A kinetic study on the structural and functional roles of lanthana in iron-based high temperature water-gas shift catalysts

被引:14
|
作者
Hallac, Basseem B. [1 ]
Brown, Jared C. [1 ]
Baxter, Larry L. [1 ]
Argyle, Morris D. [1 ]
机构
[1] Brigham Young Univ, Ira A Fulton Sch Engn & Technol, Dept Chem Engn, Provo, UT 84602 USA
关键词
Water-gas shift; Lanthana; Iron catalyst; Spinel; Kinetics; Stability; OXIDE; REDUCTION; TRANSIENT; MODEL;
D O I
10.1016/j.ijhydene.2014.02.170
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
The structural and functional roles of varying amounts of lanthana in co-precipitated high temperature Fe2O3/Cr2O3/CuO water-gas shift catalysts were studied at 1 atm and 350-425 degrees C temperature range. Addition of 0.5 wt% of lanthana enhanced the reducibility of the catalyst, increased its surface area and its WGS activity from 24 to 31 mmol CO/(g(cat) min), and reduced the deactivation rate at 400 degrees C from 23% to 11% relative to a similar catalyst with no lanthana. XRD results suggested that 0.5 wt% of lanthana stabilized the iron-chromium cubic spinel structure most efficiently under the operating conditions; however, further additions appeared to disrupt the spinel structure and degrade the performance of the catalysts. The power-law and Langmuir-Hinshelwood models provided much better fits to the rate data than either the redox or the Eley-Rideal models, suggesting that the reaction tends to follow an adsorptive mechanism. The CO adsorption equilibrium constant was largest for the catalyst with 0.5 wt% lanthana, indicating that the addition of lanthana might facilitate CO adsorption. Water inhibited the reaction as it strongly adsorbed on the catalyst surface. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:7306 / 7317
页数:12
相关论文
共 50 条
  • [31] COMPARISON OF THE DYNAMICS OF THE HIGH-TEMPERATURE WATER-GAS SHIFT REACTION ON OXIDE CATALYSTS
    HAKKARAINEN, R
    SALMI, T
    KEISKI, RL
    CATALYSIS TODAY, 1994, 20 (03) : 395 - 408
  • [32] Study on the supported Cu-based catalysts for the low-temperature water-gas shift reaction
    Yahiro, Hidenori
    Murawaki, Keisuke
    Saiki, Kazuhiko
    Yamamoto, Tetsuya
    Yamaura, Hiroyuki
    CATALYSIS TODAY, 2007, 126 (3-4) : 436 - 440
  • [33] Low temperature water-gas shift: comparison of thoria and ceria catalysts
    Jacobs, G
    Crawford, A
    Williams, L
    Patterson, PM
    Davis, BH
    APPLIED CATALYSIS A-GENERAL, 2004, 267 (1-2) : 27 - 33
  • [34] Computational study of nanoparticle catalysts in the water-gas shift reaction
    Haug, Kenneth
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2015, 250
  • [35] Fischer Tropsch and Water Gas Shift chemical regimes on supported iron-based catalysts at high metal loading
    Pirola, C.
    Bianchi, C. L.
    Di Michele, A.
    Vitali, S.
    Ragaini, V.
    CATALYSIS COMMUNICATIONS, 2009, 10 (06) : 823 - 827
  • [36] Design of Cr-Free Promoted Copper-Iron Oxide-Based High-Temperature Water-Gas Shift Catalysts
    Yalcin, Ozgen
    Sourav, Sagar
    Wachs, Israel E.
    ACS CATALYSIS, 2023, 13 (19): : 12681 - 12691
  • [37] A facile method for preparation of iron based catalysts for high temperature water gas shift reaction
    Meshkani, Fereshteh
    Rezaei, Mehran
    JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2014, 20 (05) : 3297 - 3302
  • [38] COBALT PROMOTED IRON BASED CATALYSTS FOR WATER-GAS SHIFT REACTION - STRUCTURE AND CATALYTIC ACTIVITY
    HALACHEV, T
    MATVEEV, V
    IDAKIEV, V
    MAKSIMOV, Y
    ANDREEV, A
    REACTION KINETICS AND CATALYSIS LETTERS, 1986, 32 (02): : 257 - 262
  • [39] High-stability water-gas shift catalysts based on nanocrystalline ceria.
    Fu, Q
    Kudriavtseva, S
    Saltsburg, H
    Flytzani-Stephanopoulos, M
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2001, 221 : U470 - U470
  • [40] Synthesis of copper promoted high temperature water-gas shift catalysts by oxidation-precipitation
    Dufour, J.
    Martos, C.
    Ruiz, A.
    Marono, M.
    Sanchez, J. M.
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (31) : 17600 - 17607