Ga and In modified ceria as supports for cobalt-catalyzed Fischer-Tropsch synthesis

被引:6
作者
Gnanamani, Muthu Kumaran [1 ]
Jacobs, Gary [1 ,2 ]
Shafer, Wilson D. [1 ]
Martinelli, Michela [1 ]
Cronauer, Donald C. [3 ]
Kropf, A. Jeremy [3 ]
Marshall, Christopher L. [3 ]
Davis, Burtron H. [1 ]
机构
[1] Univ Kentucky, Ctr Appl Energy Res, 2540 Res Pk Dr, Lexington, KY 40511 USA
[2] Univ Texas San Antonio, Chem Engn Program, Dept Biomed, UTSA Circle, San Antonio, TX 78249 USA
[3] Argonne Natl Lab, Chem Sci & Engn Div, Argonne, IL 60439 USA
关键词
Fischer-Tropsch synthesis; Ag promoter; CeO2; CeO2-Ga2O3; CeO2-In2O3; Oxygenates; L-III EDGES; CO/AL2O3; CATALYSTS; REDUCTION PROPERTY; CO; DEACTIVATION; IRON; SELECTIVITY; XANES; REDUCIBILITY; HYDROCARBONS;
D O I
10.1016/j.apcata.2017.08.026
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
Ga- and In-modified ceria (Ce0.8Ga0.2O2, Ce0.8In0.2O2) materials were used as supports for cobalt-catalyzed Fischer-Tropsch synthesis (FTS). The addition of Ga to ceria was found to improve CO conversion for cobalt-catalyzed FTS, while the addition of In tended to decrease it. A similar trend was observed with the Ag-promoted cobalt/ceria catalysts. Doping of ceria with Ga or In decreased methane and increased the selectivity to olefins and alcohols for Ag-promoted cobalt/ceria. The sum of the products of olefins and alcohols for various catalysts exhibited a decreasing trend as follows: Ag-Co/Ce-Ga > Ag-Co/Ce-In > Ag-Co/Ce. Results of H-2-TPR-XANES showed that adding of Ga or In to ceria increases the fraction of Ce3+ in the surface shell for both unpromoted and Ag-promoted catalysts in the range of temperature typical of catalyst activation. This partially reduced ceria plays an important role in controlling the product selectivity of cobalt-catalyzed FT synthesis.
引用
收藏
页码:115 / 123
页数:9
相关论文
共 53 条
[1]   PROPERTIES OF SILICA-SUPPORTED CU CO BIMETALLIC CATALYSTS IN THE SYNTHESIS OF HIGHER ALCOHOLS [J].
BAKER, JE ;
BURCH, R ;
HIBBLE, SJ ;
LOADER, PK .
APPLIED CATALYSIS, 1990, 65 (02) :281-292
[3]   INFLUENCE OF REACTION CONDITIONS ON THE EFFECT OF CO-FEEDING ETHENE IN THE FISCHER-TROPSCH SYNTHESIS ON A FUSED-IRON CATALYST IN THE LIQUID-PHASE [J].
BOELEE, JH ;
CUSTERS, JMG ;
VANDERWIELE, K .
APPLIED CATALYSIS, 1989, 53 (01) :1-13
[4]   Fischer-Tropsch synthesis: Cobalt particle size and support effects on intrinsic activity and product distribution [J].
Borg, Oyvind ;
Dietzel, Pascal D. C. ;
Spjelkavik, Aud I. ;
Tveten, Erik Z. ;
Walmsley, John C. ;
Diplas, Spyridon ;
Eri, Sigrid ;
Holmen, Anders ;
Ryttera, Erling .
JOURNAL OF CATALYSIS, 2008, 259 (02) :161-164
[5]   A comparison of cobalt and iron based slurry phase Fischer-Tropsch synthesis [J].
Botes, F. G. ;
Niemantsverdriet, J. W. ;
van de Loosdrecht, J. .
CATALYSIS TODAY, 2013, 215 :112-120
[6]  
Chakrabarti D., 2016, CHEM IND, P183
[7]   Effect of the ZrO2 pore structure on the reduction of a supported cobalt oxide in catalysts for Fischer-Tropsch synthesis [J].
Chernavskii, PA ;
Lermontov, AS ;
Pankina, GV ;
Torbin, SN ;
Lunin, VV .
KINETICS AND CATALYSIS, 2002, 43 (02) :268-274
[8]   Fischer-Tropsch synthesis: Comparison of performances of iron and cobalt catalysts [J].
Davis, Burtron H. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (26) :8938-8945
[9]   The renaissance of iron-based Fischer-Tropsch synthesis: on the multifaceted catalyst deactivation behaviour [J].
de Smit, Emiel ;
Weckhuysen, Bert M. .
CHEMICAL SOCIETY REVIEWS, 2008, 37 (12) :2758-2781
[10]  
Desheng W., 2000, J NAT GAS CHEM, V9, P249