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<article article-type="research-article" dtd-version="1.3" xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xml:lang="en"><front><journal-meta><journal-id journal-id-type="publisher-id">chemicallytech</journal-id><journal-title-group><journal-title xml:lang="en">Fine Chemical Technologies</journal-title><trans-title-group xml:lang="ru"><trans-title>Тонкие химические технологии</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">2410-6593</issn><issn pub-type="epub">2686-7575</issn><publisher><publisher-name>MIREA – Russian Technological University (RTU MIREA).</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.32362/2410-6593-2025-20-5-407-429</article-id><article-id custom-type="edn" pub-id-type="custom">AEQBMZ</article-id><article-id custom-type="elpub" pub-id-type="custom">chemicallytech-2299</article-id><article-categories><subj-group subj-group-type="heading"><subject>Research Article</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>THEORETICAL BASIS OF CHEMICAL TECHNOLOGY</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="ru"><subject>ТЕОРЕТИЧЕСКИЕ ОСНОВЫ ХИМИЧЕСКОЙ ТЕХНОЛОГИИ</subject></subj-group></article-categories><title-group><article-title>Comparative analysis of liquid mixture separation flowsheets</article-title><trans-title-group xml:lang="ru"><trans-title>Сравнительный анализ схем разделения жидких смесей, основанных на различных процессах и методах</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0001-5675-5777</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Фролкова</surname><given-names>А. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Frolkova</surname><given-names>A. V.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Фролкова Анастасия Валериевна, д.т.н., доцент, профессор кафедры химии и технологии основного органического синтеза,</p><p>119454, Москва, пр-т Вернадского, д. 78</p><p>Scopus Author ID 12782832700, ResearcherID N-4517-2014</p></bio><bio xml:lang="en"><p>Anastasiya V. Frolkova, Dr.Sci. (Eng.), Professor, Department of Chemistry and Technology of Basic Organic Synthesis</p><p>78, Vernadskogo pr., Moscow, 119454</p><p>Scopus Author ID 12782832700, ResearcherID N-4517-2014</p></bio><email xlink:type="simple">frolkova_nastya@mail.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0009-0008-1637-8266</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Новрузова</surname><given-names>А. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Novruzova</surname><given-names>A. N.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Новрузова Альбина Назимовна, аспирант, кафедра химии и технологии основного органического синтеза,</p><p>119454, Москва, пр-т Вернадского, д. 78</p></bio><bio xml:lang="en"><p>Albina N. Novruzova, Postgraduate Student, Department of Chemistry and Technology of Basic Organic Synthesis</p><p>78, Vernadskogo pr., Moscow, 119454</p></bio><email xlink:type="simple">albina.novruzova2018@yandex.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>МИРЭА – Российский технологический университет (Институт тонких химических технологий им. М.В. Ломоносова)</institution><country>Россия</country></aff><aff xml:lang="en"><institution>MIREA – Russian Technological University (Lomonosov Institute of Fine Chemical Technologies)</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2025</year></pub-date><pub-date pub-type="epub"><day>07</day><month>11</month><year>2025</year></pub-date><volume>20</volume><issue>5</issue><fpage>407</fpage><lpage>429</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Frolkova A.V., Novruzova A.N., 2025</copyright-statement><copyright-year>2025</copyright-year><copyright-holder xml:lang="ru">Фролкова А.В., Новрузова А.Н.</copyright-holder><copyright-holder xml:lang="en">Frolkova A.V., Novruzova A.N.</copyright-holder><license xml:lang="ru" license-type="creative-commons-attribution" xlink:href="https://creativecommons.org/licenses/by/4.0/" xlink:type="simple"><license-p>Данная работа распространяется под лицензией Creative Commons Attribution 4.0.</license-p></license><license xml:lang="en" license-type="creative-commons-attribution" xlink:href="https://creativecommons.org/licenses/by/4.0/" xlink:type="simple"><license-p>This work is licensed under a Creative Commons Attribution 4.0 License.</license-p></license></permissions><self-uri xlink:href="https://www.finechem-mirea.ru/jour/article/view/2299">https://www.finechem-mirea.ru/jour/article/view/2299</self-uri><abstract><sec><title>Objectives</title><p>Objectives. When developing separation flowsheets for liquid mixtures, preference is often given to a specific process or flowsheet. Although alternative separation variants are sometimes considered, these tend to be based on a single-phase process, usually distillation. And while review papers on the specifics of implementing a particular separation technique exist, these mainly focus on the specific process of extractive distillation, combination of distillation and splitting processes, and extraction. Moreover, studies comparing the separation flowsheets of mixtures of different physicochemical nature based on different processes and special methods are fragmentary. This study presents a comparative analysis of the processes and methods of liquid mixtures separation based on a critical review of the literature and the authors’ own research results.</p></sec><sec><title>Methods</title><p>Methods. The study is based on the critical analysis of literature and mathematical modeling of phase equilibria using local composition equations via freely distributed software packages.</p></sec><sec><title>Results</title><p>Results. Specific liquid mixture separation methods, including combining various processes in one flowsheet (including hybrid technologies), are compared in terms of their advantages and disadvantages.</p></sec><sec><title>Conclusions</title><p>Conclusions. Promising areas of further research in the field of synthesis of organic mixtures separation flowsheets through the use of various separation processes and methods are identified. The effectiveness of the various processes (extraction, splitting, special distillation techniques) is estimated at different stages of different number of components mixtures separation. A comparative analysis of extractive and heteroazeotropic distillation processes when separating mixtures of different initial composition highlights the areas of energy advantage of each process. The effectiveness of the flowsheets is estimated by combining extraction with other processes, depending on the stage of extractant regeneration.