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

Computers and Chemical Engineering

Volumn 27, Issue 10, 2003, Pages 1485-1497

  Wang, Lin ^a   Li, Pu ^a   Wozny, Günter ^a   Wang, Shuqing ^b  

^a TECHNISCHE UNIVERSITÄT BERLIN   (Germany)

^b ZHEJIANG UNIVERSITY   (China)

Author keywords

Batch distillation; Cold state; Experimental verification; gPROMS; Modeling; Non equilibrium; Phase transition; Simulation; Startup

Indexed keywords

COMPUTER SIMULATION; ENERGY TRANSFER; METHANOL; PHASE EQUILIBRIA; REBOILERS;

BUBBLE-POINT TEMPERATURE;

DISTILLATION;

DISTILLATION COLUMN; LIQUID-LIQUID SEPARATION; MATHEMATICAL MODELING; OPTIMIZATION; VAPOR-LIQUID EQUILIBRIUM;

BATCH DISTILLATION; DISTILLATION; ENERGY TRANSFER; MODEL; PHASE TRANSITION; REVIEW; SIMULATION; TEMPERATURE;

EID: 0042467404     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0098-1354(03)00094-2     Document Type: Article

References (17)

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. Barton, P. I., & Pantelides, C. C. (1994). Modeling of combined discrete/continuous process. American Institute of Chemical Engineering Journal 40, 966-979.
4. Diwekar, U. M., & Madhavan, K. P. (1991). Multicomponent batch distillation column design. Industrial Engineering and Chemical Research 30, 713-721.
5. gPROMS Introductory User Guide (2000). Release 1.8.0, Process Systems Enterprise Limited, London.
6. Hangos, K. M., Hallager, L., Csaki, Z. S., & Jorgensen, S. B. (1991). A qualitative model for simulation of the startup of a distillation column with Energy Feedback. In L. Puigjaner & A. Espuna (Eds.), Computer-Oriented Process Engineering (pp. 87-92).
7. Jimenez, L., Basualdo, M., Toselli, L., & Rosa, M. (2000). Dynamic modeling of batch distillation: comparison between commercial software. In: S. Pierucci, Proceedings of ESCAPE-10 (pp. 1153-1158).
8. Löwe, K. (2001). Theoretische und experimentelle Untersuchungen über das Anfahren und die Prozessfuehrung energetisch und stofflich gekoppelter Destillationskolonnen, Ph.D. thesis, Technische Universität Berlin.
9. Li, P., & Wozny, G. (1999). Tracking the predefined optimal policies for multiple-fraction batch distillation by using adaptive control. Computers and Chemical Engineering suppl. 23, S281-S284.
10. Li, P., Arellano-Garcia, H., Wozny, G., & Reuter, E. (1998). Optimization of a semibatch distillation process with model validation on the industrial site. Industrial Engineering and Chemical Research 37, 1341-1350.
11. Mujtaba, M., & Macchietto, S. (1993). Optimal operation of multicomponent batch distillation - multiperiod formulation and solution. Computers and Chemical Engineering 17, 1191-1207.
12. Nad, M., Spiegel, L. (1987). Simulation of batch distillation by computer and comparison with experiment, Proc. CET'87 (pp. 737-742) Italy.
13. Perry, R. H., Green, D. W., & Maloney, J. O. (1997). Perry's chemical engineers' handbook (7th ed.). New York: McGraw-Hill.
14. Rix, A. (1998). Modellierung und Prozeßführung wämeintegrierter Destillationskolonnen, Ph.D. thesis, Technische Universität Berlin.
15. Ruiz, C. A., Cameron, I. T., & Gani, R. (1988). A generalized dynamic model for distillation columns - III. Study of startup operations. Computers and Chemical Engineering 12, 1-14.
16. Smith, B. (1963). Design of equilibrium stage process. New York: McGraw-Hill.
17. Sørensen, E., & Skogestad, S. (1996). Optimal startup procedure for batch distillation. Computers and Chemical Engineering 20 (Suppl), S1257-S1262.