A short note on control structures for thermally coupled distillation sequences for four-component mixtures

Industrial and Engineering Chemistry Research

Volumn 44, Issue 15, 2005, Pages 5857-5863

  Hernández, Salvador ^a   Gudiño Mares, Ivan R ^a   Cárdenas, J Carlos ^a   Segovia Hernández, Juan Gabriel ^a   Rico Ramírez, Vicente ^b  

^a UNIVERSITY OF GUANAJUATO   (Mexico)

^b DEPARTAMENTO DE INGENIERÍA QUÍMICA   (Mexico)

Author keywords

[No Author keywords available]

Indexed keywords

COSTS; DISTILLATION COLUMNS; DYNAMIC RESPONSE; HYDROCARBONS; MIXTURES; SEPARATION;

CLOSED-LOOP OPERATION; DIVIDED-WALL DISTILLATION COLUMN; MULTICOMPONENT MIXTURES; THERMALLY COUPLED DISTILLATION;

DISTILLATION;

CHEMICAL ENGINEERING; DISTILLATION; SEPARATION;

EID: 22944448660     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie050169r     Document Type: Article

References (26)

1. Tedder, D. W.; Rudd, D. F. Parametric Studies in Industrial Distillation: Part I. Design Comparisons. AIChE J. 1978, 24, 303.
2. Glinos, K.; Malone, F. Optimality Regions for Complex Column Alternatives in Distillation Systems. Chem. Eng. Res. Des. 1988, 66, 229.
3. Fidkowski, Z.; Krolikowski, L. Energy Requirements of Nonconventional Distillation Systems. AIChE J. 1990, 36, 1275.
4. Triantafyllou, C.; Smith, R. The Design and Optimisation of Fully Thermally Coupled Distillation Columns. Trans. Inst. Chem. Eng. 1992, 70, 118.
5. Finn, A. J. Consider Thermally Coupled Distillation. Chem. Eng. Prog. 1993, 10, 41.
6. Wolff, E. A.; Skogestad, S. Operation of Integrated Three-Product (Petlyuk) Distillation Columns. Ind. Eng. Chem. Res. 1995, 34, 2094.
7. Hernández, S.; Jiménez, A. Design of Optimal Thermally-Coupled Distillation Systems Using a Dynamic Model. Trans. Inst. Chem. Eng. 1996, 74, 357.
8. Hernández, S.; Jiménez, A. Design of Energy-Efficient Petlyuk Systems. Comput. Chem. Eng. 1999, 23, 1005.
9. Hernández, S.; Jiménez, A. Controllability Analysis of Thermally Coupled Distillation Systems. Ind. Eng. Chem. Res. 1999, 38, 3957.
10. Shah, P. B. Squeeze More out of Complex Columns. Chem. Eng. Prog. 2002, July, 46.
11. Schultz, M. A.; Stewart, D. G.; Harris, J. M.; Rosenblum, S. P.; Shakur, M. S.; O'Brien, D. E. Reduce Costs with Dividing-Wall Caolumns. Chem. Eng. Prog. 2002, May, 64.
12. Rong, B. G.; Kraslawski, A.; Turunen, I. Synthesis of Functionally Distinct Thermally Coupled Configurations for Quaternary Distillation. Ind. Eng. Chem. Res. 2003, 42, 1204
13. Hernández, S.; Pereira-Pech, S.; Jiménez, A.; Rico-Ramírez, V. Energy Efficiency of an Indirect Thermally Coupled Distillation Sequence. Can. J. Chem. Eng. 2003, 81, 1087.
14. Christiansen, A. C.; Skogestad, S.; Lien, K. Complex Distillation Arrangements: Extending the Petlyuk Ideas. Comput. Chem. Eng. 1997, 21, S237.
15. Rong, B. G.; Kraslawski, A. Optimal Design of Distillation Flowsheets with a Lower Number of Thermal Couplings for Multicomponent Separations. Ind. Eng. Chem. Res. 2002, 41, 5716.
16. King, C. J. Separation Processes, 2nd ed.; McGraw-Hill: New York, 1980.
17. Kaibel, G.; Schoenmakers, H. Process Synthesis and Design in Industrial Practice. In Proceedings of ESCAPE-12 (Computer Aided Process Engineering 10); Grievink, J., Schijndel, J. V., Eds.; Elsevier: Amsterdam, The Netherlands, 2002; p 9.
18. Blancarte-Palacios, J. L.; Bautista-Valdés, M. N.; Hernández, S.; Rico-Ramírez, V.; Jiménez, A. Energy-Efficient Designs of Thermally Coupled Distillation Sequences for Four-Component Mixtures. Ind. Eng. Chem. Res. 2003, 42, 5157.
19. min Diagram for Two-Product Column. Ind. Eng. Chem. Res. 2003, 42, 596.
20. Halvorsen, I. J.; Skogestad, S. Minimum Energy Consumption in Multicomponent Distillation. 2. Three-Product Petlyuk Arrangements. Ind. Eng. Chem. Res. 2003, 42, 605.
21. Halvorsen, I. J.; Skogestad, S. Minimum Energy Consumption in Multicomponent Distillation. 3. More Than Three Products and Generalized Petlyuk Arrangements. Ind. Eng. Chem. Res. 2003, 42, 616.
22. Halvorsen, I. J.; Skogestad, S. Shortcut Analysis of Optimal Operation of Petlyuk Distillation. Ind. Eng. Chem. Res. 2004, 43, 3994.
23. Stephanopoulos, G. Chemical Process Control. An Introduction to Theory and Practice; Prentice Hall Inc.: Upper Saddle River, NJ, 1984.
24. Cárdenas, J. C.; Hernández, S.; Gudino-Mares, I. R.; Esparza-Hernández, F.; Irianda-Araraujo, C. Y.; Dominguez-Lira, L. M. Analysis of Control Properties of Thermally Coupled Distillation Sequences for Four-Component Mixtures. Ind. Eng. Chem. Res. 2005, 44, 391-399.
25. Jiménez, A.; Hernández, S.; Montoy, F. A.; Zavala-García, M. Analysis of Control Properties of Conventional and Non-conventional Distillation Sequences. Ind. Eng. Chem. Res. 2001, 40, 3757.
26. Santos-Méndez, J.; Hernández, S. Effect of Recycle Streams on the Closed Loop Dynamics of Thermally Coupled Distillation Sequences. Chem. Eng. Commun. 2005, 192, 1085.