作者: Seong-Joong Kim , Pyung Soo Lee , Min-Jeong Park , Dong-Wook Lee , You-In Park
DOI: 10.1080/01496395.2016.1198378
关键词: Membrane reactor 、 Chemical engineering 、 Dimethyl ether 、 Chemistry 、 Water-gas shift reaction 、 Hydrogen 、 Proton exchange membrane fuel cell 、 Permeation 、 Steam reforming 、 Flux (metallurgy) 、 Chromatography
摘要: ABSTRACTHigh flux tubular membrane reactors were designed for dimethyl ether (DME) steam reforming. Considering the facile scale-up and high of hydrogen, stainless steel supports employed reactors. At 500°C, DME conversion reached ~100%, while hydrogen recovery 20%. However, contamination by CO was rather (>1%), making this process unsuitable proton exchange fuel cell applications, which require a concentration <100 ppm. This result showed that an additional polishing step needed to reduce concentration. Membrane further modified perform water–gas shift reaction on permeate employing fixed bed reactor, yielded high-purity (~99%) along with low content (<20 ppm).