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LaCoO3对H2S选择氧化性能的影响

喻昕蕾 潘伟童 高瑞 高德志 刘霞 代正华 于广锁 王辅臣

喻昕蕾, 潘伟童, 高瑞, 高德志, 刘霞, 代正华, 于广锁, 王辅臣. LaCoO3对H2S选择氧化性能的影响[J]. 燃料化学学报(中英文), 2019, 47(8): 973-979.
引用本文: 喻昕蕾, 潘伟童, 高瑞, 高德志, 刘霞, 代正华, 于广锁, 王辅臣. LaCoO3对H2S选择氧化性能的影响[J]. 燃料化学学报(中英文), 2019, 47(8): 973-979.
YU Xin-lei, PAN Wei-tong, GAO Rui, GAO De-zhi, LIU Xia, DAI Zheng-hua, YU Guang-suo, WANG Fu-chen. Selective oxidation of H2S over the LaCoO3 catalyst[J]. Journal of Fuel Chemistry and Technology, 2019, 47(8): 973-979.
Citation: YU Xin-lei, PAN Wei-tong, GAO Rui, GAO De-zhi, LIU Xia, DAI Zheng-hua, YU Guang-suo, WANG Fu-chen. Selective oxidation of H2S over the LaCoO3 catalyst[J]. Journal of Fuel Chemistry and Technology, 2019, 47(8): 973-979.

LaCoO3对H2S选择氧化性能的影响

基金项目: 

国家自然科学基金 21776086

详细信息
  • 中图分类号: TQ541

Selective oxidation of H2S over the LaCoO3 catalyst

Funds: 

the National Natural Science Foundation of China 21776086

More Information
  • 摘要: 使用溶胶-凝胶法制备了LaCoO3催化剂,采用XRD、BET和XPS等方式对催化剂进行了表征,考察了该催化剂制备过程中煅烧温度、表面活性剂PEG-6000和PEG-20000含量对其H2S选择氧化制硫磺反应催化活性的影响。结果表明,表面活性剂PEG-6000及PEG-20000的添加能明显提高LaCoO3的催化活性。0.02 mol La(NO33+0.02mol Co(NO32溶液中添加0.30 g PEG-20000、煅烧温度为650℃时所制备的LaCoO3催化活性最好;在最佳反应温度260℃下,H2S的转化率达到96.10%,硫选择性为93.77%。
  • 图  1  煅烧温度对LaCoO3催化剂的H2S选择性氧化活性的影响

    Figure  1  Effect of calcination temperature on the activity of LaCoO3 catalysts in the selective oxidation of H2S

    : H2S conversion; : sulfur selectivity; : sulfur yield

    图  2  PEG-6000含量对LaCoO3催化剂的H2S选择性氧化活性的影响

    Figure  2  Effect of surfactant PEG-6000 contents on the activity of LaCoO3 catalysts in the selective oxidation of H2S

    : H2S conversion; : sulfur selectivity; : sulfur yield

    图  3  PEG-20000含量对LaCoO3催化剂的H2S选择性氧化活性的影响

    Figure  3  Effect of PEG-20000 contents on the activity of LaCoO3 catalysts in the selective oxidation of H2S

    : H2S conversion; : sulfur selectivity; : sulfur yield

    图  4  反应温度对LaCoO3催化剂H2S选择性氧化活性的影响

    Figure  4  Effect of reaction temperature on the selective oxidation of H2S over the LaCoO3 catalysts

    : H2S conversion; : sulfur selectivity; : sulfur yield

    图  5  LaCoO3催化剂的稳定性能

    Figure  5  Stability of the LaCoO3 catalyst in the selective oxidation of H2S

    图  6  不同煅烧温度下LaCoO3的XRD谱图

    Figure  6  XRD patterns of the LaCoO3 catalysts obtained at different calcination temperatures

    图  7  不同PEG-20000含量下催化剂的XRD谱图

    Figure  7  XRD patterns of the LaCoO3 catalysts obtained with different PEG-20000 surfactant contents

    图  8  LaCoO3催化剂的XPS谱图

    Figure  8  XPS spectra of the LaCoO3 catalyst

    (a): overview; (b): La 3d; (c): Co 2p; (d): O 1s

    表  1  LaCoO3催化剂的制备条件

    Table  1  Preparation conditions of LaCoO3 catalysts

    Entry Calcination temperature t/℃ PEG-6000 content m/g PEG-20000 content m/g
    1 600 - -
    2 650 - -
    3 700 - -
    4 750 - -
    5 650 0.15 -
    6 650 0.3 -
    7 650 0.45 -
    8 650 0.6 -
    9 650 - 0.15
    10 650 - 0.3
    11 650 - 0.45
    12 650 - 0.6
    下载: 导出CSV

    表  2  催化剂的比表面积以及平均粒径

    Table  2  Specific surface area and average particle size of the LaCoO3 catalysts obtained with different surfactant contents

    Surfactant content Calcination temperature t/℃ ABET /(m2·g-1) dP/nm vP/(cm3·g-1)
    - 650 7.495 7.396 1.941×10-2
    0.45 g PEG-6000 650 8.543 9.276 1.981×10-2
    0.30 g PEG-20000 650 9.626 8.413 2.025×10-2
    下载: 导出CSV
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  • 被引次数: 0
出版历程
  • 收稿日期:  2019-04-25
  • 修回日期:  2019-06-24
  • 网络出版日期:  2021-01-23
  • 刊出日期:  2019-08-10

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