Characterization of Ni, Mo and Ni-Mo catalysts supported on alumina-pillared α-zirconium phosphate and reactivity for the thiophene HDS reaction

被引:42
作者
Mérida-Robles, J [1 ]
Rodríguez-Castellón, E [1 ]
Jiménez-López, A [1 ]
机构
[1] Univ Malaga, Fac Ciencias, Dept Quim Inorgan Cristalog & Mineral, E-29071 Malaga, Spain
关键词
pillared; alumina; nickel; molybdenum; HDS; catalysis; zirconium phosphate;
D O I
10.1016/S1381-1169(99)00048-5
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
A series of fluorinated alumina pillared a-zirconium phosphate supported with nickel, molybdenum and nickel-molybdenum sulfide catalysts was prepared in order to investigate the use of an alumina-pillared material, i.e., an alumina diluted within another inorganic matrix, as a support of sulfide catalysts. The catalysts were prepared by impregnation, with loadings of 4, 8, 12 wt.% of Ni; 13 wt.% of Mo and 2.1-9, 3-13 wt.% of Ni-Mo followed by calcination at 673 K. Sulfidation was performed at 673 K for 2 h. They were characterised by X-ray diffraction (XRD), temperature-programmed reduction (TPR) and X-ray photoelectron spectroscopy (XPS). The set of data indicated that in the Ni-based catalysts a fraction of the loaded Ni2+ interacts with the support and cannot be sulfided at 673 K. However, a total sulfidation of Ni2+ is reached in the NiMo-based catalysts. The Ni 2p(3/2) binding energy (B.E) of Ni-Mo sulfided catalysts shifted to higher values (> 1 eV) with respect to those observed in Ni-based catalysts suggesting the existence of different environments for Ni in these materials. The catalysts can be easily regenerated by treatment with 5% (v/v) O-2/N-2 mixture at 673 K without noticeable loss of activity. The catalysts exhibited a high activity and stability for thiophene HDS particularly the NiMo catalysts due to the promotion of Ni for Mo-based catalysts. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
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页码:169 / 181
页数:13
相关论文
共 52 条
[11]  
Cid R, 1995, BOL SOC CHIL QUIM, V40, P371
[12]  
CLAUSEN BS, 1981, B SOC CHIM BELG, V90, P1249
[13]   CHARACTERIZATION OF THE STANDARD NICKEL SILICA CATALYST EURONI-1 .3. INVESTIGATIONS OF CATALYST STRUCTURE [J].
COENEN, JWE .
APPLIED CATALYSIS, 1991, 75 (02) :193-223
[14]   RELATIONSHIP BETWEEN REDUCED NICKEL AND ACTIVITY FOR BENZENE HYDROGENATION ON NI-USY ZEOLITE CATALYSTS [J].
DAZA, L ;
PAWELEC, B ;
ANDERSON, JA ;
FIERRO, JLG .
APPLIED CATALYSIS A-GENERAL, 1992, 87 (01) :145-156
[15]  
DELMON B, 1979, P 3 INT C CHEM US MO, P73
[16]   IN-SITU POISONING OF THE THIOPHENE HYDRODESULFURIZATION ACTIVITY OF CARBON-SUPPORTED TRANSITION-METAL SULFIDE CATALYSTS BY PHOSPHORUS [J].
EIJSBOUTS, S ;
VANGESTEL, JNM ;
VANOERS, EM ;
PRINS, R ;
VANVEEN, JAR ;
DEBEER, VHJ .
APPLIED CATALYSIS A-GENERAL, 1994, 119 (02) :293-303
[17]   EFFECT OF THE REDUCTION TEMPERATURE ON THE SELECTIVITY OF THE HIGH-TEMPERATURE REACTION OF ACETONE AND HYDROGEN OVER ALUMINA AND TITANIA-SUPPORTED NICKEL AND COBALT CATALYSTS [J].
GANDIA, LM ;
MONTES, M .
JOURNAL OF MOLECULAR CATALYSIS, 1994, 94 (03) :347-367
[18]  
GATES BC, 1979, CHEM CATALYTIC PROCE, P390
[19]   INFLUENCE OF THE PREPARATION METHOD AND THE NATURE OF THE SUPPORT ON THE STABILITY OF NICKEL-CATALYSTS [J].
GIL, A ;
DIAZ, A ;
GANDIA, LM ;
MONTES, M .
APPLIED CATALYSIS A-GENERAL, 1994, 109 (02) :167-179
[20]   CATALYTIC HYDRODESULFURIZATION [J].
GRANGE, P .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1980, 21 (01) :135-181