Enhancement of hydrogen production from glucose by nitrogen gas sparging

被引:452
作者
Mizuno, O
Dinsdale, R
Hawkes, FR
Hawkes, DL [1 ]
Noike, T
机构
[1] Univ Glamorgan, Sch Design & Adv Technol, Pontypridd CF37 1DL, M Glam, Wales
[2] Tohoku Univ, Dept Civil Engn, Grad Sch Engn, Sendai, Miyagi 9808597, Japan
[3] Univ Glamorgan, Sch Appl Sci, Pontypridd CF37 1DL, M Glam, Wales
基金
英国工程与自然科学研究理事会;
关键词
hydrogen partial pressure; biological hydrogen production; hydrogen yield; N-2; sparging;
D O I
10.1016/S0960-8524(99)00130-3
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The effect on hydrogen yield of N-2 Sparging was investigated in non-sterile conditions using a hydrogen-producing mixed culture previously enriched from soya bean meal. A continuous stirred-tank reactor (CSTR) at 35 degrees C and pH 6.0 was operated on a mineral salts-glucose (10 g l(-1)) medium at a hydraulic retention time (HRT) of 8.5 h, and organic loading rate of 27.02 g glucose litre reactor(-1) day(-1). Results are reported from an 8 week period of continuous operation, and the enrichment culture gave stable results over an extended period. A hydrogen yield of 0.85 moles H-2/mole glucose consumed was obtained after 5 HRT, the gas produced being 53.4% H-2 With N-2 Sparging at a flow rate approximately 15 times the hydrogen production rate, the hydrogen yield was 1.43 moles H-2/mole glucose consumed. The specific hydrogen production rate increased from 1.446 mi hydrogen min(-1)g(-1) biomass to 3.131 mi hydrogen min(-1) g(-1) biomass under sparging conditions. It is suggested that hydrogen partial pressure in the liquid phase was an important factor affecting hydrogen yield. Energy could be recovered as hydrogen from processes generating volatile fatty acids for fine chemicals and liquid bio-fuels or from acidification reactors preceding normal anaerobic biological treatment of sugary wastewaters. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:59 / 65
页数:7
相关论文
共 29 条
[1]  
Andel J. G., 1985, APPL MICROBIOL BIOT, V23, P21, DOI 10.1007/bf02660113
[2]  
APHA, 1992, STAND METH EX WAST W
[3]  
BAHL H, 1984, BIOTECHNOL BIOENG S, V14, P215
[4]   Hydrogen biotechnology: Progress and prospects [J].
Benemann, J .
NATURE BIOTECHNOLOGY, 1996, 14 (09) :1101-1103
[5]  
BROSSEAU JD, 1982, J CHEM TECHNOL BIOT, V32, P496
[6]   INHIBITORY EFFECTS OF H-2 ON GROWTH OF CLOSTRIDIUM-CELLOBIOPARUM [J].
CHUNG, KT .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 1976, 31 (03) :342-348
[7]   ANAEROBIC DIGESTION OF GLUCOSE WITH SEPARATED ACID PRODUCTION AND METHANE FORMATION [J].
COHEN, A ;
ZOETEMEYER, RJ ;
VANDEURSEN, A ;
VANANDEL, JG .
WATER RESEARCH, 1979, 13 (07) :571-580
[8]   PARAMETERS AFFECTING SOLVENT PRODUCTION BY CLOSTRIDIUM-PASTEURIANUM [J].
DABROCK, B ;
BAHL, H ;
GOTTSCHALK, G .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 1992, 58 (04) :1233-1239
[9]  
DUBOIS M, 1956, ANAL CHEM, V28, P356, DOI DOI 10.1021/AC60111A017
[10]  
*ESPRIT, 1989, RES REP EXPL SOYB ME