The influence of supported Ni catalysts on the product gas distribution and H2 yield during cellulose pyrolysis

被引:71
作者
Zhao, Ming [1 ]
Florin, Nicholas H. [2 ]
Harris, Andrew T. [1 ]
机构
[1] Univ Sydney, Lab Sustainable Technol, Sch Chem & Biomol Engn, Sydney, NSW 2006, Australia
[2] Univ London Imperial Coll Sci Technol & Med, Grantham Inst Climate Change, London SW7 2AZ, England
基金
澳大利亚研究理事会;
关键词
Cellulose pyrolysis; H-2; yield; Supported Ni catalyst; gamma-Al2O3; MCM-41; HYDROGEN-PRODUCTION; STEAM GASIFICATION; ENERGY-PRODUCTION; TAR REMOVAL; BIOMASS; HYDROCARBONS; CONVERSION; KINETICS; METHANOL; CAPTURE;
D O I
10.1016/j.apcatb.2009.07.011
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
Two groups of Ni catalysts, supported on gamma-Al2O3 and MCM-41, respectively, were prepared by incipient wetness impregnation and tested for their influence on the pyrolytic decomposition of cellulose. A thermogravimetric analyser coupled with a mass spectrometer (TG-MS) was used to examine the influence of catalyst loading, support material, and the presence of additional water vapour on H-2 selectivity. Normalization of the raw MS data enabled semi-quantitative analysis of the product gas distribution, which facilitated reliable comparison between different experimental conditions. Catalysts were characterized by BET, XRD, SEM/EDX and TEM. MCM-41 supported Ni significantly elevated the yield of H2 and total gaseous product, both under Ar and with the injection of additional water vapour when compared with the gamma-Al2O3 support. 15 wt.%Ni/-y-Al2O3 and 5 wt.%Ni/MCM-41 were identified as the most active catalysts from the two groups with regards to H-2 selectivity and yield. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:185 / 193
页数:9
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