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Статті в журналах з теми "Anaerobic Digestor Effluent"
Morel, E., K. Santamaria, M. Perrier, S. R. Guiot, and B. Tartakovsky. "Multi-wavelength fluorometry for anaerobic digestion process monitoring." Water Science and Technology 52, no. 1-2 (July 1, 2005): 465–71. http://dx.doi.org/10.2166/wst.2005.0554.
Повний текст джерелаSacks, J., and C. A. Buckley. "Anaerobic treatment of textile size effluent." Water Science and Technology 40, no. 1 (July 1, 1999): 177–82. http://dx.doi.org/10.2166/wst.1999.0038.
Повний текст джерелаSousa, Francine Aparecida, Alessandro Torres Campos, Pedro Ivo Sodré Amaral, Daiane Cecchin, and Alessandro Vieira Veloso. "PRODUÇÃO DE BIOGÁS PROVENIENTE DE CAMAS SOBREPOSTAS DE SUÍNOS." ENERGIA NA AGRICULTURA 32, no. 3 (December 20, 2017): 229. http://dx.doi.org/10.17224/energagric.2017v32n3p229-236.
Повний текст джерелаSacks, J., C. A. Buckley, E. Senior, and H. Kasan. "An assessment of the feasibility of anaerobic digestion as a treatment method for high strength or toxic organic effluents." Water Science and Technology 39, no. 10-11 (May 1, 1999): 347–51. http://dx.doi.org/10.2166/wst.1999.0680.
Повний текст джерелаSasaki, Ken, Tohru Tanaka, Yoshinori Nishizawa, and Mitsunori Hayashi. "Production of a herbicide, 5-aminolevulinic acid, by Rhodobacter sphaeroides using the effluent of swine waste from an anaerobic digestor." Applied Microbiology and Biotechnology 32, no. 6 (March 1990): 727–31. http://dx.doi.org/10.1007/bf00164749.
Повний текст джерелаGunnarsson, Anita, Börje Lindén, and Ulla Gertsson. "Biodigestion of Plant Material Can Improve Nitrogen Use Efficiency in a Red Beet Crop Sequence." HortScience 46, no. 5 (May 2011): 765–75. http://dx.doi.org/10.21273/hortsci.46.5.765.
Повний текст джерелаAbid, Aasima, Huriyah Khan, Tehseen Fatima Zeb, Syed Muneeb Uddin, Rafat Amin, Sadaf Khan, and Shaukat Ali. "Macromolecular characterization and growth kinetics of Arthrospira platensis and Chlorella Vulgaris as affected by different media (synthetic and Anaerobic Digestor Effluent) - A comparative study." INTERNATIONAL JOURNAL OF ENDORSING HEALTH SCIENCE RESEARCH (IJEHSR) 8, no. 4 (December 1, 2020): 188–201. http://dx.doi.org/10.29052/ijehsr.v8.i4.2020.188-201.
Повний текст джерелаAbid, Aasima, Huriyah Khan, Tehseen Fatima Zeb, Syed Muneeb Uddin, Rafat Amin, Sadaf Khan, and Shaukat Ali. "Macromolecular characterization and growth kinetics of Arthrospira platensis and Chlorella Vulgaris as affected by different media (synthetic and Anaerobic Digestor Effluent) - A comparative study." INTERNATIONAL JOURNAL OF ENDORSING HEALTH SCIENCE RESEARCH (IJEHSR) 8, no. 4 (December 1, 2020): 188–201. http://dx.doi.org/10.29052/ijehsr.v8.i4.2020.188-201.
Повний текст джерелаHemmati, Sadaf, M. Mostafa Elnegihi, Chee Hoong Lee, Darren Yu Lun Chong, Dominic C. Y. Foo, Bing Shen How, and ChangKyoo Yoo. "Synthesis of Large-Scale Bio-Hydrogen Network Using Waste Gas from Landfill and Anaerobic Digestion: A P-Graph Approach." Processes 8, no. 5 (April 26, 2020): 505. http://dx.doi.org/10.3390/pr8050505.
Повний текст джерелаRönner-Holm, S. G. E., A. Żak, and N. C. Holm. "Comparison of different conditions, substrates and operation modes by dynamic simulation of a full-scale anaerobic SBR plant." Water Science and Technology 65, no. 3 (February 1, 2012): 558–66. http://dx.doi.org/10.2166/wst.2012.887.