</p></sec></abstract><trans-abstract xml:lang="ru"><sec><title>Цели</title><p>Цели. При разработке схем разделения жидких смесей часто отдается предпочтение конкретному процессу или схеме. В редких случаях рассматривается не один, а несколько альтернативных вариантов разделения, чаще основанных на одном фазовом процессе, как правило, ректификации. Имеющиеся на сегодня обзорные работы по особенностям реализации того или иного приема разделения сконцентрированы на конкретном процессе: экстрактивная ректификация, сочетание ректификации и расслаивания, экстракция. Комплексные исследования по сравнению схем разделения смесей разной физико-химической природы, базирующихся на разных процессах и специальных методах, не проводились. Научные публикации в данной области представлены фрагментарно и относятся к определенным объектам исследования. Целью настоящей работы является сравнительный анализ процессов и методов разделения жидких смесей на основе критического обзора литературы и результатов собственных исследований.</p></sec><sec><title>Методы</title><p>Методы. Работа базируется на критическом анализе литературы и математическом моделировании фазовых равновесий на основе уравнений локальных составов с использованием свободно распространяемых программных комплексов.</p></sec><sec><title>Результаты</title><p>Результаты. Проведен обзор научной литературы, на основе которого показаны достоинства и недостатки конкретных приемов разделения жидких смесей, преимущества и ограничения на сочетание в одной схеме различных процессов (в том числе в гибридных технологиях).</p></sec><sec><title>Выводы</title><p>Выводы. Перспективными направлениями дальнейших исследований в области синтеза и сравнения схем разделения смесей органических продуктов за счет использования различных методов и процессов разделения являются: оценка эффективности применения различных процессов (экстракции, расслаивания, специальных приемов ректификации) на разных этапах разделения смеси различной компонентности; сравнительный анализ процессов экстрактивной и гетероазеотропной ректификации при разделении смесей разного исходного состава (выделение областей энергетического преимущества каждого процесса); оценка эффективности реализации схем, основанных на сочетании экстракции с другими процессами, в зависимости от стадии регенерации экстрагента.</p></sec></trans-abstract><kwd-group xml:lang="ru"><kwd>схема разделения</kwd><kwd>фазовые равновесия</kwd><kwd>ректификация</kwd><kwd>расслаивание</kwd><kwd>варьирование давления</kwd><kwd>экстракция</kwd><kwd>экстрактивные агенты</kwd><kwd>энергозатраты</kwd></kwd-group><kwd-group xml:lang="en"><kwd>separation flowsheet</kwd><kwd>phase equilibria</kwd><kwd>distillation</kwd><kwd>splitting</kwd><kwd>pressure swing-distillation</kwd><kwd>extraction</kwd><kwd>separating agents</kwd><kwd>energy consumption</kwd></kwd-group><funding-group><funding-statement xml:lang="ru">Работа проведена в рамках выполнения государственного задания Российской Федерации, грант № FSFZ-2023-0003.</funding-statement><funding-statement xml:lang="en">The work was conducted within the framework of the State Assignment of the Russian Federation, grant No. FSFZ-2023-0003.</funding-statement></funding-group></article-meta></front><back><ref-list><title>References</title><ref id="cit1"><label>1</label><citation-alternatives><mixed-citation xml:lang="ru">Тимофеев В.С., Серафимов Л.А., Тимошенко А.В. Принципы технологии основного органического и нефтехимического синтеза. М.: Высшая школа; 2010. 408 с. ISBN 978-5-06-006067-6</mixed-citation><mixed-citation xml:lang="en">Timofeev V.S., Serafimov L.A., Timoshenko A.V. Printsipy tekhnologii osnovnogo organicheskogo i neftekhimicheskogo sinteza (The Principles of the Technology of Basic Organic and Petrochemical Synthesis). Moscow: Vysshaya shkola; 2010. 408 p. (in Russ.). ISBN 978-5-06-006067-6</mixed-citation></citation-alternatives></ref><ref id="cit2"><label>2</label><citation-alternatives><mixed-citation xml:lang="ru">Жаров В.Т., Серафимов Л.А. Физико-химические основы дистилляции и ректификации. Л.: Химия; 1975. 240 с.</mixed-citation><mixed-citation xml:lang="en">Zharov V.T., Serafimov L.A. Fiziko-khimicheskie osnovy distillyatsii i rektifikatsii (Physicoсhemical Principles of Distillation and Rectification). Leningrad: Khimiya; 1975. 240 p. (in Russ.).</mixed-citation></citation-alternatives></ref><ref id="cit3"><label>3</label><citation-alternatives><mixed-citation xml:lang="ru">Фролкова А.К. Разделение азеотропных смесей. Физикохимические основы и технологические приемы: монография. М.: ВЛАДОС; 2010. 192 с. ISBN 978-5-691-01743-8</mixed-citation><mixed-citation xml:lang="en">Frolkova A.K. Razdelenie azeotropnykh smesei. Fizikokhimicheskie osnovy i tekhnologicheskie priemy (Separation of Azeotropic Mixtures. Physicoсhemical Fundamentals and Technological Methods). Moscow: VLADOS; 2010. 192 p. (in Russ.). ISBN 978-5-691-01743-8</mixed-citation></citation-alternatives></ref><ref id="cit4"><label>4</label><citation-alternatives><mixed-citation xml:lang="ru">Zhigang L., Chengyue L., Biaohua C. Extractive Distillation: A Review. Sep. Purif. Rev. 2003;32(2):121–213. https://doi.org/10.1081/SPM-120026627</mixed-citation><mixed-citation xml:lang="en">Zhigang L., Chengyue L., Biaohua C. Extractive Distillation: A Review. Sep. Purif. Rev. 2003;32(2):121–213. https://doi.org/10.1081/SPM-120026627</mixed-citation></citation-alternatives></ref><ref id="cit5"><label>5</label><citation-alternatives><mixed-citation xml:lang="ru">Gerbaud V., Rodriguez-Donis I., Hegely L., Lang P., Denes F., You X. Review of Extractive Distillation. Process design, operation, optimization and control. Chem. Eng. Res. Des. 2019;141:229–271. https://doi.org/10.1016/j.cherd.2018.09.020</mixed-citation><mixed-citation xml:lang="en">Gerbaud V., Rodriguez-donis I., Hegely L., Lang P., Denes F., You X. Review of Extractive Distillation. Process design, operation, optimization and control. Chem. Eng. Res. Des. 2019;141:229–271. https://doi.org/10.1016/j.cherd.2018.09.020</mixed-citation></citation-alternatives></ref><ref id="cit6"><label>6</label><citation-alternatives><mixed-citation xml:lang="ru">Hilal N., Yousef G., Langston P. The reduction of extractive agent in extractive distillation and auto-extractive distillation. Chemical Engineering and Processing: Process Intensification. 2002;41(8): 673–679. https://doi.org/10.1016/S0255-2701(01)00187-8</mixed-citation><mixed-citation xml:lang="en">Hilal N., Yousef G., Langston P. The reduction of extractive agent in extractive distillation and auto-extractive distillation. Chemical Engineering and Processing: Process Intensification. 