Deactivation due to sulfur poisoning and carbon deposition on Rh-Ni/Al2O3 catalyst during steam reforming of sulfur-doped n-hexadecane

被引:120
作者
Lakhapatri, Satish L. [2 ]
Abraham, Martin A. [1 ]
机构
[1] Youngstown State Univ, Coll Sci Technol Engn & Math, Youngstown, OH 44555 USA
[2] Univ Toledo, Dept Chem & Environm Engn, Toledo, OH 43606 USA
关键词
Steam reforming; Sulfur poisoning; Carbon deposition; Ni/Al2O3; TEM; Logistic fuels; ENSEMBLE SIZE-REDUCTION; AUXILIARY POWER UNITS; LIQUID HYDROCARBONS; HYDROGEN-PRODUCTION; PLATINUM-RHENIUM; NICKEL-CATALYSTS; COKE FORMATION; TEMPERATURE; FUEL; SURFACES;
D O I
10.1016/j.apcata.2009.05.035
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
Deactivation by sulfur poisoning and carbon deposition of steam reforming catalyst used for hydrogen production from diesel or jet fuel creates a significant barrier to commercialization of fuel cell technologies. Steam reforming of n-hexadecane on a rhodium/nickel catalyst supported on gamma-alumina, a formulation previously proposed for steam reforming of logistic fuel, was used to study the deactivation mechanisms. The steam reforming activity was measured in terms of H-2 yields and showed that the catalysts were stable in the absence of sulfur but deactivated over a period of 10 h when sulfur was present at high loading. Stability and activity were higher with higher amounts of Rh content when Ni was kept constant. TEM-EDS of used catalysts revealed preferential adsorption of sulfur on the surface of Ni crystallites: EDS and XRD analysis showed no bulk sulfide formation. Excessive carbon deposition was observed during steam reforming of sulfur-containing fuel. Blocking of reactant species on the surface of the catalyst due to the formation of aromatic/polymeric carbon on the support was also seen, although higher Rh content inhibited this phenomenon. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:113 / 121
页数:9
相关论文
共 49 条
[1]   THE ROLE OF CATALYST PRESULFURIZATION IN SOME REACTIONS OF CATALYTIC REFORMING AND HYDROGENOLYSIS [J].
APESTEGUIA, CR ;
BARBIER, J .
JOURNAL OF CATALYSIS, 1982, 78 (02) :352-359
[2]   DEACTIVATION OF REFORMING CATALYSTS BY COKING - A REVIEW [J].
BARBIER, J .
APPLIED CATALYSIS, 1986, 23 (02) :225-243
[3]   COKE FORMATION ON BIMETALLIC PLATINUM RHENIUM AND PLATINUM IRIDIUM CATALYSTS [J].
BARBIER, J ;
CORRO, G ;
ZHANG, Y ;
BOURNVILLE, JP ;
FRANCK, JP .
APPLIED CATALYSIS, 1985, 16 (02) :169-177
[4]   Mechanisms of catalyst deactivation [J].
Bartholomew, CH .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :17-60
[5]   SULFUR POISONING OF METALS [J].
BARTHOLOMEW, CH ;
AGRAWAL, PK ;
KATZER, JR .
ADVANCES IN CATALYSIS, 1982, 31 :135-242
[6]   ROLE OF SULFUR IN CATALYTIC REFORMING OF HYDROCARBONS ON PLATINUM-RHENIUM ALUMINA [J].
BICKLE, GM ;
BELTRAMINI, JN ;
DO, DD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (09) :1801-1807
[7]   ROLE OF SULFUR IN CATALYTIC REFORMING OF HYDROCARBONS ON PLATINUM ALUMINA [J].
BICKLE, GM ;
BISWAS, J ;
DO, DD .
APPLIED CATALYSIS, 1988, 36 (1-2) :259-276
[8]  
BICKLE GM, 1989, THESIS U QUEENSLAND
[9]   THE ROLE OF DEPOSITED POISONS AND CRYSTALLITE SURFACE-STRUCTURE IN THE ACTIVITY AND SELECTIVITY OF REFORMING CATALYSTS [J].
BISWAS, J ;
BICKLE, GM ;
GRAY, PG ;
DO, DD ;
BARBIER, J .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1988, 30 (02) :161-247
[10]   ADDITIVE EFFECTS IN THE SELECTIVE HYDROGENATION OF UNSATURATED-HYDROCARBONS ON PLATINUM AND RHODIUM CATALYSTS .2. INFLUENCE OF VARIOUS COMPOUNDS CONTAINING PHOSPHORUS, OXYGEN, SULFUR AND CHLORINE ON THE CATALYTIC PERFORMANCE OF PLATINUM CATALYST [J].
BOITIAUX, JP ;
COSYNS, J ;
ROBERT, E .
APPLIED CATALYSIS, 1989, 49 (02) :235-246