Effect of different gas releasing methods on anaerobic fermentative hydrogen production in batch cultures
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Chang, Sheng
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Harbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R ChinaHarbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R China
Chang, Sheng
[1
]
Li, Jianzheng
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Harbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R ChinaHarbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R China
Li, Jianzheng
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]
Liu, Feng
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Harbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R ChinaHarbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R China
Liu, Feng
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]
Yu, Ze
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Harbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R ChinaHarbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R China
Yu, Ze
[1
]
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[1] Harbin Inst Technol, Sch Municipal & Environm Engn, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R China
Decreasing hydrogen partial pressure can not only increase the activity of the hydrogen enzyme but also decrease the products inhibition, so it is an appropriate method to enhance the fermentative hydrogen production from anaerobic mixed culture. The effect of biogas release method on anaerobic fermentative hydrogen production in batch culture system was compared, i.e., Owen method with intermediately release, continuous releasing method, and continuous releasing + CO2 absorbing. The experimental results showed that, at 35A degrees C, initial pH 7.0 and glucose concentration of 10 g center dot L-1, the hydrogen production was only 28 mL when releasing gas by Owen method, while it increased two times when releasing the biogas continuously. The cumulative hydrogen production could reach 155 mL when carbon dioxide in the gas stream was continuously absorbed by 1 mol center dot L-1 NaOH. The results showed that acetate was dominated, accounting for 43% in the dissolved fermentation products in Owen method, whereas the butyrate predominated and reached 47%-53% of the total liquid end products when releasing gas continuously. It is concluded that the homoacetogenesis could be suppressed when absorbing CO2 in the gas phase in fermentative hydrogen production system.
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页码:901 / 906
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
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Arizona State Univ, Sch Life Sci, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
Zhang, Husen
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
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Arizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USAArizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USA
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Arizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USAArizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USA
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
Lee, Hyung-Sool
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Arizona State Univ, Sch Life Sci, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
Vermaas, Wim F. J.
Rittmann, Bruce E.
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
Lee, Hyung-Sool
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Krajmalnik-Brown, Rosa
Zhang, Husen
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
Zhang, Husen
Rittmann, Bruce E.
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Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USAArizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
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Arizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USAArizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USA
Lee, Hyung-Sool
Rittmann, Bruce E.
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Arizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USAArizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USA