Cracking of ethylene over coal char or quartz
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Abstract
The cracking of ethylene as one of the major components of oil refinery over a bed of Binxian char and quartz, respectively, has been studied in a fixed bed reactor at temperatures between 850℃ and 1000℃ and atmospheric pressure. The results show that the conversions of ethylene increases with increasing temperature. The products of ethylene cracking are H2, CH4, C2H6 and C. The higher the reaction temperature, the more complete ethylene cracking and the more H2 produced. The higher initial conversion rate of ethylene cracking at 850℃ to 950℃ is only observed over Binxian char but not on quartz and an empty reactor. This indicates a significant catalytic effect of Binxian char on ethylene cracking. Ethylene conversion decreases with reaction time due to carbon deposition on the char surface. The conversion of ethylene is 94% over quartz and in the empty reactor at 1000℃, suggesting that ethylene can completely decompose through thermal cracking without catalyst.
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