Synthesis and characterization of gallium-promoted copper-ceria catalyst and its application for methanol steam reforming in a packed bed reactor

被引:37
|
作者
Pohar, A. [1 ]
Hocevar, S. [1 ]
Likozar, B. [1 ,2 ]
Levec, J. [1 ,2 ]
机构
[1] Natl Inst Chem, Lab Catalysis & Chem React Engn, Ljubljana 1000, Slovenia
[2] Univ Ljubljana, Fac Chem & Chem Technol, Ljubljana 1000, Slovenia
关键词
Methanol steam reforming; Catalysis; Copper; Ceria; Gallium; Kinetic modeling; HYDROGEN-PRODUCTION; CARBON-MONOXIDE; HOMOGENEOUS PRECIPITATION; SELECTIVE OXIDATION; CU/ZNO; NONPOLAR;
D O I
10.1016/j.cattod.2015.01.043
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A co-precipitation method was used for the synthesis of a novel copper-ceria catalyst promoted with gallium. Structural characterization was performed by SEM, EDS, BET, XRD, and XPS techniques. Methanol steam reforming was conducted inside a miniaturized LTCC packed bed reactor in the temperature range of 300-400 degrees C, and hydrogen was successfully produced from a water and methanol mixture. The kinetics of the reforming process were evaluated and the operation of the miniaturized reactor was described with a 3D finite element model, which included all governing mechanisms: fluid dynamics, transport phenomena and reaction kinetics. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:358 / 364
页数:7
相关论文
共 50 条
  • [1] Gallium-Promoted Strong Metal-Support Interaction over a Supported Cu/ZnO Catalyst for Methanol Steam Reforming
    Li, Didi
    Yan, Haitao
    Jiang, Zhaocong
    Qiu, Runfa
    Liu, Qi
    Zhu, Minghui
    ACS CATALYSIS, 2024, 14 (12): : 9511 - 9520
  • [2] Methanol steam reforming: A comparison of different kinetics in the simulation of a packed bed reactor
    Tesser, R.
    Di Serio, M.
    Santacesaria, E.
    CHEMICAL ENGINEERING JOURNAL, 2009, 154 (1-3) : 69 - 75
  • [3] Comparison of steam and autothermal reforming of methanol using a packed-bed low-cost copper catalyst
    Tang, Hong-Yue
    Erickson, Paul
    Yoon, Hyung Chul
    Liao, Chang-Hsien
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (18) : 7656 - 7665
  • [4] Experiment of catalyst activity distribution effect on methanol steam reforming performance in the packed bed plate-type reactor
    Wang, Guoqiang
    Wang, Feng
    Li, Longjian
    Zhang, Guofu
    ENERGY, 2013, 51 : 267 - 272
  • [5] Methanol Steam Reforming in a Reactor with a Palladium–Copper Membrane in the Presence of a Nickel–Copper Catalyst
    E. Yu. Mironova
    A. A. Lytkina
    M. M. Ermilova
    N. V. Orekhova
    N. A. Zhilyaeva
    N. R. Roshan
    V. M. Ievlev
    A. B. Yaroslavtsev
    Petroleum Chemistry, 2020, 60 : 1232 - 1238
  • [6] Influence of Geometry on Pressure and Velocity Distribution in Packed-bed Methanol Steam Reforming Reactor
    Ivanovic, Ivana
    Sedmak, Aleksandar
    Milosevic, Milos
    Cvetkovic, Ivana
    Pohar, Andrej
    Likozar, Blaz
    PROCEEDINGS OF THE INTERNATIONAL CONFERENCE ON NUMERICAL ANALYSIS AND APPLIED MATHEMATICS 2016 (ICNAAM-2016), 2017, 1863
  • [7] Dynamic modelling of methanol steam reforming to hydrogen in a packed bed reactor for shipboard fuel cells
    Grenko, Bojan
    de Jong, Wiebren
    van de Ketterij, Robert
    van Biert, Lindert
    CHEMICAL ENGINEERING JOURNAL, 2025, 507
  • [8] Using various copper catalysts with ceria sol washcoated in a microchannel reactor for steam reforming of methanol
    Wang, Pao-Ya
    Wang, Jung-Hui
    Shen, Chia-Chieh
    Yeh, Chuin-Tih
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2009, 238
  • [9] Hydrogen production by oxidative steam reforming of methanol using ceria promoted copper-alumina catalysts
    Patel, Sanjay
    Pant, K. K.
    FUEL PROCESSING TECHNOLOGY, 2007, 88 (08) : 825 - 832
  • [10] Synthesis and characterization of a novel methanol-steam reforming catalyst.
    Idem, RO
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2000, 219 : U535 - U535