Control structure selection for energy integrated distillation column

Journal of Process Control

Volumn 8, Issue 3, 1998, Pages 185-195

  Hansen, Jens Erik ^a   Jørgensen, Sten Bay ^a   Heath, Jonathan ^b   Perkins, John D ^b  

^a TECHNICAL UNIVERSITY OF DENMARK   (Denmark)

^b IMPERIAL COLLEGE LONDON   (United Kingdom)

Author keywords

Control structure selection; Distillation; Mixed integer linear programming (MILP)

Indexed keywords

ACTUATORS; BOILERS; COMPUTER SIMULATION; CONDENSERS (LIQUEFIERS); CONTROL SYSTEM SYNTHESIS; DISTILLATION COLUMNS; HEAT PUMP SYSTEMS; HIERARCHICAL SYSTEMS; LINEAR PROGRAMMING; MATHEMATICAL MODELS; SET THEORY; STATE SPACE METHODS;

CONDITION NUMBER; CONTROL STRUCTURE SELECTION; LINEAR STATE SPACE MODEL; MIXED INTEGER LINEAR PROGRAMMING; PRODUCT PURITY CONTROL; RELATIVE DISTURBANCE GAIN; RELATIVE GAIN ARRAY; VARIABLES;

PROCESS CONTROL;

EID: 0032099302     PISSN: 09591524     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0959-1524(97)00039-5     Document Type: Article

References (15)

1. Foss, A. S., Critique of chemical process control theory. American Institute of Chemical Engineers Journal, 1973, 19(2), 209.
2. Morari, M., Arkun, Y. and Stephanopoulos, G., Studies in the synthesis of control structure for chemical processes. American Institute of Chemical Engineers Journal, 1980, 26(2), 220.
3. Georgiou, A. and Floudas, C. A., Structural analysis and synthesis of feasible control systems: theory and applications. Chemical Engineering Research and Design, 1989, 67(11), 600-618.
4. Narrawya, L. T. and Perkins, J. D., Selection of process control structure based on linear dynamic economics. Industrial & Engineering Chemistry Research, 1993, 32(11), 2681-2692.
5. Skogestad, S. and Postlethwaite, I., Multivariable Feedback Control-Analysis and Design. John Wiley & Sons, New York, 1996.
6. Morari, M. and Zafiriou, E., Robust Process Control. Prentice-Hall, Englewood Cliffs, NJ, 1988.
7. Koggersbøl, A. and Jørgensen, S. B., Distillation column control benchmarks: four typical problems. In DYCORD'95, 4th Symposium on Dynamics and Control of Chemical Reactors, Distillation Column and Batch Processes, ed. J. B. Rawlings. Danish Automation Society, Copenhagen, June 1995, pp. 323-325.
8. Heath, J., Perkins, J. D. and Walsh, S., Control structure selection based on linear dynamic economics - multiloop PI structures for multiple disturbances. Technical report, Centre for Process Systems Engineering, Imperial College, London, 1996.
9. Koggersbøl, A., Distillation column dynamics, operability and control. P.h.D. thesis, Technical University of Denmark, 1995.
10. Bristol, J. G., On a new measure of interaction for multivariable process control. IEEE Transactions on Automatic Control, 1996, AC-11, 133-134.
11. Hovd, M. and Skogestad, S., Simple frequency-dependent tools for control system analysis, structure selection and design. Automatica, 1992, 28(5), 989-996.
12. Skogestad, S. and Morari, M., Implication of large RGA-elements on control performance. Industrial & Engineering Chemistry Research, 1987, 26, 2323-2330.
13. Stanley, G., Marion-Galarrage, M. and McAvoy, T. J., Shortcut operability analysis. I. The relative disturbance gain. Industrial & Engineering Chemistry Process Design and Development, 1985, 24, 1181-1188.
14. Koggersbøl, A., Andersen, B. R., Nielsen, J. S. and Jørgensen, S. B., Control configuration for an energy integrated distillation. Computers in Chemical Engineering, 1996, 20(B), S835.
15. Koggersbøl, A., Andersen, T. R., Bagterp, J. and Jørgensen, S. B., An output multiplicity in binary distillation: experimental verification. Computers in Chemical Engineering, 1996, 20(B), S253.