Optimal Design of Dynamic Systems under Uncertainty

AIChE Journal

Volumn 42, Issue 8, 1996, Pages 2251-2272

  Mohideen, M Jezri ^a   Perkins, John D ^a   Pistikopoulos, Efstratios N ^a  

^a IMPERIAL COLLEGE LONDON   (United Kingdom)

Author keywords

[No Author keywords available]

Indexed keywords

ALGORITHMS; CONSTRAINT THEORY; DISTILLATION; ECONOMICS; ITERATIVE METHODS; MATHEMATICAL MODELS; MIXING; OPTIMAL CONTROL SYSTEMS; PROBLEM SOLVING; PROCESS CONTROL; RANDOM PROCESSES; TIME VARYING CONTROL SYSTEMS;

DYNAMIC SYSTEMS; END POINT CONSTRAINTS; INTERIOR CONSTRAINTS; ITERATIVE DECOMPOSITION ALGORITHM; MIXING TANK; PARAMETRIC UNCERTAINTY; PATH CONSTRAINTS; PROCESS DISTURBANCES; TERNARY DISTILLATION;

SYSTEMS ANALYSIS;

EID: 0030213541     PISSN: 00011541     EISSN: None     Source Type: Journal    
DOI: 10.1002/aic.690420814     Document Type: Article

References (30)

1. Brooke, A., D. Kendrick, and M. Meeraus, GAMS: A User's Guide, Scientific Press, Redwood City, CA (1988).
2. Bahri, P. A., J. A. Bandoni, and J. A. Romagnoli, "Effect of Disturbances in Optimizing Control: Steady-State Open-Loop Back-Off Calculation," AIChE J., 42(4), 983 (1996).
3. Ciric, A. R., and D. Gu, "Synthesis of Nonequilibrium Reactive Distillation Processes by MINLP Optimization, AIChE J., 40(9), 1479 (1994).
4. Cuthrell, J. E., and L. T. Biegler, "Strategies for Simultaneous Solution and Optimization of Differential-Algebraic Systems," AIChE J., 33(8), 1257 (1987).
5. Dimitriadis, V. D., and E. N. Pistikopoulos, "Feasibility and Flexibility Analysis of Dynamic Systems," Ind. Eng. Chem. Res., 34, 4451 (1995).
6. Douglas, J. M., Conceptual Design of Chemical Processes, McGraw-Hill, New York (1988).
7. Geoffrion, A. M., "Generalized Benders Decomposition," JOTA, 10, 237 (1972).
8. Grossmann, I. E., and D. A. Straub, "Recent Development in the Evaluation and Optimization of Flexible Chemical Processes," Computer-Oriented Proc. Eng., L. Puigjaner and A. Espuña, eds., Elsevier, Amsterdam, p. 49 (1991).
9. Grossmann, I. E., and C. A. Floudas, "Active Constraint Strategy for Flexibility Analysis in Chemical Processes," Comput. Chem. Eng., 11, 675 (1987).
10. Grossmann, I. E., and M. Morari, "Operability, Resilience and Flexibility: Process Design Objectives for a Changing World," Proc. FOCAPD, Snowmass, CO, p. 931 (1983).
11. Grossmann, I. E., and K. P. Halemane, "Decomposition Strategies for Designing Flexible Chemical Plants," AIChE J., 28(4), 686 (1982).
12. Grossmann, I. E., and R. W. H. Sargent, "Optimum Design of Chemical Plants with Uncertain Parameters," AIChE J., 24, 1021 (1978).
13. Gustafson, S. A., "A Three-Phase Algorithm for Semi-Infinite Programs," Lecture Notes in Economics and Mathematical Systems: Semi-Infinite Programming and Applications, A. V. Fiacco and K. O. Kortanek, eds., Springer-Verlag, Berlin, p. 138 (1981).
14. Heath, J. A., and J. D. Perkins, "Control Structure Selection Based on Economics., IChemE Research Event 1994," IChemE Proc., Rugby, U.K., p. 841 (1994).
15. Luyben, M. L., and C. A. Floudas, "Analyzing the Interaction of Design and Control: 1. A Multiobjective Framework and Application to Binary Distillation in Synthesis," Comput. Chem. Eng., 18, 33 (1994a).
16. Luyben, M. L., and C. A. Floudas, "Analyzing the Interacting of Design and Control: 2. Reaction-Separator-Recycle System," Comput. Chem. Eng., 18, 971 (1994b).
17. Madsen, K., and H. Schjaer-Jacobsen, "Linearly Constrained Minimax Optimization," Math. Prog., 14, 208 (1978).
18. Morari, M., and J. D. Perkins, "Design for Operations," Proc. FOCAPD-94, Snowmass, CO (1994).
19. Narraway, L. T., and J. D. Perkins, "Selection of Process Control Structure Based on Economics," Comp. Chem. Eng., 18, S511 (1993a).
20. Narraway, L. T., and J. D. Perkins, "Selection of Process Control Structure Based on Linear Dynamic Economics," Ind. Eng. Chem. Res., 32, 2681 (1993b).
21. Papalexandri, K. P., and E. N. Pistikopoulos, "Synthesis and Retrofit Design of Operable Heat Exchanger Networks: 1. Flexibility and Structural Controllability Aspects," Ind. Eng. Chem. Res., 33, 1718 (1994a).
22. Papalexandri, K. P., and E. N. Pistikopoulos, "Synthesis and Retrofit Design of Operable Heat Exchanger Networks: II. Dynamics and Control Structure Considerations," Ind. Eng. Chem. Res., 33, 1738 (1994b).
23. Paules, G. E. IV, and C. A. Floudas, "APROS: Algorithmic Development Methodology for Discrete-Continuous Optimization Problems," Oper Res., 37(6), 902 (1989).
24. Perkins, J. D., and S. P. K. Walsh, "Optimization as a Tool for Design/ Control Integration," Proc. IFAC Workshop on Integration of Process Design and Control, E. Zafiriou, ed., Pergamon, Oxford, p. 1 (1994).
25. Pistikopoulos, E. N., "Uncertainty in Process Design and Operation," Comp. Chem. Eng., 18, S553 (1995).
26. Sounders, M., and G. G. Brown, "Design of Fractionating Columns Entrainment and Capacity," Ind. Eng. Chem., 26, 98 (1934).
27. Tanarkit, P., and L. T. Biegler, "Boundary Value Approach for Dynamic Optimization," EDRC 06-170-94 Tech. Rep., Carnegie Mellon Univ., Pittsburgh (1993).
28. Varvarezos, D. K., I. E. Grossmann, and L. T. Biegler, "Multiperiod Design Optimization with SQP Decomposition," Comput. Chem. Eng., 18(7), 579 (1994).
29. Walsh, S. P. K., and J. D. Perkins, "Integrated Process and Control System Design to Waste Water Neutralization," Comp. Chem. Eng., 18, S183 (1994).
30. Zangwill, W. I., Nonlinear Programming: A Unified Approach, Prentice-Hall, Englewood Cliffs, N.J. (1969).