particles, polystyrene and nylon were accomplished, aiming at the choice of the best particle in formation terms and biofilme development for subsequent use in the reactor. The three particles were shown favorable to the adhesion and colonization of microorganisms. The fluidized bed reactor was inoculated with sludge from reactor UASB treating effluent frompoultry slaughterhouse. The volume of the reactor was of 770 cm3, operating with hydraulic detention time of 24 h. Polystyrene particles were used as material support. The reactor was operated for 122 days, being applied diluted vinasse to values of COD 1009 mg/L ranging to 15874 mg/L and organic loading rate (OLR) of 1,0 Kg/m3.d to 15,9 Kg/m3.d, presenting efficiency COD removal of 51% - 70% and OLR removal of 0,5 Kg/m3.d - 7,9 Kg/m3.d. Microscopic observations in MEV showed good microbial adhesion in the particles of polystyrene, in all the phases of the reactor.
Wusiman, Apiredan. "Treatment of Small-Scale Brewery Wastewater: Anaerobic Biochemical Methane Potential (BMP) Trials and Moving Bed Biofilm Reactor (MBBR) Field Study." Thesis, Université d'Ottawa / University of Ottawa, 2021. http://hdl.handle.net/10393/42248.
Повний текст джерелаGilmore, Kevin R. "Treatment of High-Strength Nitrogen Wasetewater With a Hollow-Fiber Membrane-Aerated Biofilm Reactor: A Comprehensive Evaluation." Diss., Virginia Tech, 2008. http://hdl.handle.net/10919/28711.
Повний текст джерелаPh. D.
Asiedu, Kofi. "Evaluating Biological Treatment Systems: (i) Moving Bed Biofilm Reactor versus Biological Aerated Filtration, and (ii) Sulfide-Induced corrosion in Anaerobic Digester Gas Piping." Thesis, Virginia Tech, 2001. http://hdl.handle.net/10919/35156.
Повний текст джерелаThe first section evaluated and compared the performance of a laboratory-scale MBBR and BAF for organic carbon and suspended solids removal. A kinetic study was also performed on the MBBR to evaluate the system performance. The purpose was to recommend one of the systems for the Force Provider project, which provides a containerized "city" for the U.S. Army. The effluent criteria against which the systems were evaluated were total 5-day biochemical oxygen demand (TBOD5) and total suspended solids (TSS) of 30 mg/L each. The report is based on a 5-month laboratory -scale study of the two reactors.
The MBBR performance depended on the percent of media provided in the reactor and the organic loading. At a media volume, which displaced the reactor volume by 40 % (heretofore called 40 % media volume), and surface area loading rate (SALR) of 20 g BOD5/m2-d, the system performance deteriorated with time. At 40 % media volume and SALR below 15 g BOD5/m2-d, the system performance improved but still did not meet effluent criteria or average. TBOD5 reduction was generally poor (approximately 50 %). Soluble BOD5 (SBOD5) concentrations were frequently below 30 mg/L and TSS concentrations were often higher than influent TSS. Overall, TSS wastage from the system (both effluent TSS and intentional wastage) averaged 0.032 kg/d.
BAF system performance was excellent for TBOD5, CBOD5, SBOD5 and TSS removal, and were consistently less that 30 mg/L. Overall TSS wastage from the BAF (both via effluent and backwash) average 0.027 kg/d and was 16 % less than for the MBBR. Based on demonstrated performance, the BAF was the only viable reactor for the project.
Section II of the report focused on possible causes of deposition in an anaerobic digester gas piping at a local wastewater treatment facility (Peppers ferry regional wastewater treatment facility).
Industrial waste input to the treatment facility has increased lately and accounts for 40 % of the plant's wastewater inflow. An industry in Pulaski, VA, Magnox Inc. generates and disposes highly concentrated sodium sulfate, (70,000 mg/L) which is a by-product of its activities, to PFRWTF wastewater influent stream. As a result of Magnox industrial waste input, a pilot study was carried out to determine the effect of its waste on the activated sludge treatment units. Results indicated that Magnox industrial waste input would not have adverse effect on the aeration basins. However production of H2S, which can have effect on the anaerobic digester was reported (Olver Inc., 1995). Field analysis of data reported by Olver Inc. (2000) showed that H2S concentration in PFRWTF anaerobic digester gas was rising. X-ray photoelectron spectroscopy analysis of deposits found in the digester pipe together with results obtained from the laboratory-scale study revealed that iron and sulfur played a role in the deposition in the digester gas pipe. The laboratory scale study revealed that ferrous ion in the digester feed possibly precipitated over 90 % of the hydrogen sulfide gas produced in the digester, thus protecting the digester from adverse effects caused by hydrogen sulfide.
