生物量(生态学)
木屑
木材气体发生器
制氢
环境科学
原材料
制浆造纸工业
流化床
生物质气化
合成气
废物管理
燃烧热
颗粒
氢
材料科学
化学
工程类
农学
煤
燃烧
有机化学
复合材料
生物
作者
Weijuan Lan,Huiling Ding,Xin Jin,Dongxue Yin,Yingxian Wang,Jiangtao Ji
标识
DOI:10.1093/ijlct/ctac022
摘要
Abstract This paper reports on the investigation of the gasification from biomass using a laboratory scale fluidized bed gasifier. Main influencing factors, such as the temperature, steam flow rate and CaO to biomass mass ratio were studied. A model was developed for hydrogen-rich gas production from biomass via using ASPEN PLUS software. Sawdust was used as raw material for this study. Different operating conditions were considered and the model was verified. The results showed that the production of H2 and CO2 increased while the production of CO and CH4 decreased with increasing temperature. When the steam was used as the gasifying agent at different temperatures, the production of H2 increased significantly and its growth rate was ~48%. The increase of CaO to biomass mass ratio from 0% to 50% resulted in hydrogen content increasing from 40% to 68%. Simulation results showed that the model was suitable for biomass gasification process, which could provide some reference value for further biomass gasification experiment.
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