Methods of Optimization Thermodynamics in Distillation Processes

A. M. Tsirlin; Цирлин А. М.; A. I. Balunov; Балунов А. И.; I. A. Sukin; Сукин И. А.; A. M. Vasilyev; Васильев А. М.

doi:10.31857/S0040357123040164

Methods of Optimization Thermodynamics in Distillation Processes

Authors: Tsirlin A.M.¹, Balunov A.I.¹, Sukin I.A.¹, Vasilyev A.M.¹
Affiliations:
1. Ailamazyan Institute of Program Systems, Russian Academy of Sciences
Issue: Vol 57, No 4 (2023)
Pages: 467-478
Section: Articles
Published: 01.07.2023
URL: https://rjmseer.com/0040-3571/article/view/652877
DOI: https://doi.org/10.31857/S0040357123040164
EDN: https://elibrary.ru/VKFXLF
ID: 652877

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Abstract
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Abstract

The methodology of optimization thermodynamics was used for the mathematical description and optimization of distillation processes. The following problems were considered: construction of a set of feasible operating conditions of columns separating binary and multicomponent mixtures, selection of the sequence of separation of a multicomponent mixture, feasibility of using a separating agent, selection of the feed temperature and feed point, and optimization of parallel and sequential systems of distillation columns. Calculation formulas for entropy production and heat transfer coefficients in the reboiler and reflux condenser of the column were obtained.

Keywords

distillation, thermal efficiency, close-cut separation, maximum performance, minimum heat consumption

References

Новиков И.И. Эффективный коэффициент полезного действия атомной энергетической установки // Атомная энергия. 1957. № 11. С. 409–412.
Curzon F.L., Ahlborn B. Efficiency of a Carnot engine at maximum power output // Am. J. Phys., 1975. V. 43. № 22. P. 22–24.
Berry R.S., Kasakov V.A., Sieniutycz S., Szwast Z., Tsirlin A.M. Thermodynamic Optimization of Finite Time Processes. Chichester: Wiley, 1999.
Chen L., Wu C., Sun F. Finite time thermodynamic optimization or entropy generation minimization of energy systems // J. Non-Equilib. Thermodyn., 1999. V. 24. P. 327–359.
Tsirlin A.M., Mironova V.A., Amelkin S.A., Kazakov V.A. Finite-time thermodynamics: Conditions of minimal dissipation for thermodynamic process with given rate // Phys. Rev. E., 1998. V. 58. № 1. P. 215–223.
Гельперин Н.И. Основные процессы и аппараты химической технологии. М.: Химия, 1981. 384 с.
Петлюк Ф.Б., Серафимов Л.А. Многокомпонентная ректификация. Теория и расчет. М.: Химия, 1983.
Балунов А.И., Майков В.П. Энтропия и информация в теории ректификации // Известия ВУЗов: Химия и химическая технология, 2003. Т. 46. № 9. С. 54–67.
Плановский А.Н., Николаев П.И. Процессы и аппараты химической и нефтехимической технологии. М.: Химия, 1987. 400 с.
Holland C.D. Fundamentals of Multicomponent Distillation. McGraw-Hill, 1981.
Kister H.Z. Distillation Design. New York: McGraw-Hill, 1992.
Tsirlin A.M., Balunov A.I., Sukin I.A. Estimates of energy consumption and selection of optimal distillation sequence for multicomponent distillation // Theor. Found. Chem. Eng., 2016. V. 50. № 3. P. 258–267.
Tsirlin A.M., Sukin I.A., Balunov A.I., Schwalbe K. The Rule of Temperature Coefficients for Selection of Optimal Separation Sequence for Multicomponent Mixtures in Thermal Systems // J. Non-Equilib. Thermodyn, 2017. V. 42. № 4. P. 359–369.
Tsirlin A.M., Mazikov A.A. Thermodynamic indicators of the perfection of heat exchange systems // J. Eng. Phys. Thermophys., 2023. V. 96. № 3. P. 516–531.
Розоноэр Л.И., Цирлин А.М. Оптимальное управление термодинамическими системами // Автоматика и телемеханика, 1983. № 1. С. 70–79; № 2. С. 88–101; № 3. С. 50–64.
Zaeva M.A., Tsirlin A.M., Sukin I.A. Influence of the Kinetics of Heat and Mass Transfer in a Binary-Rectification Column on the Realizability Range of its Regimes // J. Eng. Phys. Thermophys., 2018. V. 91. P. 515–530.
Зиятдинов Н.Н., Островский Г.М., Емельянов И.И. Построение системы теплообмена при реконструкции и синтезе оптимальных систем ректификационных колонн // Теоретические основы химической технологии. 2016. Т. 50. № 2. С. 184–193.