Advances on methane steam reforming to produce hydrogen through membrane reactors technology: A review

被引：286

作者：

Iulianelli, Adolfo ^{[1
]}

Liguori, Simona ^{[2
]}

Wilcox, Jennifer ^{[2
]}

Basile, Angelo ^{[1
]}

机构：

[1] Univ Calabria, ITM CNR, Via P Bucci Cubo 17-C, I-87036 Arcavacata Di Rende, CS, Italy

[2] Stanford Univ, Dept Energy Resources Engn, Stanford, CA 94305 USA

来源：

CATALYSIS REVIEWS-SCIENCE AND ENGINEERING | 2016年 / 58卷 / 01期

关键词：

methane steam reforming; membrane reactor; hydrogen; Catalysts; WATER-GAS SHIFT; FLUIDIZED-BED REACTOR; LOW-TEMPERATURE; PALLADIUM MEMBRANE; CARBON FORMATION; NI CATALYSTS; NICKEL-CATALYSTS; H-2; PRODUCTION; BIOGAS STEAM; MODEL BIOGAS;

D O I：

10.1080/01614940.2015.1099882

中图分类号：

O64 [物理化学（理论化学）、化学物理学];

学科分类号：

070304 ; 081704 ;

摘要：

Methane steam reforming is the most common industrial process used for almost the 50% of the world's hydrogen production. Commonly, this reaction is performed in fixed bed reactors and several stages are needed for separating hydrogen with the desired purity. The membrane reactors represent a valid alternative to the fixed bed reactors, by combining the reforming reaction for producing hydrogen and its separation in only one stage. This article deals with the recent progress on methane steam reforming reaction, giving a short overview on catalysts utilization as well as on the fundamentals of membrane reactors, also summarizing the relevant advancements in this field.

引用

页码：1 / 35

页数：35

共 155 条

[1]

Abashar MEE, 2004, INT J HYDROGEN ENERG, V29, P799, DOI 10.1016/j.jjhydene.2003.09.010

[2] Application of the generic fluidized-bed reactor model to the fluidized-bed membrane reactor process for steam methane reforming with oxygen input [J].