Preview

Fine Chemical Technologies

Advanced search

SELECTION OF EXTRACTIVE AGENTS FOR THE SEPARATION OF CHLOROFORM - METHANOL - TETRAHYDROFURAN MIXTURE

https://doi.org/10.32362/24106593-2018-13-3-30-40

Abstract

Variants of the extractive distillation of chloroform - methanol - tetrahydrofuran equimolar mixture with industrial separating agents are considered. The basic system shows opposite deviations from the ideal behavior, because it contains binary azeotropes with minimum and maximum boiling points (3.3.1-4 system according to Serafimov’s classification). The choice of selective substances for extractive distillation was carried out taking into account the concentration dependences of the excess molar Gibbs energy of the binary constituents of the derivative system “chloroform - methanol - tetrahydrofuran - industrial test agent (ethylene glycol (EG), dimethyl sulfoxide (DMSO), N-methylpyrrolidone (N-MP))” at 101.32 kPa. Based on the results of the evaluation of the thermodynamic criterion, DMSO and N-MP are recommended. Both agents show selective effect when separating two binary constituents. EG is selective only with respect to chloroform-tetrahydrofuran mixture. Since the tested agents show different selective effects, the final agent choice determines the qualitative composition of the product flows in the column for the extractive distillation of the three-component mixture (the first column of the flowsheet) and, accordingly, the structure of the total flowsheet. The schemes consist of two two-column complexes for extractive distillation (for the basic three-component mixture and for the binary mixture). The maximum contribution to the total reboiler energy consumption of the distillation columns is made by the first extractive distillation column: 65% (EG), 53% (N-MP) and 24% (DMSO). The use of the most selective agent reduces the energy consumption of this column: the reboiler load is maximal in the case of EG, in comparison with which the load is 47% lower in the case of N-MP and 76% lower in the case of DMSO.

About the Authors

V. M. Raeva
MIREA - Russian Technological University (M.V. Lomonosov Institute of Fine Chemical Technologies)
Russian Federation

Ph.D. (Eng.), Associate Professor, Chair of Chemistry and Technology of Basic Organic Synthesis

86, Vernadskogo Pr., Moscow 119571, Russia



D. I. Sukhov
MIREA - Russian Technological University (M.V. Lomonosov Institute of Fine Chemical Technologies)
Russian Federation

2nd-year student of the Master's Degree, Chair of Chemistry and Technology of Basic Organic Synthesis

86, Vernadskogo Pr., Moscow 119571, Russia



References

1. Momoh S.O. Assessing the accuracy of selectivity as a basis for solvent screening in extractive distillation processes. Sep. Sci. & Technol. 1991; 26(5): 729-742.

2. Zhigang Lei, Chengyue Li, Biaohua Chen. Extractive distillation: a review. Sep. & Purif. Rev. 2003; 32(2): 121-213.

3. Frolkova A.K. Separation of azeotropic mixtures. Physicochemical basis and technological methods. M.: Humanitarian Publishing Center “VLADOS”, 2010. 192 p. (in Russ.)

4. Anokhina E.А. Energy saving in the processes of extractive rectification. Vestnik MITHT (Fine Chemical Technologies). 2013; 8(5): 3-19. (in Russ.)

5. Berg L., Yeh An-I. The separation of isopropyl ether from methyl ethyl ketone by extractive distillation. Chem. Eng. Comm. 1984; 29(1-6): 283-289.

6. Berg L., Vosburgh M.G., Christensen R.W., Shanahan M.J. The separation of lower boiling alcohols by extractive distillation. Chem. Eng. Comm. 1988; 61(1): 1-21.

7. Yeh An-I., Berg L., Warren K.J. The separation of acetone - methanol mixture by extractive distillation. Chem. Eng. Comm. 1988; 68(1): 69-79.

8. Myul´khi E.P., Khristenko M.S., Andryukhova M.V. Choice of extractive separating agent for the 1-pentanol-cyclohexanone binary mixture. Russ. J. Appl. Chem. 2006; 79(7): 1076-1082.

9. Xu S., Wang H. A new entrainer for separation of tetrahydrofuran - water azeotropic mixture by extractive distillation. Chem. Eng. & Proc. 2006; 45(11): 954-958.

10. Jyun-Yang Yao, Sheng-Yu Lin, I-Lung Chien. Operation and control of batch extractive distillation for the separation of mixtures with minimum-boiling azeotrope. J. Chin. Instit. Chem. Eng. 2007; 38: 371-383.

11. Gómez P., Gil I. Simulation of the tetrahydrofuran dehydration process by extractive distillation in Aspen Plus. Latin Amer. Appl. Res. 2009; 39(4): 275-284.

12. Lek-Utaiwan P., Suphanit B., Douglas P.L., Mongkolsiri N. Design of extractive distillation for the separation of close-boiling mixtures: Solvent selection and column optimization. Comp. & Chem. Eng. 2011; 35(6): 1088-1100.

13. Zhang Z., Huang D., Lv M., Jia P., Sun D., Li W. Entrainer selection for separating tetrahydrofuran/water azeotropic mixture by extractive distillation. Sep.& Purif. Technol. 2014; 122: 73-77.

14. Raeva V.М., Capranova А.S. Comparison efficiency of extractive agents at the separation of mixture acetone - methanol. Khimicheskaya promyshlennost’ segodnya = Chemical Industry Today. 2015; 3: 33-46. (in Russ.)

15. Sazonova A.Yu., Raeva V.M. Recovery of acetonitrile from aqueous solutions by extractive distillation – Effect of entrainer. Int. J. Chem., Nucl., Metallurg. & Mat. Eng. 2015; 9(2): 195-198.

