期刊
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
卷 61, 期 16, 页码 5429-5441出版社
AMER CHEMICAL SOC
DOI: 10.1021/acs.iecr.2c00045
关键词
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资金
- National Natural Science Foundation of China [92034302, 21822810, 22021004]
- National Key Research and Development Program of China [2020YFA0210900]
- National Supercomputer Center in Tianjin
This study investigates the mechanism and microkinetics of 1-butene catalytic cracking. The optimal paths for 1-butene isomerization and dimerization-cracking are clarified, and a new aromatization mechanism is proposed. Additionally, the effect of reaction temperature variation on product distribution is clarified, with increasing temperature having negative effects on the reaction rate.
In this study, the mechanism and microkinetics of 1-butenecatalytic cracking were investigated. Based on the calculation results of thefull reaction, the optimal paths for 1-butene isomerization anddimerization-cracking were clarified, and a new aromatization mechanismis proposed. In addition, the effect of reaction temperature variation onthe product distribution was clarified. Limited by the amount of 1-buteneadsorbed, increasing the temperature will gradually change the rate-determining step of the system and have negative effects on the reactionrate. In the temperature range suitable for the production of ethylene andpropylene, this effect becomes very significant. Therefore, appropriatelyincreasing the number of Bronsted acid sites in the catalyst to ensure highadsorption amount of 1-butene at high temperatures is an effective way toimprove the production of ethylene and propylene in catalytic cracking ofbutene
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