Separating an azeotropic mixture of toluene and ethanol via heat integration pressure swing distillation

Computers and Chemical Engineering

Volumn 76, Issue , 2015, Pages 137-149

  Zhu, Zhaoyou ^a   Wang, Lili ^a   Ma, Yixin ^a   Wang, Wanling ^a   Wang, Yinglong ^a  

^a QINGDAO UNIVERSITY OF SCIENCE AND TECHNOLOGY   (China)

Author keywords

Dynamic simulation; Ethanol; Heat integration; Pressure swing distillation; Toluene

Indexed keywords

AZEOTROPES; CASCADE CONTROL SYSTEMS; COMPUTER SIMULATION; DISTILLATION; ETHANOL; TOLUENE;

AZEOTROPIC MIXTURE; CASCADE CONTROL STRUCTURE; COMPENSATED TEMPERATURE; HEAT INTEGRATION; MINIMUM BOILING AZEOTROPES; OBJECTIVE FUNCTIONS; PRESSURE SWING DISTILLATION; STEADY-STATE SIMULATIONS;

INTEGRATION;

EID: 84924984983     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.compchemeng.2015.02.016     Document Type: Article

References (35)

1. Abu-Eishah S.I., Luyben W.L. Design and control of a two-column azeotropic distillation system. Ind Eng Chem Process Des Dev 1985, 24:132-140.
2. Arifin S., Chien I.-L. Design and control of an isopropyl alcohol dehydration process via extractive distillation using dimethyl sulfoxide as an entrainer. Ind Eng Chem Res 2008, 47:790-803.
3. Chiang T.P., Luyben W.L. Comparison of the dynamic performances of three heat integration distillation configurations. Ind Eng Chem Res 1988, 27:99-104.
4. Chien I., Zeng K.-L., Chao H.-Y., Hong Liu J. Design and control of acetic acid dehydration system via heterogeneous azeotropic distillation. Chem Eng Sci 2004, 59:4547-4550.
5. Douglas J.M. Conceptual design of chemical processes 1988.
6. Fanaei Shykholeslami M.A. Dynamic simulation and control of vapor recompression column. J Math 2011.
7. Gil I.D., Botia D.C., Ortiz P., Sanchez O.F. Extractive distillation of acetone/methanol mixture using water as entrainer. Ind Eng Chem Res 2009, 48:4858-4860.
8. Hosgor E., Kucuk T., Oksal I.N., Kaymak D.B. Design and control of distillation processes for methanol-chloroform separation. Comput Chem Eng 2014, 67:166-177.
9. Huang K., Shan L., Zhu Q., Qian J. Design and control of an ideal heat integration distillation column (ideal HIDiC) system separating a close-boiling ternary mixture. Energy 2007, 32:2148-2150.
10. Kaushik V. Dynamics and control of distillation using Aspen 2011.
11. Knapp J.P., Doherty M.F. A new pressure-swing-distillation process for separating homogeneous azeotropic mixtures. Ind Eng Chem Res 1992, 31:346-357.
12. Langston P., Hilal N., Shingfield S., Webb S. Simulation and optimisation of extractive distillation with water as solvent. Chem Eng Process: Process Intensif 2005, 44:345-351.
13. Li W., Shi L., Yu B., Xia M., Luo J., Shi H., Xu C. New pressure-swing distillation for separating pressure-insensitive maximum boiling azeotrope via introducing a heavy entrainer: design and control. Ind Eng Chem Res 2013, 52:7836-7840.
14. Ling H., Luyben W.L. New control structure for divided-wall columns. Ind Eng Chem Res 2009, 48:6034-6040.
15. Luo H., Liang K., Li W., Li Y., Xia M., Xu C. Comparison of pressure-swing distillation and extractive distillation methods for isopropyl alcohol/diisopropyl ether separation. Ind Eng Chem Res 2014, 53:15167-15170.
16. Luyben W.L. Plantwide control of an isopropyl alcohol dehydration process. AIChE J 2006, 52:2290-2300.
17. Luyben W.L. Comparison of extractive distillation and pressure-swing distillation for acetone-methanol separation. Ind Eng Chem Res 2008, 47:2696-2700.
18. Luyben W.L. Control of the maximum-boiling acetone/chloroform azeotropic distillation system. Ind Eng Chem Res 2008, 47:6140-6150.
19. Luyben W.L. Design and control of a fully heat integration pressure-swing azeotropic distillation system. Ind Eng Chem Res 2008, 47:2681-2690.
20. Luyben W.L. Pressure-swing distillation for minimum-and maximum-boiling homogeneous azeotropes. Ind Eng Chem Res 2012, 51:10881-10890.
21. Luyben W.L. Distillation design and control using Aspen simulation 2013, John Wiley & Sons.
22. Luyben W.L., Chien I. Dynamics and control in aspen dynamics. Design and control of distillation systems for separating azeotropes 2010, 97-145.
23. Luyben W.L., Chien I. Maximum-boiling azeotropes. Design and control of distillation systems for separating azeotropes 2010, 369-383.
24. Luyben W.L., Chien I. Pressure-swing azeotropic distillation. Design and control of distillation systems for separating azeotropes 2010, 149-164.
25. Luyben W.L., Chien I.-L. Design and control of distillation systems for separating azeotropes 2011, John Wiley & Sons.
26. Munoz R., Monton J., Burguet M., de la Torre J. Separation of isobutyl alcohol and isobutyl acetate by extractive distillation and pressure-swing distillation: simulation and optimization. Sep Purif Technol 2006, 50:175-183.
27. Nakaiwa M., Huang K., Endo A., Ohmori T., Akiya T., Takamatsu T. Internally heat integration distillation columns: a review. Chem Eng Res Des 2003, 81:162-177.
28. Orchillés A.V., Miguel P.J., Vercher E., Martínez-Andreu A. Using 1-ethyl-3-methylimidazolium trifluoromethanesulfonate as an entrainer for the extractive distillation of ethanol+water mixtures. J Chem Eng Data 2009, 55:1669-1670.
29. Ross R., Perkins J., Pistikopoulos E., Koot G., Van Schijndel J. Optimal design and control of a high-purity industrial distillation system. Comput Chem Eng 2001, 25:141-150.
30. Sorensen J. Heat integration distillation. Google Patents 2001.
31. Suphanit B. Optimal heat distribution in the internally heat integration distillation column (HIDiC). Energy 2011, 36:4171-4180.
32. Wang Y., Cui P., Zhang Z. Heat integration pressure-swing-distillation process for separation of tetrahydrofuran/methanol with different feed compositions. Ind Eng Chem Res 2014, 53:7186-7190.
33. Wei H.-M., Wang F., Zhang J.-L., Liao B., Zhao N., Xiao F.-k., Wei W., Sun Y.-H. Design and control of dimethyl carbonate-methanol separation via pressure-swing distillation. Ind Eng Chem Res 2013, 52:11463-11470.
34. Xu S., Wang H. A new entrainer for separation of tetrahydrofuran-water azeotropic mixture by extractive distillation. Chem Eng Process: Process Intensif 2006, 45:954-958.
35. Xu S., Wang H. Separation of tetrahydrofuran-water azeotropic mixture by batch extractive distillation process. Chem Eng Res Des 2006, 84:478-482.