16. Gromova О.V., Gutencov V.S., Rayeva V.М. Extraction distillation of binary mixtures with maximum boiling azeotropes. Vestnik nauki i obrazovaniyа = Bulletin of Science and Education. 2016; 5(9(17)): 8-14. (in Russ.)

17. Berg L., An-I Yeh, Ratanapupech P. The recovery of ethyl acetate by extractive distillation. Chem. Eng. Comm. 1985; 39(1-6): 193-199.

18. Berg L., Vosburgh M.G. Separation of isopropanol from isopropyl acetate and water by extractive distillation: pat. 786,629 USA. № 4,666,560; filled 11.10.1985; publ. 19.05.1987.

19. Berg L., Vosburgh M. G. Separation of isopropanol from isopropyl acetate by extractive distillation: pat. 19,423 USA. № 4,718,989; filled 26.02.1987; publ. 12.01.1988.

20. Berg L., An-I Yeh. Separation of isopropyl acetate from isopropanol by extractive distillation: pat. 869,733 USA. № 4,826,576; filled 2.06.1986; publ. 2.05.1989.

21. Berg L. Separation of ethanol, isopropanol and water mixtures by extractive distillation: pat. 845,107 USA. № 5,800,681; filled 21.04.1997; publ. 1.09.1998.

22. Berg L., An-I Yeh. Separation of n-butyl acetate from n-butanol by extractive distillation: pat. 608,071 USA. № 4,507,176; filled 7.05.1984; publ. 26.03.1985.

23. Berg L., An-I Yeh. Separation of n-butyl acetate from n-butanol by extractive distillation: pat. 608,040 USA. № 4,525,245; filled. 7.05.1984; publ. 25.06.1985.

24. Berg L., An-I Yeh. Separation of isobutyl acetate from isobutanol by extractive distillation: pat. 709,415 USA. № 4,642,167; filled 7.03.1985; publ. 10.02.1987.

25. Berg L., An-I Yeh. Separation of isobutyl acetate from isobutanol by extractive distillation: pat. 878,787 USA. № 4,724,049; filled 26.06.1986; publ. 9.02.1988.

26. Berg L., An-I Yeh. Separation of isopropyl ether from isopropanol and water by extractive distillation: pat. 800,155 USA. № 4,666,563; filled 20.11.1985; publ. 19.05.1987.

27. Dolmatov B.B., Timoshenko A.V., Volkov А.G., Anokhina E.А. Areas of energy optimality of the schemes of extractive rectification of a mixture of methanol-npropyl acetate-toluene and aniline. Vestnik MITHT (Fine Chemical Technologies). 2009; 4(5): 60-68. (in Russ.)

28. Honghai Wang, Xiaoying Cui, Chunli Li, Jing Fang. Separation of ethyl acetate - dichloromethane - ethanol by extractive distillation: simulation and optimization. Chem. Eng. Technol. 2013; 36(4): 627-634.

29. Benyounes Н., Frolkova A.K. Аspects of multicomponent mixture separation in the presence of selective solvents. Chem. Eng. Comm. 2010; 197(7): 901-918.

30. Raeva V.M., Sazonova A.Yu. Separation of ternary mixtures by extractive distillation with 1,2-ethandiol and glycerol. Chem. Eng. Res. Design. 2015; 99: 125-131.

31. Sazonova A.Yu. Selection of separating agents and patterns of extractive rectification of mixtures of organic products: Ph.D. (Eng.) Thesis. Moscow, 2015. 225 p. (in Russ.)

32. Raeva V.M., Sazonova A.Yu., Frolkova A.K. Synergetic effect of binary separating agents in extractive rectification of homogeneous mixtures. Theoretical Foundations of Chemical Engineering. 2013; 47(5): 649-659.

33. Zhigang Zhang, Ming Lv, Donghao Huang [et al.]. Isobaric vapor–liquid equilibrium for the extractive distillation of acetonitrile + water mixtures using dimethyl sulfoxide at 101.3 kPa. J. Chem. Eng. Data. 2013; 58(12): 3364-3369.

34. Luyben W.L. Control of the maximum boiling acetone/chloroform azeotropic distillation system. Ind. Eng. Chem. Res. 2008; 47(16): 6140-6149.

35. Luyben W.L. Effect of solvent on controllability in extractive distillation. Ind. Eng. Chem. Res. 2008; 47(13): 4425-4439.

36. Gayle А.А., Zalishevskiy G.D. N-Methylpyrrolidone. Preparation, properties and use as a selective solvent. SaintPetersburg: Khimizdat Publ., 2005. 704 р. (in Russ.)

37. Kirk-Othmer Encyclopedia of Chemical Technology. Vol. 8. 5th Edition. John Wiley and Sons, 2004. 880 p.

38. Kogan V.B. Azeotropic and extractive rectification. Leningrad: Khimiya Publ., 1971. 439 p. (in Russ.)

39. Sazonova А.Yu., Raeva V.M., Chelyuskina Т.V., Frolkova А.K. The choice of extractive agents for the separation of a biazeotropic mixture of benzene - perfluorobenzene based on the thermodynamic criterion. Teoreticheskie osnovy khimicheskoy tekhnologii = Theoretical Foundations of Chemical Engineering. 2014; 48(2) 163-172. (in Russ.)


Review

For citations:


Raeva V.M., Sukhov D.I. SELECTION OF EXTRACTIVE AGENTS FOR THE SEPARATION OF CHLOROFORM - METHANOL - TETRAHYDROFURAN MIXTURE. Fine Chemical Technologies. 2018;13(3):30-40. (In Russ.) https://doi.org/10.32362/24106593-2018-13-3-30-40

Views: 1045


ISSN 2410-6593 (Print)
ISSN 2686-7575 (Online)