Distillation control configuration selection

Journal of Process Control

Volumn 13, Issue 4, 2003, Pages 357-362

  Hurowitz, Scott ^a,d   Anderson, Joe ^b,d   Duvall, Marshall ^c,d   Riggs, James B ^d  

^a Aspentech   (United States)

^b DOW CHEMICAL COMPANY   (United States)

^c EXXONMOBIL UPSTREAM RESEARCH COMPANY   (United States)

^d Department of Electrical and Computer Engineering   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

CLOSED LOOP CONTROL SYSTEMS; CONTROLLABILITY; DISTILLATION COLUMNS; FEEDBACK CONTROL;

FEEDFORWARD CONTROL;

PROCESS CONTROL;

EID: 0037408957     PISSN: 09591524     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0959-1524(02)00032-X     Document Type: Article

References (22)

1. J.L. Humphrey, A.F. Seibert, R.A. Koort, Separation Technologies - Advances and Priorities, DOE Contract AC07-901D12920, February 1991.
2. F.G. Skinskey, Distillation Control, 2nd Edition, McGraw-Hill, 1984.
3. Skogestad S., Lundstrom P., Jacobsen E.W. Selecting the best distillation control configuration. AIChE J. 36:1990;753-764.
4. McCune L.C., Gallier P.W. Digital simulation. a tool for the analysis and design of distillation control ISA Trans. 12:1973;193.
5. Takamatsu T., Hashimoto I., Hashimoto Y. Selection of manipulated variables to minimize interaction in multivariate control of distillation column. Int. Chem. Eng. 27:1987;669.
6. K.V. Waller, in: W.L. Luyben (Ed.), Experimental Comparison of Control Structures, Practical Distillation Control, 1992, pp. 313-330.
7. Finco M.V., Luyben W.L., Polleck R.E. Control of distillation columns with low relative volatilities. Ind. Eng. Chem. Res. 29:1989;75-83.
8. S. Skogestad, Dynamics and Control of Distillation Columns - A Critical Survey, Modeling, Identification, and Control, 1997.
9. G.E. Hill, Propylene- Propane Vapor-Liquid Equilibria, presented at the AIChE National meeting, Atlantic City, NJ, 1959.
10. Choe Y.S., Luyben W.L. Rigorous dynamic models for distillation columns. Ind. Eng. Chem. Res. 26:1987;2158-2161.
11. Soave G. Chem. Eng. Sci. 27:1992;1197.
12. S.E. Hurowitz, Superfractionator Process Control, PhD dissertation, Texas Tech University, 1998.
13. J.J. Anderson, Vacuum Distillation Control, PhD dissertation, Texas Tech University, 1998.
14. P.M. Duvall, On Control of High Relative Volatility Distillation Columns, PhD dissertation, Texas Tech University, 1999.
15. Riggs J.B. Chemical Process Control. 2nd Edition:2001;Ferret Publishing, Lubbock, TX.
16. K.J. Astrom, T. Hagglund, Automatic Tuning of PID Controllers, ISA, Research Triangle Park, 1988.
17. Tyreus B.D., Luyben W.L. Tuning PI controllers for integrator/deadtime processes. I&ECR. 31:1992;2625.
18. Ziegler J.G., Nichols N.B. Optimum settings for automatic controllers. Trans. ASME. 64:1942;759.
19. Ryskamp C.J. New stradegy improves dual composition column control. Hydrocarb. Proc. 59:1980;51-59.
20. Bristol E.H. On a new measure of interaction for multivariable process control. IEEE Trans. Auto Con. AC-11:1966;133-134.
21. T.J. McAvoy, Interaction Analysis, Instrument Society of America, Triangle Park, NC, 1983.
22. Haggblom K.E., Waller K.V. Control structures for disturbance rejection and decoupling of distillation. AIChE J. 36:1990;1107-1113.