2002;41(8):673–679. https://doi.org/10.1016/S0255-2701(01)00187-8</mixed-citation></citation-alternatives></ref><ref id="cit7"><label>7</label><citation-alternatives><mixed-citation xml:lang="ru">Анохина Е.А. Энергосбережение в процессах экстрактивной ректификации. Тонкие химические технологии. 2013;8(5):3–19.</mixed-citation><mixed-citation xml:lang="en">Anokhina E.A. Energy saving in extractive distillation. Fine Chem. Technol. 2013;8(5):3–19 (in Russ.).</mixed-citation></citation-alternatives></ref><ref id="cit8"><label>8</label><citation-alternatives><mixed-citation xml:lang="ru">Раева В.М., Сазонова А.Ю., Себякин А.Ю., Кудрявцева Д.Ю. Критерий выбора потенциальных разделяющих агентов экстрактивной дистилляции. Тонкие химические технологии. 2011;6(4):20–27.</mixed-citation><mixed-citation xml:lang="en">Raeva V.M., Sazonova A.Yu., Sebyakin A.Yu., Kudryavtseva D.Yu. Criterion of choosing potential entrainers for extractive distillation. Fine Chem. Technol. 2011;6(4): 20–27 (in Russ.).</mixed-citation></citation-alternatives></ref><ref id="cit9"><label>9</label><citation-alternatives><mixed-citation xml:lang="ru">Фролкова А.В., Меркульева А.Д., Гаганов И.С. Синтез схем разделения расслаивающихся смесей: современное состояние проблемы. Тонкие химические технологии. 2018;13(3): 5–22. https://doi.org/10.32362/24106593-2018-13-3-5-22</mixed-citation><mixed-citation xml:lang="en">Frolkova A.V., Merkulyeva A.D., Gaganov I.S. Synthesis of flowsheets for separation of multiphase mixtures: state of the art. Fine Chem. Technol. 2018;13(3):5–22 (in Russ.). https://doi.org/10.32362/24106593-2018-13-3-5-22</mixed-citation></citation-alternatives></ref><ref id="cit10"><label>10</label><citation-alternatives><mixed-citation xml:lang="ru">Фролкова А.В., Фролкова А.К., Подтягина А.В., Спирякова В.В. Энергосбережение в схемах, основанных на сочетании ректификации и расслаивания. Теор. основы хим. технологии. 2018;52(5):489–496. https://doi.org/10.1134/S0040357118050032</mixed-citation><mixed-citation xml:lang="en">Frolkova A.V., Frolkova A.K., Podtiagina A.V., et al. Energy savings in flowsheets based on combination of distillation and splitting processes. Theor. Found. Chem. Eng. 2018;52(5): 771–778. https://doi.org/10.1134/S0040579518050329 [Original Russian Text: Frolkova A.V., Frolkova A.K., Podtiagina A.V., Spiriakova V.V. Energy savings in flowsheets based on combination of distillation and splitting processes. Teoreticheskie osnovy khimicheskoi tekhnologii. 2018;52(5): 489–496 (in Russ.). https://doi.org/10.1134/S0040357118050032 ]</mixed-citation></citation-alternatives></ref><ref id="cit11"><label>11</label><citation-alternatives><mixed-citation xml:lang="ru">Sosa J.E., Araújo J.M.M., Amado-González E., Pereiro A.B. Separation of azeotropic mixtures using protic ionic liquids as extraction solvents. J. Mol. Liquids. 2019;297:111733. https://doi.org/10.1016/j.molliq.2019.111733</mixed-citation><mixed-citation xml:lang="en">Sosa J.E., Araújo J.M.M., Amado-González E., Pereiro A.B. Separation of azeotropic mixtures using protic ionic liquids as extraction solvents. J. Mol. Liquids. 2019;297:111733. https://doi.org/10.1016/j.molliq.2019.111733</mixed-citation></citation-alternatives></ref><ref id="cit12"><label>12</label><citation-alternatives><mixed-citation xml:lang="ru">Patel K., Panchal N., Ingle Dr.Pr. Review of Extraction Techniques Extraction Methods: Microwave, Ultrasonic, Pressurized Fluid, Soxhlet Extraction, Etc. International Journal of Advanced Research in Chemical Science (IJARCS). 2018;6(3):6–21. http://doi.org/10.20431/2349-0403.0603002</mixed-citation><mixed-citation xml:lang="en">Patel K., Panchal N., Ingle Dr.Pr. Review of Extraction Techniques Extraction Methods: Microwave, Ultrasonic, Pressurized Fluid, Soxhlet Extraction, Etc. International Journal of Advanced Research in Chemical Science (IJARCS). 2018;6(3):6–21. http://doi.org/10.20431/2349-0403.0603002</mixed-citation></citation-alternatives></ref><ref id="cit13"><label>13</label><citation-alternatives><mixed-citation xml:lang="ru">Silvestre Cr.I.C., Santos J.L.M., Lima J.L.F.C., Zagatto E.A.G. Liquid–liquid extraction in flow analysis: A critical review. Anal. Chim. Acta. 2009;652(1–2):54–65. https://doi.org/10.1016/j.aca.2009.05.042</mixed-citation><mixed-citation xml:lang="en">Silvestre Cr.I.C., Santos J.L.M., Lima J.L.F.C., Zagatto E.A.G. Liquid–liquid extraction in flow analysis: A critical review. Anal. Chim. Acta. 2009;652(1–2):54–65. https://doi.org/10.1016/j.aca.2009.05.042</mixed-citation></citation-alternatives></ref><ref id="cit14"><label>14</label><citation-alternatives><mixed-citation xml:lang="ru">Носов Г.А., Михайлов М.В., Абсаттаров А.И. Разделение смесей путем сочетания процессов ректификации и фракционной крислаллизации. Тонкие химические технологии. 2017;12(3): 44–51. https://doi.org/10.32362/2410-6593-2017-12-3-44-51</mixed-citation><mixed-citation xml:lang="en">Nosov G.A., Mikhailov M.V., Absattarov A.I. Separation of mixtures by combining rectification and fractional crystallization processes. Fine Chem. Technol. 2017;12(3):44–51 (in Russ.). https://doi.org/10.32362/2410-6593-2017-12-3-44-51</mixed-citation></citation-alternatives></ref><ref id="cit15"><label>15</label><citation-alternatives><mixed-citation xml:lang="ru">Berry D.A, Ng K.M. Synthesis of crystallization-distillation hybrid separation processes. AIChE J. 1997;43(7):1751–1762. https://doi.org/10.1002/aic.690430712</mixed-citation><mixed-citation xml:lang="en">Berry D.A, Ng K.M. Synthesis of crystallization-distillation hybrid separation processes. AIChE J. 1997;43(7):1751–1762. https://doi.org/10.1002/aic.690430712</mixed-citation></citation-alternatives></ref><ref id="cit16"><label>16</label><citation-alternatives><mixed-citation xml:lang="ru">Cisternas L.A., Vasquez C.M., Swaney R.E. On the Design of Crystallization-Based Separation Processes: Review and Extension. AIChE J. 2006;52(5):1754–1769. https://doi.org/10.1002/aic.10768</mixed-citation><mixed-citation xml:lang="en">Cisternas L.A., Vasquez C.M., Swaney R.E. On the Design of Crystallization-Based Separation Processes: Review and Extension. AIChE J. 2006;52(5):1754–1769. https://doi.org/10.1002/aic.10768</mixed-citation></citation-alternatives></ref><ref id="cit17"><label>17</label><citation-alternatives><mixed-citation xml:lang="ru">Серафимов Л.А. Современное состояние термодинамикотопологического анализа фазовых диаграмм. Теор. основы хим. технологии. 2009;43(3):284–294.