Experimental and theoretical studies of the dynamics of startup and product switchover operations of distillation columns-Reference-Cited by-同舟云学术

Experimental and theoretical studies of the dynamics of startup and product switchover operations of distillation columns

Published:1993-10 Issue:5 Volume:32 Page:283-290
ISSN:0255-2701
Container-title:Chemical Engineering and Processing: Process Intensification
language:en
Short-container-title:Chemical Engineering and Processing: Process Intensification

Author:

Fieg G.,Wozny G.,Kruse Chr.

Publisher

Elsevier BV

Subject

Industrial and Manufacturing Engineering,Process Chemistry and Technology,Energy Engineering and Power Technology,General Chemical Engineering,General Chemistry

Reference19 articles.

1. Optimal control of industrial chemical system startup;Balakirev;Theor. Found. Chem. Eng. USSR,1990

2. Die Reaktionstechnik der katalytischen Polymerisation unter hohem Druck;Bucka;Chem. Tech.,1991

3. Time-optimal startup control algorithm for batch processes;Westerholt;Ind. Eng. Chem., Res.,1991

4. Probleme des dynamischen Verhaltens von Rührkessel-Reaktorkaskaden;Lippert;Chem. Tech.,1989

5. Adaptive control strategies for achieving desired temperature profiles during process startup. Model development and simulation studies;Phillips;Ind. Eng. Chem. Res.,1988

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