Two-point temperature control structure selection for dividing-wall distillation columns

Industrial and Engineering Chemistry Research

Volumn 51, Issue 48, 2012, Pages 15683-15695

  Kim, Kwangil ^a   Lee, Moonyong ^b   Park, Sunwon ^a  

^a Korea Advanced Institute of Science and Technology (KAIST)   (South Korea)

^b Yeungnam University   (South Korea)

Author keywords

[No Author keywords available]

Indexed keywords

CLOSED-LOOP RESPONSE; CONTROL PERFORMANCE; CONTROL STRATEGIES; CONTROL STRUCTURE; FEED COMPONENTS; INTERMEDIATE COMPONENTS; RELATIVE VOLATILITY; RIGOROUS SIMULATION; TWO-POINT;

COMPUTER SIMULATION;

TEMPERATURE CONTROL;

EID: 84870851969     PISSN: 08885885     EISSN: 15205045     Source Type: Journal    
DOI: 10.1021/ie301457a     Document Type: Article

References (35)

1. Fidkowski, Z.; Krolikowski, L. Energy Requirements of Nonconventional Distillation Systems AIChE J. 1990, 36, 1275-1278
2. Hernández, S.; Jiménez, A. Design of Energy-Efficient Petlyuk Systems Comput. Chem. Eng. 1999, 23, 1005-1010
3. Jiménez, A.; Ramírez, N.; Castro, A.; Hernández, S. Design and Energy Performance of Alternative Schemes to the Petlyuk Distillation System Trans. Inst. Chem. Eng. 2003, 81 (A5) 518-524
4. Halversen, I. J.; Skogestad, S. Minimum Energy Consumption in Multicomponent Distillation. 2. Three-Product Petlyuk Arrangements Ind. Eng. Chem. Res. 2003, 42, 605-615
5. Halversen, I. J.; Skogestad, S. Shortcut Analysis of Optimal Operation of Petlyuk Distillation Ind. Eng. Chem. Res. 2004, 43, 3994-3999
6. Aspiron, N.; Kaibel, G. Dividing Wall Columns: Fundamentals and Recent Advances Chem. Eng. Process. 2010, 49, 139-146
7. Long, N.; Lee, S.; Lee, M. Design and Optimization of a Dividing Wall Column for Debottlenecking of the Acetic Acid Purification Process Chem. Eng. Process. 2010, 49, 825-835
8. Long, N.; Lee, M. Improved Energy Efficiency in Debottlenecking Using a Fully Thermally Coupled Distillation Column Asia-Pac. J. Chem. Eng. 2011, 6, 338-348
9. Shin, J.; Lee, S.; Lee, J.; Lee, M. Manage Risks with Dividing-Wall Column Installations Hydrocarbon Process. 2011, 90, 59-62
10. Long, N.; Lee, M. Improvement of the Deethanizing and Depropanizing Fractionation Steps in NGL Recovery Process Using Dividing Wall Column J. Chem. Eng. Jpn. 2012, 45 (4) 1-10
11. Wright, R. O. Fractionation Apparatus. U.S. Patent 2,471,134, 1949.
12. Kaibel, G.; Schoenmakers, H. Process Synthesis and Design in Industrial Practice Proc. ESCAPE-12 2002, 9
13. Agrawal, R.; Fidkowski, Z. T. Are Thermally Coupled Distillation Columns Always Thermodynamically More Efficient for Ternary Distillations? Ind. Eng. Chem. Res. 1998, 37, 3444-3454
14. Wolff, E. A.; Skogestad, S. Operation of Integrated Three-Product (Petlyuk) Distillation Columns Ind. Eng. Chem. Res. 1995, 34, 2094-2103
15. Annakou; Meszaros, A.; Fonyo, Z.; Mizsey, P. Operability Investigation of Energy Integrated Distillation Schemes Hung. J. Ind. Chem. 1996, 24, 155-160
16. Mutalib, M. I. A.; Smith, R. Operation and Control of Dividing Wall Distillation Columns: Part 1 Trans. Inst. Chem. Eng. 1998, 76, 308-318
17. Hernández, S.; Jiménez, A. Controllability Analysis of Thermally Coupled Distillation Systems Ind. Eng. Chem. Res. 1999, 38, 3957-3963
18. Serra, M.; Perrier, M.; Espuna, A.; Puigjaner, L. Analysis of Different Control Possibilities for the Divided Wall Column: Feedback Diagonal and Dynamic Matrix Control Comput. Chem. Eng. 2001, 25, 859-866
19. Adrian, T.; Schoenmakers, H.; Boll, M. Model Predictive Control of Integrated Unit Operations: Control of A Divided Wall Column Chem. Eng. Process. 2004, 43, 347-355
20. Segovia-Hernández, J. G.; Hernández, S.; Ramírez, V. R.; Jiménez, A. A Comparison of the Feedback Control Behavior Between Thermally Coupled and Conventional Distillation Schemes Comput. Chem. Eng. 2004, 28, 811-819
21. Cho, Y.; Kim, B.; Kim, D.; Han, M.; Lee, M. Operation of Divided Wall Column with Vapor Sidedraw Using Profile Position Control J. Process Control. 2009, 19, 932-941
22. Mutalib, M. I. A.; Smith, R. Operation and Control of Dividing Wall Distillation Columns: Part 2 Trans. Inst. Chem. Eng. 1998, 76, 319-334
23. Joseph, B.; Brosilow, C. B. Inferential Control of Processes: Part I. Steady State Analysis and Design AIChE J. 1978, 24, 485-492
24. Fidkowski, Z.; Krolikowski, L. Minimum Energy Requirements of Thermally Coupled Distillation Systems AIChE J. 1987, 33, 643-653
25. Yu, C. C.; Luyben, W. L. Use of Multiple Temperatures for the Control of Multicomponent Distillation Columns Ind. Eng. Chem. Res. 1984, 23, 590-597
26. Lee, S.; Shamsuzzoha, M.; Han, M.; Kim, Y.; Lee, M. Study of the Structural Characteristics of a Divided Wall Column Using The Sloppy Distillation Arrangement Korean J. Chem. Eng. 2011, 28, 348-356
27. Tedder, D. W.; Rudd, D. F. Parametric Studies in Industrial Distillation. Part I. Design Comparisons AIChE J. 1978, 24, 303-315
28. Kister, H. Z. Distillation Operation; McGraw-Hill: New York, 1990.
29. Moore, C. F. Selection of Controlled and Manipulated Variables. Practical Distillation Control; Luyben, W. L., Ed.; Van Nostrand Reinhold: New York, Chapter 8, 1992; pp 140-177.
30. Bristol, E. H. On a New Measure of Interaction for Multivariable Process Control IEEE Trans. Autom. Control 1966, AC-11, 133-134
31. Deshpande, P. B. Multivariable Process Control; Instrument Society of America: Research Triangle Park, NC, 1989.
32. Niederlinski, A. A Heuristic Approach to the Design of Linear Multivariable Control System Automatica 1971, 7, 691-701
33. Astrom, K. J.; Hagglund, T. A Frequency Domain Method for Automatic Tuning of Simple Feedback Loops. Proceedings of the 23rd Conference on Decision and Control; IEEE: Las Vegas, NV, 1984; pp 299-304.
34. Lieberman, N. P.; Lieberman, E. T. Working Guide to Process Equipment, 2 nd ed.; McGraw-Hill: New York, 2003.
35. Kiss, A. A.; Bildea, C. S. A Control Perspective on Process Intensification in Dividing-Wall Columns Chem. Eng. Process. 2011, 50, 281-292