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污泥热解残渣水蒸气气化制取富氢燃气
引用本文:张艳丽,肖波,胡智泉,成功,何丕文,江程程.污泥热解残渣水蒸气气化制取富氢燃气[J].可再生能源,2012(1):67-71.
作者姓名:张艳丽  肖波  胡智泉  成功  何丕文  江程程
作者单位:1. 华中科技大学环境学院,湖北武汉,430074
2. 华中科技大学环境学院,湖北武汉430074;长江大学城市建设学院,湖北荆州434023
基金项目:国家自然科学基金,湖北省科技攻关项目,中央高校基本科研业务费
摘    要:采用固定床反应器,进行了污泥热解残渣水蒸气气化制取富氢燃气的研究。考察了反应温度、固相停留时间、水蒸气流量及催化剂对气化效果及气体产物组成的影响。结果表明:随着反应温度的升高,气体产率由0.096 7 m3/kg逐渐增加到0.460 0 m3/kg,燃气中H2含量由17.87%逐渐增加到52.44%;在最佳固相停留时间为15min时,气体产率达到0.540 m3/kg;最佳水蒸气流量为1.19 g/min,此时产气量达到最大值0.61 m3/kg,H2含量为64.7%;添加催化剂有利于气体中H2含量的提高。

关 键 词:污泥热解残渣  水蒸气  气化  富氢燃气

Preparation of hydrogen-rich gas from steam gasification of sludge pyrolysis residues
ZHANG Yan-li , XIAO Bo , HU Zhi-quan , CHENG Gong , HE Pi-wen , JIANG Cheng-cheng.Preparation of hydrogen-rich gas from steam gasification of sludge pyrolysis residues[J].Renewable Energy,2012(1):67-71.
Authors:ZHANG Yan-li  XIAO Bo  HU Zhi-quan  CHENG Gong  HE Pi-wen  JIANG Cheng-cheng
Affiliation:1(1.School of Environmental Science and Engineering,Huazhong University of Science and Technology,Wuhan 430074,China;2.School of Urban Construction,Yangtze university,Jingzhou 434023,China)
Abstract:Preparation of hydrogen-rich gas from steam gasification of sludge pyrolysis residues was studied in a fixed bed reactor.The influence factors of gasification temperature,solid residence time,steam flow and catalyst on gasification performance and composition were investigated.The results indicated that the gas yield increased from 0.096 7 m3/kg to 0.460 0 m3/kg gradually with the temperature increased.And the concentration of H2 in fuel gas increased from 17.87% to 52.44%.The optimum solid residence time was 15 min.The maximum H2 yield production reached 0.61 m3/kg.when the optimum steam flow was 1.19 g/min.the maximum gas production is 0.61 m3/kg,with the 64.7% H2 contents,、by additing catalyst could increase the H2 concentration in the gas.
Keywords:residue of sludge pyrolysis  water vapor  gasification  hydrogen-rich gas
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