Master of Science
Gaudencio, Bruno Orlando. "Reator anaeróbio híbrido (leito fixo e manta de lodo) em escala plena tratando esgoto sanitário: avaliação da nova configuração." Universidade de São Paulo, 2016. http://www.teses.usp.br/teses/disponiveis/18/18138/tde-29032017-114253/.
Повний текст джерелаThis study aimed to assess the feasibility of implementing a hybrid anaerobic reactor (HAnR) at full scale for treating wastewater containing Biobob® as a packing material for cell immobilization. The reactor volume is 2,495 m3 and was the result of an adaptation of a UASB reactor by introducing 1,000 m3 of packing material Biobob® in the reaction volume of the reactor, turning it into a hybrid anaerobic reactor with fixed bed and sludge blanket. The reactor was monitored for 480 consecutive days and evaluated their performance with the gradual increase of the average flow and the flow resulting from peak hours and periods of high rainfall. The reactor showed good performance throughout the operational period, maintaining the quality of treated efluente (COD effluent of 178 ± 30 mg. L-1 and TSS 54 ± 25 mg. L-1) even when subjected to high hydraulic loads provided by rainy periods, showing up as an excellent alternative to increase the UASB treatment capacity without the need for expansion physical the reactor. For an average HRT of 5.8 h, which corresponds to a period in which there were several peaks flow, the reactor remained stable throughout the period, with values in the effluent COD and TSS of 169 ± 24 mg.L-1 and 47 ± 17 mg.L-1, respectively. Approximately 70% of the total biomass present in the reactor was in suspension in the sludge bed and 30% adhered to the support material, and both fractions fundamental to the performance and stability of the treatment. The observed yield of biomass production (Yobs) was 0.182 g CODr.VSS.g-1. Considering the organic load removed by the total COD of influent and effluent COD filtered, the Y\'obs was 0.143 g CODr.VSS.g-1. The sludge production (considering only the disposal of solid by conventional means) was 0.073 g COD.TS.g-1 .Both biomass fractions (suspended and attached) have similar potential to methanogenic conditions with organic load of 0.57 g COD.g-1 SVT. The production of electricity estimated to reuse biogas generated in HAnR, for the average flow of the period 7,170 m3.d-1, was 31,798 kW.h.mês-1, equivalent to 10% of the current monthly energy consumption in the sewage treatment plant. The use of this energy would result in a monthly savings of R$ 17,170.73.
Cattony, Eduardo Bosco Mattos. "Remoção de etanol, benzeno e tolueno em reator anaeróbio horizontal de leito fixo na presença de sulfato." Universidade de São Paulo, 2005. http://www.teses.usp.br/teses/disponiveis/18/18138/tde-08032016-120648/.
Повний текст джерелаPreviously, enrichment assays in batch reactors were used to evaluation of best nutritional condition, Beller or Zinder medium, to microorganism growth and sulfate removal. Further, the chosen nutritional condition was used in two horizontal-flow anaerobic immobilized biomass (HAIB) reactors under sulphate-reducing condition, which were exposed to different amounts of ethanol, toluene and benzene. The systems were inoculated with sludge taken from up-flow anaerobic sludge blanket (UASB) reactors treating refuses from a poultry slaughterhouse. The HAIB reactors comprised of an immobilized biomass on polyurethane foam and ferrous and sodium sulphate solutions were used (91 and 550 mg/L, respectively), to promote a sulphate-reducing environment. Toluene and benzene were added at an initial concentration of 2.0 mg/L followed by an increased range of different amendments. Ethanol was added at an initial concentration of 170 mg/L followed by an increased range of 960 mg/L. The reactors were operated at 30 (± 2) °C with hydraulic detention time of 12 h. Organic matter removal efficiency of 90%, in both systems, with a maximum toluene degradation rate of 0.06 mg toluene/mg vss.d and with a maximum benzene degradation rate of 0.07 mg benzene/mg vss.d. Sulfate reduction was dose to 99.9% for all-nutritional amendments in both systems. Biofilm microscopic characterization revealed a diversity of microbial morphologies and DGGE-profiling showed a variation of bacterial and sulphate reducing bacteria (SRB) populations, which were, significantly, associated with toluene and benzene amendments. Thus, this work demonstrates that compact units of HAIB reactors, under sulphate reducing conditions, are a potential alternative for in situ aromatic compounds bioremediation.
