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
  • [31] REFORMULATED GASOLINE, OPPORTUNITIES FOR NEW CATALYST TECHNOLOGY
    SEDDON, D
    [J]. CATALYSIS TODAY, 1992, 15 (01) : 1 - 21
  • [32] STEINBERG KH, 1989, P 2 INT C SPILL K MA, P150
  • [33] CHARACTERIZATION OF DEALUMINATED LARGE-PORT MORDENITES
    VANNIEKERK, MJ
    FLETCHER, JCQ
    OCONNOR, CT
    [J]. JOURNAL OF CATALYSIS, 1992, 138 (01) : 150 - 163
  • [34] VASINA TV, 2001, STUD SURF SCI CATAL, V138, P93
  • [35] HYDROISOMERIZATION OF NORMAL PENTANE OVER A ZEOLITE CATALYST
    VOORHIES, A
    BRYANT, PA
    [J]. AICHE JOURNAL, 1968, 14 (06) : 852 - &
  • [36] HYDROGEN CHEMISORPTION SUPPRESSION IN RU-ZEOLITE CATALYSTS
    WANG, HT
    CHEN, YW
    GOODWIN, JG
    [J]. ZEOLITES, 1984, 4 (01): : 56 - 60
  • [37] Segregation of platinum from mordenite channels on calcination and reduction pretreatments
    Yuvaraj, S
    Chang, TH
    Yeh, CT
    [J]. JOURNAL OF CATALYSIS, 2004, 221 (02) : 466 - 473
  • [38] ISOMERIZATION OF N-PENTANE AND OTHER LIGHT-HYDROCARBONS ON HYBRID CATALYST - EFFECT OF HYDROGEN SPILLOVER
    ZHANG, AH
    NAKAMURA, I
    AIMOTO, K
    FUJIMOTO, K
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (04) : 1074 - 1080
  • [39] IDENTIFICATION OF ISOLATED PT ATOMS IN H-MORDENITE
    ZHOLOBENKO, VL
    LEI, GD
    CARVILL, BT
    LERNER, BA
    SACHTLER, WMH
    [J]. JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS, 1994, 90 (01): : 233 - 238