Development of sulfur tolerant catalysts for the synthesis of high quality transportation fuels

被引:70
作者
Koizumi, N [1 ]
Murai, K [1 ]
Ozaki, T [1 ]
Yamada, M [1 ]
机构
[1] Tohoku Univ, Grad Sch Engn, Dept Appl Chem, Aoba Ku, Sendai, Miyagi 9808579, Japan
基金
日本学术振兴会;
关键词
sulfur tolerant catalysts; Fischer-Tropsch synthesis; methanol synthesis; DME synthesis; Fe-based catalysts; transition metal sulfide catalysts;
D O I
10.1016/j.cattod.2004.02.002
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
In this paper, results concerning the development of sulfur tolerant catalysts for Fischer-Tropsch synthesis (FTS), C2+ alcohol synthesis, methanol and/or DME synthesis are presented. In the FTS reaction on Fe using H-2-rich syngas such as the biomass-derived syngas, the composition of catalyst pretreatment gas and the addition of MnO on Fe had strong impacts on its sulfur resistance as well as activity. Especially the Fe/MnO catalyst pretreated with CO showed a much lower deactivation rate and a higher FTS activity than an Fe/Cu/K catalyst in the presence of H2S. For C2+ alcohol synthesis a novel preparation method was developed for a highly active MoS2-based catalyst that is well known as the sulfur tolerant catalyst. Besides some metal sulfides were found to show higher CO hydrogenation activities than MoS2. In particular, both Rh and Pd sulfides were active and selective for the methanol synthesis. Modified Pd sulfide catalyst, i.e. sulfided Ca/Pd/SiO2, showed an activity that was about 60% of that of a Cu/ZnO/Al2O3 catalyst in the absence of H2S. This catalyst preserved 35% of the initial activity even in the presence of H2S. The sulfided Ca/Pd/SiO2 mixed with gamma-Al2O3 was also available for in situ DME synthesis in the presence of H2S. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:465 / 478
页数:14
相关论文
共 65 条
[21]   CRYSTAL STRUCTURE OF SUPERCONDUCTOR RH17S15 [J].
GELLER, S .
ACTA CRYSTALLOGRAPHICA, 1962, 15 (DEC) :1198-&
[22]   EVIDENCE FOR PRODUCTION OF SURFACE FORMATE UPON DIRECT REACTION OF CO WITH ALUMINA AND MAGNESIA [J].
GOPAL, PG ;
SCHNEIDER, RL ;
WATTERS, KL .
JOURNAL OF CATALYSIS, 1987, 105 (02) :366-372
[23]   Basic metal oxides as co-catalysts in the conversion of synthesis gas to methanol on supported palladium catalysts [J].
Gotti, A ;
Prins, R .
JOURNAL OF CATALYSIS, 1998, 175 (02) :302-311
[24]   EFFECT OF IRON-MANGANESE OXIDE SOLID-SOLUTIONS ON SELECTIVITY FOR LOWER HYDROCARBONS FROM CARBON-MONOXIDE HYDROGENATION [J].
HUTCHINGS, GJ ;
BOEYENS, JCA .
JOURNAL OF CATALYSIS, 1986, 100 (02) :507-511
[26]  
ICHIKAWA M, 1981, J MOL CATAL, V11, P167, DOI 10.1007/BF01210391
[27]  
Ichikawa M., 1979, SHOKUBAI, V21, P253
[28]  
Jahnek F.C., 1999, PETROTECH, V22, P943
[29]   Adsorption properties of cobalt and cobalt-manganese catalysts studied by in situ diffuse reflectance FTIR using CO and CO+H2 as probes [J].
Jiang, M ;
Koizumi, N ;
Ozaki, T ;
Yamada, M .
APPLIED CATALYSIS A-GENERAL, 2001, 209 (1-2) :59-70
[30]   Adsorption properties of iron and iron-manganese catalysts investigated by in-situ diffuse reflectance FTIR spectroscopy [J].
Jiang, M ;
Koizumi, N ;
Yamada, M .
JOURNAL OF PHYSICAL CHEMISTRY B, 2000, 104 (32) :7636-7643