The role of pH in the fermentative H2 production from an acidogenic granule-based reactor

被引:72
作者
Mu, Yang [1 ]
Yu, Han-Qing [1 ]
Wang, Yi [1 ]
机构
[1] Univ Sci & Technol China, Sch Chem, Lab Environm Engn, Hefei 230026, Anhui, Peoples R China
基金
中国国家自然科学基金;
关键词
acidogenesis; granule; H-2; neural network; pH; upflow anaerobic sludge blanket reactor (UASB); volatile fatty acids (VFA);
D O I
10.1016/j.chemosphere.2005.12.048
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The role of pH in the fermentative H-2 production from an upflow acidogenic granule-based reactor was investigated in this study. Experimental results show that all H-2 partial pressure, H-2 production rate and H-2 yield were pH-dependent, in the range of 2.8 x 10(4)-5.2 x 10(4) Pa, 61-145 ml-H-2 l(-1) h(-1) and 0.68-1.61 mol-H-2 mol-glucose-1, respectively. The maximum H-2 partial pressure was observed at pH 3.4, while both maximum H-2 production rate and H-2 yield were found at pH 4.2. Acetate, propionate, butyrate, i-butyrate, valerate, caporate and ethanol were present in the effluent of this UASB reactor, and their distribution was also pH-dependent. As pH was decreased from 4.2 to a lower level of 3.4 or increased to a higher level of 6.3, the fermentative type of this H-2-producing reactor would shift from butyrate-type to caporate- or ethanol-type. Thermodynamic analysis was performed to explore the possible metabolic pathways of caproate and valerate formation. The metabolic pathway of caproate formation was pH-dependent, while that of valerate formation was pH-independent. A neural network model was designed, trained and validated. It was able to successfully describe the daily variations of H-2 partial pressure and H-2 Yield of the reactor, and to predict its steady state performance at various pHs. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:350 / 358
页数:9
相关论文
共 31 条
[11]   Feasibility of biological hydrogen production from organic fraction of municipal solid waste [J].
Lay, JJ ;
Lee, YJ ;
Noike, T .
WATER RESEARCH, 1999, 33 (11) :2579-2586
[12]  
Lay JJ, 2000, BIOTECHNOL BIOENG, V68, P269, DOI 10.1002/(SICI)1097-0290(20000505)68:3<269::AID-BIT5>3.0.CO
[13]  
2-T
[14]   Biohydrogen production: prospects and limitations to practical application [J].
Levin, DB ;
Pitt, L ;
Love, M .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2004, 29 (02) :173-185
[15]   A nutrient formulation for fermentative hydrogen production using anaerobic sewage sludge microflora [J].
Lin, CY ;
Lay, CH .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2005, 30 (03) :285-292
[16]   Hydrogen production from sucrose using an anaerobic sequencing batch reactor process [J].
Lin, CY ;
Jo, CH .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2003, 78 (06) :678-684
[17]   Biological hydrogen production measured in batch anaerobic respirometers [J].
Logan, BE ;
Oh, SE ;
Kim, IS ;
Van Ginkel, S .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2002, 36 (11) :2530-2535
[18]   Microbial production of hydrogen: An overview [J].
Nandi, R ;
Sengupta, S .
CRITICAL REVIEWS IN MICROBIOLOGY, 1998, 24 (01) :61-84
[19]   Hydrogen production from organic waste [J].
Nielsen, AT ;
Amandusson, H ;
Bjorklund, R ;
Dannetun, H ;
Ejlertsson, J ;
Ekedahl, LG ;
Lundström, I ;
Svensson, BH .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2001, 26 (06) :547-550
[20]   Hydrogen fermentation of organic municipal wastes [J].
Noike, T ;
Mizuno, O .
WATER SCIENCE AND TECHNOLOGY, 2000, 42 (12) :155-162