SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2018, Vol. 26 ›› Issue (9): 1920-1927.DOI: 10.1016/j.cjche.2018.03.031

• Catalysis, Kinetics and Reaction Engineering • 上一篇    下一篇

Sulfur production from smelter off-gas using CO-H2 gas mixture as the reducing agent over modified Fe/γ-Al2O3 catalysts

Tingting Ge1, Cuncun Zuo2,3, Lubin Wei1, Chunshan Li2,3   

  1. 1 School of Chemical and Environmental Engineering, China University of Mining & Technology-Beijing, Beijing 100083, China;
    2 Beijing Key Laboratory of Ionic Liquids Clean Process, State Key Laboratory of Multiphase Complex Systems, The National Key Laboratory of Clean and Efficient Coking Technology, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China;
    3 College of Chemistry and Chemical Engineering, University of Chinese Academy of Sciences, Beijing 100190, China
  • 收稿日期:2018-01-29 修回日期:2018-03-23 出版日期:2018-09-28 发布日期:2018-10-17
  • 通讯作者: Lubin Wei,E-mail addresses:wlb@cumtb.edu.cn;Chunshan Li,E-mail addresses:csli@ipe.ac.cn
  • 基金资助:

    Supported by the National Science Fund for Excellent Young Scholars (21422607), Key Program of National Natural Science Foundation of China (91434203).

Sulfur production from smelter off-gas using CO-H2 gas mixture as the reducing agent over modified Fe/γ-Al2O3 catalysts

Tingting Ge1, Cuncun Zuo2,3, Lubin Wei1, Chunshan Li2,3   

  1. 1 School of Chemical and Environmental Engineering, China University of Mining & Technology-Beijing, Beijing 100083, China;
    2 Beijing Key Laboratory of Ionic Liquids Clean Process, State Key Laboratory of Multiphase Complex Systems, The National Key Laboratory of Clean and Efficient Coking Technology, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China;
    3 College of Chemistry and Chemical Engineering, University of Chinese Academy of Sciences, Beijing 100190, China
  • Received:2018-01-29 Revised:2018-03-23 Online:2018-09-28 Published:2018-10-17
  • Contact: Lubin Wei,E-mail addresses:wlb@cumtb.edu.cn;Chunshan Li,E-mail addresses:csli@ipe.ac.cn
  • Supported by:

    Supported by the National Science Fund for Excellent Young Scholars (21422607), Key Program of National Natural Science Foundation of China (91434203).

摘要: A series of modified γ-Al2O3 supported iron-based catalysts (M-Fe/γ-Al2O3) was developed to reduce SO2 in actual smelter off-gases using CO-H2 gas mixture as reducing agent for sulfur production. Used as modifiers, three metal additives-Ni, Co, and Ce were added to Fe/γ-Al2O3 catalysts. Changes in catalyst structure and active phase were characterized with X-ray diffraction, XPS, SEM, and EDS. The reduction ability of catalysts was exhibited via CO-TPR. The prepared catalysts only need to be pre-reacted for a period of time, eliminating the need for presulfidation treatment. Reaction conditions were optimized in a fixed bed reactor to achieve high SO2 conversion and sulfur selectivity. XRD characterization was carried out to verify the resulting sulfur products. Combining in situ infrared characterization and catalyst evaluation of support and active component, the reaction mechanism was investigated and proposed.

关键词: Iron-based catalysts, Sulfur production, CO-H2 gas mixture, Reaction mechanism

Abstract: A series of modified γ-Al2O3 supported iron-based catalysts (M-Fe/γ-Al2O3) was developed to reduce SO2 in actual smelter off-gases using CO-H2 gas mixture as reducing agent for sulfur production. Used as modifiers, three metal additives-Ni, Co, and Ce were added to Fe/γ-Al2O3 catalysts. Changes in catalyst structure and active phase were characterized with X-ray diffraction, XPS, SEM, and EDS. The reduction ability of catalysts was exhibited via CO-TPR. The prepared catalysts only need to be pre-reacted for a period of time, eliminating the need for presulfidation treatment. Reaction conditions were optimized in a fixed bed reactor to achieve high SO2 conversion and sulfur selectivity. XRD characterization was carried out to verify the resulting sulfur products. Combining in situ infrared characterization and catalyst evaluation of support and active component, the reaction mechanism was investigated and proposed.

Key words: Iron-based catalysts, Sulfur production, CO-H2 gas mixture, Reaction mechanism