Повний текст джерелаДисертації з теми "Anaerobic Digestor Effluent"
Ledesma, Lina Marcela Sánchez. "Produção de estruvita a partir de esgoto doméstico." Universidade de São Paulo, 2014. http://www.teses.usp.br/teses/disponiveis/3/3147/tde-14082015-144656/.
Повний текст джерелаThe shortage of the phosphorus sources and high-energy consumption associated to the nitrogen fertilizers production will be problems in the future. The nutrient recovery from wastewater as struvite has been considered as an alternative to alleviate these problems. In Latin America, production of struvite from wastewater is not yet a wellknown technology and therefore the purpose of this work is to contribute to a better understanding of the phenomena involved. This research work was performed in three phases: 1) production of struvite from upflow anaerobic sludge blanket reactor effluent; 2) production of struvite from anaerobic digester supernatant of enhanced biological phosphorus removal process (ADS-EBPR) and 3) influence of calcium in the struvite produced in the phase 2. In three phases, the magnesium concentrations were adjusted to obtain the preset phosphorus:magnesium (P:Mg) ratios and the pH was adjusted between 8,00 and 10,50. The results of the first phase showed that it is not possible to produce struvite in the upflow anaerobic sludge blanket reactor effluent in the tested conditions. However, removal of nitrogen and phosphorus was observed because amorphous calcium and magnesium phosphates were produced. The results of the second phase showed that it is possible to produce struvite in the ADS-EBPR and the molar consumptions of phosphate (PO43-), ammonia (NH4+) and magnesium (Mg2+) or removals (%) should not be the only parameters to evaluate the struvite formation, because other compounds crystallize or precipitate and reduce the quality of the mineral. In the similar conditions tested in this phase, a P:Mg ratio 1:2 and pH 9,50 assure maximum nutrients recovery as struvite with minimum impurities concentration, facilitating its subsequent use as fertilizer. The results of the third phase showed that amorphous calcium or magnesium phosphates were produced on the struvite surface.
Wahal, Shantanu. "Nutrient Utilization from Anaerobic Digester Effluent Through Algae Cultivation." DigitalCommons@USU, 2010. https://digitalcommons.usu.edu/etd/671.
Повний текст джерелаFoster, Louise. "Microalgae culture to treat anaerobic digestion abattoir effluent (ADAE)." Thesis, Foster, Louise (2019) Microalgae culture to treat anaerobic digestion abattoir effluent (ADAE). Masters by Coursework thesis, Murdoch University, 2019. https://researchrepository.murdoch.edu.au/id/eprint/51443/.
Повний текст джерелаLloyd, Magaretha Hester. "Anaerobic digestion application in the treatment of gelatin-manufacturing effluent." Thesis, Stellenbosch : Stellenbosch University, 2000. http://hdl.handle.net/10019.1/51582.
Повний текст джерелаENGLISH ABSTRACT: A severely polluted industrial effluent is generated by the local gelatinmanufacturing industry. Due to increasingly stringent restrictions on discharge qualities enforced by the National Water Act of 1998 and National Environmental Management Act of 1998, as well as increasing trade-effluent charges implemented via the Local Municipal Bylaws, the industry is compelled to consider a system to pre-treat the polluted effluent. A study was undertaken to examine the viability of anaerobic treatment of the gelatin-manufacturing effluent, since the anaerobic digestion technology is well recognised for the high success rate in the treatment of high-strength, complex wastewaters. Various laboratory and pilot-scale studies were done, using different hybrid Upflow Anaerobic Sludge Blanket (UASB) and contact designs. Two mesophilic laboratory-scale hybrid UASB digester designs, fitted with polyethylene (AD-1) and polyurethane (AD-2), performed well at a hydraulic retention time (HRT) of 1.0 d. Chemical oxygen demand (COD) removal efficiencies of up to 90% (avg. 53%) for AD-1 and 83% (avg. 60%) for AD-2 at organic loading rates (OLR) of 9.56 and 4.62 kg COD.m-3.d-1, respectively, were obtained. High sulphate (S04) removal efficiencies of up to 96% (avg. 86%) for AD-1 and 98% (avg. 82%) for AD-2 were also achieved, respectively. A maximum total solid (TS) removal of 65% (avg. 25%) for AD-1 and 62% (avg. 28%) for AD-2 was reported. An average methane content of 80% (AD-1) and 79% (AD-2) with average methane yields per COD removed of 2.19 and 1.86 m3. kg CODremoved.df-o1r AD-1 and AD-2 were found, respectively. When the same digesters (AD-1 and AD-2) were combined in a muItiphase series configuration, a total COD removal efficiency of up to 97% (avg. 80%) at an OLR of 8.32 kg COD.m-3.d-1,was achieved. Excellent total S04 removals of 96% (avg. 69%) were accomplished. Up to 82% TS (avg. 29%) was also removed during this study and the biogas consisted of 89% methane (avg. 79%). For this multi-phase combination up to 92% volatile fatty acids (VFA) (avg. 48%) were removed, indicating possible selective phase separation of the respective fatty acid producing/utilising bacterial populations. The use of a laboratory-scale UASB bioreactor with recirculation, resulted in COD removal efficiencies of up to 96% (avg. 51%) at an HRT of 3.0 d, and 95% (avg. 54%) at a HRT of 1.0 d. Low performances were generally found, with average S04 and TS removals of 59% (max. 97%) and 26% (max. 67%), respectively at an HRT of 1.0 d. The biogas production was very low throughout the study (0.05 - 0.63 I,d-1 ). A pilot-scale UASB reactor (300 I) was constructed and performed satisfactory with a 58% average COD removal and maximum of 96%. S04 and TS removals up to 96% (avg. 44%) and 93% (avg. 63%), respectively, were obtained. The methane content of the biogas was 85%. The pilot-scale studies were conducted under actual field conditions, where various shock and organic loads had to be absorbed by the system. The pilot-scale contact configuration (300 I) did not perform satisfactory as a result of continuous blockages experienced in the feed and recirculation lines. Maximum COD, S04, VFA and TS removal efficiencies of 41% (avg. 27%), 62% (avg. 41%), 64% (avg. 27%) and 39% (avg. 21%), respectively, were obtained. The results of all the studies indicated acceptable COD removals with increasing OLR's. Indications of the presence of active methanogenic and sulphate-reducing bacterial populations were apparent throughout the studies. One possibility for the successful start-up and commissioning of the anaerobic reactors was the use of a well-adjusted biomass, which consisted of highly selected and adapted microbial consortium for the specific gelatinmanufacturing effluent. It was clear from this study that gelatin-manufacturing effluent can be treated successfully, especially with the use of the UASB design. A welldefined data base was constructed which could be of great value for further upscaling to a full-scale digester.
AFRIKAANSE OPSOMMING: 'n Hoogs besoedelde industriele uitvloeisel word gegenereer deur die plaaslike gelatien-vervaardigings industrie. As gevolg van toenemende streng beperkings op die kwaliteit van uitvloeisels wat bepaal word deur die Nasionale Water Wet van 1998 en Nasionale Omgewings Bestuurs Wet van 1998, asook toenemende munisipale heffings wat geimplementeer word via Plaaslike Munisipale Wette, word die industrie verplig om die uitvloeisel vooraf te behandel. 