Effects of coking on the transport properties of H-mordenite*1

作者: J BUTT

DOI: 10.1016/0021-9517(75)90145-1

关键词:

摘要: Abstract An experimental study of the relationships between coke content, catalyst activity, and intraparticle diffusivity is reported for cumene cracking on a commercial H-mordenite. Coking conditions were varied from 230 to 350 °C at space velocities 0.20 0.65 wt/hr/wt time stream up 6 hr. Effective diffusivities catalysts found decrease by over factor 2 during coking process are nonlinearly related level, independent temperature coking. Under strong diffusion limitation, this change in alters catalytic effectiveness proportion square root ratio, ( D eff 0 ) 1 .

参考文章(4)
Alexis Voorhies, Carbon Formation in Catalytic Cracking Industrial & Engineering Chemistry. ,vol. 37, pp. 318- 322 ,(1945) , 10.1021/IE50424A010
J. H. Ramser, P. B. Hill, Physical Structure of Silica-Alumina Catalysts Industrial & Engineering Chemistry. ,vol. 50, pp. 117- 124 ,(1958) , 10.1021/IE50577A048
C. H. Tan, O. M. Fuller, A model fouling reaction in a zeolite catalyst The Canadian Journal of Chemical Engineering. ,vol. 48, pp. 174- 178 ,(1970) , 10.1002/CJCE.5450480214
R. G. Haldeman, M. C. Botty, On the Nature of the Carbon Deposit of Cracking Catalysts The Journal of Physical Chemistry. ,vol. 63, pp. 489- 496 ,(1959) , 10.1021/J150574A010