Development of a bench-scale fluid catalytic cracking microriser

被引:0
作者
Helmsing, MP
Makkee, M
Moulijn, JA
机构
来源
DEACTIVATION AND TESTING OF HYDROCARBON-PROCESSING CATALYSTS | 1996年 / 634卷
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中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Catalyst performance testing procedures for fluid cracking catalysts have been evaluated. A benchscale microriser is described and results are compared with those of a so-called microsimulation test. The two tests result in significant differences in light cycle oil, gasoline and LPG yield. The microriser experiments yielded a higher LPG olefinicity. This is explained by the dilution of the feed with the nitrogen carrier gas, which decreases the amount of bi-molecular hydrogen transfer reactions. Experiments at a very short contact time of 0.7 seconds were carried out. It is striking that the coke yield does not differ significantly from that in experiments performed at a much greater contact time of 5 seconds. This indicates that the majority all the coke formed during reaction is already deposited in the first few tenths of a second.
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页码:322 / 339
页数:18
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