Catalyst design of pt-modified Ni/Al2O3 catalyst with flat temperature profile in methane reforming with CO2 and O2

被引:72
作者
Tomishige, K
Kanazawa, S
Sato, M
Ikushima, K
Kunimori, K
机构
[1] Univ Tsukuba, Inst Mat Sci, Tsukuba, Ibaraki 3058573, Japan
[2] Univ Tokyo, Sch Engn, Dept Appl Chem, Bunkyo Ku, Tokyo 1138656, Japan
[3] Japan Natl Oil Corp, Nat Gas & Project Planning Dept, Chiyoda Ku, Tokyo 1008511, Japan
[4] Petr Energy Ctr, Technol Res & Dev Dept, Minato Ku, Tokyo 1050001, Japan
关键词
methane; reforming; combustion; heat supply; Pt-Ni bimetallic catalyst;
D O I
10.1023/A:1021076601653
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
Pt(0.3)/Ni(10)/Al2O3, prepared by a sequential impregnation method, exhibited a more excellent performance in methane reforming with CO2 and O-2 in terms of the catalytic activity and the temperature profile of the catalyst bed than Pt(0.3) + Ni(10)/Al2O3 prepared by a coimpregnation method, Ni(10)/Al2O3, Pt(0.3)/Al2O3, and Pt(10)/Al2O3. It is thought that this is because the surface Pt atoms on Ni catalyst can contribute to the enhancement of the catalyst reducibility.
引用
收藏
页码:69 / 74
页数:6
相关论文
共 32 条
[1]  
[Anonymous], FREE ENERGY FORMATIO
[2]   SELECTIVE OXIDATION OF METHANE TO SYNTHESIS GAS-USING TRANSITION-METAL CATALYSTS [J].
ASHCROFT, AT ;
CHEETHAM, AK ;
FOORD, JS ;
GREEN, MLH ;
GREY, CP ;
MURRELL, AJ ;
VERNON, PDF .
NATURE, 1990, 344 (6264) :319-321
[3]   Partial oxidation of methane -: Effect of reaction parameters and catalyst composition on the thermal profile and heat distribution [J].
Basile, F ;
Fornasari, G ;
Trifirò, F ;
Vaccari, A .
CATALYSIS TODAY, 2001, 64 (1-2) :21-30
[4]   SYNTHESIS GAS-FORMATION BY CATALYTIC-OXIDATION OF METHANE IN FLUIDIZED-BED REACTORS [J].
BHARADWAJ, SS ;
SCHMIDT, LD .
JOURNAL OF CATALYSIS, 1994, 146 (01) :11-21
[5]   Noble metal promoted Ni0.03Mg0.97O solid solution catalysts for the reforming of CH4 with CO2 [J].
Chen, YG ;
Yamazaki, O ;
Tomishige, K ;
Fujimoto, K .
CATALYSIS LETTERS, 1996, 39 (1-2) :91-95
[6]   Promoting effect of Pt, Pd and Rh noble metals to the Ni0.03Mg0.97O solid solution catalysts for the reforming of CH4 with CO2 [J].
Chen, YG ;
Tomishige, K ;
Yokoyama, K ;
Fujimoto, K .
APPLIED CATALYSIS A-GENERAL, 1997, 165 (1-2) :335-347
[7]   ENERGY-EFFICIENT METHANE-TO-SYNGAS CONVERSION WITH LOW H-2/CO RATIO BY SIMULTANEOUS CATALYTIC REACTIONS OF METHANE WITH CARBON-DIOXIDE AND OXYGEN [J].
CHOUDHARY, VR ;
RAJPUT, AM ;
PRABHAKAR, B .
CATALYSIS LETTERS, 1995, 32 (3-4) :391-396
[8]   Simulation of the catalytic partial oxidation of methane to synthesis gas [J].
DeGroote, AM ;
Froment, GF .
APPLIED CATALYSIS A-GENERAL, 1996, 138 (02) :245-264
[9]   ARE THE EQUILIBRIUM CONCENTRATIONS OF CO AND H-2 EXCEEDED DURING THE OXIDATION OF CH4 OVER A NI/YB2O3 CATALYST [J].
DISSANAYAKE, D ;
ROSYNEK, MP ;
LUNSFORD, JH .
JOURNAL OF PHYSICAL CHEMISTRY, 1993, 97 (15) :3644-3646
[10]   PARTIAL OXIDATION OF METHANE TO CARBON-MONOXIDE AND HYDROGEN OVER A NI/AL2O3 CATALYST [J].
DISSANAYAKE, D ;
ROSYNEK, MP ;
KHARAS, KCC ;
LUNSFORD, JH .
JOURNAL OF CATALYSIS, 1991, 132 (01) :117-127