Author/Authors :
Martin G. Sneesby، نويسنده , , Moses O. Tade and Terence N. Smith، نويسنده ,
DocumentNumber :
1384283
Title Of Article :
Two-point control of a reactive distillation column for composition and conversion
شماره ركورد :
11347
Latin Abstract :
Reactive distillation is a hybrid process with dual process objectives: reactant conversion and product composition, Control schemes for reactive distillation frequently neglect the effect of the principal operating parameters on the reactant conversion, and this has a detrimental effect on the overall process profitability. An ETBE reactive distillation column has been used as a case study to show how a two-point control configuration, which recognises the importance of both composition and conversion, can be developed and implemented for a reactive distillation process. The combined composition and conversion control configuration was tested using SpeedUp dynamic simulations and proved to be effective in maintaining a high isobutylene conversion despite process disturbances. The two-point control scheme also had superior disturbance rejection capability, especially for feed rate changes, and composition set-point sensitivity compared with a one-point control scheme.
From Page :
19
NaturalLanguageKeyword :
Two-point control , inferential model , Reactive distillation
JournalTitle :
Studia Iranica
To Page :
31
To Page :
31
Link To Document :
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