Asian Journal of Information Technology

Year: 2016
Volume: 15
Issue: 17
Page No. 3356 - 3365

Comparison of Decoupler with PID Controller and Model Predictive Controller for the Fluid Catalytic Cracking Unit in Petroleum Refinery

Authors : P. Elamurugan and K. Siva

References

Ahari, J.S., A. Farshi and K. Forsat, 2008. A mathematical modeling of the riser reactor in industrial FCC unit. Petrol. Coal, 50: 15-24.

Han, I.S., C.B. Chung and J.B. Riggs, 2000. Modeling of a fluidized catalytic cracking process. Comput. Chem. Eng., 24: 1681-1687.
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Lee, E. and F.R. Groves, 1985. Mathematical model of the fluidized bed catalytic cracking plant. Trans. Soc. Comp. Sim, 2: 219-236.
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Roman, R., Z.K. Nagy, M.V. Cristea and S.P. Agachi, 2009. Dynamic modelling and nonlinear model predictive control of a fluid catalytic cracking unit. Comput. Chem. Eng., 33: 605-617.
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