Catalytic cracking, general reaction kinetics

We have shown that additive coke (Cat]j) has much less impact on catalyst activity than catalytic coke (Ccal) at the same coke-on-catalyst level, but the initial catalyst deactivation rate during ARO cracking is greaier than ihat of VGO cracking because of the fast deposition of additional coke on the caialyst surface. The general correlations developed in this paper can be conveniently u sod in the modeling of catalytic cracking reaction kinetics. 

Unfortunately the transient carbonium ions presumably formed in catalytic cracking cannot be easily observed. Furthermore, there remain many questions about degrees of adsorption bonding involved with these intermediates, as well as need of information about structures and possible alternative reaction paths. In general, however, this lack of exact knowledge is characteristic of almost all reaction kinetics, catalytic or otherwise. 

The kinetic expressions derived by Antipina and Frost have general applicability to monomolecular heterogeneous catalytic reactions which occur on a uniform surface. The expression can be made to describe the cracking of synthin or decomposition of octene over silica-alumina as well as hydrogen disproportionation of gasoline and cracking of gas oils over the silica-alumina. Numerous other applications are discussed. 

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