'n Studie is onderneem om die lewensvatbaarheid van anaërobe behandeling van gelatien-vervaardigings uitvloeisel te ondersoek, aangesien anaërobe verterings tegnologie alombekend is vir die goeie sukses behaal in die behandeling van hoë-sterkte, komplekse uitvloeisels. Verskeie laboratorium- en loods-skaal studies is gedoen, met verskillende hibried Opvloei Anaërobe Slykkombers (OAS) en kontak ontwerpe. Goeie werksverrigting was verkry by 'n hidroliese retensie tyd (HRT) van 1.0 d met twee mesofiliese laboratorium-skaal hibried OAS verteerder ontwerpe wat uitgevoer was met poli-etileen (AD-1) en poli-uretaan (AD-2) materiaal. Chemiese suurstof behoefte (CSB) verwyderings van so hoog as 90% (gem. 53%) vir AD-1 en 83% (gem. 60%) vir AD-2 by organiese ladingstempo's (OLT) van 9.56 en 4.62 kg CSB.m-3.d-1,was onderskeidelik verkry. Hoë sulfaat (S04) verwyderings van tot 96% (gem. 86%) vir AD-1 en 98% (gem. 82%) vir AD-2 was ook onderskeidelik verkry. 'n Maksimum totale vaste stof (TVS) verwydering van 65% (gem. 25%) vir AD-1 en 62% (gem. 28%) vir AD-2 is gerapporteer. 'n Gemiddelde metaan inhoud van 80% (AD-1) en 79% (AD-2) met 'n gemiddelde metaan opbrengs per CSB verwyder van 2.19 en 1.86 m3.kg CSBverwyder.dv-i1r AD-1 en AD-2, was onderskeidelik gevind. Met die aanwending van dieselfde twee verteerders (AD-1 en AD-2) in 'n series gekoppelde multi-fase konfigurasie, is 'n totale CSB verwydering so hoog as 97% (gem. 80%) verkry by 'n OLT van 8.32 kg CSB.m-3.d-1. Uitstekende totale S04 verwydering van 96% (gem. 69%) is behaal. Tot 82% TVS (gem. 29%) was vewyder gedurende die studie en die biogas het uit 89% metaan (gem. 79%) bestaan. Vir die multi-fase kombinasie is 'n maksimum van 92% vlugtige vetsure (WS) (gem. 48%) verwyder, wat dui op die moontlike skeiding van selektiewe fases van die onderskeie vetsuur produserende/verbruiker bakteriële populasies. CSB verwydering van tot 96% (gem. 51%) by 'n HRT van 3.0 d en 95% (gem. 54%) met 'n HRT van 1.0 d was verkry, tydens die gebruik van In laboratorium-skaal OAS bioreaktor met hersirkulasie. Lae werksverrigting was oor die algemeen waargeneem, met gemiddelde S04 en TVS verwyderings van 59% (maks. 97%) en 26% (maks. 67%) by In HRT van 1.0 d. Die biogas produksie was baie laag gedurende die studie (0.05 - 0.63 I,d-\ In Loods-skaal OAS verteerder was opgerig en bevredigende resultate was verkry met In gemiddeld van 58% CSB verwydering en maksimum van 96%. S04 en TVS verwyderings so hoog as 96% (gem. 44%) en 93% (gem. 63%) is onderskeidelik verkry. Die metaan inhoud van die biogas was 85%. Die loods-skaal studie was uitgevoer gedurende ware veld kondisies, waartydens verskeie skok en organiese ladings deur die sisteem geabsorbeer is. Die loods-skaal kontak konfigurasie (300 I) het nie bevredigende resultate getoon nie, as gevolg van voortdurende blokkasies wat ondervind is in die toevoer en hersirkulasie pype. Maksimum CSB, S04, WS en TVS verwyderings van 41% (gem. 27%), 62% (gem. 41%), 64% (gem. 27%) en 39% (gem. 21%) was onderskeidelik verkry. Die resultate van al die studies het aanvaarbare CSB verwydering aangedui by toenemende OLT's. Indikasies van aktiewe metanogene en sulfaat-reduserende bakteriële populasies was ook teenwoordig gedurende die studies. Die suksesvolle aansit-prosedure en begin van die anaërobe verteerders kan toegeskryf word aan die gebruik van In goed aangepaste biomassa, wat uit hoogs selektiewe en aangepaste mikrobiese populasies vir die spesifieke uitvloeisel bestaan. Hierdie studie het getoon dat gelatien-vervaardigings uitvloeisel suksesvol met die OAS ontwerp behandel kan word. In Goed gedefinieerde data basis kan voorsien word, wat van groot waarde sal wees vir verdere opgradering na In volskaalse verteerder.
Fell, Christopher John. "Monitoring and control of anaerobic digesters treating industrial effluents." Thesis, Loughborough University, 1999. https://dspace.lboro.ac.uk/2134/32621.
Повний текст джерелаVoegel, Célestine. "Impact BIochimique des effluents agricoles et agroindustriels sur les structures/ouvrages en BEtOn dans la filière de valorisation par Méthanisation (ou codigestion anaérobie)." Thesis, Toulouse, INPT, 2017. http://www.theses.fr/2017INPT0044/document.
