Hydrogen generation by catalytic partial dehydrogenation of low-sulfur fractions produced from kerosene Jet A-1

被引:5
作者
Gianotti, Elia [1 ]
Reyes-Carmona, Alvaro [1 ]
Pearson, Karolina [2 ]
Taillades-Jacquin, Melanie [1 ]
Kraaij, Gerard [2 ]
Woerner, Antje [2 ]
Roziere, Jacques [1 ]
Jones, Deborah J. [1 ]
机构
[1] Univ Montpellier, Inst Charles Gerhardt, UMR 5253, Agregats Interfaces & Mat Energie, F-34095 Montpellier 5, France
[2] German Aerosp Ctr, Inst Engn Thermodynam Thermal Proc Technol, D-569 Stuttgart, Germany
关键词
Rectification; Fractionation; Partial dehydrogenation; Kerosene Jet A-1; Hydrogen production; Sulfur poisoning; Pt-Sn; HIGH-PURITY HYDROGEN; COKE FORMATION; PT-SN/GAMMA-AL2O3; RECTIFICATION; COMPONENTS; PLATINUM;
D O I
10.1016/j.apcatb.2015.04.018
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
Fractionation of kerosene by rectification leads to fuel fractions characterized by different proportions of iso-paraffins, n-paraffins, cyclic, dicyclic, aromatics and diaromatics. Fractions of progressively higher boiling point range are characterized by progressively higher average carbon chain length, as well as increasing content of sulfur containing molecules. Three fractions, corresponding to 5, 14 and 32 wt.%.of the original kerosene and having boiling point ranges 140-150 degrees C; 150-160 degrees C; 160-170 degrees CM, respectively, containing predominantly C-8-C-9, C-9-C-10 and C-10, respectively, and 4, 12 and 24 ppm sulfur, respectively, were fed to a partial dehydrogenation reactor using a Pt-Sn/BaO-gamma-Al2O3 catalyst. A hydrogen productivity increase up to a factor 3 for the low-boiling point fraction compared to the original kerosene is observed. The catalyst durability is significantly increased due to lower sulfur and coke deposition on the catalyst for the low boiling point fraction. The fractionation of kerosene Jet A-1 fuel by rectification is a promising approach for the enhancement of durable hydrogen generation via partial dehydrogenation. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:480 / 485
页数:6
相关论文
共 31 条
  • [21] The chemical properties of bimetallic surfaces:: Importance of ensemble and electronic effects in the adsorption of sulfur and SO2
    Rodriguez, JA
    [J]. PROGRESS IN SURFACE SCIENCE, 2006, 81 (04) : 141 - 189
  • [22] Mechanistic Study of Pt-Re/γ-Al2O3 Catalyst Deactivation by Chemical Imaging of Carbonaceous Deposits Using Advanced X-ray Detection in Scanning Transmission Electron Microscopy
    Sanchez, Sergio I.
    Moser, Mark D.
    Bradley, Steven A.
    [J]. ACS CATALYSIS, 2014, 4 (01): : 220 - 228
  • [23] COKE FORMATION DURING THERMAL-CRACKING OF N-OCTANE
    SHAH, YT
    STUART, EB
    SHETH, KD
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1976, 15 (04): : 518 - 524
  • [24] MECHANISM OF SULFUR POISONING OF PLATINUM CATALYSTS
    SOMORJAI, GA
    [J]. JOURNAL OF CATALYSIS, 1972, 27 (03) : 453 - &
  • [25] Stichlmair J.G., 2000, DISTILLATION RECTIFI, P2015
  • [26] Effect of the nature of the support on the activity of Pt-Sn based catalysts for hydrogen production by dehydrogenation of Ultra Low Sulfur Kerosene Jet A-1
    Taillades-Jacquin, Melanie
    Resini, Carlo
    Liew, Kan-Ern
    Taillades, Gilles
    Gabellini, Ilenia
    Wails, David
    Roziere, Jacques
    Jones, Deborah
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2013, 142 : 112 - 118
  • [27] ACTIVITIES AND SELECTIVITIES FOR REFORMING REACTIONS ON UNSULFIDED AND SULFIDED COMMERCIAL PLATINUM AND PLATINUM-RHENIUM CATALYSTS
    VANTRIMPONT, PA
    MARIN, GB
    FROMENT, GF
    [J]. APPLIED CATALYSIS, 1985, 17 (01): : 161 - 173
  • [28] Pt-Sn alloy phases and coke mobility over Pt-Sn/Al2O3 and Pt-Sn/ZnAl2O4 catalysts for propane dehydrogenation
    Vu, Bao Khanh
    Song, Myoung Bok
    Ahn, In Young
    Suh, Young-Woong
    Suh, Dong Jin
    Kim, Won-Il
    Koh, Hyoung-Lim
    Choi, Young Gyo
    Shin, Eun Woo
    [J]. APPLIED CATALYSIS A-GENERAL, 2011, 400 (1-2) : 25 - 33
  • [29] CO-free hydrogen production via dehydrogenation of a Jet A hydrocarbon mixture
    Wang, Bo
    Froment, Gilbert F.
    Goodman, D. Wayne
    [J]. JOURNAL OF CATALYSIS, 2008, 253 (02) : 239 - 243
  • [30] Operation planning in the rectification of essential oils
    Zamar, SD
    Salomone, HE
    Iribarren, OA
    [J]. JOURNAL OF FOOD ENGINEERING, 2005, 69 (02) : 207 - 215