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作 者:李洪亮[1,2] 李金鸿 李彦豪[1] 方书起[1,2] 陈俊英[1,2] 刘利平 白净[1,2] LI Hongliang;LI Jinhong;LI Yanhao;FANG Shuqi;CHEN Junying;LIU Liping;BAI Jing(School of Chemical Engineering and Energy,Zhengzhou University,Zhengzhou 450001,Henan,China;Engineering Laboratory of Henan Province for Biorefinery Technology and Equipment,Zhengzhou 450001,Henan,China)
机构地区:[1]郑州大学化工与能源学院,河南郑州450001 [2]生物质炼制技术与装备河南省工程实验室,河南郑州450001
出 处:《化工进展》2017年第11期4017-4021,共5页Chemical Industry and Engineering Progress
摘 要:在流化床实验装置上以水蒸气为气化剂,对稻壳进行热解气化的实验研究,分别考察单因素反应温度(500~700℃)、蒸气流量(7~11kg/h)和进料速率(1.2~3.6kg/h)对产气率及其主要组分(H2、CO、CH4、CO2)的影响。实验结果表明:温度的升高可提高气化气产率及气体组分中CH4和H2的含量,同时降低了CO2的含量,随温度升高,CO的含量呈先增加再降低的趋势。蒸气流量和进料速率的增加对产气率影响分别在500℃和700℃呈现出了不同的规律,说明了在不同反应温度下床内起主导作用的反应不同。在700℃,随蒸气流量和进料速率增加,气化气中H2、CO和CO2的含量都有小幅度变化,CH4体积分数稳定在12%左右。在条件考察范围内,当反应温度为700℃、蒸气流量为7kg/h、进料速率为1.2kg/h时,产气率和H2体积分数分别有最大值,为725L/h和18.05%。The rice husk gasification experiments were performed in a fluidized bed gasifier with steam as gasifying agent.The effects of reaction temperature(500-700℃),steam flow rate(7-11kg/h),and feed rate(1.2-3.6kg/h)on gas yield and the compositions of the main components(H2,CO,CH4,CO2)were investigated,respectively.The results showed that the higher reaction temperature could lead to higher gas yield and higher content of H2and CH4.With the increase of the reaction temperatures,the content of CO first decreased then increased.The effect of the increase of steam flow and feed rate on gas yield at500℃and700℃was not the same,which indicated that the leading reactions in the fluidized bed at different reaction temperature were different.At700℃,the increase of the steam flow and feed rates did niot change the content of H2,CO,and CO2significanly;and the volume fraction of CH4remained about12%.Within the scope of the experimental conditions,when the reaction temperature was700℃,steam flow7kg/h,and feed rate1.2kg/h,the gas yield and the volume fraction of H2reached the maximum values of725L/h and18.05%,respectively.
分 类 号:TK6[动力工程及工程热物理—生物能]
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