合成气
制氢
膜反应器
氢
膜
部分氧化
蒸汽重整
化学工程
催化作用
氧气
焦炭
甲烷
化学
材料科学
分解水
工艺工程
工程类
有机化学
生物化学
光催化
作者
Wei Fang,Frank Steinbach,Zhongwei Cao,Xuefeng Zhu,Armin Feldhoff
标识
DOI:10.1002/anie.201603528
摘要
Water splitting coupled with partial oxidation of methane (POM) using an oxygen-transporting membrane (OTM) would be a potentially ideal way to produce high-purity hydrogen as well as syngas. Over the past decades, substantial efforts have been devoted to the development of supported membranes with appropriate configurations to achieve considerable performance improvements. Herein, we describe the design of a novel symmetrical membrane reactor with a sandwich-like structure, whereby a largescale production (>10 mL min(-1) cm(-2) ) of hydrogen and syngas can be obtained simultaneously on opposite sides of the OTM. Furthermore, this special membrane reactor could regenerate the coke-deactivated catalyst in situ by water steam in a single unit. These results represent an important first step in the development of membrane separation technologies for the integration of multiple chemical processes.
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