Nonlinear adaptive control algorithm for a multicomponent batch distillation column

Chemical Engineering Science

Volumn 62, Issue 4, 2007, Pages 1111-1124

  Murlidhar, Gundale Mangesh ^a   Jana, Amiya Kumar ^a  

^a BIRLA INSTITUTE OF TECHNOLOGY AND SCIENCE   (India)

Author keywords

Adaptive control algorithm; Adaptive state estimator; Generic model controller; Multicomponent batch distillation

Indexed keywords

ADAPTIVE ALGORITHMS; ADAPTIVE CONTROL SYSTEMS; CONVERGENCE OF NUMERICAL METHODS; NONLINEAR SYSTEMS; PARAMETER ESTIMATION; SYSTEMS ANALYSIS;

ADAPTIVE CONTROL ALGORITHMS; ADAPTIVE STATE ESTIMATORS; GENERIC MODEL CONTROLLERS; MULTICOMPONENT BATCH DISTILLATION;

DISTILLATION COLUMNS;

ADAPTIVE ALGORITHMS; ADAPTIVE CONTROL SYSTEMS; CONVERGENCE OF NUMERICAL METHODS; DISTILLATION COLUMNS; NONLINEAR SYSTEMS; PARAMETER ESTIMATION; SYSTEMS ANALYSIS;

EID: 33845865000     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2006.11.006     Document Type: Article

References (39)

