Steam reforming of propane in a fluidized bed membrane reactor for hydrogen production

被引:83
|
作者
Rakib, Mohammad A. [1 ]
Grace, John R. [1 ]
Lim, C. Jim [1 ]
Elnashaie, Said S. E. H.
Ghiasi, Bahman [1 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, Vancouver, BC V6T 1Z3, Canada
基金
加拿大自然科学与工程研究理事会; 加拿大创新基金会;
关键词
Hydrogen production; Propane; Steam reforming; Membrane reactor; Fluidized bed reactor; Experiments; PORTABLE POWER-GENERATION; FUEL PROCESSOR; SYNTHESIS GAS; CATALYTIC-OXIDATION; LIQUID HYDROCARBONS; NICKEL-CATALYSTS; METHANE; SYSTEM; LPG; PROMOTERS;
D O I
10.1016/j.ijhydene.2010.03.136
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
Steam reforming of propane was carried out in a fluidized bed membrane reactor to investigate a feedstock other than natural gas for production of pure hydrogen. Close to equilibrium conditions were achieved inside the reactor with fluidized catalyst due to the very fast steam reforming reactions. Use of hydrogen permselective Pd77Ag23 membrane panels to extract pure hydrogen shifted the reaction towards complete conversion of the hydrocarbons, including methane, the key intermediate product. Irreversible propane steam reforming is limited by the reversibility of the steam reforming of this methane. To assess the performance improvement due to pure hydrogen withdrawal, experiments were conducted with one and six membrane panels installed along the height of the reactor. The results indicate that a compact reformer can be achieved for pure hydrogen production for a light hydrocarbon feedstock like propane, at moderate operating temperatures of 475-550 degrees C, with increased hydrogen yield. (C) 2010 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:6276 / 6290
页数:15
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