</mixed-citation><mixed-citation xml:lang="en">Serafimov L.A. State of the art in the thermodynamic and topological analysis of phase diagrams. Theor. Found. Chem. Eng. 2009;43(3):268–278. https://doi.org/10.1134/S0040579509030051 [Original Russian Text: Serafimov L.A. State of the art in the thermodynamic and topological analysis of phase diagrams. Teoreticheskie osnovy khimicheskoi tekhnologii. 2009;43(3):284–294 (in Russ.).]</mixed-citation></citation-alternatives></ref><ref id="cit18"><label>18</label><citation-alternatives><mixed-citation xml:lang="ru">Kiss А.А., Suszwalak D. J-.P.C. Enhanced bioethanol dehydration by extractive and azeotropic distillation in dividing-wall columns. Sep. Purif. Technol. 2012;86:70–78. https://doi.org/10.1016/j.seppur.2011.10.022</mixed-citation><mixed-citation xml:lang="en">Kiss А.А., Suszwalak D. J-.P.C. Enhanced bioethanol dehydration by extractive and azeotropic distillation in dividing-wall columns. Sep. Purif. Technol. 2012;86:70–78. https://doi.org/10.1016/j.seppur.2011.10.022</mixed-citation></citation-alternatives></ref><ref id="cit19"><label>19</label><citation-alternatives><mixed-citation xml:lang="ru">Frolkova A.V., Frolkova A.K., Gaganov I.S. Comparison of Extractive and Heteroazeotropic Distillation of High-Boiling Aqueous Mixtures. ChemEngineering 2022;6(5):83. https://doi.org/10.3390/chemengineering6050083</mixed-citation><mixed-citation xml:lang="en">Frolkova A.V., Frolkova A.K., Gaganov I.S. Comparison of Extractive and Heteroazeotropic Distillation of HighBoiling Aqueous Mixtures. ChemEngineering 2022;6(5):83. https://doi.org/10.3390/chemengineering6050083</mixed-citation></citation-alternatives></ref><ref id="cit20"><label>20</label><citation-alternatives><mixed-citation xml:lang="ru">Chen Y.-Ch., Yu B.-Y., Hsu Ch.-Ch., Chien I-L. Comparison of heteroazeotropic and extractive distillation for the dehydration of propylene glycol methyl ether. Chem. Eng. Res. Des. 2016;111:184–195. https://doi.org/10.1016/j.cherd.2016.05.003</mixed-citation><mixed-citation xml:lang="en">Chen Y.-Ch., Yu B.-Y., Hsu Ch.-Ch., Chien I-L. Comparison of heteroazeotropic and extractive distillation for the dehydration of propylene glycol methyl ether. Chem. Eng. Res. Des. 2016;111:184–195. https://doi.org/10.1016/j.cherd.2016.05.003</mixed-citation></citation-alternatives></ref><ref id="cit21"><label>21</label><citation-alternatives><mixed-citation xml:lang="ru">Zhao L., Lyu X., Wang W., Shan J., Qiu T. Comparison of heterogeneous azeotropic distillation and extractive distillation methods for ternary azeotrope ethanol/toluene/ water separation. Comput. Chem. Eng. 2017;100:27–37 https://doi.org/10.1016/j.compchemeng.2017.02.007</mixed-citation><mixed-citation xml:lang="en">Zhao L., Lyu X., Wang W., Shan J., Qiu T. Comparison of heterogeneous azeotropic distillation and extractive distillation methods for ternary azeotrope ethanol/toluene/ water separation. Comput. Chem. Eng. 2017;100:27–37 https://doi.org/10.1016/j.compchemeng.2017.02.007</mixed-citation></citation-alternatives></ref><ref id="cit22"><label>22</label><citation-alternatives><mixed-citation xml:lang="ru">Фролкова А.В., Фролкова А.К., Гаганов И.С. Комбинирование специальных приемов при разработке схем разделения смеси метанол + вода + метилметакрилат. Химическая технология. 2023;24(8):314–320. https://doi.org/10.31044/1684-5811-2023-24-8-314-320</mixed-citation><mixed-citation xml:lang="en">Frolkova A.V., Frolkova A.K., Gaganov I.S. Combination special techniques in development of separation schemes for mixture of methanol + water + methyl methacrylate. Khimicheskaya Tekhnologiya. 2023;24(8):314–320 (in Russ.). https://doi.org/10.31044/1684-5811-2023-24-8-314-320</mixed-citation></citation-alternatives></ref><ref id="cit23"><label>23</label><citation-alternatives><mixed-citation xml:lang="ru">Серафимов Л.А. Правило азеотропии и классификация многокомпонентных смесей VII. Диаграммы трехкомпонентных смесей. Журн. физ. химии. 1970;44(4):1021–1027.</mixed-citation><mixed-citation xml:lang="en">Serafimov L.A. The azeotropic rule and the classification of multicomponent mixtures: VII. Diagrams for ternary systems mixtures. Russ. J. Phys. Chem. 1970;44(4):567–571. [Original Russian Text: Serafimov L.A. The azeotropic rule and the classification of multicomponent mixtures: VII. Diagrams for ternary systems mixtures. Zhurnal fizicheskoi khimii. 1970;44(4):1021–1027 (in Russ.).]</mixed-citation></citation-alternatives></ref><ref id="cit24"><label>24</label><citation-alternatives><mixed-citation xml:lang="ru">Клинов А.В., Фазлыев А.Р., Хайруллина А.Р., Алексеев К.А., Латыпов Д.Р. Экстрактивная ректификация смеси этанол – вода с использованием этиленгликоля. Вестник технологического университета. 2023;26(1): 44–47. https://doi.org/10.55421/1998-7072_2023_26_1_44</mixed-citation><mixed-citation xml:lang="en">Klinov A.V., Fazlyev A.R., Khairullina A.R., Alekseev K.A., Latypov D.R. Extractive rectification of ethanol-water mixture using ethylene glycol. Vestnik tekhnologicheskogo universiteta = Herald of Technological University. 2023;26(1):44–47 (in Russ.). https://doi.org/10.55421/1998-7072_2023_26_1_44</mixed-citation></citation-alternatives></ref><ref id="cit25"><label>25</label><citation-alternatives><mixed-citation xml:lang="ru">Фролкова А.К., Фролкова А.В., Раева В.М., Жучков В.И. Особенности дистилляционного разделения многокомпонентных смесей. Тонкие химические технологии. 2022;17(3): 87–106. https://doi.org/10.32362/2410-6593-2022-17-2-87-106</mixed-citation><mixed-citation xml:lang="en">Frolkova A.K., Frolkova A.V., Raeva V.M., Zhuchkov V.I. Features of distillation separation of multicomponent mixtures. Fine Chem. Technol. 2022;17(3):87–106. https://doi.org/10.32362/2410-6593-2022-17-2-87-106</mixed-citation></citation-alternatives></ref><ref id="cit26"><label>26</label><citation-alternatives><mixed-citation xml:lang="ru">Frolkova A., Frolkova A., Gaganov I. Extractive and Auto-Extractive Distillation of Azeotropic Mixtures. Chem. Eng. Technol. 2021;44(8):1397–1402. https://doi.org/10.1002/ceat.202100024</mixed-citation><mixed-citation xml:lang="en">Frolkova A., Frolkova A., Gaganov I. Extractive and AutoExtractive Distillation of Azeotropic Mixtures. Chem. Eng. Technol. 