Bioreactor design for continuous dark fermentative hydrogen production

被引:146
|
作者
Jung, Kyung-Won [1 ]
Kim, Dong-Hoon [2 ]
Kim, Sang-Hyoun [3 ]
Shin, Hang-Sik [1 ]
机构
[1] Korea Adv Inst Sci & Technol, Dept Civil & Environm Engn, Taejon 305701, South Korea
[2] Korea Inst Energy Res, Wastes Energy Res Ctr, Taejon 305343, South Korea
[3] Daegu Univ, Dept Environm Engn, Gyongsan 712714, Gyeongbuk, South Korea
基金
新加坡国家研究基金会;
关键词
Dark fermentative H-2 production; Continuous systems; Suspended bioreactor; Immobilized bioreactor; Operational parameters; EXPANDED GRANULAR SLUDGE; CONTINUOUS STIRRED-TANK; ANAEROBIC MIXED MICROFLORA; ETHANOL-TYPE FERMENTATION; HYDRAULIC RETENTION TIME; FLUIDIZED-BED REACTORS; WASTE-WATER-TREATMENT; BIOHYDROGEN-PRODUCTION; SEWAGE-SLUDGE; H-2; PRODUCTION;
D O I
10.1016/j.biortech.2011.03.056
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Dark fermentative H-2 production (DFHP) has received increasing attention in recent years due to its high H-2 production rate (HPR) as well as the versatility of the substrates used in the process. For most studies in this field, batch reactors have been applied due to their simple operation and efficient control; however, continuous DFHP operation is necessary from economical and practical points of view. Continuous systems can be classified into two categories, suspended and immobilized bioreactors, according to the life forms of H-2 producing bacteria (HPB) used in the reactor. This paper reviews operational parameters for bioreactor design including pH, temperature, hydraulic retention time (HRT), and H-2 partial pressure. Also, in this review, various bioreactor configurations and performance parameters including H-2 yield (HY), HPR, and specific H-2 production rate (SHPR) are evaluated and presented. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:8612 / 8620
页数:9
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