合成气
生物量(生态学)
材料科学
生物质气化
膜反应器
陶瓷
化学工程
膜
废物管理
陶瓷膜
环境科学
催化作用
整体气化联合循环
制浆造纸工业
工艺工程
煤气化
化学
工作(物理)
作者
Shuncheng Li,Zongliang Kou,Qiaoqiao Zhou,Feng Zeng,Xuerui Wang,Huanhao Chen,Xuehong Gu
标识
DOI:10.1021/acs.iecr.6c01600
摘要
Membrane reactors could integrate biomass gasification, particulate matter (PM) removal, and tar-reforming in situ, offering a promising pathway to streamline the production of clean syngas from biomass. However, achieving continuous and stable biomass gasification within such reactors remains a significant challenge. In this study, we present a scalable packed-bed ceramic membrane reactor for continuous biomass gasification to produce clean hydrogen-rich syngas. Under optimized conditions (biomass feed rate of 6 g min –1 and steam feed rate of 1.5 mL min –1 ), the reactor achieved a stable H 2 /CO ratio of ∼1.4 and a syngas yield of ∼1.34 m 3 kg corncob –1 . Continuous 330 h operation maintained stable syngas composition, with periodic maintenance every 110 h to remove membrane carbon deposits. This study establishes a framework for developing durable packed-bed ceramic membrane reactors for efficient, continuous syngas production from biomass.
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