2021;44(8):1397–1402. https://doi.org/10.1002/ceat.202100024</mixed-citation></citation-alternatives></ref><ref id="cit27"><label>27</label><citation-alternatives><mixed-citation xml:lang="ru">Luo H., Liang K., Li W., Ming Xia Y., Xu C. Comparison of Pressure-Swing Distillation and Extractive Distillation Methods for Isopropyl Alcohol/Diisopropyl Ether Separation. Ind. Eng. Chem. Res. 2014;53(39):15167–15182. https://doi.org/10.1021/ie502735g</mixed-citation><mixed-citation xml:lang="en">Luo H., Liang K., Li W., Ming Xia Y., Xu C. Comparison of PressureSwing Distillation and Extractive Distillation Methods for Isopropyl Alcohol/Diisopropyl Ether Separation. Ind. Eng. Chem. Res. 2014;53(39):15167–15182. https://doi.org/10.1021/ie502735g</mixed-citation></citation-alternatives></ref><ref id="cit28"><label>28</label><citation-alternatives><mixed-citation xml:lang="ru">Lladosa E., Montón J.B., Burguet M. Separation of di-n-propyl ether and n-propyl alcohol by extractive distillation and pressureswing distillation: Computer simulation and economic optimization. Chem. Eng. Process.: Process Intensif. 2011;50(11–12): 1266–1274. https://doi.org/10.1016/j.cep.2011.07.010</mixed-citation><mixed-citation xml:lang="en">Lladosa E., Montón J.B., Burguet M. Separation of di-n-propyl ether and n-propyl alcohol by extractive distillation and pressure-swing distillation: Computer simulation and economic optimization. Chem. Eng. Process.: Process Intensif. 2011;50(11–12):1266–1274. https://doi.org/10.1016/j.cep.2011.07.010</mixed-citation></citation-alternatives></ref><ref id="cit29"><label>29</label><citation-alternatives><mixed-citation xml:lang="ru">Wang X., Xie L., Tian P., Tian G. Design and control of extractive dividing wall column and pressure-swing distillation for separating azeotropic mixture of acetonitrile/N-propanol. Chem. Eng. Process.: Process Intensif. 2016;110:172–187. https://doi.org/10.1016/j.cep.2016.10.009</mixed-citation><mixed-citation xml:lang="en">Wang X., Xie L., Tian P., Tian G. Design and control of extractive dividing wall column and pressure-swing distillation for separating azeotropic mixture of acetonitrile/N-propanol. Chem. Eng. Process.: Process Intensif. 2016;110:172–187. https://doi.org/10.1016/j.cep.2016.10.009</mixed-citation></citation-alternatives></ref><ref id="cit30"><label>30</label><citation-alternatives><mixed-citation xml:lang="ru">Ghuge Pr.D., Mali N.A., Joshi S.S. Comparative Analysis of Extractive and Pressure Swing Distillation for Separation of THF-Water Separation. Comput. Chem. Eng. 2017;103:188–200. http://dx.doi.org/10.1016/j.compchemeng.2017.03.019</mixed-citation><mixed-citation xml:lang="en">Ghuge Pr.D., Mali N.A., Joshi S.S. Comparative Analysis of Extractive and Pressure Swing Distillation for Separation of THF-Water Separation. Comput. Chem. Eng. 2017;103: 188–200. http://doi.org/10.1016/j.compchemeng.2017.03.019</mixed-citation></citation-alternatives></ref><ref id="cit31"><label>31</label><citation-alternatives><mixed-citation xml:lang="ru">Muñoz R., Montón J.B., Burguet M.C., de laTorre J. Separation of isobutyl alcohol and isobutyl acetate by extractive distillation and pressure-swing distillation: Simulation and optimization. Sep. Purif. Technol. 2006;50(2):175–183. https://doi.org/10.1016/j.seppur.2005.11.022</mixed-citation><mixed-citation xml:lang="en">MuñozR., Montón J.B., Burguet M.C., de laTorre J. Separation of isobutyl alcohol and isobutyl acetate by extractive distillation and pressure-swing distillation: Simulation and optimization. Sep. Purif. Technol. 2006;50(2):175–183. https://doi.org/10.1016/j.seppur.2005.11.022</mixed-citation></citation-alternatives></ref><ref id="cit32"><label>32</label><citation-alternatives><mixed-citation xml:lang="ru">Cao Y., Hu J., Jia H., Bu G., Zhu Zh., Wang Y. Comparison of pressureswing distillation and extractive distillation with varied-diameter column in economics and dynamic control. J. Process Control. 2017;49:9–25. https://doi.org/10.1016/j.jprocont.2016.11.005</mixed-citation><mixed-citation xml:lang="en">CaoY., Hu J., JiaH., BuG., ZhuZh., WangY. Comparison of pressureswing distillation and extractive distillation with varied-diameter column in economics and dynamic control. J. Process Control. 2017;49:9–25. https://doi.org/10.1016/j.jprocont.2016.11.005</mixed-citation></citation-alternatives></ref><ref id="cit33"><label>33</label><citation-alternatives><mixed-citation xml:lang="ru">Luyben W.L. Comparison of pressure-swing and extractivedistillation methods for methanol-recovery systems in the TAME reactive-distillation process. Ind. Eng. Chem. Res. 2005;44(15):5715–5725. https://doi.org/10.1021/ie058006q</mixed-citation><mixed-citation xml:lang="en">Luyben W.L. Comparison of pressure-swing and extractivedistillation methods for methanol-recovery systems in the TAME reactive-distillation process. Ind. Eng. Chem. Res. 2005;44(15):5715–5725. https://doi.org/10.1021/ie058006q</mixed-citation></citation-alternatives></ref><ref id="cit34"><label>34</label><citation-alternatives><mixed-citation xml:lang="ru">Modla G., Lang P. Removal and Recovery of Organic Solvents from Aqueous Waste Mixtures by Extractive and Pressure Swing Distillation. Ind. Eng. Chem. Res. 2012;51(35): 11473–11481. https://doi.org/10.1021/ie300331d</mixed-citation><mixed-citation xml:lang="en">Modla G., Lang P. Removal and Recovery of Organic Solvents from Aqueous Waste Mixtures by Extractive and Pressure Swing Distillation. Ind. Eng. Chem. Res. 2012;51(35): 11473–11481. https://doi.org/10.1021/ie300331d</mixed-citation></citation-alternatives></ref><ref id="cit35"><label>35</label><citation-alternatives><mixed-citation xml:lang="ru">Luyben W.L. Comparison of extractive distillation and pressure swing distillation for acetone-methanol separation. Ind. Eng. Chem. Res. 2008;47(8):2696−2707. https://doi.org/10.1021/ie701695u</mixed-citation><mixed-citation xml:lang="en">Luyben W.L. Comparison of extractive distillation and pressure swing distillation for acetone-methanol separation. Ind. Eng. Chem. Res. 2008;47(8):2696−2707. https://doi.org/10.1021/ie701695u</mixed-citation></citation-alternatives></ref><ref id="cit36"><label>36</label><citation-alternatives><mixed-citation xml:lang="ru">LuybenW.L. Comparison of extractive distillation and pressure-swing distillation for acetone/chloroform separation. Comput. Chem. Eng. 2013;50:1–7. https://doi.org/10.1016/j.compchemeng.2012.10.014</mixed-citation><mixed-citation xml:lang="en">Luyben W.L. Comparison of extractive distillation and pressure-swing distillation for acetone/chloroform separation. Comput. Chem. Eng. 2013;50:1–7. https://doi.org/10.1016/j.compchemeng.2012.10.014</mixed-citation></citation-alternatives></ref><ref id="cit37"><label>37</label><citation-alternatives><mixed-citation xml:lang="ru">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. https://doi.org/10.1016/j.compchemeng.2014.03.026</mixed-citation><mixed-citation xml:lang="en">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. https://doi.org/10.1016/j.compchemeng.2014.03.026</mixed-citation></citation-alternatives></ref><ref id="cit38"><label>38</label><citation-alternatives><mixed-citation xml:lang="ru">Фролкова А.