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Dynamics and Control of Chemical Reactors, Distillation by J. G. Balchen, E. D. Gilles, K. V. Waller, J. B. Rawlings

By J. G. Balchen, E. D. Gilles, K. V. Waller, J. B. Rawlings

As well as the 3 major topics: chemical reactors, distillation columns, and batch tactics this quantity additionally addresses a number of the new tendencies in dynamics and regulate technique resembling version established predictive keep watch over, new equipment for id of dynamic versions, nonlinear keep watch over concept and the appliance of neural networks to identity and keep watch over. offers an invaluable reference resource of the key advances within the box.

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Extra info for Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes. Selected Papers from the 3rd IFAC Symposium, Maryland, USA, 26–29 April 1992

Example text

Loffier, C. and Dubus, J . P. FA G Symp. Adchem 91 , Toulouse, France, 391-396. M. ( 1 946), "Control of fractionation columns" , Petr. Refiner, 25, 147- 1 5 1 . F. ( 1 988) , "Modern control tricks solve distillation problems" , Hydrocarbon Processing, 67, 4750. S . L. S. ( 1 985) , Design of distillation column control systems, Instrument Society of America, Research Triangle Park, USA. A. K. ( 1 987) , "Transient re­ sponse behaviour of a depropanizer" , Distillation and Ab­ sorbtion 87, Brighton, UK.

By using the DY-configuration as suggested by Skogestad, 1988, Alsop and Edgar, 1990 , Andersen and Kiimmel , 199 1 , Kuong and McGregor , 199 1 ) , or by adjusting the steady-state gains to match an estimated steady-state RGA-value as suggested by J acobsen et al. ( 1 991a), or by using a "perturbed model" (Kapoor et al. , 1986) based on steady-state where the RGA-elements are smaller. The basis for the two last suggestions is that the steady-state be­ havior is not of primary importance, but rather the initial response .

A. J. ( 1 987), "Application ( 1 975), Dynamics and control of continuous distillation of dynamic matrix control to moderate- and high-purity columns, Elsevier, Amsterdam. distillation towers" , Ind. Eng. Chem. , 26, 1 0 1 11018. Rasmussen , K . H . S. B. , Palazoglu, A. W. ( 1 990), "Identification of distillation process dynamics (1988), "Impact of model uncertainty descriptions for comparing process knowledge and black box based ap­ high-purity distillation control" , A IChE Journal, 34, proaches" , Proc.

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