Fuel-Rich Combustion Synthesized Co/Al2O3 Catalysts for Wax and Liquid Fuel Production via Fischer-Tropsch Reaction

被引:17
作者
Ail, Snehesh Shivananda [1 ]
Benedetti, Vittoria [1 ]
Baratieri, Marco [1 ]
Dasappa, Srinivasaiah [2 ]
机构
[1] Free Univ Bozen Bolzano, Fac Sci & Technol, I-39100 Bolzano Bz, Italy
[2] Indian Inst Sci, Ctr Sustainable Technol, Bangalore 560012, Karnataka, India
关键词
SUPPORTED COBALT CATALYSTS; CO/SIO2; CATALYSTS; PARTICLE-SIZE; TEMPERATURE; REDUCTION; ALUMINA; CO; DEACTIVATION; PROMOTER; OXIDE;
D O I
10.1021/acs.iecr.7b04174
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Alumina supported cobalt catalysts were synthesized for Fischer-Tropsch (FT) reaction using combustion synthesis (CS) method via the redox reaction of hexamethylenetetramine and cobalt nitrate with equivalence ratios (phi) of 1, 1.2, and 1.5. Higher equivalence ratios (phi > 1.0) were selected to increase the synthesis temperature and thereby decrease the formation of cobalt aluminates. Chemisorption and XPS studies of CS(phi = 1.2) and CS(phi = 1.5) catalysts showed high degree of reduction, high metal dispersion, and decreased formation of cobalt aluminates compared to CS(phi = 1) catalysts. Higher FT activity was observed for catalysts synthesized with equivalence ratios of 1.2 and 1.5 compared to the catalysts synthesized with phi = 1. Simultaneously, the hydrocarbon product spectrum shifted from predominantly waxes (C24+) for CS(phi = 1) catalysts to mixed fractions of liquid fuel (C-6-C-24) and waxes for CS(phi = 1.2) and CS(phi = 1.5) catalysts. This work investigates the impact of CS stoichiometry on catalyst properties, in particular the metal support interaction, and its outcome on FT activity and selectivity.
引用
收藏
页码:3833 / 3843
页数:11
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