В., Шашкова Ю.И., Фролкова А.К., Маевский М.А. Сравнение альтернативных методов разделения смеси метилацетат – метанол – уксусная кислота – уксусный ангидрид. Тонкие химические технологии. 2019;14(5): 51–60. https://doi.org/10.32362/2410-6593-2019-14-5-51-60</mixed-citation><mixed-citation xml:lang="en">Frolkova A.V., Shashkova Y.I., Frolkova A.K., Mayevskiy M.A. Comparison of alternative methods for methyl acetate + methanol + acetic acid + acetic anhydride mixture separation. Fine Chem. Technol. 2019;14(5):51–60. https://doi.org/10.32362/2410-6593-2019-14-5-51-60</mixed-citation></citation-alternatives></ref><ref id="cit39"><label>39</label><citation-alternatives><mixed-citation xml:lang="ru">Qin Y., Zhuang Y., Wang Ch., Dong Y., Zhang L., Liu L., Du J. Comparison of Pressure-Swing Distillation and Extractive Distillation for the Separation of the Non-Pressure-Sensitive Azeotropes. In: Proceedings of the 24th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction. 2021. URL: https://www.researchgate.net/publication/355982388_Comparison_of_Pressure-Swing_Distillation_and_Extractive_Distillation_for_the_Separation_of_the_Non-Pressure-Sensitive_Azeotropes. Accessed September 08, 2025.</mixed-citation><mixed-citation xml:lang="en">Qin Y., Zhuang Y., Wang Ch., Dong Y., Zhang L., Liu L., Du J. Comparison of Pressure-Swing Distillation and Extractive Distillation for the Separation of the Non-Pressure-Sensitive Azeotropes. In: Proceedings of the 24th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction. 2021. URL: https://www.researchgate.net/publication/355982388_Comparison_of_Pressure-Swing_Distillation_and_Extractive_Distillation_for_the_Separation_of_the_Non-Pressure-Sensitive_Azeotropes. Accessed September 08, 2025.</mixed-citation></citation-alternatives></ref><ref id="cit40"><label>40</label><citation-alternatives><mixed-citation xml:lang="ru">Раева В.М., Капранова А.С. Сравнение эффективности экстрактивных агентов при разделении смеси ацетон – метанол. Химическая промышленность сегодня. 2015;3:33–46.</mixed-citation><mixed-citation xml:lang="en">Raeva V.M., Kapranova A.S. Comparison efficiency of extractive agents at the separation of mixture acetone– methanol. Khimicheskaya promyshlennost’ segodnya = Chemical Industry Developments. 2015;3:33–46 (in Russ.).</mixed-citation></citation-alternatives></ref><ref id="cit41"><label>41</label><citation-alternatives><mixed-citation xml:lang="ru">Guang C., Shi X., Zhang Z., Wang C., Wang C., Gao J. Comparison of heterogeneous azeotropic and pressure-swing distillations for separating the diisopropylether/isopropanol/ water mixtures. Chem. Eng. Res. Design. 2019;143:249–260. https://doi.org/10.1016/j.cherd.2019.01.021</mixed-citation><mixed-citation xml:lang="en">Guang C., Shi X., Zhang Z., Wang C., Wang C., Gao J. Comparison of heterogeneous azeotropic and pressure-swing distillations for separating the diisopropylether/isopropanol/ water mixtures. Chem. Eng. Res. Design. 2019;143:249–260. https://doi.org/10.1016/j.cherd.2019.01.021</mixed-citation></citation-alternatives></ref><ref id="cit42"><label>42</label><citation-alternatives><mixed-citation xml:lang="ru">Cui Y., Shi X., Guang C., Zhang Z., Wang C., Wang C. Comparison of pressure-swing distillation and heterogeneous azeotropic distillation for recovering benzene and isopropanol from wastewater. Process Saf. Environ. Protection. 2018;122:1–12. https://doi.org/10.1016/j.psep.2018.11.017</mixed-citation><mixed-citation xml:lang="en">Cui Y., Shi X., Guang C., Zhang Z., Wang C., Wang C. Comparison of pressure-swing distillation and heterogeneous azeotropic distillation for recovering benzene and isopropanol from wastewater. Process Saf. Environ. Protection. 2018;122:1–12. https://doi.org/10.1016/j.psep.2018.11.017</mixed-citation></citation-alternatives></ref><ref id="cit43"><label>43</label><citation-alternatives><mixed-citation xml:lang="ru">Tripodi A., Compagnoni M., Ramis G., Rossetti I. Pressureswing or extraction-distillation for the recovery of pure acetonitrile from ethanol ammoxidation process: A comparison of efficiency and cost. Chem. Eng. Res. Design. 2017;127: 92–102. https://doi.org/10.1016/j.cherd.2017.09.018</mixed-citation><mixed-citation xml:lang="en">Tripodi A., Compagnoni M., Ramis G., Rossetti I. Pressureswing or extraction-distillation for the recovery of pure acetonitrile from ethanol ammoxidation process: A comparison of efficiency and cost. Chem. Eng. Res. Design. 2017;127: 92–102. https://doi.org/10.1016/j.cherd.2017.09.018</mixed-citation></citation-alternatives></ref><ref id="cit44"><label>44</label><citation-alternatives><mixed-citation xml:lang="ru">Zhu Z., Wang Y., Hu J., Qi X., Wang Y. Extractive distillation process combined with decanter for separating ternary azeotropic mixture of toluene-methanol-water. Chem. Eng. Trans. 2017;61:763–768. https://doi.org/10.3303/CET1761125</mixed-citation><mixed-citation xml:lang="en">Zhu Z., Wang Y., Hu J., Qi X., Wang Y. Extractive distillation process combined with decanter for separating ternary azeotropic mixture of toluene-methanol-water. Chem. Eng. Trans. 2017;61:763–768. https://doi.org/10.3303/CET1761125</mixed-citation></citation-alternatives></ref><ref id="cit45"><label>45</label><citation-alternatives><mixed-citation xml:lang="ru">Гаганов И.С., Белим С.С., Фролкова А.В., Фролкова А.К. Разработка схем разделения смеси получения фенола на основе анализа диаграмм фазового равновесия. Теор. основы хим. технологии. 2023;57(1):38–47. https://doi.org/10.31857/S0040357123010049</mixed-citation><mixed-citation xml:lang="en">Gaganov I.S., Belim S.S., Frolkova A.V., Frolkova A.K. Development of Flowsheet of Separation of a Phenol Production Mixture Based on the Analysis of Phase Equilibrium Diagrams. Theor. Found. Chem. Eng. 2023;57(1):35–44. https://doi.org/10.1134/S0040579523010049 [Original Russian Text: Gaganov I.S., Belim S.S., Frolkova A.V., Frolkova A.K. Development of Flowsheet of Separation of a Phenol Production Mixture Based on the Analysis of Phase Equilibrium Diagrams. Teoreticheskie osnovy khimicheskoi tekhnologii. 2023;57(1):38–47 (in Russ.). https://doi.org/10.31857/S0040357123010049 ]</mixed-citation></citation-alternatives></ref><ref id="cit46"><label>46</label><citation-alternatives><mixed-citation xml:lang="ru">Новрузова А.Н., Фролкова А.В. Сравнение технологических схем разделения смеси ацетонитрил – вода, основанных на разных массообменных процессах. В сб.: Химия и химическая технология: достижения и перспективы: Сборник тезисов I Международной VII Всероссийской конференции. 