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Separation of water – formic acid – acetic acid mixtures in the presence of sulfolane

https://doi.org/10.32362/2410-6593-2019-14-4-24-32

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Abstract

In this paper, extractive distillation flowsheets for water–formic acid–acetic acid mixtures were designed. Flowsheets not involving preliminary dehydration were considered, and the relative volatilities of the components in the presence of sulfolane were analyzed. The result of extractive distillation depends on the amount of sulfolane. The structure of the flowsheet is determined by the results of the basic ternary mixture extractive distillation. In three-column flowsheets (schemes I, II), water is isolated in the distillate of the extractive distillation column. In the second column, distillation of the formic acid–acetic acid–sulfolane mixture is carried out, yielding formic acid (90 wt %) and acetic acid (80 wt %). The recycled flow is returned to the first column. Dilution of the formic acid–acetic acid–sulfolane mixture with sulfolane (second column of flowsheet II) allows for acids of higher quality (main substance content equal to or more than 98.5 wt %) to be obtained. Flowsheet III includes four columns and two recycling stages. First, the water–formic acid mixture is isolated in the distillate of the extractive distillation column. Then, water and formic acid are separated in a two-column complex by extractive distillation, also with sulfolane. We were carrying out calculations for column working pressure 101.32 and 13.33 kPa. To prevent thermal decomposition of sulfolane, working pressure for regeneration columns was always 13.33 kPa. The extractive distillation column of the basic three-component mixture is the main factor contributing to the total energy consumption for separation (in all schemes).

About the Authors

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

Cand. of Sci. (Engineering), Associate Professor of the Chair of Chemistry and Technology of Basic Organic Synthesis

86, Vernadskogo pr., Moscow, 119571, Russia

Scopus Author ID 6602836975

ResearcherID C-8812-2014


Competing Interests: Авторы заявляют об отсутствии конфликта интересов.


O. V. Gromova
MIREA – Russian Technological University (M.V. Lomonosov Institute of Fine Chemical Technologies)
Russian Federation

Master, Chair of Chemistry and Technology of Basic Organic Synthesis

86, Vernadskogo pr., Moscow, 119571, Russia


Competing Interests: Авторы заявляют об отсутствии конфликта интересов.


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55. Gayle A.A., Somov V.Ye., Varshavskiy O.M., Semenov L.V. Sulfolan: Properties and use as a selective solvent. Saint-Petersburg: Khimizdat Publ., 1998. 144 p. (in Russ.).

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58. Raeva V.M. Features of the behavior of azeotropic mixtures and their separation with varying pressure: thesis ... Cand. of Sci. (Engineering). Moscow, 1998. 168 p. (in Russ.).

59. Raeva V.M., Frolkova A.K. Separation of azeotropic mixtures using pressure-based complexes. Russian Journal of General Chemistry. 1998;XLII(6):76- 88 (in Russ.).

60. Bates R.G., Pawlak Z. Solvent effects on acid-base behavior: Five uncharged acids in water-sulfolane solvents. J. Solution Chem. 1976;5(3):213-222. https://doi.org/10.1007/BF00654338


Supplementary files

1. Fig. 1. The diagram of the vapor−liquid equilibrium (VLE) for the water (W)−formic acid (FA)−acetic acid (AA) system. Black line – 13.33 kPa; grey line – 101.32 kPa
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Raeva V.M., Gromova O.V. Separation of water – formic acid – acetic acid mixtures in the presence of sulfolane. Fine Chemical Technologies. 2019;14(4):24-32. https://doi.org/10.32362/2410-6593-2019-14-4-24-32

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