合成气
二氧化碳重整
甲烷
合成气制汽油
镍
制氢
二氧化碳
氢
甲烷转化炉
化学工程
蒸汽重整
材料科学
膜反应器
化学
废物管理
有机化学
工程类
作者
Yuan Chen,Jie Wang,Claudia Li,Guanlong Geng,Jian Song,Naitao Yang,Sibudjing Kawi,Mingming Wang,Xiaoyao Tan,Shaomin Liu
标识
DOI:10.1021/acs.iecr.4c04860
摘要
CH4 and CO2 are two major greenhouse gases, and converting them into useful chemicals (hydrogen and syngas) via dry reforming would be one of the best strategies. The utilization of membrane reactors enables the integration of H2 production and separation into a single unit. Herein, we investigated the hollow fiber (HF) membrane reactor performance for H2 production through dry reforming of methane (DRM) at various operating conditions. Ni hollow fiber membranes alleviate carbon deposition in DRM processes by leveraging their inherent catalytic properties, high thermal stability, optimized surface design, and unique hollow fiber geometry, ensuring sustained operation and durability. With the incorporation of a catalyst, the catalytic membrane reactors could maintain high conversion rates exceeding 95% even for a higher feed flow rate at 900 °C. For the operation of 80 h, the membrane reactors gave a very stable performance with a total H2 formation rate of 94 mL min–1, while both H2 and CO selectivity fluctuated up and down within 92–96%. The fabricated Ni membrane exhibited excellent thermal cycling operation performance and possessed high resistance to poisoning agents such as CO, CO2, and H2O. These findings provide a solid foundation for the widespread application of Ni-based membranes in cleaner H2 production via reforming reactions by minimizing the carbon footprint and further contributing to global decarbonization initiatives.
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