Methane steam reforming over Ni/Ce-ZrO2 catalyst:: Influences of Ce-ZrO2 support on reactivity, resistance toward carbon formation, and intrinsic reaction kinetics

被引:203
作者
Laosiripojana, N
Assabumrungrat, S
机构
[1] King Mongkuts Univ Technol Thonburi, Joint Grad Sch Energy & Environm, Bangkok 10140, Thailand
[2] Chulalongkorn Univ, Fac Engn, Dept Chem Engn, Ctr Excellence Catalysis & Catalyt React Engn, Bangkok 10330, Thailand
关键词
D O I
10.1016/j.apcata.2005.05.026
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
Ni/Ce-ZrO2 showed good methane steam reforming performance in term of stability toward the deactivation by carbon deposition. It was first observed that the catalyst with Cc/Zr ratio of 3/1 showed the best activity among Ni/Ce-ZrO2 samples with the Cc/Zr ratios of 1/0, 1/1, 1/ 3, and 3/1. Temperature-programmed oxidation (TPO) experiments indicated the excellent resistance toward carbon formation for this catalyst, compared to conventional Ni/Al2O3; the requirement of inlet H2O/CH4 to operate without the formation of carbon species is much lower. These benefits are related to the high oxygen storage capacity (OSC) of Ce-ZrO2. During the steam reforming process, in addition to the reactions on Ni surface (*), the redox reactions between the gaseous components present in the system and the lattice oxygen (O-x) on CeZrO2 surface also take place. Among these reactions, the redox reactions between the high carbon formation potential compounds (CH4, CHx-*n and CO) and the lattice oxygen (0,) can prevent the formation of carbon species from the methane decomposition and Boudard reactions, even at low inlet H2O/CH4 ratio (1.0/1.0). Regarding the intrinsic kinetic studies in the present work, the reaction order in methane over Ni/Ce-ZrO2 was observed to be approximately 1.0 in all conditions. The dependence of steam on the rate was non-monotonic, whereas addition of oxygen as an autothermal reforming promoted the rate but reduced CO and H-2 production selectivities. The addition of a small amount of hydrogen increased the conversion of methane, however, this positive effect became less pronounced and the methane conversion was eventually inhibited when high hydrogen concentration was added. Ni/Ce-ZrO2 showed significantly stronger negative impact of hydrogen than Ni/Al2O3. The redox mechanism on ceria proposed by Otsuka et al. [K. Otsuka, T. Ushiyama, I. Yamanaka, Chem. Lett. (1993) 1517; K. Otsuka, M. Hatano, A. Morikawa, J. Catal. 79 (1983) 493; K. Otsuka, M. Hatano, A. Morikawa, Inorg. Chim. Acta 109 (1985) 193] can explain this high inhibition. (c) 2005 Elsevier B.V. All rights reserved.
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页码:200 / 211
页数:12
相关论文
共 49 条
[1]   The multiple roles for catalysis in the production of H2 [J].
Armor, JN .
APPLIED CATALYSIS A-GENERAL, 1999, 176 (02) :159-176
[2]   Surface and reduction energetics of the CeO2-ZrO2 catalysts [J].
Balducci, G ;
Kaspar, J ;
Fornasiero, P ;
Graziani, M ;
Islam, MS .
JOURNAL OF PHYSICAL CHEMISTRY B, 1998, 102 (03) :557-561
[3]   Promoting effect of CeO2 in a Cu/CeO2 catalyst:: lowering of redox potentials of Cu species in the CeO2 matrix [J].
Bera, P ;
Mitra, S ;
Sampath, S ;
Hegde, MS .
CHEMICAL COMMUNICATIONS, 2001, (10) :927-928
[4]   Intrinsic reaction kinetics of methane steam reforming on a nickel/zirconia anode [J].
Dicks, AL ;
Pointon, KD ;
Siddle, A .
JOURNAL OF POWER SOURCES, 2000, 86 (1-2) :523-530
[5]   Methane reforming over Ni/Ce-ZrO2 catalysts:: effect of nickel content [J].
Dong, WS ;
Roh, HS ;
Jun, KW ;
Park, SE ;
Oh, YS .
APPLIED CATALYSIS A-GENERAL, 2002, 226 (1-2) :63-72
[6]  
Elnashaie S., 1993, MODELING SIMULATION
[7]   ON THE NON-MONOTONIC BEHAVIOR OF METHANE STEAM REFORMING KINETICS [J].
ELNASHAIE, SSEH ;
ADRIS, AM ;
ALUBAID, AS ;
SOLIMAN, MA .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (02) :491-501
[8]   RH-LOADED CEO2-ZRO2 SOLID-SOLUTIONS AS HIGHLY EFFICIENT OXYGEN EXCHANGERS - DEPENDENCE OF THE REDUCTION BEHAVIOR AND THE OXYGEN STORAGE CAPACITY ON THE STRUCTURAL-PROPERTIES [J].
FORNASIERO, P ;
DIMONTE, R ;
RAO, GR ;
KASPAR, J ;
MERIANI, S ;
TROVARELLI, A ;
GRAZIANI, M .
JOURNAL OF CATALYSIS, 1995, 151 (01) :168-177
[9]   OXYGEN STORAGE CAPACITY OF ALUMINA-SUPPORTED RH/CEO2 CATALYST [J].
HANEDA, M ;
MIKI, T ;
KAKUTA, N ;
UENO, A ;
TATEISHI, S ;
MATSUURA, S ;
SATO, M .
NIPPON KAGAKU KAISHI, 1990, (08) :820-823
[10]   LATTICE-PARAMETERS, IONIC CONDUCTIVITIES, AND SOLUBILITY LIMITS IN FLUORITE-STRUCTURE HF-4+O2, ZR-4+O2, CE-4+O2, TH-4+O2, V-4+O2 OXIDE SOLID-SOLUTIONS [J].
KIM, DJ .
JOURNAL OF THE AMERICAN CERAMIC SOCIETY, 1989, 72 (08) :1415-1421