SBA-15 supported Ni-Co bimetallic catalysts for enhanced hydrogen production during cellulose decomposition

被引:72
|
作者
Zhao, Ming [1 ]
Church, Tamara L. [1 ]
Harris, Andrew T. [1 ]
机构
[1] Univ Sydney, Sch Chem & Biomol Engn, Lab Sustainable Technol, Sydney, NSW 2006, Australia
基金
澳大利亚研究理事会;
关键词
Hydrogen production; Cellulose; SBA-15; Ni-Co bimetallic catalyst; TG-MS; CARBON-MONOXIDE HYDROGENATION; STEAM GASIFICATION; MESOPOROUS SILICA; ENERGY-PRODUCTION; DIOXIDE CAPTURE; BIOMASS; NICKEL; COBALT; PYROLYSIS; METHANE;
D O I
10.1016/j.apcatb.2010.10.024
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
SBA-15 supported Ni-Co bimetallic catalysts with various loadings and Ni/Co ratios were prepared by incipient wetness impregnation and tested as catalysts in the pyrolytic decomposition of methyl cellulose. A thermogravimetric analyser coupled with a mass spectrometer (TG-MS) was used to examine the activity and selectivity for H(2) production by semi-quantitative analysis, and the new catalysts were compared with monometallic Ni and Co supported on SBA-15 and MCM-41. Catalysts were characterized by physisorption, chemisorption, reducibility test, X-ray diffraction, and scanning and transmission electron microscopy. 10 wt.% NiCo(2)/SBA-15 was the most active bimetallic catalyst, yielding 295 ml H(2)/g cellulose. The addition of water further enhanced the H(2) yield to 405 ml/g cellulose and gave an H(2) selectivity of up to 28.9 vol.%. This superior performance over monometallic catalysts indicated a synergy between Ni and Co, combining and enlarging individual activity and selectivity upon the main heterogeneous reactions. The improved reducibility and dispersion of Ni-Co alloying sites also contributed to this enhancement. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:522 / 530
页数:9
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