Catalytic behaviour of bifunctional pumice-supported and zeolite/pumice hybrid catalysts for n-pentane hydroisomerization

被引:13
作者
Consuelo Alvarez-Galvan, M. [2 ]
Brito, Andrea [2 ]
Garcia-Alvarez, Francisco J. [2 ]
de la Pena O'Shea, Victor A. [3 ]
Borges, Emma [2 ]
Pawelec, Barbara [1 ]
机构
[1] CSIC, Inst Catalisis & Petr Quim, Madrid 28049, Spain
[2] Univ La Laguna, Dept Ingn Quim & Tecnol Farmaceut, Tenerife 38200, Canary Isl, Spain
[3] ENERGIA, Inst Madrileno Estudios Avanzados, Madrid 28933, Spain
关键词
Pumice; Mordenite; ZSM-5; Platinum; n-Pentane hydroisomerization;
D O I
10.1016/j.apcata.2008.07.046
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 phillipsite(zeolite)-rich pumice-based supports with different acidity, Si/Al ratios and textural properties were prepared by acid leaching using hydrochloric acid. The NH3-TPD profiles, chemical composition and nitrogen adsorption-desorption isotherms pointed out that textural and acidity properties depend largely on the acidification treatment conditions. Bifunctional catalysts based on platinum supported over protonated pumice have been prepared by ethanol impregnation and tested in n-pentane hydroisomerization. Very low conversions and yields to isopentane have been obtained. The small size of phillipsite channels, lower than the pentane molecule and the intermediate products, may be hindering the access of these molecules to the acidic sites, contributing to their low activity in the target reaction. However, the catalysts constituted by a physical mixture of pumice-supported platinum, with protonated commercial zeolites (H-Mordenite or H-ZSM-5), widely used for light paraffin isomerization, resulted in higher isopentane yields than the bifunctional commercial zeolite-based catalysts. These results are explained by the greater accessibility of metal sites in a wider pore support and by the lesser blocking of the acid surface placed in the zeolite micropores. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:38 / 45
页数:8
相关论文
共 39 条
  • [11] CORMA A, 1998, NATO ASI SER, V3, P35
  • [12] EVERING BL, 1954, ADV CATALYSIS, V6
  • [13] HYDROISOMERIZATION OF N-PENTANE OVER HYBRID CATALYSTS CONTAINING A SUPPORTED HYDROGENATION CATALYST
    FUJIMOTO, K
    MAEDA, K
    AIMOTO, K
    [J]. APPLIED CATALYSIS A-GENERAL, 1992, 91 (02) : 81 - 86
  • [14] CONVERSION OF BUTANE OVER THE SOLID SUPERACID ZRO2/SO4(2-) IN THE PRESENCE OF HYDROGEN
    GARIN, F
    ANDRIAMASINORO, D
    ABDULSAMAD, A
    SOMMER, J
    [J]. JOURNAL OF CATALYSIS, 1991, 131 (01) : 199 - 203
  • [15] Single and composite bifunctional catalysts of H-MOR or SO42--ZrO2 for n-octane hydroisomerization-cracking. Influence of the porosity of the acid component
    Grau, JM
    Parera, JM
    [J]. APPLIED CATALYSIS A-GENERAL, 1997, 162 (1-2) : 17 - 27
  • [16] CONVERSION OF HEAVY N-ALKANES INTO LIGHT ISOMERS OVER H-MORDENITE, PLATINUM/H-MORDENITE, PLATINUM/ALUMINA AND COMPOSITE CATALYSTS
    GRAU, JM
    PARERA, JM
    [J]. APPLIED CATALYSIS A-GENERAL, 1993, 106 (01) : 27 - 49
  • [17] ISOMERIZATION OF N-HEXANE ON PLATINUM DEALUMINATED MORDENITE CATALYSTS .1. INFLUENCE OF THE SILICON-TO-ALUMINUM RATIO OF THE ZEOLITE
    GUISNET, M
    FOUCHE, V
    BELLOUM, M
    BOURNOVILLE, JP
    TRAVERS, C
    [J]. APPLIED CATALYSIS, 1991, 71 (02): : 283 - 293
  • [18] HAAG WO, 1983, Patent No. 4374296
  • [19] SOLID-STATE NMR-STUDIES OF MOLECULAR-SIEVE CATALYSTS
    KLINOWSKI, J
    [J]. CHEMICAL REVIEWS, 1991, 91 (07) : 1459 - 1479
  • [20] Synthesis of zeolite ZSM-57 and its catalytic evaluation for the 1-butene skeletal isomerization and n-octane cracking
    Lee, SH
    Lee, DK
    Shin, CH
    Paik, WC
    Lee, WM
    Hong, SB
    [J]. JOURNAL OF CATALYSIS, 2000, 196 (01) : 158 - 166