Yeshanew, Martha Minale. "Amélioration des rendements de traitement des déchets par digestion anaérobie : rôle d'un pré-traitement thermique et d'un traitement en bioréacteur en deux étapes." Thesis, Paris Est, 2016. http://www.theses.fr/2016PESC1166.
Повний текст джерелаAnaerobic digestion (AD) has been used over a century for an effective treatment of organic wastes. Interest in anaerobic treatment is continually increasing since it presents significant advantages when compared to alternative biological treatments and waste disposal options. This research study was mainly focused on optimization of the AD process, that was achieved through two different strategies. The first aimed at increasing the substrate biodegradability by a means of thermal pretreatment. The second was focused on the application of a biofilm based system to improve the biogas production rates and minimize the reactor size.Food waste (FW) was mainly used as a model substrate due to its suitable composition, abundance and renewability. In this thesis the influence of thermal pretreatment temperature on organic matter solubilization and methane yield of FW under different operational conditions was investigated. Significant improvement of the FW solubilization and biodegradability were observed for all thermally pretreated FW compared to the untreated FW. The highest biodegradability enhancement, i.e. + 28 %, was observed for FW treated at the lowest thermal pretreatment temperature, i.e. 80 ⁰C. The results showed a strong correlation between the substrate type (e.g. carbohydrate, protein and lipid content), the thermal pretreatment temperature and its effectiveness in promoting the biodegradability.In the second part of the work, a prolonged operation of an integrated two-stage system, including a continuously stirred tank and an anaerobic biofilm reactor, was carried out to produce biohythane (biohydrogen and methane) from the FW. The anaerobic biofilm reactor was employed to overcome the biomass wash-out from the reactor. The formation of a well-matured and balanced AD biomass greatly improved the process stability, which was not affected by shortening the hydraulic retention time (HRT) from 6 to 3.7 days in the first reactor and from 20 to 1.5 days in the second reactor. Moreover a two-stage system, comprised of a pilot scale batch dark fermenter and an anaerobic biofilm reactor co-producing hydrogen and methane from the organic fraction of municipal solid waste (OFMSW), was used to assess the capability of the anaerobic biofilm reactor to face an organic shock loads. The results showed a faster recovery of anaerobic biofilm reactor performance after the shock load events
McDonald, Heather Brown. "The effect of sulfide inhibition and organic shock loading on anaerobic biofilm reactors treating a low-temperature, high-sulfate wastewater." Diss., University of Iowa, 2007. http://ir.uiowa.edu/etd/129.
Повний текст джерелаКниги з теми "Anaerobic biofilm reactor"
Celeste, Stephen J. Biodegradation of chlorinated methanes using a methylotrophic/anaerobic biofilm reactor. 1990.
Знайти повний текст джерелаPolonsky, Jon D. The development of a gas-permeable-membrane-supported (GPMS) biofilm reactor for the combined anaerobic/aerobic treatment of polychlorinated biphenyls. 1988.
Знайти повний текст джерелаPolonsky, Jon D. The development of a gas-permeable-membrane-supported (GPMS) biofilm reactor for the combined anaerobic/aerobic treatment of polychlorinated biphenyls. 1988.
Знайти повний текст джерелаЧастини книг з теми "Anaerobic biofilm reactor"
Diez, V., F. Fdz-Polanco, and P. A. García. "Biofilm Growth in an Anaerobic Fluidized Bed Reactor." In Biofilms — Science and Technology, 443–48. Dordrecht: Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-1824-8_38.
