Dry anaerobic digestion in batch mode: Design and operation of a laboratory-scale, completely mixed reactor
A laboratory-scale (40 l) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling complete mixing in the reactor. Three consecutive batch dry digestion tests of municipal solid waste were performed under mesophilic conditions a...
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Published in | Waste management (Elmsford) Vol. 30; no. 10; pp. 1768 - 1771 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
United States
Elsevier Ltd
01.10.2010
Elsevier |
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Abstract | A laboratory-scale (40
l) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling complete mixing in the reactor. Three consecutive batch dry digestion tests of municipal solid waste were performed under mesophilic conditions and compared to operation results obtained on a pilot-scale (21
m
3) with the same feedstock. Biogas and methane production at the end of the tests were similar (around 200
m
3 CH
4STP/tVS), and the dynamics of methane production and VFA accumulation concurred. However, the maximal levels of VFA transitory accumulation varied between reactors and between runs in a same reactor. Ammonia levels were similar in both reactors. These results show that the new reactor accurately imitates the conditions found in larger ones. Adaptation of micro-organisms to the waste and operating conditions was also pointed out along the consecutive batches. |
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AbstractList | A laboratory-scale (40
l) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling complete mixing in the reactor. Three consecutive batch dry digestion tests of municipal solid waste were performed under mesophilic conditions and compared to operation results obtained on a pilot-scale (21
m
3) with the same feedstock. Biogas and methane production at the end of the tests were similar (around 200
m
3 CH
4STP/tVS), and the dynamics of methane production and VFA accumulation concurred. However, the maximal levels of VFA transitory accumulation varied between reactors and between runs in a same reactor. Ammonia levels were similar in both reactors. These results show that the new reactor accurately imitates the conditions found in larger ones. Adaptation of micro-organisms to the waste and operating conditions was also pointed out along the consecutive batches. A laboratory-scale (40 l) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling complete mixing in the reactor. Three consecutive batch dry digestion tests of municipal solid waste were performed under mesophilic conditions and compared to operation results obtained on a pilot-scale (21 m(3)) with the same feedstock. Biogas and methane production at the end of the tests were similar (around 200 m(3) CH(4)STP/tVS), and the dynamics of methane production and VFA accumulation concurred. However, the maximal levels of VFA transitory accumulation varied between reactors and between runs in a same reactor. Ammonia levels were similar in both reactors. These results show that the new reactor accurately imitates the conditions found in larger ones. Adaptation of micro-organisms to the waste and operating conditions was also pointed out along the consecutive batches. A laboratory-scale (401) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling complete mixing in the reactor. Three consecutive batch dry digestion tests of municipal solid waste were performed under mesophilic conditions and compared to operation results obtained on a pilot-scale (21 m(3)) with the same feedstock. Biogas and methane production at the end of the tests were similar (around 200 m(3) CH4STP/tVS), and the dynamics of methane production and VFA accumulation concurred. However, the maximal levels of VFA transitory accumulation varied between reactors and between runs in a same reactor. Ammonia levels were similar in both reactors. These results show that the new reactor accurately imitates the conditions found in larger ones. Adaptation of micro-organisms to the waste and operating conditions was also pointed out along the consecutive batches. A laboratory-scale (40l) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling complete mixing in the reactor. Three consecutive batch dry digestion tests of municipal solid waste were performed under mesophilic conditions and compared to operation results obtained on a pilot-scale (21m3) with the same feedstock. Biogas and methane production at the end of the tests were similar (around 200m3 CH4STP/tVS), and the dynamics of methane production and VFA accumulation concurred. However, the maximal levels of VFA transitory accumulation varied between reactors and between runs in a same reactor. Ammonia levels were similar in both reactors. These results show that the new reactor accurately imitates the conditions found in larger ones. Adaptation of micro-organisms to the waste and operating conditions was also pointed out along the consecutive batches. |
Author | Guendouz, J. Cacho, J. Buffière, P. Carrère, M. Delgenes, J.-P. |
Author_xml | – sequence: 1 givenname: J. surname: Guendouz fullname: Guendouz, J. organization: Centre de Recherche sur la Propreté (VEOLIA), Zone Portuaire de Limay, 291 Avenue Dreyfous Ducas, Limay, F-78250, France – sequence: 2 givenname: P. surname: Buffière fullname: Buffière, P. email: pierre.buffiere@insa-lyon.fr organization: Université de Lyon, INSA-Lyon, Laboratoire de Génie Civil et d’Ingénierie Environnementale, 9 rue de la Physique, F-69621, Villeurbanne cedex, France – sequence: 3 givenname: J. surname: Cacho fullname: Cacho, J. organization: Centre de Recherche sur la Propreté (VEOLIA), Zone Portuaire de Limay, 291 Avenue Dreyfous Ducas, Limay, F-78250, France – sequence: 4 givenname: M. surname: Carrère fullname: Carrère, M. organization: Centre de Recherche sur la Propreté (VEOLIA), Zone Portuaire de Limay, 291 Avenue Dreyfous Ducas, Limay, F-78250, France – sequence: 5 givenname: J.-P. surname: Delgenes fullname: Delgenes, J.-P. organization: INRA, UR50, Laboratoire de Biotechnologie de l’Environnement, Avenue des Etangs, Narbonne, F-11100, France |
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l) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling... A laboratory-scale (40 l) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling... A laboratory-scale (40l) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling... A laboratory-scale (401) reactor was designed to investigate dry anaerobic digestion. The reactor is equipped with an intermittent paddle mixer, enabling... |
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SubjectTerms | Ammonia Ammonia - metabolism Anaerobic digestion Bacteria, Anaerobic - metabolism Bioreactors Chromatography, Gas Digestion Drying Environment and Society Environmental Sciences Feedstock Methane Methane - biosynthesis Reactors Refuse Disposal - instrumentation Refuse Disposal - methods Waste management Wastes |
Title | Dry anaerobic digestion in batch mode: Design and operation of a laboratory-scale, completely mixed reactor |
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