Feed Preconditioning Targets for Distillation through Invariant Rectifying-Stripping Curves

Industrial and Engineering Chemistry Research

Volumn 42, Issue 26, 2003, Pages 6851-6861

  Bandyopadhyay, Santanu ^a   Malik, Ranjan K ^a   Shenoy, Uday V ^a  

^a INDIAN INSTITUTE OF TECHNOLOGY BOMBAY   (India)

Author keywords

[No Author keywords available]

Indexed keywords

COMPUTER SIMULATION; DISTILLATION; DISTILLATION COLUMNS; ENTHALPY; GRAPHIC METHODS; THERMODYNAMIC PROPERTIES;

UTILITY PARTITIONING CURVES (UPC);

ENGINEERING RESEARCH;

BENZENE; TOLUENE;

DISTILLATION; INDUSTRIAL APPLICATION; MATHEMATICAL METHOD; PROCESS CONTROL;

ARTICLE; BOILER; CHEMICAL ENGINEERING; DISTILLATION; ENTHALPY; MATHEMATICAL ANALYSIS; SIMULATION; TEMPERATURE; THERMODYNAMICS;

EID: 0348167650     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie020894r     Document Type: Article

References (32)

1. Peterson, W. C.; Wells, T. A. Energy-Saving Schemes in Distillation. Chem. Eng. 1977, 84, 78.
2. Liebert, T. Distillation Feed Preheat - Is It Energy Efficient? Hydrocarbon Process. 1993, 37.
3. Naka, Y.; Terashita, M.; Hayashiguchi, S.; Takamatsu, T. An Intermediate Heating and Cooling Method for a Distillation Column. J. Chem. Eng. Jpn. 1980, 13, 123.
4. Terranova, B. E.; Westerberg, A. W. Temperature-Heat Diagrams for Complex Columns. 1. Intercooled/Interheated Distillation Columns. Ind. Eng. Chem. Res. 1989, 28, 1374.
5. Dhole, V. R.; Linnhoff, B. Distillation Column Targets. Comput. Chem. Eng. 1993, 17, 549.
6. Shenoy, U. V. Heat Exchanger Network Synthesis: Process Optimization by Energy and Resource Analysis; Gulf Publishing Co.: Houston, 1995.
7. Ognisty, T. P. Analyze Distillation Columns with Thermodynamics. Chem. Eng. Prog. 1995, 40.
8. Hall, S. G.; Ognisty, T. P.; Northup, A. H. Use Process Integration to Improve FCC/VRU Design. Part 1. Hydrocarbon Process. 1995, 63.
9. Trivedi, K. K.; Pang, K. H.; O'Young, D. L.; Klavers, H. W.; Linnhoff, B. Optimize a Licensor's Design Using Pinch Technology. Hydrocarbon Process. 1996, 113.
10. Bandyopadhyay, S.; Malik, R. K.; Shenoy, U. V. Temperature-Enthalpy Curve for Energy Targeting of Distillation Columns. Comput. Chem. Eng. 1998, 22, 1733.
11. Bandyopadhyay, S.; Malik, R. K.; Shenoy, U. V. Invariant Rectifying-Stripping Curves for Targeting Minimum Energy and Feed Location in Distillation. Comput. Chem. Eng. 1999, 23, 1109.
12. Bandyopadhyay, S. Effect of Feed on Optimal Thermodynamic Performance of a Distillation Column. Chem. Eng. J. 2002, 88, 175.
13. Benedict, M. Multistage Separation Processes. Trans. AIChE 1947, 43, 41.
14. Fonyó, Z. Thermodynamic Analysis of Rectification. I. Reversible Model of Rectification. Int. Chem. Eng. 1974, 14, 18.
15. Fitzmorris, R. E.; Mah, R. S. H. Improving Distillation Column Design Using Thermodynamic Availability Analysis. AIChE J. 1980, 26, 265.
16. King, C. J. Separation Processes; McGraw-Hill: New York, 1980.
17. Ho, F. G.; Keller, G. E. Process Integration. In Recent Developments in Chemical Process and Plant Design; Liu, Y. A., McGee, H. A., Epperly, W. G., Eds.; Wiley: New York, 1987.
18. Franklin, N. L.; Wilkinson, M. B. Reversibility in the Separation of Multicomponent Mixtures. Trans. Inst. Chem Eng. (Part A) 1982, 60, 276.
19. Rajah, W.; Polley, G. T. Synthesis of Practical Distillation Schemes. Trans. Inst. Chem. Eng. 1995, 73, 953.
20. Bandyopadhyay, S. Energy Targeting for Optimisation of Distillation Processes. Ph.D. Thesis, Indian Institute of Technology, Bombay, 1999.
21. Koehler, J.; Aguirre, P.; Blass, E. Minimum Reflux Calculations for Nonideal Mixtures Using the Reversible Distillation Model. Chem. Eng. Sci. 1991, 46, 3007.
22. Gilliland, E. R. Multicomponent Rectification: Estimation of Number of Theoretical Plates as a Function of Reflux Ratio. Ind. Eng. Chem. 1940, 32, 1220.
23. Robinson, C. S.; Gilliland, E. R. Elements of Fractional Distillation, 4th ed.; McGraw-Hill: New York, 1950.
24. Guerreri, G. Short-cut Distillation Design: Beware! Hydrocarbon Process. 1969, 48, 137.
25. Donnell, J. W.; Cooper, C. M. Plates vs Vapor Rates-By a Quick Simple Method. Chem. Eng. 1950, 57, 121.
26. PRO/II, Version 4.1, Simulation Sciences, Inc., Brea, CA, 1994-95.
27. Stupin, W. J.; Lockhart, F. J. The Distribution of Non-Key Component in Multicomponent Distillation. Paper presented at the AIChE annual meeting, Los Angeles, Dec 1968.
28. Johnson, J. E.; Morgan, D. J. Graphical Techniques for Process Engineering. Chem. Eng. 1985, July 8, 72.
29. Campagne, W. v. L. Use Ponchon-Savarit in Your Process Simulation. Hydrocarbon Process. 1993, 41.
30. Agrawal, R.; Herron, D. M. Optimal Thermodynamic Feed Conditions for Distillation of Ideal Binary Mixtures. AIChE J. 1997, 43, 2984.
31. Linnhoff, B.; Townsend, D. W.; Boland, D.; Hewitt, G. F.; Thomas, B. E. A.; Guy, A. R.; Marsland, R. H. User Guide on Process Integration for the Efficient Use of Energy; The Institution of Chemical Engineers: Rugby, UK, 1982.
32. Shenoy, U. V.; Sinha, A.; Bandyopadhyay, S. Multiple Utilities Targeting for Heat Exchanger Networks. Trans. Inst. Chem Eng. (Part A) 1998, 76, 259.