The production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (UASB)

© 2016 Penerbit UTM Press. All rights reserved. The main objective was to separately generate biohydrogen (H 2 ) and biomethane (CH 4 ) with the cassava wastewater via the upflow anaerobic sludge blanket reactors (UASB) under the mesophilic temperature (37 ºC). For the first part, the production of...

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Main Authors: Intanoo P., Chavadej S., Khongsumran O.
Format: Journal
Published: 2017
Online Access:https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84968764967&origin=inward
http://cmuir.cmu.ac.th/jspui/handle/6653943832/42515
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Institution: Chiang Mai University
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spelling th-cmuir.6653943832-425152017-09-28T04:27:33Z The production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (UASB) Intanoo P. Chavadej S. Khongsumran O. © 2016 Penerbit UTM Press. All rights reserved. The main objective was to separately generate biohydrogen (H 2 ) and biomethane (CH 4 ) with the cassava wastewater via the upflow anaerobic sludge blanket reactors (UASB) under the mesophilic temperature (37 ºC). For the first part, the production of H 2 , the controlled system was managed on the fixed temperature (37 º C) and pH (5.5) included the varied organic concentration in term of chemical oxygen demand (COD) loading rates. As the proper COD loading rate of 25 kg/m 3 d, H 2 and carbon dioxide (CO 2 ) were mainly generated gases which provided the highest specific H 2 production rate of 0.39 l H 2 /l d and the highest H 2 yield of 39.83 l H 2 /kg COD removed. For the second part, the effluent liquid that generated from the stage of H2 production on COD loading rate of 25 kg/m 3 d was fed to the UASB with the fixed temperature (37 °C) and no pH control. The highest specific CH 4 production rate of 0.91 l CH 4 /l d and the highest CH 4 yield of 115.23 l CH 4 /kg COD removed were shown on the proper COD loading rate of 8 kg/m 3 d. 2017-09-28T04:27:33Z 2017-09-28T04:27:33Z 2016-01-01 Journal 01279696 2-s2.0-84968764967 10.11113/jt.v78.8629 https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84968764967&origin=inward http://cmuir.cmu.ac.th/jspui/handle/6653943832/42515
institution Chiang Mai University
building Chiang Mai University Library
country Thailand
collection CMU Intellectual Repository
description © 2016 Penerbit UTM Press. All rights reserved. The main objective was to separately generate biohydrogen (H 2 ) and biomethane (CH 4 ) with the cassava wastewater via the upflow anaerobic sludge blanket reactors (UASB) under the mesophilic temperature (37 ºC). For the first part, the production of H 2 , the controlled system was managed on the fixed temperature (37 º C) and pH (5.5) included the varied organic concentration in term of chemical oxygen demand (COD) loading rates. As the proper COD loading rate of 25 kg/m 3 d, H 2 and carbon dioxide (CO 2 ) were mainly generated gases which provided the highest specific H 2 production rate of 0.39 l H 2 /l d and the highest H 2 yield of 39.83 l H 2 /kg COD removed. For the second part, the effluent liquid that generated from the stage of H2 production on COD loading rate of 25 kg/m 3 d was fed to the UASB with the fixed temperature (37 °C) and no pH control. The highest specific CH 4 production rate of 0.91 l CH 4 /l d and the highest CH 4 yield of 115.23 l CH 4 /kg COD removed were shown on the proper COD loading rate of 8 kg/m 3 d.
format Journal
author Intanoo P.
Chavadej S.
Khongsumran O.
spellingShingle Intanoo P.
Chavadej S.
Khongsumran O.
The production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (UASB)
author_facet Intanoo P.
Chavadej S.
Khongsumran O.
author_sort Intanoo P.
title The production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (UASB)
title_short The production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (UASB)
title_full The production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (UASB)
title_fullStr The production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (UASB)
title_full_unstemmed The production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (UASB)
title_sort production of biohydrogen and biomethane from cassava wastewater under mesophilic anaerobic fermentation by using upflow anaerobic sludge blanket reactors (uasb)
publishDate 2017
url https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84968764967&origin=inward
http://cmuir.cmu.ac.th/jspui/handle/6653943832/42515
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