Fermentative hydrogen production from fresh leachate in batch and continuous bioreactors

被引:15
|
作者
Liu, Qiang [1 ]
Zhang, Xiaolei [1 ]
Yu, Lijia [2 ]
Zhao, Aihua [3 ]
Tai, Jun [3 ]
Liu, Jianyong [1 ]
Qian, Guangren [1 ]
Xu, Zhi Ping [4 ]
机构
[1] Shanghai Univ, Sch Environm & Chem Engn, Shanghai 200444, Peoples R China
[2] Shanghai Pucheng Thermal Power Energy Co Ltd, Shanghai 201204, Peoples R China
[3] Shanghai Engn Res Municipal Solid Waste Treatment, Shanghai 200232, Peoples R China
[4] Univ Queensland, ARC Ctr Excellence Funct Nanomat, Australian Inst Bioengn & Nanotechnol, Brisbane, Qld 4072, Australia
基金
澳大利亚研究理事会;
关键词
Hydrogen bioproduction; Fresh leachate; Batch bioreactor; Expanded granular sludge bed (EGSB) bioreactor; Phosphate; ETHANOL-TYPE FERMENTATION; WASTE-WATER TREATMENT; BIOHYDROGEN PRODUCTION; LANDFILL LEACHATE; METHANE PRODUCTION; MIXED CULTURE; REACTOR; SLUDGE; MICROFLORA; COMMUNITY;
D O I
10.1016/j.biortech.2010.10.061
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
This research for the first time investigated hydrogen production from the fresh leachate originated from municipal solid wastes. We found that fermentation of the leachate generated H(2) and was very much enhanced in the presence of extra phosphate in the batch reactor. The continuous expanded granular sludge bed (EGSB) reactor started to generate H(2) at day 20 and continued to 176 days with 120 mg/l of extra phosphate present. The highest chemical oxygen demand (COD) removal efficiency (66.9%) was achieved at liquid up-flow velocity of 3.7 m/h and hydraulic retention time of 12 h. Under proposed optimal operation conditions, the mean H(2) production rate reached up to 2155 ml/(1 day). We also found that over 80% liquid metabolites were acetic acid and ethanol, suggesting the ethanol-type fermentation was dominant in the bioreactor. These findings indicate that the fresh leachate can be used as the source for continuous hydrogen production. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:5411 / 5417
页数:7
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