1. Alvarez-Ramirez J. Adaptive control of feedback linearizable systems: a modeling error compensation approach. International Journal of Robust and Nonlinear Control 9 (1999) 361-377
2. Alvarez-Ramirez J., Monroy-Loperena R., Cervantes I., and Morales A. A novel proportional-integral-derivative control configuration with application to the control of batch distillation. Industrial & Engineering Chemistry Research 39 (2000) 432-440
3. Baratti R., Bertucco A., Da Rold A., and Morbidelli M. Development of a composition estimator for binary distillation columns. Application to a pilot plant. Chemical Engineering Science 50 (1995) 1541-1550
4. Barolo M., and Berto F. Composition control in batch distillation: binary and multicomponent mixtures. Industrial & Engineering Chemistry Research 37 (1998) 4689-4698
5. Barolo M., and Berto F. An advanced strategy for composition control in batch distillation. In: Georgakis C. (Ed). edited preprints of DYCOPS-5-5th IFAC Symposium on Dynamics and Control of Process Systems (1998) 430-435
6. Barolo M., Pistillo A., and Trotta A. Issues in the development of a composition estimator for a middle-vessel batch column. In: Camacho E.F., Basanez L., and de la Puente J.A. (Eds). Advanced Control of Chemical Processes 2000-IFAC ADCHEM 2000 (2000), Elsevier, Oxford, UK 923-928
7. Bequette, B.W., 2003. Process Control: Modeling, Design, and Simulation. Prentice-Hall, New Delhi, pp. 361-362.
8. Cott B.J., Durham R.G., Lee P.L., and Sullivan G.R. Process model based engineering. Computers and Chemical Engineering 13 (1989) 973-984
9. Dechechi E.C., Luz Jr. L.F.L., Assis A.J., Maciel M.R.W., and Maciel Filho R. Interactive supervision of batch distillation with advanced control capabilities. Computers and Chemical Engineering 22 (1998) S867-S870
10. Farza M., Busawon K., and Hammouri H. Simple nonlinear observers for on-line estimation of kinetic rates in bioreactors. Automatica 34 (1998) 301-318
11. Farza M., Hammouri H., Jallut C., and Lieto J. State observation of a nonlinear system: application to (bio)chemical processes. A.I.Ch.E. Journal 45 (1999) 93-106
12. Finefrock, Q.B., Bosley, J.R., Edgar, T.F., 1994. Gain-scheduled PID control of batch distillation to overcome changing system dynamics. A.I.Ch.E. Annual Meeting.
13. Frattini-Fileti A.M., and Rocha-Pereira J.A.F. The development and experimental testing of two adaptive control strategies for batch distillation. In: Darton R. (Ed). Distillation and Absorption '97 (1997), IChemE, Rugby, UK 249
14. Galindez H., and Fredenslund A.A. Simulation of multicomponent batch distillation processes. Computers and Chemical Engineering 12 (1988) 281-288
15. Gauthier J.P., Hammouri H., and Othman S. A simple observer for nonlinear systems applications to bioreactors. IEEE Transactions on Automatic Control 37 (1992) 875-880
16. Guo B., Jiang A., Hua X., and Jutan A. Nonlinear adaptive control for multivariable chemical processes. Chemical Engineering Science 56 (2001) 6781-6791
17. Han M., and Park S. Profile position control of batch distillation based on a nonlinear wave model. Industrial & Engineering Chemistry Research 40 (2001) 4111-4120
18. Henley E.J., and Seader J.D. Equilibrium-Stage Separation Operations in Chemical Engineering (1981), Wiley, New York
19. Henson M.A., and Seborg D.E. An internal model control strategy for nonlinear systems. A.I.Ch.E. Journal 37 (1991) 1065-1081
20. Hunt L.R., Su R., and Meyer G. Global transformations of nonlinear systems. IEEE Transactions on Automatic Control 28 (1983) 24-31
21. Isidori A. Nonlinear Control Systems (1989), Springer, New York
22. Jana A.K., Samanta A.N., and Ganguly S. Globally linearized control system design of a constrained multivariable distillation column. Journal of Process Control 15 (2005) 169-181
23. Kim Y.H. Optimal design and operation of multi-product batch distillation column using dynamic models. Chemical Engineering and Processing 38 (1999) 61-72
24. Kravaris C., and Chung C.B. Nonlinear state feedback synthesis by global input/output linearization. A.I.Ch.E. Journal 33 (1987) 592-603
25. Lee P.L., and Sullivan G.R. Generic model control (GMC). Computers and Chemical Engineering 12 (1988) 573-580
26. Li P., and Wozny G. Optimization of multiple-fraction batch distillation with detailed dynamic process model. In: Darton R. (Ed). Distillation and Absorption '97 (1997), IChemE, Rugby, UK 289
27. Li P., and Wozny G. Tracking the predefined optimal policies for multiple-fraction batch distillation by using adaptive control. Computers and Chemical Engineering 25 (2001) 97-107
28. Luyben W.L. Multicomponent batch distillation. Part 1. Ternary systems with slops recycle. Industrial & Engineering Chemistry Research 27 (1988) 642-647
29. Luyben, W.L., 1990. Process Modeling, Simulation and Control for Chemical Engineers. McGraw-Hill, Singapore, pp. 133-138.
30. Monroy-Loperena R., and Alvarez-Ramirez J. A note on the identification and control of batch distillation columns. Chemical Engineering Science 58 (2003) 4729-4737
31. Oisiovici R.M., and Cruz S.L. State estimation of batch distillation columns using an extended Kalman filter. Chemical Engineering Science 55 (2000) 4667-4680
32. Oisiovici R.M., and Cruz S.L. Inferential control of high-purity multicomponent batch distillation columns using an extended Kalman filter. Industrial & Engineering Chemistry Research 40 (2001) 2628-2639
33. Quintero-Marmol E., and Luyben W.L. Inferential model-based control of multicomponent batch distillation. Chemical Engineering Science 47 (1992) 887-898
34. Quintero-Marmol E., Luyben W.L., and Georgakis C. Application of an extended Luenberger observer to the control of multicomponent batch distillation. Industrial & Engineering Chemistry Research 30 (1991) 1870-1880
35. Riggs J.B. Nonlinear process model based control of a propylene sidestream draw column. Industrial & Engineering Chemistry Research 29 (1990) 2221-2226
36. Signal P.D., and Lee P.L. Generic model adaptive control. Chemical Engineering Communications 115 (1992) 35-52
37. Venkateswarlu C., and Avantika S. Optimal state estimation of multicomponent batch distillation. Chemical Engineering Science 56 (2001) 5771-5786
38. Yamuna K.R., and Gangiah K. Adaptive generic model control: dual composition control of distillation. A.I.Ch.E. Journal 37 (1991) 1634-1642
39. Zamprogna E., Barolo M., and Seborg D.E. Estimating product composition profiles in batch distillation via partial least squares regression. Control Engineering Practice 12 (2004) 917-929