Sorption enhanced hydrogen production by steam methane reforming using Li2ZrO3 as sorbent:: Sorption kinetics and reactor simulation

被引:152
作者
Ochoa-Fernández, E [1 ]
Rusten, HK [1 ]
Jakobsen, HA [1 ]
Ronning, M [1 ]
Holmen, A [1 ]
Chen, D [1 ]
机构
[1] Norwegian Univ Sci & Technol, Dept Chem Engn, N-7491 Trondheim, Norway
关键词
CO2; sorption; H-2; production; lithium zirconate; enhanced steam reforming; Ni;
D O I
10.1016/j.cattod.2005.07.146
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The kinetics of CO2 sorption on a solid adsorbent, namely lithium zirconate, have been studied in an oscillating microbalance. The solid sorbent has been prepared by a novel route resulting in a high capacity, good stability and much improved sorption rates, making it suitable for its application in sorption enhanced hydrogen production by steam methane reforming. A kinetic equation for the sorption kinetics as a function of CO2 partial pressure and temperature has been developed. The hydrogen production by sorption enhanced reaction process has been simulated by a dynamic one-dimensional pseudo-homogenous model of a fixed-bed reactor, where a hydrotalcite-derived Ni catalyst has been used as steam reforming catalysts. Simulation results show that hydrogen purer than 95% with a concentration of carbon monoxide lower than 0.2 mol% can be produced in a single step. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:41 / 46
页数:6
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