Повний текст джерелаAnaerobic digestion consists in the degradation of organic matter by the successive actions of microorganisms, industrially operated in digesters made of concrete. Microbial metabolites (volatile fatty acids (VFA), NH4+, CO2) produced during this process attack the cementitious matrix of the concrete. To ensure the development of this new industrial field, it appears essential to understand first the alteration phenomena, then to propose durable solutions for digesters’ construction materials. The thesis’ objectives were first to identify and to quantify the aggressive agents for concrete in anaerobic digestion media, then to understand their impacts on the cementitious materials’ alteration mechanisms. Finally, the impacts of those media were compared on different cement pastes made of : ordinary Portland cement, blast furnace slag cement, calcium aluminate cement or alkali activated materials. During laboratory tests, the maximal concentration in aggressive agents measured during the digestion of a synthetic biowaste were 3 000 mg.L-1 of VFA, 800 mg.L-1 of NH4+, and 140 mg.L-1 of dissolved CO2. The colonization of the microorganisms able to produce the aggressive agents has been observed on the cementitious materials’ surfaces exposed to the biowaste during digestion. The external degraded layers of the exposed cementitious materials are partially decalcified, most likely regarding to the action of the VFA and the NH4+. Carbonation has also been detected caused by the dissolved CO2. In situ experiments, in real conditions, achieved in an experimental anaerobic digestion platform, confirmed the alteration phenomena distinguished in the laboratory tests. In terms of durability, calcium aluminate cement present the best performances against the biochemical attacks compared to ordinary cement or blast furnace slag cement in laboratory or in situ anaerobic digestion systems
Fallon, Dillon. "Co-Digestion of Cattle Manure and Cheese Whey for Biogas Production and Characterization of Biomass Effluent." DigitalCommons@USU, 2018. https://digitalcommons.usu.edu/etd/7308.
Повний текст джерелаFernandes, Aline [UNESP]. "Água residuária de laticínio em co-digestão com dejetos de bovinos leiteiros." Universidade Estadual Paulista (UNESP), 2016. http://hdl.handle.net/11449/143781.
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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
A pecuária leiteira bem como a industrialização do leite produzem resíduos que podem impactar o meio se lançados de forma imprópria. Sendo assim, objetivou-se avaliar o efeito da co-digestão de água residuária de laticínio com dejetos bovinos em biodigestores do tipo batelada e contínuo sobre a produção de biogás e biofertilizante. O experimento foi dividido em duas fases. A primeira fase desenvolvida com biodigestores batelada e a segunda subdividida em dois períodos com biodigestores contínuos. Avaliou-se o efeito da inclusão de água residuária de laticínio (ARL) na primeira etapa: 0% de ARL, 50% de ARL, 77,5% de ARL, 100% de ARL e tratamento ARL. Para segunda fase no primeiro período tratamento com 0% de ARL e 50% de ARL. E no segundo período com tratamentos de 0% ARL e 63,5% ARL. Para análise dos dados considerou-se um delineamento inteiramente casualizado, utilizando-se o programa SAS® com nível de significância de 5%. Para a primeira fase, observou–se que o tratamento ARL foi o que apresentou menor produção de biogás (0,00753 m3) em relação aos demais. Para os potenciais de produção o tratamento com 50% de ARL apresentou as menores médias. Nos dois períodos da segunda fase, ou seja, com biodigestores contínuos, os resultados demonstram que os tratamentos contendo água residuária foram eficientes sem diferença de produção de biogás entre os tratamentos. O aproveitamento da água residuária para compor substrato em co-digestão com dejetos bovinos leiteiros apresentou condições favoráveis de produção e qualidade de biogás e biofertilizante.
The dairy farming and industrialization of milk produce waste that may impact the environment if disposed improperly. Thus, this study aimed to evaluate the effect of co-digestion of dairy production wastewater with cattle manure in biodigesters in the batch and continuous type on the production of biogas and biofertilizers. The experiment was divided into two phases. The first phase developed with batch digesters and second divided in two periods with continuous digesters. We evaluated the effect of the inclusion of dairy wastewater (DW) in the first stage: 0% of DW, 50% of DW, 77,5% of DW, 100% of DW and DW treatment. For the second phase the first treatment period with 0% and 50% DW. And in the second period with treatments of 0% and 63.5% DW. Data analysis was considered a completely randomized design, using the SAS® program with 5% significance level. For the first phase, it was observed that the DW treatment showed the lower production of biogas (0.00753 m3) compared to the others treatments. For the production potential treatment with 50% of DW had the lowest means. In the second phase in both periods, with continuous digesters, the results show that the treatments containing wastewater were effective and there is no difference in biogas production between the treatments. The use of wastewater to form substrate co-digestion of dairy cattle manure showed favorable production conditions and quality of biogas and biofertilizers.
