Abstract
Novel VOx/SrO-γAl2O3 catalysts have been investigated in oxidative cracking of n-hexane to light olefins. The supports, with different SrO/γAl2O3 ratios, were synthesized by a surfactant-free method, while VOx was incorporated on SrO-γAl2O3 by impregnation. NH3-TPD showed that the acidity of the catalysts decreased with the increase of SrO. The incorporation of SrO also modified the reducibility (H2-TPR) of the catalysts. VOx appeared as amorphous polymeric species on the support, confirmed by XRD, Raman and FTIR analyses. The oxidative cracking of n-hexane was conducted by using a fluidized CREC Riser Simulator in absence of gas phase oxygen. Under the studied reaction conditions (525−600 °C; 10−25 s), the products contained mainly light olefins (ethylene, propylene and butenes), paraffins, and carbon oxides. Among the synthesized catalysts, VOx/SrO-γAl2O3 1:1 showed highest olefins selectivity (88%) at high n-hexane conversion (84%) because of its balanced acidity and moderate VOx-support interactions.
Original language | English |
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Pages (from-to) | 339-350 |
Number of pages | 12 |
Journal | Journal of Industrial and Engineering Chemistry |
Volume | 89 |
DOIs | |
State | Published - 25 Sep 2020 |
Bibliographical note
Publisher Copyright:© 2020 The Korean Society of Industrial and Engineering Chemistry
Keywords
- Catalytic oxidative cracking
- Fluidizable catalyst
- Light olefins
- VO catalysts
- n-Hexane
ASJC Scopus subject areas
- General Chemical Engineering