Повний текст джерелаManariotis, Ioannis D., Sotirios G. Grigoropoulos, and Yung-Tse Hung. "Anaerobic Treatment of Low-Strength Wastewater by a Biofilm Reactor." In Environmental Bioengineering, 445–96. Totowa, NJ: Humana Press, 2010. http://dx.doi.org/10.1007/978-1-60327-031-1_14.
Повний текст джерелаAlmendrala, Michelle, Shekinah Mae Villaflor, Zhane Ann Tizon, Bonifacio Doma, and Ralph Carlo Evidente. "Immobilized Anaerobic Digestion of Molasses-Based Distillery Wastewater in Moving Bed Biofilm Reactor." In Proceedings of the 2022 12th International Conference on Environment Science and Engineering (ICESE 2022), 29–36. Singapore: Springer Nature Singapore, 2023. http://dx.doi.org/10.1007/978-981-99-1381-7_3.
Повний текст джерелаSkiadas, Ioannis V., Hariklia N. Gavala, Jens E. Schmidt, and Birgitte K. Ahring. "Anaerobic Granular Sludge and Biofilm Reactors." In Advances in Biochemical Engineering/Biotechnology, 35–67. Berlin, Heidelberg: Springer Berlin Heidelberg, 2003. http://dx.doi.org/10.1007/3-540-45838-7_2.
Повний текст джерелаJördening, H. J. "Anaerobic Biofilms in Fluidized Bed Reactors." In Biofilms — Science and Technology, 435–42. Dordrecht: Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-1824-8_37.
Повний текст джерелаLoganath, R., J. Senophiyah-Mary, and Teema Thomas. "A Study on Selection of the Biofilm for the Hybrid Up-Flow Anaerobic Sludge Blanket (HUASB) Reactor Using the Computational Fluid Dynamics (CFD) Analysis." In Emerging Technologies for Waste Valorization and Environmental Protection, 19–27. Singapore: Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-5736-1_3.
Повний текст джерелаMol, N., E. Heinzle, S. Petrozzi, O. M. Kut, and I. J. Dunn. "Carrier Influence for the Treatment of Industrial Wastewaters in Anaerobic Biofilm Fluidized Bed Reactors." In Recent Advances in Biotechnology, 419–24. Dordrecht: Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2468-3_25.
Повний текст джерелаSatya, Awalina, Fauziyah Istiqomah Arrahmah, and Tjandra Setiadi. "Anaerobic biofilm reactor: fundamentals and applications." In Current Developments in Biotechnology and Bioengineering, 407–50. Elsevier, 2022. http://dx.doi.org/10.1016/b978-0-323-99874-1.00013-0.
Повний текст джерелаHassan, Siti Roshayu Binti, Mohamad Johari Abu, and Irvan Dahlan. "Industrial Wastewater Treatment." In Handbook of Research on Resource Management for Pollution and Waste Treatment, 318–38. IGI Global, 2020. http://dx.doi.org/10.4018/978-1-7998-0369-0.ch014.
Повний текст джерелаFuentes, Mauren, Pío A. Aguirre, and Nicolás J. Scenna. "Heterogeneous Anaerobic Biofilm Reactor Models Application to UASB, EGSB and AFB Reactors." In Computer Aided Chemical Engineering, 297–302. Elsevier, 2009. http://dx.doi.org/10.1016/s1570-7946(09)70270-6.
Повний текст джерелаТези доповідей конференцій з теми "Anaerobic biofilm reactor"
Safitri, Anissa Sukma, and Roald Kommedal. "Effect of temperatures on anaerobic granulated biofilm modelling." In 63rd International Conference of Scandinavian Simulation Society, SIMS 2022, Trondheim, Norway, September 20-21, 2022. Linköping University Electronic Press, 2022. http://dx.doi.org/10.3384/ecp192030.
Повний текст джерелаRowena T. Romano and Ruihong Zhang. "Anaerobic Digestion of Juice from Pressed Onion Waste using a Mixed Biofilm Reactor." In 2005 Tampa, FL July 17-20, 2005. St. Joseph, MI: American Society of Agricultural and Biological Engineers, 2005. http://dx.doi.org/10.13031/2013.19932.
