New Nickel-Based Catalyst for Tar Reforming, with Superior Resistance to Coking and Sulfur Poisoning in Biomass Gasification Processes
Author:
Affiliation:
1. Research Center, Energy and Environmental Technology Division, Takuma Co., Ltd.
2. Department of Chemical Processes and Environments, Faculty of Environmental Engineering, The University of Kitakyushu
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
http://www.jstage.jst.go.jp/article/jcej/40/10/40_06WE245/_pdf
Reference20 articles.
1. Asadullah, M., S. Ito, K. Kunimori, M. Yamada and K. Tomishige; “Biomass Gasification to Hydrogen and Syngas at Low Temperature: Novel Catalytic System Using Fluidized-Bed Reactor,” J. Catal., 208, 255–259 (2002)
2. Aznar, M. P., M. A. Caballero, J. Gil, J. A. Martin and J. Corella; “Commercial Steam Reforming Catalysts to Improve Biomass Gasification with Steam-Oxgen Mixtures. 2. Catalytic Tar Removal,” Ind. Eng. Chem. Res., 37, 2668–2680 (1998)
3. Chen, I. and D. W. Shiue; “Resistivity to Sulfur Poisoning of Nickel–Alumina Catalysts,” Ind. Eng. Chem. Res., 27, 1391–1396 (1988)
4. Furusawa, T. and A. Tsutsumi; “Comparison of Co/MgO and Ni/MgO Catalysts for the Steam Reforming of Naphthalene as a Model Compound of Tar Derived from Biomass Gasification,” Appl. Catal., A, 278, 207–212 (2005)
5. Sulphur poisoning of nickel-based hot gas cleaning catalysts in synthetic gasification gasII. Chemisorption of hydrogen sulphide
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