Sekar, Samantha. "The Effects of Biochar and Anaerobic Digester Effluent on Soil Quality and Crop Growth in Karnataka, India." The Ohio State University, 2012. http://rave.ohiolink.edu/etdc/view?acc_num=osu1343750717.
Повний текст джерелаRodriguez-Chiang, Lourdes. "Enhancement of methane production from the anaerobic digestion of chemical pulp and paper mill effluents." Doctoral thesis, Universitat Politècnica de Catalunya, 2018. http://hdl.handle.net/10803/669251.
Повний текст джерелаLa sostenibilidad en la gestión de recursos como la energía, el agua y los residuos se ha convertido en un aspecto clave en nuestra economía actual. Para grandes industrias que consumen mucha agua y energía, como la industria de pulpa y papel (P&P) este es un tema especialmente relevante. Los grandes y heterogéneos volúmenes de efluentes que producen las fábricas de P&P hacen que su adecuado tratamiento sea una tarea difícil. La digestión anaerobia es una tecnología eficiente para el tratamiento de aguas residuales; que limpia el efluente, reduce el lodo producido y simultáneamente produce metano que puede usarse como fuente de energía. El objetivo del trabajo de investigación descrito en esta tesis es aumentar la producción de metano a partir de la digestión anaerobia de diferentes efluentes producidos en fábricas de pulpa. A través de la caracterización del efluente, determinación de parámetros del proceso, agentes promotores y la evaluación de pruebas de producción de metano bioquímico se evaluaron los beneficios de tres métodos potenciales para mejorar los rendimientos de metano de los efluentes. Asimismo, se exploró la conversión directa de fibras de pulpa química a metano. Los efluentes fácilmente degradables, como los filtrados hidrolizados y los condensados del evaporador, contienen altas concentraciones de azúcares y ácido acético, respectivamente, lo que podría provocar una sobresaturación de ácidos durante la acidogénesis. Se ha demostrado que una relación de inóculo a sustrato de 2 resulta óptima para aumentar la capacidad tampón del sistema y neutralizar el pH y producir rendimientos de metano significativamente altos, de hasta 333 mLCH4/gVS. La alta productividad de estos efluentes hace que se puedan considerar para la co-digestión con efluentes más difíciles de tratar, como las aguas ricas en lignina. Claramente la lignina obstaculiza la producción de metano, tal y como indica la correlación lineal negativa encontrada entre el contenido de lignina y el rendimiento de metano. La co-digestión del efluente rico en lignina con el condensado de evaporadores de pulpa semi-química de sulfito ha demostrado mejorar la productividad de metano en el tratamiento de aguas residuales de la planta. Además, la adición de hidrotalcitas (HT) como catatlizadores contribuye hacia un aumento en la producción de metano, tasas de producción más rápidas y una mayor eliminación de lignina. Con HT calcinadas se han obtenido rendimientos bajos, lo que sugiere que las ventajas de la adición de HT provienen de su estructura laminar. Finalmente, además de establecer el potencial de metano que existen en los efluentes de P&P, la evaluación de la productividad de metano de diferentes fibras de pulpa y sus productos ha demostrado ser una nueva alternativa energética para explorar. El uso de pulpa blanqueada, sin blanquear y deslignificada con oxígeno muestran biodegradabilidades de hasta 90% y rendimientos de metano de hasta 380 mLCH4/gVS. Con la cambiante bioeconomía actual, este último enfoque estimula la exploración de usos alternativos y novedosos para productos de plantas de pulpa química.
Книги з теми "Anaerobic Digestor Effluent"
Horan, Nigel, Abu Zahrim Yaser, and Newati Wid. Anaerobic Digestion Processes: Applications and Effluent Treatment. Springer, 2018.
Знайти повний текст джерелаAnaerobic Digestion Processes: Applications and Effluent Treatment. Springer, 2018.
Знайти повний текст джерелаFell, Chris John. Monitoring and control of anaerobic digesters treating industrial effluents. 1999.
