A startup model for simulation of batch distillation starting from a cold state

Author:

Wang Lin,Li Pu,Wozny Günter,Wang Shuqing

Publisher

Elsevier BV

Subject

Computer Science Applications,General Chemical Engineering

Reference17 articles.

1. Albet, J., LeLann, J. M., Joulia, X., & Koehret, B. (1991). Rigorous simulation of multicomponent multisequence batch reactive distillation, Proceedings of COPE-91, Barcelona, Spain, 14–16 October 1991. Process Technology Proceedings, 10, Elsevier, 75–81.

2. Albet, J., LeLann, J. M., Joulia, X., & Koehret, B. (1994). Operation policies for startup in the case of batch rectification involving chemical reactions, Proceedings of ESCAPE-4, Dublin, Ireland, 28–30 March 1994. IChemE Symposium Series 133, 63–70.

3. Modeling of combined discrete/continuous process;Barton;American Institute of Chemical Engineering Journal,1994

4. Multicomponent batch distillation column design;Diwekar;Industrial Engineering and Chemical Research,1991

5. gPROMS Introductory User Guide (2000). Release 1.8.0, Process Systems Enterprise Limited, London.

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