Synthesis of two-point linear controllers for binary distillation columns

Chemical Engineering Communications

Volumn 193, Issue 2, 2006, Pages 206-232

  Castellanos Sahagún, Eduardo ^a   Alvarez, Jesús ^a  

^a DEPARTAMENTO DE QUÍMICA   (Mexico)

Author keywords

Distillation columns; Linear control; Observer based control; Stability assessment

Indexed keywords

CLOSED LOOP CONTROL SYSTEMS; COMPUTER SIMULATION; CONTROL SYSTEM SYNTHESIS; LINEAR CONTROL SYSTEMS; OBSERVABILITY; PROCESS CONTROL; SYSTEM STABILITY;

BINARY DISTILLATION COLUMNS; OBSERVER BASED CONTROL; STABILITY ASSESSMENT;

DISTILLATION COLUMNS;

CLOSED LOOP CONTROL SYSTEMS; COMPUTER SIMULATION; CONTROL SYSTEM SYNTHESIS; DISTILLATION COLUMNS; LINEAR CONTROL SYSTEMS; OBSERVABILITY; PROCESS CONTROL; SYSTEM STABILITY;

EID: 31544447503     PISSN: 00986445     EISSN: 15635201     Source Type: Journal    
DOI: 10.1080/009864490949071     Document Type: Article

References (39)

1. Alvarez-Ramírez, J., Alvarez, J., and Morales, A. (2002). Int. J. Adapt. Control Signal Process, 16, 681-701.
2. Balasubramhanya, L. A. and Doyle III, F. J. (1997). AIChE J., 43(3), 703-714. [CROSSREF]
3. Betlem, B. H. L., Rijnsdorp, J. E., and Azink, R. F. (1998). Chem. Eng. Sci., 53(23), 3991-4003. [CROSSREF]
4. Bloemen, H. H. J., Chou, C. T., van den Boom, T. J. J., Verdult, V., Verhaegen, M., and Backx, T. C. (2001). J. Process Control, 11, 601-620. [CROSSREF]
5. Castellanos-Sahagún, E. (2005). Multivariable control design for binary distillation columns. Ph.D. diss., U. Autónoma Metropolitana, Mexico. [in Spanish].
6. Castellanos-Sahagún, E. and Alvarez, J. (Submitted). An adaptive cascade multivariable control for a class of binary distillation columns, Int. J. Adaptive Control Signal Process.
7. Castellanos-Sahagún, E., Alvarez-Ramírez, J., and Alvarez, J. (2005). Two-point temperature control structure and algorithm design for binary distillation columns, Ind. Eng. Chem. Res., 44(1), 142-152. [CROSSREF]
8. Castro, R., Alvarez, J., and Alvarez, J. (1990). Automatica, 26(3), 567-572. [CROSSREF]
9. D'azzo, J. J. and Houpis, C. H. (1981). Linear Control Systems, Analysis and Design, McGraw-Hill, New York.
10. Doherty, M. F. and Perkins, J. D. (1982). Chem. Eng. Sci., 37(4), 381-392. [CROSSREF]
11. Fagervik, K. C., Waller, K. V., and Hammarström, L. (1983). Chem. Eng. Commun., 21, 235-249.
12. Fruehauf, P. S. and Mahoney, D. P. (1994). Chem. Eng. Prog., 90(3), 75-83.
13. Gjøsæter, O. B. and Foss, B. A. (1997). Automatica, 33, 427-432. [CROSSREF]
14. Hirschorn, R. M. (1979). IEEE Trans. Automat. Contr., 24(6), 855.[CROSSREF]
15. Humphrey, J. L., Seibert, A. F., and Koort, R. A. (1991). Separation Technologies - Advances and Priorities, U.S. DOE Contract AC07-901D12920, February 1991.
16. Isidori, A. (1995). Nonlinear Control Systems. An Introduction, 3rd ed., Springer-Verlag, New York.
17. Khalil, H. K. (2002). Nonlinear Systems, 3rd ed., Prentice-Hall, Upper Saddle River, N.J.
18. Kothare, M., Campo, P. J., Morari, M., and Nett, C. L. (1994). Automatica, 30(12), 1869-1883. [CROSSREF]
19. Lévine, J. and Rouchon, P. (1991). Automatica, 27, 463-480. [CROSSREF]
20. Levy, R. E., Foss, A. S., and Grens II, E. A. (1969). Ind. Eng. Chem. Fundam., 8(4), 765-776. [CROSSREF]
21. Luyben, W. L. (1970). AIChE J., 16, 198-203. [CROSSREF]
22. Luyben, W. L. (1975). Ind. Eng. Chem. Fundam., 14(4), 321-325. [CROSSREF]
23. Luyben, W. L. (1990). Process Modeling, Simulation and Control for Chemical Engineers, 2nd ed., McGraw-Hill, New York.
24. Luyben, W. L. (2004). The need for simultaneous design education, in The Integration of Process Design and Control, eds. P.Seferlis and M. C.Georgiadis, Elsevier, Amsterdam.
25. McCabe, W. L. and Thiele, E. W. (1925). Ind. Eng. Chem., 17(6), 605-611. [CROSSREF]
26. Morari, M. and Zafiriou, E. (1989). Robust Process Control, Prentice-Hall, Englewood Cliffs, N.J.
27. Niederlinski, A. (1971). AIChE J., 17(5), 1261-1263. [CROSSREF]
28. Patel, P. M., Schorr, G. R., Schah, P. N., and Yaws, C. (1976). Chem. Eng., Nov. 22, 159.
29. Riggs, J. B. and Huang, H. (2002). Ind. Eng. Chem. Res., 41, 4048-4053. [CROSSREF]
30. Riggs, J. B., Beauford, M., and Watts, J. (1993). Using tray-to-tray models for distillation control, in Nonlinear Process Control: Applications of Generic Model Control, ed. P. Lee, Springer-Verlag, New York.
31. Sepulchre, R., Janković, M., and Kokotović, P. R. (1997). Constructive Nonlinear Control, Springer-Verlag, London.
32. Shin, J., Seo, H., Han, M., and Park, S. (2000). Chem. Eng. Sci., 55, 807-816. [CROSSREF]
33. Shinskey, F. G. (1988). Process-Control Systems, 3rd ed., McGraw-Hill, New York.
34. Shinskey, F. G. (2002). Ind. Eng. Chem. Res., 41, 3745-3750. [CROSSREF]
35. Skogestad, S. (1997). Model. Identif. Control, 18(3), 177-217.
36. Skogestad, S. and Lundström, P. (1990). Comput. Chem. Eng., 14(4/ 5), 401-413. [CROSSREF]
37. Skogestad, S. and Lundström, P. (1995). J. Process Control, 5(4), 249-261. [CROSSREF]
38. Sontag, E. D. (2000). The ISS philosophy as a unifying framework for stability-like behavior, in Nonlinear Control in the Year 2000, eds. A. Isidori, F. Lamnabhi-Lagarrigue, and W. Respondek, Vol. 2, Springer-Verlag, Berlin.
39. Wood, R. K. and Berry, M. W. (1973). Chem. Eng. Sci., 28, 1707-1717. [CROSSREF]