4.8 Article

Influence of gelation and calcination temperature on the structure-performance of porous VOX-SiO2 solids in non-oxidative propane dehydrogenation

期刊

JOURNAL OF CATALYSIS
卷 358, 期 -, 页码 108-117

出版社

ACADEMIC PRESS INC ELSEVIER SCIENCE
DOI: 10.1016/j.jcat.2017.12.004

关键词

Propane dehydrogenation; Vanadium oxide; Porous silica solid; Gelation temperature; Calcination temperature

资金

  1. Science and Technology Commission of Shanghai Municipality [14520502900]
  2. Ministry of Education of China [PCSIRT_IRT_16R49]
  3. International Joint Laboratory on Resource Chemistry (IJLRC)

向作者/读者索取更多资源

VOX-doped porous SiO2 solids (VOX-SiO2) were synthesized at different gelation and calcination temperatures through an in-situ one-step synthesis and evaluated by non-oxidative propane dehydrogenation (PDH), exhibiting excellent catalytic performance. VOX-SiO2 catalysts were characterized by XRD, low temperature N-2 adsorption/desorption, SEM, TEM, UV-Vis, Raman, XPS, NH3-TPD, H-2-TPR, and TGA. The structural and performance results for the catalysts reveal that gelation temperature has only a slight effect on the surface acidity, textural properties and VOX species dispersion of VOX-SiO2 catalysts within a reasonable temperature range (30-60 degrees C). The 60-VOX-SiO2-580 catalyst, with a gelation temperature of 60 degrees C, a calcination temperature of 580 degrees C, and prepared by the one-step synthesis method, obviously shortens gelation process time by half compared to catalyst gelled at 30 degrees C and exhibits superior catalytic performance for PDH. Over high gelation temperature (>= 75 degrees C) leads to the loss of integrity and decreases catalytic activity of the VOX-SiO2 catalysts. Compared with the VOX-MCM-41 catalyst prepared by a one-step hydrothermal method, VOX-SiO2 catalysts exhibit better catalytic activity and stability. Importantly, at a reaction temperature of 580 degrees C, the 60-VOX-SiO2-580 catalyst exhibits remarkable long-term catalytic stability in the eight reaction-regeneration cycles for PDH. Its propane conversion shows a slow decrease from 55% to 45% for a 4 h reaction duration, but the propene selectivity remains at approximately 91%. The results of this work will be beneficial for further industrial development and application of porous VOX-SiO2 solids in catalysis. (C) 2017 Elsevier Inc. All rights reserved.

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