A bench scale study of fermentative hydrogen and methane production from food waste in integrated two-stage process

被引:179
|
作者
Wang, Xing [1 ]
Zhao, You-cai [1 ]
机构
[1] Tongji Univ, State Key Lab Pollut Control & Resource Reuse, Shanghai 200092, Peoples R China
关键词
Integrated two-stage process; Fermentative hydrogen production; None-heat treatment of inoculum; Indigenous microbial cultures; 2-PHASE ANAEROBIC-DIGESTION; COMMUNITY STRUCTURE; HYDROLYSIS RATES; AMMONIA; OPTIMIZATION; INHIBITION; TOXICITY; BATCH;
D O I
10.1016/j.ijhydene.2008.09.100
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A two-Stage fermentation process combining hydrogen and methane production for the treatment of food waste was investigated in this paper. in hydrogen fermentation reactor, the indigenous mixed microbial cultures contained in food waste were used for hydrogen production. No foreign inoculum was used in the hydrogen fermentation stage, the traditional heat treatment of inoculum was not applied either in this bench scale experiment. The effects of the stepwise increased organic loading rate (OLR) and solid retention time (SRT) on integrated two-stage process were investigated. At steady state, the optimal OLR and SRT for the integrated two-stage process were found to be 22.65 kg VS/m(3) d (160 h) for hydrogen fermentation reactor and 4.61 (26.67 d) for methane fermentation reactor, respectively. Under the optimum conditions, the maximum yields of hydrogen (0.065 m(3) H-2/kg VS) and methane (0.546 m(-3) CH4/kg VS) were achieved with the hydrogen and methane contents ranging from 29.42 to 30.86%, 64.33 to 71.48%, respectively. Biodegradability analysis showed that 5.78% of the influent COD was converted to the hydrogen in H-2-SCRD and 82.18% of the influent COD was converted to the methane in CH4-SCSTR under the optimum conditions. (C) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:245 / 254
页数:10
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