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负载型Pt/CeO2-Al2O3催化剂的制备及其脱氢性能

赵欣 何峰 熊果 李功华 王威燕 李文松 杨运泉

赵欣, 何峰, 熊果, 李功华, 王威燕, 李文松, 杨运泉. 负载型Pt/CeO2-Al2O3催化剂的制备及其脱氢性能[J]. 燃料化学学报(中英文), 2016, 44(6): 718-725.
引用本文: 赵欣, 何峰, 熊果, 李功华, 王威燕, 李文松, 杨运泉. 负载型Pt/CeO2-Al2O3催化剂的制备及其脱氢性能[J]. 燃料化学学报(中英文), 2016, 44(6): 718-725.
ZHAO Xin, HE Feng, XIONG Guo, LI Gong-hua, WANG Wei-yan, LI Wen-song, YANG Yun-quan. Preparation of supported Pt/CeO2-Al2O3 catalyst and its performance in the dehydrogenation of methylcyclohexane[J]. Journal of Fuel Chemistry and Technology, 2016, 44(6): 718-725.
Citation: ZHAO Xin, HE Feng, XIONG Guo, LI Gong-hua, WANG Wei-yan, LI Wen-song, YANG Yun-quan. Preparation of supported Pt/CeO2-Al2O3 catalyst and its performance in the dehydrogenation of methylcyclohexane[J]. Journal of Fuel Chemistry and Technology, 2016, 44(6): 718-725.

负载型Pt/CeO2-Al2O3催化剂的制备及其脱氢性能

基金项目: 

湖南省研究生科研创新 CX2010B258

详细信息
  • 中图分类号: TQ031.4;TQ032.41

Preparation of supported Pt/CeO2-Al2O3 catalyst and its performance in the dehydrogenation of methylcyclohexane

More Information
  • 摘要: 通过超声辅助共沉淀法制备了具有高比表面积、大孔容和大孔径的CeO2-Al2O3复合载体, 并以此制备了一系列负载型Pt/CeO2-Al2O3催化剂, 采用XRD、氮吸附、NH3-TPD、SEM和TEM等方法对复合载体和催化剂进行了表征; 以甲基环己烷为模型化合物, 考察了Pt/CeO2-Al2O3催化剂的脱氢性能, 研究了载体中Ce/Al物质的量比及反应温度对其催化脱氢性能的影响。结果表明, 当Ce/Al物质的量比为0.5时, Pt/CeO2-Al2O3催化剂在450℃下具有较高的脱氢性能; 甲基环己烷转化率达到88.53%, 甲苯的选择性达94.63%。
  • 图  1  复合载体X-CeO2-Al2O3的XRD谱图

    Figure  1  XRD patterns of various X-CeO2-Al2O3 supports with different Ce/Al mol ratios

    a: 1.0; b: 0.5; c: 2.0

    图  2  负载Pt后X-CeO2-Al2O3催化剂的XRD谱图

    Figure  2  XRD patterns of X-CeO2-Al2O3 catalysts with different Ce/Al mol ratios

    a: 1.0; b: 0.5; c: 2.0

    图  3  样品的N2物理吸附-脱附曲线

    Figure  3  Nitrogen adsorption-desorption isotherms of various CeO2-Al2O3 supports with different Ce/Al mol ratios

    a: 1.0; b: 0.5; c: 2.0

    图  4  样品的孔径分布

    Figure  4  Pore diameter size distribution of various CeO2-Al2O3 supports with different Ce/Al mol ratios

    a: 1.0; b: 0.5; c: 2.0

    图  5  负载1%贵金属Pt后催化剂的NH3-TPD谱图

    Figure  5  NH3-TPD profiles of the 1%Pt/CeO2-Al2O3 catalysts with different Ce/Al mol ratios

    a: 1.0; b: 0.5; c: 2.0

    图  6  负载1%贵金属Pt的催化剂SEM照片

    Figure  6  SEM images of 1%Pt/CeO2-Al2O3 catalysts with different Ce/Al mol ratios

    (a): 1.0; (b): 0.5; (c): 2.0

    图  7  负载1%贵金属Pt的催化剂TEM照片

    Figure  7  TEM images of 1%Pt/CeO2-Al2O3 catalysts with different Ce/Al mol ratios

    (a): 1.0; (b): 0.5; (c): 2.0

    图  8  负载1%贵金属Pt后的催化剂H2-TPR谱图

    Figure  8  H2-TPR profiles of 1%Pt/CeO2-Al2O3 catalysts with different Ce/Al mol ratios

    a: 1.0; b: 0.5; c: 2.0

    图  9  进料速率对MCH转化率的影响

    Figure  9  Effect of feed rate on the conversion of methylcyclohexane for the dehydrogenation of methylcyclohexane over the 1%Pt/CeO2-Al2O3 catalyst (1.0g, Ce/Al mol ratio=0.5) at atmospheric pressure and 450℃

    图  10  反应温度对MCH转化率和产物选择性的影响

    Figure  10  Effect of reaction temperature on the methylcyclohexane conversion and selectivity to toluene over the 1%Pt/CeO2-Al2O3 catalysts with different Ce/Al mol ratios

    (a): 1.0; (b): 0.5; (c): 2.0 (1-conversion of MCH; 2-selectivity to toluene; 3-selectivity to methylcyclohexene)

    图  11  催化剂的脱氢效率评价

    Figure  11  Dehydrogenation efficiency of the 1%Pt/CeO2-Al2O3 catalysts with different Ce/Al mol ratios

    a: 1.0; b: 0.5; c: 2.0

    表  1  不同Ce/Al物质的量比复合载体CeO2-Al2O3的孔结构性质

    Table  1  Textural properties of CeO2-Al2O3 composite supports with different Ce/Al mol ratios

    Ce/Al
    (mol ratio)
    Specific area
    A/(m2·g-1)
    Pore volume
    v/(mL·g-1)
    Pore diameter
    d/nm
    1.0100.00.4112.12
    0.5102.00.469.60
    2.047.00.199.59
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出版历程
  • 收稿日期:  2015-12-15
  • 修回日期:  2016-03-13
  • 网络出版日期:  2021-01-23
  • 刊出日期:  2016-06-10

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