Progress in Methanol Steam Reforming Modelling via Membrane Reactors Technology

被引:23
|
作者
Iulianelli, Adolfo [1 ]
Ghasemzadeh, Kamran [2 ]
Basile, Angelo [1 ]
机构
[1] CNR, ITM, Via P Bucci Cubo 17-C, I-87036 Arcavacata Di Rende, CS, Italy
[2] Urmia Univ Technol, Dept Chem Engn, Orumiyeh 5716693187, Iran
关键词
methanol steam reforming; hydrogen production; modelling; membrane reactors; GAS SHIFT REACTION; HYDROGEN SELECTIVE MEMBRANES; MOLECULAR-SIEVE MEMBRANES; H-2; PRODUCTION; PROCESS INTENSIFICATION; ALLOY MEMBRANES; DENSE MEMBRANES; FLUIDIZED-BED; PALLADIUM; GENERATION;
D O I
10.3390/membranes8030065
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Hydrogen has attracted growing attention for various uses, and, particularly, for polymer electrolyte membrane fuel cells (PEMFCs) supply. However, PEMFCs need high grade hydrogen, which is difficult in storing and transportation. To solve these issues, hydrogen generation from alcohols and hydrocarbons steam reforming reaction has gained great consideration. Among the various renewable fuels, methanol is an interesting hydrogen source because at room temperature it is liquid, and then, easy to handle and to store. Furthermore, it shows a relatively high H/C ratio and low reforming temperature, ranging from 200 to 300 degrees C. In the field of hydrogen generation from methanol steam reforming reaction, a consistent literature is noticeable. Despite various reviews that are more devoted to describe from an experimental point of view the state of the art about methanol steam reforming reaction carried in conventional and membrane reactors, this work describes the progress in the last two decades about the modelling studies on the same reaction in membrane reactors.
引用
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页数:22
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