SCI和EI收录∣中国化工学会会刊

中国化学工程学报 ›› 2020, Vol. 28 ›› Issue (12): 3035-3043.DOI: 10.1016/j.cjche.2020.04.022

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

The effect of the Ce content on the oxidative dehydrogenation of propane over CrOy-CeO2/γ-Al2O3 catalysts

Cheng Zuo1, Man Wu1, Qingjie Guo1,2   

  1. 1 Key Laboratory of Clean Chemical Processing of Shandong Province, College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao 266042, China;
    2 State Key Laboratory of High-efficiency Coal Utilization and Green Chemical Engineering, College of Chemistry and Chemical Engineering, Ningxia University, Yinchuan 750021, China
  • 收稿日期:2020-01-28 修回日期:2020-04-17 出版日期:2020-12-28 发布日期:2021-01-11
  • 通讯作者: Qingjie Guo
  • 基金资助:
    The authors gratefully acknowledge the support from the National Key Research and Development Program (2018YFB0605401), Key Research and Development Program of the Ningxia Hui Autonomous Region (2018BCE01002), and National Natural Science Foundation of China (21868025).

The effect of the Ce content on the oxidative dehydrogenation of propane over CrOy-CeO2/γ-Al2O3 catalysts

Cheng Zuo1, Man Wu1, Qingjie Guo1,2   

  1. 1 Key Laboratory of Clean Chemical Processing of Shandong Province, College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao 266042, China;
    2 State Key Laboratory of High-efficiency Coal Utilization and Green Chemical Engineering, College of Chemistry and Chemical Engineering, Ningxia University, Yinchuan 750021, China
  • Received:2020-01-28 Revised:2020-04-17 Online:2020-12-28 Published:2021-01-11
  • Contact: Qingjie Guo
  • Supported by:
    The authors gratefully acknowledge the support from the National Key Research and Development Program (2018YFB0605401), Key Research and Development Program of the Ningxia Hui Autonomous Region (2018BCE01002), and National Natural Science Foundation of China (21868025).

摘要: A series of CrOy (17.5 wt%)-CeO2 (X wt%)/γ-Al2O3 catalysts (X=0, 0.5, 2, 5, 8) with various Ce contents were prepared by a wetness impregnation method and were applied to the dehydrogenation of propane to propylene at 550℃ and 0.1 MPa. The prepared catalysts were characterized by BET, H2-TPR, O2-TPD, XPS, XRD, SEM-EDS and Raman spectroscopy. Among the prepared catalysts, the 17.5Cr-2Ce/Al catalyst with the largest amount of lattice oxygen exhibited the best catalytic performance for the dehydrogenation of propane to propylene with lattice oxygen. The decreased presence of oxygen defects and reducibility were the factors responsible for the improved dehydrogenation activity of the catalysts. The CeO2 layer could inhibit the evolution of lattice oxygen (O2-) to electrophilic oxygen species (O2-), and the oxygen defects on the catalyst surface were reduced. The inhibited lattice oxygen evolution prevented the deep oxidation of propane or propylene, the average COx selectivity decreased from 24.41% (17.5Cr/Al) to 5.71% (17.5Cr-2Ce/Al), and the average propylene selectivity increased from 60.15% (17.5Cr/Al) to 85.05% (17.5Cr-2Ce/Al).

关键词: Oxidation, Selectivity, Propane, Propylene, Fluidized-bed, Oxygen carrier

Abstract: A series of CrOy (17.5 wt%)-CeO2 (X wt%)/γ-Al2O3 catalysts (X=0, 0.5, 2, 5, 8) with various Ce contents were prepared by a wetness impregnation method and were applied to the dehydrogenation of propane to propylene at 550℃ and 0.1 MPa. The prepared catalysts were characterized by BET, H2-TPR, O2-TPD, XPS, XRD, SEM-EDS and Raman spectroscopy. Among the prepared catalysts, the 17.5Cr-2Ce/Al catalyst with the largest amount of lattice oxygen exhibited the best catalytic performance for the dehydrogenation of propane to propylene with lattice oxygen. The decreased presence of oxygen defects and reducibility were the factors responsible for the improved dehydrogenation activity of the catalysts. The CeO2 layer could inhibit the evolution of lattice oxygen (O2-) to electrophilic oxygen species (O2-), and the oxygen defects on the catalyst surface were reduced. The inhibited lattice oxygen evolution prevented the deep oxidation of propane or propylene, the average COx selectivity decreased from 24.41% (17.5Cr/Al) to 5.71% (17.5Cr-2Ce/Al), and the average propylene selectivity increased from 60.15% (17.5Cr/Al) to 85.05% (17.5Cr-2Ce/Al).

Key words: Oxidation, Selectivity, Propane, Propylene, Fluidized-bed, Oxygen carrier