Simulation and model predictive control of a UOP fluid catalytic cracking unit
Tài liệu tham khảo
Avidan, 1990, Development of catalytic cracking technology. A lesson in chemical reactor design, Ind. Eng. Chem. Res., 29, 931, 10.1021/ie00102a001
Advanced Process Control Handbook VII, Hydrocarbon Processing, 1992, May, pp. 122–126.
Arbel, 1995, Dynamics and control of fluidized catalytic crackers. 1. Modeling of the current generation of FCCUs, Ind. Eng. Chem. Res., 34, 1228, 10.1021/ie00043a027
A. Arbel, Z. Huang. I. Rinard, R. Shinnar, Partial Control of FCC Units: Input Multiplicities and Control Structures, AIChE Annual Meeting, 1993, St. Louis, MO.
McFarlane, 1993, Dynamic simulator for a model IV fluid catalytic cracking unit, Computers Chem. Eng., 17, 275, 10.1016/0098-1354(93)80021-E
Emad, 1997, Nonlinear model predictive control of industrial type IV fluid catalytic cracking units for maximum gasoline yield, Ind. Chem. Eng. Res., 36, 389, 10.1021/ie9603575
Karla, 1994, Effect of process nonlinearity on performance of linear model predictive controllers for environmentally safe operation of a fluid catalytic cracking unit, Ind. Eng. Chem. Res., 33, 3063, 10.1021/ie00036a022
Cristea, 1997, Dynamic simulator for a UOP model fluid catalytic cracking unit, Studia Universitatis “Babeş-Bolyai”, Ser. Chemia, 42, 97
Weekman, 1970, Kinetics of catalytic cracking selectivity in fixed, moving, and fluid bed reactors, AIChE J., 16, 397, 10.1002/aic.690160316
Jacob, 1976, A lumping and reaction scheme for catalytic cracking, AIChE J., 22, 701, 10.1002/aic.690220412
H. Rhemann, G. Schwartz, T. Badgwell, M. Darby, D. White, On-line FCCU advanced control and optimization, Hydrocarbon Processing, 1989, June.
G. McDonald, B. Harkins, Maximizing Profits by Process Optimization, in: NPRA Annual Meeting, 1987, March 29–31, San Antonio, Texas.
M. Hovd, S. Skogestad, Controllability analysis for the fluid catalytic cracking process, in: AIChE Annual Meeting, 1991, November 17–22, Los Angeles.
M. Morari, I. Huq, S.P. Agachi, J. Bomberger, B. Donno, A. Zengh, Modeling and control studies on model IV FCCUs, Joint Research between Chevron Research and Technology Company and California Institute of Technology, 1993.
Yang, 1996, A multivariable coordinated control system based on predictive control strategy for FCC reactor–regenerator system, Chem. Eng. Sci., 51, 2977, 10.1016/0009-2509(96)00184-4
M.V. Cristea, V. Marinoiu, S.P. Agachi, Multivariable model based predictive control of a UOP fluid catalytic cracking unit, in: 2nd Conference on Process Integration, Modeling and Optimization for Energy Saving and Pollution Reduction, 1999, 31 May–2 June, Budapest, pp. 223–228.
M.V. Cristea, S.P. Agachi, Controllability analysis of a model IV FCCU, in: 12th International Congress of Chemical and Process Engineering CHISA, 1996, Prague, p. 10.
Garcia, 1989, Model predictive control: theory and practice—a survey, Automatica, 25, 335, 10.1016/0005-1098(89)90002-2
Semino, 1994, A method for robust tuning of linear quadratic optimal controllers, Ind. Eng. Chem. Res., 33, 889, 10.1021/ie00028a015
H. Chen, F. Allgower, Nonlinear model predictive control schemes with guaranteed stability, NATO Advanced Study Institute on Nonlinear Model Based Process Control, 1997, 10–20 August, Antalya, Turkey, pp. 1–28.
Lee, 1994, Tuning of model predictive controllers for robust performance, Comp. Chem. Eng., 18, 15, 10.1016/0098-1354(94)85020-8
K.J. Astrom, T. Hägglund, Automatic Tuning of PID Controllers, Instrument Society of America, 1988.
Patwardhan, 1990, Nonlinear model predictive control, Chem. Eng. Comm., 87, 123, 10.1080/00986449008940687
Richalet, 1993, Industrial applications of model based predictive control, Automatica, 29, 1251, 10.1016/0005-1098(93)90049-Y
Lee, 1985, Mathematical model of the fluidized bed catalytic cracking plant, Trans. Soc. Comp. Simulation, 3, 219
Shah, 1977, A kinematic model for an adiabatic transfer line catalytic cracking reactor, Ind. Eng. Chem., Process Des. Dev., 16, 89, 10.1021/i260061a015