Steady state disturbance propagation modelling of heat integrated distillation processes

Chemical Engineering Research and Design

Volumn 78, Issue 2, 2000, Pages 245-254

  Yang, Y H ^a   Lou, H H ^a   Huang, Y L ^a  

^a Wayne State University   (United States)

Author keywords

Distillation column; Disturbance propagation models; Heat integration; Process analysis; Process design

Indexed keywords

CONTROLLABILITY; DISTILLATION COLUMNS; MATHEMATICAL MODELS; MATRIX ALGEBRA; PROCESS CONTROL; PROCESS ENGINEERING;

DISTURBANCE PROPAGATION MODELS;

DISTILLATION;

DISTILLATION COLUMN; HEAT; INTEGRATION;

EID: 0034016701     PISSN: 02638762     EISSN: None     Source Type: Journal    
DOI: 10.1205/026387600527112     Document Type: Article

References (29)

1. Linnhoff, B., Townsend, D. W., Boland, D., Hewitt, G. F., Thomas, B. E. A., Guy, A. R. and Marsland, R. H., 1982, User Guide on Process Integration for the Efficient Use of Energy, (IChemE, UK).
2. Ho, F. G. and Keller II, G. E., 1987, Process integration, in Recent Developments in Chemical Process and Plant Design; Liu, Y. A., McGee, Jr., H. A., Epperly, W. R., Eds.; Chapter 4, (John Wiley & Sons, New York).
3. Gross, F., Baumann, E., Gesser, A., Rippin, D. W. T. and Lang, L., 1994, Modeling, simulation, and controllability analysis of a heat-integrated industrial distillation system, Proc IFAC Workshop on Integration of Process Design and Control, Baltimore, MD, June 27-28, pp 70-75.
4. Barton, G. W., Padley, M. A. and Perkins, J. D., 1992, Incorporating operability measures into the process synthesis stage of design, Proc IFAC Workshop on Integration of Process Design and Control, London.
5. Morari, M., 1982, Flexibility and resiliency of process systems, Proc Int Symp Process Systems Engineering, Kyoto, Japan, August 23-27, pp. 223-237.
6. Grossmann, I. E., Halemane, K. P. and Swaney, R. E., 1983, Optimization strategies for flexible chemical processes, Comp Chem Eng, 7: 439-462.
7. McAvoy, T. J., 1987, Integration of process design and process control, in Recent Developments in Chemical Process and Plant Design; Liu, Y. A., McGee, Jr., H. A., Epperly W. R., Ed.; Chapter 8, (John Wiley & Sons, New York).
8. Fisher, W. R., Doherty, M. F. and Douglas, J. M., 1988, The interface between design and control. 1. Process controllability, Ind Eng Chem Res, 27: 597-605.
9. Fisher, W. R., Doherty, M. F. and Douglas, J. M., 1988, The interface between design and control 2. Process operability, Ind Eng Chem Res, 27: 606-611.
10. Fisher, W. R., Doherty, M. F. and Douglas, J. M., 1988, The interface between design and control 3. Selecting a set of controlled variables, Ind Eng Chem Res, 27: 612-615.
11. Huang, Y. L. and Fan, L. T., 1992, Distributed strategy for integration of process design and control: A knowledge engineering approach to the incorporation of controllability into exchanger network synthesis, Comp Chem Eng, 32: 497-522.
12. Huang, Y. L. and Fan, L. T., 1994, HIDDEN: A hybrid intelligent system for synthesizing a highly controllable exchanger networks: Implementation of distributed strategy for integrating process design and control, Ind Eng Chem Res, 33: 1174-1181.
13. Huang, Y. L. and Fan, L. T., 1996, Analysis of work exchanger networks, Ind Eng Chem Res, 35: 3528-3538.
14. Luyben, M. L. and Floudas, C. A., 1994, Analyzing the integration of design and control - 1. A multiobjective framework and application to binary distillation synthesis, Comp Chem Eng, 18: 893-969.
15. Luyben, M. L. and Floudas, C. A., 1994, Analyzing the integration of design and control - 2. Reactor-separator-recycle system, Comp Chem Eng, 18: 971-994.
16. Bagajewicz, M. J. and Manousiouthakis, V., 1992, Mass/heat-exchange network representation of distillation networks, AIChE J, 38: 1769-1800.
17. Hoch, P. M., Eliceche, A. M. and Grossmann, I. E., 1995, Evaluation of design flexibility in distillation-column using rigorous models, Comp Chem Eng, 19: S669-S674.
18. Henry, M. and Mujtaba, I., 1997, Controlling distillation, The Chemical Engineer, 645: 32-36.
19. Elliott, T. R. and Luyben, W. L., 1995, A capacity-based economic approach for the quantitative assessment of process controllability during the conceptual design phase, Ind Eng Chem Res, 34: 3907-3915.
20. Haggblom, K. E. and Waller, K. V., 1990, Control structures for disturbance rejection and decoupling of distillation, AIChE J, 36: 1107-1113.
21. Koggersbol, A., Andersen, B. R., Nielsen, J. S. and Jorgensen, S. B., 1996, Control configurations for an energy integrated distillation, Comp Chem Eng, 20: S853-S858.
22. Yang, Y. H., Gong, J. P. and Huang, Y. L., 1996, A simplified system model for rapid evaluation of disturbance propagation through a heat exchanger network, Ind Eng Chem Res, 35: 4550-4558.
23. Yang, Y. H., Yan, Q. Z. and Huang, Y. L., 1999, A unified model for the prediction of structural disturbance propagation in mass exchange networks, Trans IChemE, Part A, 77(5): 253-266.
24. McCabe, W. L., Smith, J. C. and Harriott, P., 1993, Unit Operations of Chemical Engineering, 5th ed.; (McGraw-Hill, New York).
25. Seader, J. D. and Henley, E. J., 1998, Separation Process Principles, (John Wiley & Sons, New York).
26. King, C. J., 1980, Separation Processes; 2nd ed., (McGraw-Hill, New York).
27. Smith, J. M. and Van Ness, H. C., 1987, Introduction to Chemical Engineering Thermodynamics, 4th ed., Chapter 13, (McGraw-Hill, New York).
28. Huang, Y. L. and Edgar, T. F., 1995, Knowledge-based design approach for the simultaneous minimization of waste generation and energy consumption in a petroleum refinery. In Waste Minimization through Process Design; Rossiter, A. P., Ed.; Chapter 14, (McGraw-Hill, New York).
29. Luyben, M. L., 1993, Analyzing the interaction between process design and process control, PhD Diss (Princeton University, NJ).