Model predictive controller design with process constraints and implicit economic criteria

Conference Record - IEEE Instrumentation and Measurement Technology Conference

Volumn 1, Issue , 1997, Pages 559-563

  Patry, Jasmin F ^a   Marlin, Thomas E ^b  

^a MCMASTER UNIVERSITY   (Canada)

^b Hydromantis Inc   (Canada)

Author keywords

[No Author keywords available]

Indexed keywords

BLENDING; CONTROLLERS; PROFITABILITY; THREE TERM CONTROL SYSTEMS; TRANSIENTS; OPTIMIZATION; PROCESS CONTROL;

ADJUSTABLE PARAMETERS; CONTROLLED VARIABLES; ECONOMIC PERFORMANCE; MODEL PREDICTIVE CONTROLLERS; MULTI-LOOP PID CONTROLLER; OBJECTIVE FUNCTIONS; PROCESS CONSTRAINTS; STEADY STATE PERFORMANCE;

PROCESS CONTROL; PREDICTIVE CONTROL SYSTEMS;

GASOLINE BLENDING PROCESS; QUADRATIC/DYNAMIC MATRIX CONTROL (QDMC) CONTROLLER;

EID: 0030715435     PISSN: 10915281     EISSN: None     Source Type: Conference Proceeding    
DOI: 10.1109/IMTC.1997.604013     Document Type: Conference Paper

References (7)

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2. CE. Garcia and A.M. Morshedi, "Quadratic programming solution of Dynamic Matrix Control (QDMC)," Chem. Eng. Commun., vol. 46, pp. 73-87, 1986.
3. A. Kassidas, Model Predictive Controller Design with Implicit Economic Criteria, Master's Thesis, McMaster University, Hamilton, 1993.
4. P.A. Clark and A.W. Westerberg, "Bilevel programming for steady-state chemical process design-I. Fundamentals and algorithms," Computers chem. Engng, Vol. 14, No. 1, pp 87-97, 1990.
5. T. Edgar and D. Himmelblau, Optimization of Chemical Processes, Wiley, New York, 1988.
6. J. Patry, Real-time optimization of plant operations, Undergraduate Thesis, McMaster University, Hamilton, 1996.
7. M. Young and T. Marlin, "Integrating the effects of process controllers with steady-state, equation-based simulation," Chem. Eng. Commun., in press.