Sorption-Enhanced methane steam reforming in a circulating fluidized bed reactor system

被引:23
作者
Arstad, Bjornar [1 ]
Blom, Richard [1 ]
Bakken, Egil [1 ]
Dahl, Ival [1 ]
Jakobsen, Jana P. [2 ]
Rokke, Petter [2 ]
机构
[1] SINTEF Mat & Chem, POB 124 Blindern, N-0314 Oslo, Norway
[2] SINTEF Energy Res, NO-7465 Trondheim, Norway
来源
GREENHOUSE GAS CONTROL TECHNOLOGIES 9 | 2009年 / 1卷 / 01期
关键词
Sorption-enhanced steam methane reforming; adsorption; reforming; circulating fluidized bed; dolomite; DOLOMITE; SORBENT;
D O I
10.1016/j.egypro.2009.01.094
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A 1m high circulating fluidized bed reactor, comprising of two bubbling bed reactors connected via two loop seals and a riser, has been built for performing experiments on sorption enhanced steam methane reforming. In this system steam reforming of methane is carried out catalytically with a CO2 sorbent co-present in one reactor. Regeneration is carried out in the other reactor. The catalyst used is a 60 wt.% Ni/NiAl2O3 and the sorbent is calcined dolomite. The formed CO2 reacts with the sorbent producing a solid carbonate and the sorbent free thermodynamically equilibriums are surpassed leading to a more concentrated hydrogen stream effluent. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:715 / 720
页数:6
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