Hydrogen production from oxidative steam reforming of bio-butanol over CoIr-based catalysts: Effect of the support

被引：31

作者：

Cai, Weijie ^{[1
,2
,3
]}

Ramirez de la Piscina, Pilar ^{[1
,2
]}

Gabrowska, Klaudia ^{[1
,2
]}

Homs, Narcis ^{[1
,2
,3
]}

机构：

[1] Univ Barcelona, Dept Quim Inorgan, Barcelona 08028, Spain

[2] Univ Barcelona, Inst Nanociencia & Nanotecnol, E-08028 Barcelona, Spain

[3] Catalonia Inst Energy Res IREC, Barcelona 08930, Spain

来源：

BIORESOURCE TECHNOLOGY | 2013年 / 128卷

关键词：

Bio-butanol raw mixture; Oxidative steam reforming; Hydrogen production; H-2 from bio-butanol; Butanol/acetone/ethanol reforming; H-2; PRODUCTION; ETHANOL; NI; DEACTIVATION; PERFORMANCE; EFFICIENT; COKE;

D O I：

10.1016/j.biortech.2012.10.125

中图分类号：

S2 [农业工程];

学科分类号：

0828 ;

摘要：

This paper studies the influence of the support on the behavior of bimetallic CoIr-based catalysts (6.5 wt.% Co, 0.4 wt.% Ir) for hydrogen production from the oxidative steam reforming of bio-butanol raw mixture (butanol/acetone/ethanol = 6/3/1 mass ratio). Catalytic tests were carried out at 500 degrees C for 60 h with raw mixture/water/air/Ar = 1/10/7.5/12 molar ratio and GHSV = 7500 h(-1). Over CoIr/18CeZrO(2) and CoIr/ZnO the main process which took place was the oxidative steam reforming of the raw mixture. CoIr/18CeZrO(2) showed the better catalytic performance. Characterization of the used catalysts indicated that both active metal sintering and coke formation was prevented on the CoIr/18CeZrO(2) catalyst. (C) 2012 Elsevier Ltd. All rights reserved.

引用

页码：467 / 471

页数：5

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