2024. C. 0234.1–0234.6.</mixed-citation><mixed-citation xml:lang="en">Novruzova A.N., Frolkova A.V. Сomparison of technological schemes of separation of the mixture acetonitrile – water, based on different mass transfer processes. In: Chemistry and Chemical Technology: Achievements and Prospects: Thesis Collection I of the 7th International All-Russian Сonference. 2024. P. 0234.1-0234.6 (in Russ.).</mixed-citation></citation-alternatives></ref><ref id="cit47"><label>47</label><citation-alternatives><mixed-citation xml:lang="ru">Yu B.-Y., Huang R., Zhong X.-Y., Lee M.-J., Chien I.-L. Energy-Efficient Extraction-Distillation Process for Separating Diluted Acetonitrile-Water Mixture: Rigorous Design with Experimental Verification from Ternary Liquid-Liquid Equilibrium Data. Ind. Eng. Chem. Res. 2017;56(51):15112–15121. https://doi.org/10.1021/acs.iecr.7b04408</mixed-citation><mixed-citation xml:lang="en">Yu B.-Y., Huang R., Zhong X.-Y., Lee M.-J., Chien I.-L. Energy-Efficient Extraction-Distillation Process for Separating Diluted Acetonitrile-Water Mixture: Rigorous Design with Experimental Verification from Ternary LiquidLiquid Equilibrium Data. Ind. Eng. Chem. Res. 2017;56(51): 15112–15121. https://doi.org/10.1021/acs.iecr.7b04408</mixed-citation></citation-alternatives></ref><ref id="cit48"><label>48</label><citation-alternatives><mixed-citation xml:lang="ru">Mahdi T., Ahmad A. Nasef M.M., Ripin A. State-of-the-Art Technologies for Separation of Azeotropic Mixtures. Sep. Purif. Rev. 2015;44(4):308–330. https://doi.org/10.1080/15422119.2014.963607</mixed-citation><mixed-citation xml:lang="en">Mahdi T., Ahmad A. Nasef M.M., Ripin A. State-of-the-Art Technologies for Separation of Azeotropic Mixtures. Sep. Purif. Rev. 2015;44(4):308–330. https://doi.org/10.1080/15422119.2014.963607</mixed-citation></citation-alternatives></ref><ref id="cit49"><label>49</label><citation-alternatives><mixed-citation xml:lang="ru">Daviou M.C., Hoch P.M., Eliceche A.M. Design of membrane modules used in hybrid distillation/pervaporation systems. Ind. Eng. Chem. Res. 2004;43(13):3403–3412. https://doi.org/10.1021/ie034259c</mixed-citation><mixed-citation xml:lang="en">Daviou M.C., Hoch P.M., Eliceche A.M. Design of membrane modules used in hybrid distillation/pervaporation systems. Ind. Eng. Chem. Res. 2004;43(13):3403–3412. https://doi.org/10.1021/ie034259c</mixed-citation></citation-alternatives></ref><ref id="cit50"><label>50</label><citation-alternatives><mixed-citation xml:lang="ru">Naidu Y., Malik R.K. A generalized methodology for optimal configurations of hybrid distillation–pervaporation processes. Chem. Eng. Res. Design. 2011;89(8):1348–1361. https://doi.org/10.1016/j.cherd.2011.02.025</mixed-citation><mixed-citation xml:lang="en">Naidu Y., Malik R.K. A generalized methodology for optimal configurations of hybrid distillation–pervaporation processes. Chem. Eng. Res. Design. 2011;89(8):1348–1361. https://doi.org/10.1016/j.cherd.2011.02.025</mixed-citation></citation-alternatives></ref><ref id="cit51"><label>51</label><citation-alternatives><mixed-citation xml:lang="ru">Kookos I.K. Optimal design of membrane/distillation column hybrid processes. Ind. Eng. Chem. Res. 2003;42(8): 1731–1738. https://doi.org/10.1021/ie020616s</mixed-citation><mixed-citation xml:lang="en">Kookos I.K. Optimal design of membrane/distillation column hybrid processes. Ind. Eng. Chem. Res. 2003;42(8): 1731–1738. https://doi.org/10.1021/ie020616s</mixed-citation></citation-alternatives></ref><ref id="cit52"><label>52</label><citation-alternatives><mixed-citation xml:lang="ru">Hoof V.V., Van den Abeele L., Buekenhoudt A., Dotremont C., Leysen R. Economic comparison between azeotropic distillation and different hybrid systems combining distillation with pervaporation for the dehydration of isopropanol. Sep. Purif. Technol. 2004;37(1): 33–49. https://doi.org/10.1016/j.seppur.2003.08.003</mixed-citation><mixed-citation xml:lang="en">Hoof V.V., Van den Abeele L., Buekenhoudt A., Dotremont C., Leysen R. Economic comparison between azeotropic distillation and different hybrid systems combining distillation with pervaporation for the dehydration of isopropanol. Sep. Purif. Technol. 2004;37(1):33–49. https://doi.org/10.1016/j.seppur.2003.08.003</mixed-citation></citation-alternatives></ref><ref id="cit53"><label>53</label><citation-alternatives><mixed-citation xml:lang="ru">Nangare D.M., Suseeladevi M. Hybrid pervaporation/ distillation process for ethanol – water separation effect of distillation column side stream. Asian J. Sci. Technol. 2017;8(11):6522–6525.</mixed-citation><mixed-citation xml:lang="en">Nangare D.M., Suseeladevi M. Hybrid pervaporation/ distillation process for ethanol – water separation effect of distillation column side stream. Asian J. Sci. Technol. 2017;8(11):6522–6525.</mixed-citation></citation-alternatives></ref><ref id="cit54"><label>54</label><citation-alternatives><mixed-citation xml:lang="ru">Koczka K., Mizsey P., Fonyo Zs. Rigorous modelling and optimization of hybrid separation processes based on pervaporation. Open Chemistry. 2005;5(4):1124–1147. https://doi.org/10.2478/s11532-007-0050-8</mixed-citation><mixed-citation xml:lang="en">Koczka K., Mizsey P., Fonyo Zs. Rigorous modelling and optimization of hybrid separation processes based on pervaporation. Open Chemistry. 2005;5(4):1124–1147. https://doi.org/10.2478/s11532-007-0050-8</mixed-citation></citation-alternatives></ref><ref id="cit55"><label>55</label><citation-alternatives><mixed-citation xml:lang="ru">Han G.L., Zhang Q., Zhong J., Shao H. Separation of Dimethylformamide/H2O Mixtures Using Pervaporation-distillation Hybrid Process. Adv. Mater. Res. 2011;233–235:866–869. https://doi.org/10.4028/www.scientific.net/AMR.233-235.866</mixed-citation><mixed-citation xml:lang="en">Han G.L., Zhang Q., Zhong J., Shao H. Separation of Dimethylformamide/H2O Mixtures Using Pervaporation-distillation Hybrid Process. Adv. Mater. Res. 2011;233–235:866–869. https://doi.org/10.4028/www.scientific.net/AMR.233-235.866</mixed-citation></citation-alternatives></ref><ref id="cit56"><label>56</label><citation-alternatives><mixed-citation xml:lang="ru">Hassankhan B., Raisi A. Separation of isobutanol/water mixtures by hybrid distillationpervaporation process: Modeling, simulation and economic comparison. Chem. Eng. Process.: Process Intensif. 2020;155:108071. https://doi.org/10.1016/j.cep.2020.108071</mixed-citation><mixed-citation xml:lang="en">Hassankhan B., Raisi A. Separation of isobutanol/water mixtures by hybrid distillationpervaporation process: Modeling, simulation and economic comparison. Chem. Eng. Process.: Process Intensif. 