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• W1996935791 abstract "A new kinetic model for the fluid catalytic cracking (FCC) riser is developed. An elementary reaction scheme, for the FCC, based on cracking of a large number of lumps in the form of narrow boiling pseudocomponents is proposed. The kinetic parameters are estimated using a semi-empirical approach based on normal probability distribution. The correlation proposed for the kinetic parameters’ estimation contains four parameters that depend on the feed characteristics, catalyst activity, and coke forming tendency of the feed. This approach eliminates the need of determining a large number of rate constants required for conventional lumped models. The model seems to be more versatile than existing models and opens up a new dimension for making generic models suitable for the analysis and control studies of FCC units. The model also incorporates catalyst deactivation and two-phase flow in the riser reactor. Predictions of the model compare well with the yield pattern of industrial scale plant data reported in literature." @default.
• W1996935791 created "2016-06-24" @default.
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• W1996935791 date "2007-09-01" @default.
• W1996935791 modified "2023-09-30" @default.
• W1996935791 title "A new generic approach for the modeling of fluid catalytic cracking (FCC) riser reactor" @default.
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• W1996935791 doi "https://doi.org/10.1016/j.ces.2007.05.009" @default.
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