Повний текст джерелаJingwei Ma, Baisuo Zhao, Quanbao Zhao, Liang Yu, Craig Frear, and Shulin Chen. "Psychrophilic anaerobic sequencing batch reactor with biofilm supported by solids from dairy manure." In 2013 Kansas City, Missouri, July 21 - July 24, 2013. St. Joseph, MI: American Society of Agricultural and Biological Engineers, 2013. http://dx.doi.org/10.13031/aim.20131618715.
Повний текст джерелаTian, Zhiyong, Ping Zeng, Yonghui Song, Dong Li, and Jie Zhang. "Nitrogen Removal Potential and Biofilm Characteristics in the Anaerobic Ammonium Oxidation ('ANAMMOX') Biofilter Reactor." In 2010 4th International Conference on Bioinformatics and Biomedical Engineering (iCBBE). IEEE, 2010. http://dx.doi.org/10.1109/icbbe.2010.5514910.
Повний текст джерелаHassan, Gamal, Mohamed Azab El-Liethy, Fatma El-Gohary, Sherien Elagroudy, Mohamed Abo-Aly, and Isam Janajreh. "Two-stage Anaerobic Upflow Biofilm Reactor for Simultaneous Hydrogen and Methane Production from Food Waste." In 2018 6th International Renewable and Sustainable Energy Conference (IRSEC). IEEE, 2018. http://dx.doi.org/10.1109/irsec.2018.8702993.
Повний текст джерелаYue, Xiu-ping, Jing Wu, Qiu-jing Jiang, and Xiao-jin Liu. "Notice of Retraction: Inhibition of Ammonium Concentration on the Methanogenic Activity of Anaerobic Granular Sludge from Activated Sludge-Biofilm Anaerobic Hybrid Bio-Reactor." In 2011 5th International Conference on Bioinformatics and Biomedical Engineering. IEEE, 2011. http://dx.doi.org/10.1109/icbbe.2011.5781149.
Повний текст джерелаTizon, Zhane Ann, Louise Grace Avena, Jaira Neibel Bamba, Michelle Almendrala, and Ralph Carlo Evidente. "A REVIEW ON BIOGAS PRODUCTION BASED ON CIRCULAR ECONOMY VIA CO-DIGESTION AND IMMOBILIZED SUBSTRATES." In 22nd SGEM International Multidisciplinary Scientific GeoConference 2022. STEF92 Technology, 2022. http://dx.doi.org/10.5593/sgem2022v/4.2/s17.60.
Повний текст джерелаHongxiang, Chai, Hou Gaijuan, He Qiang, and Zhou Jian. "Comprehensive Influence of Salinity and Organic Load on Anaerobic Sequencing Batch Biofilm Reactor (ASBBR) Treating Mustard Tuber Wastewater." In 2013 Third International Conference on Intelligent System Design and Engineering Applications (ISDEA). IEEE, 2013. http://dx.doi.org/10.1109/isdea.2012.114.
Повний текст джерелаZhao Xudong, Zhao Zongsheng, Jia Weijing, Dai Jing, and Jiang Jing. "Mathematical simulations of nitrogen removal via a partial nitrification-anaerobic ammonium oxidation in a membrane-aerated biofilm reactor." In 2010 International Conference on Mechanic Automation and Control Engineering (MACE). IEEE, 2010. http://dx.doi.org/10.1109/mace.2010.5536335.
Повний текст джерелаSheli, Chai, and Rene Moletta. "Treatment of Wine Distillery Wastewater Using an Anaerobic Moving Bed Biofilm Reactor with Low Density of Polyethylene Support." In 2010 International Conference on Challenges in Environmental Science and Computer Engineering. IEEE, 2010. http://dx.doi.org/10.1109/cesce.2010.229.
Повний текст джерелаЗвіти організацій з теми "Anaerobic biofilm reactor"
Liu, B. Y. M., and J. T. Pfeffer. Modeling for Anaerobic Fixed-Bed Biofilm Reactors. Office of Scientific and Technical Information (OSTI), June 1989. http://dx.doi.org/10.2172/1129258.
Повний текст джерела