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Development and Improvement of Bioreactor for Fermentative Hydrogen Production
引用本文:LI Yong-feng REN Nan-qi YANG Chuan-ping DING Jie LI Jian-zheng. Development and Improvement of Bioreactor for Fermentative Hydrogen Production[J]. 武汉理工大学学报, 2006, 28(Z1): 69-80
作者姓名:LI Yong-feng REN Nan-qi YANG Chuan-ping DING Jie LI Jian-zheng
作者单位:LI Yong-feng(Key Wood Breeding and Biotechnology Lab of China Education Ministry, University of Northeast Forestry, Harbin 150024,China;Municipal and Environmental Engineering School, Harbin Institute of Technology, Harbin 150090, China;School of Chemistry and Chemical Engineering, Shanghai University of Engineering Sciences, Shanghai 201620, China) REN Nan-qi(Municipal and Environmental Engineering School, Harbin Institute of Technology, Harbin 150090, China) YANG Chuan-ping(Key Wood Breeding and Biotechnology Lab of China Education Ministry, University of Northeast Forestry, Harbin 150024,China) DING Jie(Municipal and Environmental Engineering School, Harbin Institute of Technology, Harbin 150090, China) LI Jian-zheng(Municipal and Environmental Engineering School, Harbin Institute of Technology, Harbin 150090, China)
基金项目:The demonstration engineering projiect of biological hydrogen production. National high-tech projects(863plan) (2003AA515030).
摘    要:

文章编号:1671-4431(2006)专辑Ⅱ-0069-12
修稿时间:2006-08-20

Development and Improvement of Bioreactor for Fermentative Hydrogen Production
LI Yong-feng,REN Nan-qi,YANG Chuan-ping,DING Jie,LI Jian-zheng. Development and Improvement of Bioreactor for Fermentative Hydrogen Production[J]. Journal of Wuhan University of Technology, 2006, 28(Z1): 69-80
Authors:LI Yong-feng  REN Nan-qi  YANG Chuan-ping  DING Jie  LI Jian-zheng
Abstract:The paper reviewed hydrogen production biotechnology on reactor development and design aspects. Biological hydrogen-producing reactor as acid-producing phase of two-phase anaerobic organism treatment system plays an important role in the following aspects: Reactor was developed as the follow ideas: 1) CSTR-type anaerobic fermentation reactor is selected to reduce the substrate concentration in reactor and increase target product operational yield and selectivity in the reactor;2)Integration structure with mixing reaction area and deposit-separating area is selected, i.e. gas-liquid-solid phase separation unit; 3)Mixture liquid in reaction area is stirred by the stirrer to reach a turbulent state in order to reduce interfacial layer thickness and temperature gradient in a floc unit particle and increase mass transfer rate;4) H2 in the particle and liquid phase is accelerated to release to prevent accumulated H2 from bringing feedback inhibition to organism metabolism, and H2/CO2conversion to acetic acid; 5) A sector turbine agitator with hoisting capacity and mixing power is selected to facilitate sludge to flow back through a effluence seam; 6 ) Interior wall in the reaction area is equipped with vertical baffles to avoid causing swirling flow of mixture liquid owing to agitation.
Keywords:hydrogen production   reactor development   wastewater
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