Знайти повний текст джерелаIndustrial wastewater and effluent treatment: A review of anaerobic digestion technology. Department of Trade and Industry, 2001.
Знайти повний текст джерелаIndustrial Scale Treatment of Chemical Effluents by the SGN Fixed Film Anaerobic Digestion Process: Energy: Energy [series]. European Communities / Union (EUR-OP/OOPEC/OPOCE), 1995.
Знайти повний текст джерелаЧастини книг з теми "Anaerobic Digestor Effluent"
Zahrim, A. Y. "Current Progress on Removal of Recalcitrance Coloured Particles from Anaerobically Treated Effluent Using Coagulation–Flocculation." In Anaerobic Digestion Processes, 149–63. Singapore: Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-10-8129-3_9.
Повний текст джерелаPoh, Phaik Eong, Ta Yeong Wu, Weng Hoong Lam, Wai Ching Poon, and Chean Shen Lim. "High-Rate Anaerobic Digestion of POME for Stable Effluent and Biogas Production." In Waste Management in the Palm Oil Industry, 45–56. Cham: Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-39550-6_4.
Повний текст джерелаXu, Hui, Yanbiao Liu, Bo Yang, Ruihong Wei, Fang Li, and Sand Wolfgang. "Role of Interspecies Electron Transfer for Boosting Methane Production by Anaerobic Digestion in Syntrophic Methanogenesis." In Combined Application of Physico-Chemical & Microbiological Processes for Industrial Effluent Treatment Plant, 65–77. Singapore: Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-0497-6_5.
Повний текст джерелаVenkatesh Babu, S., and M. Rajasimman. "Performance Analysis of Anaerobic Digestion of Textile Dyeing Industry Effluent in a Modified Sequential Batch Reactor." In Biochemical and Environmental Bioprocessing, 37–52. First edition. | Boca Raton, FL : CRC Press/Taylor & Francis Group, 2020.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429198045-3.
Повний текст джерелаRosas-Mendoza, Erik Samuel, Joahnn Hernando Palacios-Ríos, Juan Manuel Méndez-Contreras, Norma Alejandra Vallejo-Cantú, and Alejandro Alvarado-Lassman. "Designing a Supply Chain for the Generation of Bioenergy from the Anaerobic Digestion of Citrus Effluents." In Intelligent Systems Reference Library, 209–35. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-26488-8_10.
Повний текст джерелаMilia, S., G. Tocco, G. Erby, G. De Gioannis, and A. Carucci. "Preliminary Evaluation of Sharon-Anammox Process Feasibility to Treat Ammonium-Rich Effluents Produced by Double-Stage Anaerobic Digestion of Food Waste." In Lecture Notes in Civil Engineering, 536–43. Cham: Springer International Publishing, 2017. http://dx.doi.org/10.1007/978-3-319-58421-8_84.
Повний текст джерелаd’Espiney, Ana, Isabel Paula Marques, and Helena Maria Pinheiro. "Case Study: Pathways from Forest to Energy in a Circular Economy at Lafões." In Forest Biomass - From Trees to Energy. IntechOpen, 2021. http://dx.doi.org/10.5772/intechopen.93070.
Повний текст джерелаBelmonte, Marisol, Carmen Fajardo, Javiera Belén Toledo-Alarcón, Daniel Valenzuela Heredia, Lorena Jorquera, Ramón Méndez, Estela Tapia-Venegas, and Gonzalo Ruiz-Filippi. "Autotrophic Denitrification Processes." In Technologies for the Treatment and Recovery of Nutrients from Industrial Wastewater, 147–73. IGI Global, 2017. http://dx.doi.org/10.4018/978-1-5225-1037-6.ch006.
Повний текст джерела"Enhancement of Anaerobic Digestion of Pharmaceutical Effluent." In Environmental Sustainability Using Green Technologies, 191–212. Taylor & Francis Group, 6000 Broken Sound Parkway NW, Suite 300, Boca Raton, FL 33487-2742: CRC Press, 2016. http://dx.doi.org/10.1201/9781315364339-9.
Повний текст джерела"◾ Enhancement of Anaerobic Digestion of Pharmaceutical Effluent." In Environmental Sustainability Using Green Technologies, 229–50. CRC Press, 2016. http://dx.doi.org/10.1201/9781315364339-18.
