References

Symposium Series No. 32, London, 1968.

5. Shinskey, F. G., Distillation Control,

McGraw-Hill, New York, 1977.

6. McAvoy, T. J., Interaction Analysis,

ISA, Research Triangle Park, N.C., 1983.

7. Ray, W. H. Advanced Process Control,

McGraw-Hill, New York, 1981.

Ends for Profit," Proceedings, ISA Conference #27, New York, Oct. 1972.

9. Ryskamp, C. J. "New Strategy Im proves Dual Composition Control," Hydrocarb. Proc. 51-59 (lune 1980). 10. Waller, K., L. G. Hammerstrom, and K. C. Fagervik, "A Comparison of

Six Control Approaches for Two Product Control of Distillation," Report 80-2, Âbo Akademi, Department of Chemical Engineering, Process Control Laboratory, 1980.

11. Tyreus, B. D. "Multivariable Control

System Design for an Industrial Distillation Column," ZEC Proc. Des. Dev. 18:177-182 (Jan. 1979).

12. Luyben, W. L., "Distillation Decou pling," AIChE J. 16:198 (1970).

"Experimental Studies in Distillation Decoupling," Kemian Teollisuus 29 8:499-514 (1972).

14. Niederlinski, A. "Two Variable Dis tillation Control: Decouple or Not

Decouple," AIChE J. 17(5): 12611263 (Sept. 1971).

15. Waller, K. "Decoupling in Distillation,"

16. Uitti, K. "Effect of Control Point Lo cation Upon Column Control,'' ISA Paper 49-9-2.

18. Luyben, W. L. "Distillation Feedfor ward Control With Intermediate Feedback Control Trays," Chem. Eng. Sci. 24:997-1007 (1969).

19. Bristol, E. "On a New Measure for

Multivariable Control,'' TF.F.F. Trans. Auto. Contr. AC-11:133 (1966).

Sampled-Data Control of Distillation Columns

Was this article helpful?

0 0

Post a comment