Inferential control system of distillation compositions using dynamic Partial Least Squares regression

Journal of Process Control

Volumn 10, Issue 2, 2000, Pages 157-166

  Kano, Manabu ^a   Miyazaki, Koichi ^a   Hasebe, Shinji ^a   Hashimoto, Iori ^a  

^a KYOTO UNIVERSITY   (Japan)

Author keywords

[No Author keywords available]

Indexed keywords

CASCADE CONTROL SYSTEMS; COMPUTER SIMULATION; DISTILLATION COLUMNS; LEAST SQUARES APPROXIMATIONS; MATHEMATICAL MODELS; REGRESSION ANALYSIS; TEMPERATURE CONTROL; TIME SERIES ANALYSIS;

DYNAMIC PARTIAL LEAST SQUARES (PLS) REGRESSION; INFERENTIAL CONTROL SYSTEMS;

PROCESS CONTROL;

EID: 0033874839     PISSN: 09591524     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0959-1524(99)00027-X     Document Type: Article

References (20)

1. Tolliver T.L., McCune L.C. Finding the optimum temperature control trays for distillation columns. InTech. 27(9):1980;75-80.
2. Rademaker O., Rijinsdorp J.E., Maarleveld A. Dynamics and control of continuous distillation units. 1975;Elsevier, Amsterdam.
3. Yu C.C., Luyben W.L. Use of multiple temperatures for the control of multicomponent distillation columns. Ind. Eng. Chem. Res. 23:1984;590-597.
4. D.B. Whitehead and M. Parnis, Computer control improves ethylene plant operation. Hydrocarbon Processing, Nov. (1987) 105-108.
5. H.F. Bozenhardt, Modern control tricks solve distillation problems, Hydrocarbon Processing, June (1988) 47-50.
6. Weber R., Brosilow C.B. The use of secondary measurements to improve control. AIChE J. 18(3):1972;614-623.
7. Joseph B., Brosilow C.B. Inferential control of processes. AIChE J. 24(3):1978;485-509.
8. Morari M., Stephanopoulos G. Optimal selection of secondary measurements within the framework of state estimation in the presence of persistent unknown disturbances. AIChE J. 16(2):1980;247-259.
9. Moore C., Hackney J., Canter D. Selecting sensor location and type for multivariable processes. Prett D.M., Morari M. Shell process control workshop. 1987;291-308 Butterworth, Boston.
10. Kresta J.V., Marlin T.E., MacGregor J.F. Development of inferential process models using PLS. Comp. Chem. Engng. 18:1994;597-611.
11. Mejdell T., Skogestad S. Estimation of distillation compositions from multiple temperature measurements using partial-least-squares regression. Ind. Eng. Chem. Res. 30:1991;2543-2555.
12. Mejdell T., Skogestad S. Composition estimator in a pilot-plant distillation column using multiple temperatures. Ind. Eng. Chem. Res. 30:1991;2555-2564.
13. Mejdell T., Skogestad S. Output estimation using multiple secondary measurements: high-purity distillation. AIChE J. 39(10):1993;1641-1653.
14. H. Fujii, S. Lakshminarayanan, S.L. Shah, Application of the PLS technique to the estimation of distillation tower top composition. Preprints of IFAC symposium on Advanced Control of Chemical Processes (ADCHEM), Banff, Canada, 1997.
15. Glen W.G., Dun III W.J., Scott D.R. Principal component analysis and partial least squares. Tetrahedron Computer Methodology. 2:1989;349-376.
16. Nomikos P., MacGregor J.F. Monitoring batch processes using multiway principal component analysis. AIChE J. 40(8):1994;1361-1375.
17. Kano M., Shiren T., Ohshima M., Okamo U., Aoki S., Hashimoto I. On-line inference system of tube-wall temperature for an industrial olefin pyrolysis plant. AIChE Symposium Series No. 316. 93:1997;292-296.
18. Lakshminarayanan S., Shah S.L., Nandakumar K. Modeling and control of multivariable processes: dynamic PLS approach. AIChE J. 43(9):1997;2307-2322.
19. Joseph B., Brosilow C.B., Howell J.C., Kerr W.R.D. Multi-temps give better control. Hydrocarbon Processing. March:1976;127-131.
20. Skogestad S., Morari M. Understanding the dynamic behavior of distillation columns. Ind. Eng. Chem. Res. 27:1988;1848-1862.