Повний текст джерелаТези доповідей конференцій з теми "Anaerobic Digestor Effluent"
Zemke, Peter E., Byard D. Wood, and Christopher R. Rohleder. "Effect of Solids Removal From Dairy Manure Feedstock on Biogas Production in Anaerobic Digesters." In ASME 2010 4th International Conference on Energy Sustainability. ASMEDC, 2010. http://dx.doi.org/10.1115/es2010-90235.
Повний текст джерела"Comparison of digestate from solid anaerobic digesters and effluent from liquid anaerobic digesters as inocula for solid state anaerobic digestion of yard trimming." In 2015 ASABE International Meeting. American Society of Agricultural and Biological Engineers, 2015. http://dx.doi.org/10.13031/aim.20152190124.
Повний текст джерелаChin, S. K., D. T. Tan, H. M. Tan, and P. E. Poh. "Preservation of mesophilic mixed culture for anaerobic palm oil mill effluent treatment by convective drying methods." In 21st International Drying Symposium. Valencia: Universitat Politècnica València, 2018. http://dx.doi.org/10.4995/ids2018.2018.7295.
Повний текст джерелаEl Achkar, Jean H., Abrar Ben Husain, Nadeen Alotaibi, Noor Alhaddad, Taiyeba Alamgir, Husain Alshamali, Yousef Alshammari, et al. "Could Petroleum Sludge be Used to Produce Biomethane as a Renewable Energy Source?" In ADIPEC. SPE, 2022. http://dx.doi.org/10.2118/210953-ms.
Повний текст джерелаUchimura, Koki, Yuki Sago, Hirotsugu Kamahara, Yoichi Atsuta, and Hiroyuki Daimon. "Treatment of anaerobic digestion effluent of sewage sludge using soilless cultivation." In THE IRAGO CONFERENCE 2013. AIP Publishing LLC, 2014. http://dx.doi.org/10.1063/1.4866619.
Повний текст джерелаXiaohui Lei, Wei Bai, Guoqiang Liu, Chuanping Feng, and Takaaki Maekawa. "Nitrogen removal of pretreated anaerobic digestion effluent in a soil column." In International Symposium on Air Quality and Waste Management for Agriculture, 16-19 September 2007, Broomfield, Colorado. St. Joseph, MI: American Society of Agricultural and Biological Engineers, 2007. http://dx.doi.org/10.13031/2013.23807.
Повний текст джерела"Comparison of solid-state anaerobic digestion to composting of yard trimmings with effluent from liquid anaerobic digestion: effect of total solids content and feedstock to effluent ratio." In 2014 ASABE Annual International Meeting. American Society of Agricultural and Biological Engineers, 2014. http://dx.doi.org/10.13031/aim.20141897526.
Повний текст джерелаHalim, Lenny, Melly Mellyanawaty, Rochim Bakti Cahyono, Hanifrahmawan Sudibyo, and Wiratni Budhijanto. "Anaerobic digestion of palm oil mill effluent with lampung natural zeolite as microbe immobilization medium and digested cow manure as starter." In INTERNATIONAL SEMINAR ON FUNDAMENTAL AND APPLICATION OF CHEMICAL ENGINEERING 2016 (ISFAChE 2016): Proceedings of the 3rd International Seminar on Fundamental and Application of Chemical Engineering 2016. Author(s), 2017. http://dx.doi.org/10.1063/1.4982333.
Повний текст джерелаAziz, Nur Izzah Hamna A., and Marlia M. Hanafiah. "Anaerobic digestion of palm oil mill effluent (POME) using bio-methane potential (BMP) test." In THE 2017 UKM FST POSTGRADUATE COLLOQUIUM: Proceedings of the University Kebangsaan Malaysia, Faculty of Science and Technology 2017 Postgraduate Colloquium. Author(s), 2018. http://dx.doi.org/10.1063/1.5027941.
Повний текст джерелаTan, H. M., J. C. S. Lew, D. Gouwanda, and P. E. Poh. "Fuzzy logic modelling for thermophilic anaerobic digestion of palm oil mill effluent (POME) treatment." In 2017 4th International Conference on Industrial Engineering and Applications (ICIEA). IEEE, 2017. http://dx.doi.org/10.1109/iea.2017.7939219.
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