Hydrogen by glycerol steam reforming on a nickel-alumina catalyst: Deactivation processes and regeneration

被引:68
|
作者
Sanchez, Esteban A. [1 ]
Comelli, Raul A. [1 ]
机构
[1] Consejo Nacl Invest Cient & Tecn, Inst Invest Catalisis & Petroquim INCAPE FIQ UNL, RA-2654 Santiago Del Estero, Santa Fe, Argentina
关键词
Hydrogen; Glycerol; Steam reforming; Deactivation; Carbonaceous deposits; OXIDE CATALYSTS; ADSORPTION; ETHANOL; PHASES; NI;
D O I
10.1016/j.ijhydene.2011.12.088
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
Hydrogen energy has attracted considerable attention because of its efficiency and environmental benefits, and the increasing demand requires finding renewable sources of raw materials to produce it. Glycerol, by-product of biodiesel production and coming from renewable raw materials, could be a bio-renewable substrate to produce hydrogen. The glycerol steam reforming to obtain hydrogen was evaluated using a 5.1 wt% Ni impregnated on Al2O3 catalyst, characterized by nitrogen adsorption, XRD, and FTIR. Deactivation processes were analyzed in successive cycles of reaction at 700 degrees C, atmospheric pressure, 5 h(-1) WHSV, and 3:1 water:glycerol molar ratio, during 12 h. Between reaction cycles, regenerating took place using a He/Air stream. Hydrogen was the main product on the fresh catalyst, following by CO and CH4; during reaction, carbonaceous deposits deactivated catalyst, decreasing H-2 and increasing both CO and CH4. Carbonaceous deposits were characterized by TPO, showing a main peak centered at 690 degrees C; the carbon content reached 11.9%. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:14740 / 14746
页数:7
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