Adsorption, diffusion, and reaction phenomena on FCC catalysts in the CREC riser simulator

被引:16
作者
Atias, JA [1 ]
de Lasa, H [1 ]
机构
[1] Univ Western Ontario, Fac Engn, Chem Reactor Engn Ctr, London, ON N6A 5B9, Canada
关键词
D O I
10.1021/ie034197q
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Two typical FCC catalysts with similar acidities and structural properties and different crystallite sizes, CAT-SC (0.4 mum) and CAT-LC (0.9 mum), are studied in a novel CREC riser simulator using 1,3,5-triisopropylbenzene. Catalytic and thermal runs allow for the development of a heterogeneous kinetic model and the assessment of intrinsic kinetic constants and adsorption and diffusional parameters. Analysis of 1,3,5-triisopropylbenzene conversions and product distribution helps establish the influence of intracrystallite diffusion as the controlling step at lower reaction temperatures (350-450 degreesC). Moreover, product distribution and selectivity differences between the CAT-SC and CAT-LC catalysts provide evidence of cracking reactions affected by hindered diffusion of the reactant and products.
引用
收藏
页码:4709 / 4720
页数:12
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