2020;155:108071. https://doi.org/10.1016/j.cep.2020.108071</mixed-citation></citation-alternatives></ref><ref id="cit57"><label>57</label><citation-alternatives><mixed-citation xml:lang="ru">Zong Ch., Guo Q., Shen B., Yang X., Zhou H., Jin W. Heat-Integrated Pervaporation−Distillation Hybrid System for the Separation of Methyl Acetate−Methanol Azeotropes. Ind. Eng. Chem. Res. 2021;60(28):10327–10337. https://doi.org/10.1021/acs.iecr.1c01513</mixed-citation><mixed-citation xml:lang="en">Zong Ch., Guo Q., Shen B., Yang X., Zhou H., Jin W. HeatIntegrated Pervaporation−Distillation Hybrid System for the Separation of Methyl Acetate−Methanol Azeotropes. Ind, Eng. Chem. Res. 2021;60(28):10327–10337. https://doi.org/10.1021/acs.iecr.1c01513</mixed-citation></citation-alternatives></ref><ref id="cit58"><label>58</label><citation-alternatives><mixed-citation xml:lang="ru">Penkova A.V., Polotskaya G.A., Toikka A.M. Separation of acetic acid–methanol–methyl acetate–water reactive mixture. Chem. Eng. Sci. 2013;101:586–592. https://doi.org/10.1016/j.ces.2013.05.055</mixed-citation><mixed-citation xml:lang="en">Penkova A.V., Polotskaya G.A., Toikka A.M. Separation of acetic acid–methanol–methyl acetate–water reactive mixture. Chem. Eng. Sci. 2013;101:586–592. https://doi.org/10.1016/j.ces.2013.05.055</mixed-citation></citation-alternatives></ref><ref id="cit59"><label>59</label><citation-alternatives><mixed-citation xml:lang="ru">Тойкка А.М., Самаров А.А., Тойкка М.А. Фазовое и химическое равновесие в многокомпонентных флюидных системах с химической реакцией. Успехи химии. 2015;84(4):378–392. https://doi.org/10.1070/RCR4515</mixed-citation><mixed-citation xml:lang="en">Toikka A.M., Samarov A.A., Toikka M.A. Phase and chemical equilibria in multicomponent fluid systems with a chemical reaction. Russ. Chem. Rew. 2015;84(4):378–392. https://doi.org/10.1070/RCR4515 [Original Russian Text: ToikkaA.M., SamarovA.A., ToikkaM.A. Phase and chemical equilibria in multicomponent fluid systems with a chemical reaction. Uspekhi khimii. 2015;84(4):378–392 (in Russ.). https://doi.org/10.1070/RCR4515 ]</mixed-citation></citation-alternatives></ref><ref id="cit60"><label>60</label><citation-alternatives><mixed-citation xml:lang="ru">Wang Y., Zhang Z., Zhang H., Zhang Q. Control of heat integrated pressure-swing-distillation process for separating azeotropic mixture of tetrahydrofuran and methanol. Ind. Eng. Chem. Res. 2015;54(5):1646–1655. https://doi.org/10.1021/ie505024q</mixed-citation><mixed-citation xml:lang="en">Wang Y., Zhang Z., Zhang H., Zhang Q. Control of heat integrated pressure-swing-distillation process for separating azeotropic mixture of tetrahydrofuran and methanol. Ind. Eng. Chem. Res. 2015;54(5):1646–1655. https://doi.org/10.1021/ie505024q</mixed-citation></citation-alternatives></ref><ref id="cit61"><label>61</label><citation-alternatives><mixed-citation xml:lang="ru">Zhu Z., Wang L., Ma Y., Wang W., Wang Y. Separating an azeotropic mixture of toluene and ethanol via heat integration pressure swing distillation. Comput. Chem. Eng. 2015;76: 137–149. https://doi.org/10.1016/j.compchemeng.2015.02.016</mixed-citation><mixed-citation xml:lang="en">Zhu Z., Wang L., Ma Y., Wang W., Wang Y. Separating an azeotropic mixture of toluene and ethanol via heat integration pressure swing distillation. Comput. Chem. Eng. 2015;76: 137–149. https://doi.org/10.1016/j.compchemeng.2015.02.016</mixed-citation></citation-alternatives></ref><ref id="cit62"><label>62</label><citation-alternatives><mixed-citation xml:lang="ru">Анохина Е.А., Тимошенко А.В. Синтез схем ректификации со связанными тепловыми и материальными потоками. Тонкие химические технологии. 2017;12(6):46–70. https://doi.org/10.32362/2410-6593-2017-12-6-46-70</mixed-citation><mixed-citation xml:lang="en">Anokhina E.A., Timoshenko A.V. Synthesis of the thermally coupled distillation sequences. Fine Chem. Technol. 2017;12(6):46–70 (in Russ.). https://doi.org/10.32362/2410-6593-2017-12-6-46-70</mixed-citation></citation-alternatives></ref><ref id="cit63"><label>63</label><citation-alternatives><mixed-citation xml:lang="ru">Анохина Е.А., Тимошенко А.В. Влияние количества и уровня бокового отбора на расход экстрактивного агента в комплексах экстрактивной ректификации с частично связанными тепловыми и материальными потоками. Теор. основы хим. технологии. 2023;57(2):177–187. https://doi.org/10.31857/S0040357123010013</mixed-citation><mixed-citation xml:lang="en">Anokhina E.A., Timoshenko A.V. Effect of the Side-Stream Location and the Side-Stream Value on the Optimal Entrainer Flowrate in Thermally Coupled Extractive Distillation Columns. Theor. Found. Chem. Eng. 2023;57(2):165–175. https://doi.org/10.1134/s0040579523010013 [Original Russian Text: Anokhina E.A., Timoshenko A.V. Effect of the Side-Stream Location and the Side-Stream Value on the Optimal Entrainer Flowrate in Thermally Coupled Extractive Distillation Columns. Teoreticheskie osnovy khimicheskoi tekhnologii. 2023;57(2)165–175 (in Russ.). https://doi.org/10.1134/S0040579523010013 ]</mixed-citation></citation-alternatives></ref><ref id="cit64"><label>64</label><citation-alternatives><mixed-citation xml:lang="ru">Yu B., Wang Q., XuC. Design and control of distillation system for methylal/methanol separation. Part 2: pressure swing distillation with full heat integration. Ind. Eng. Chem. Res. 2012;51(3):1293–1310. https://doi.org/10.1021/ie201949q</mixed-citation><mixed-citation xml:lang="en">YuB., Wang Q., XuC. Design and control of distillation system for methylal/methanol separation. Part 2: pressure swing distillation with full heat integration. Ind. Eng. Chem. Res. 2012;51(3):1293–1310. https://doi.org/10.1021/ie201949q</mixed-citation></citation-alternatives></ref><ref id="cit65"><label>65</label><citation-alternatives><mixed-citation xml:lang="ru">Shirsat S.P. Modeling, simulation and control of an internally heat integrated pressure swing distillation process for bioethanol separation. Comput. Chem. Eng. 2013;53:201–202. https://doi.org/10.1016/j.compchemeng.2013.01.009</mixed-citation><mixed-citation xml:lang="en">Shirsat S.P. Modeling, simulation and control of an internally heat integrated pressure swing distillation process for bioethanol separation. Comput. Chem. Eng. 2013;53:201–202. https://doi.org/10.1016/j.compchemeng.2013.01.009</mixed-citation></citation-alternatives></ref><ref id="cit66"><label>66</label><citation-alternatives><mixed-citation xml:lang="ru">Liu G., Chen Z., Huang K., Shi Z., Chen H., Wang S. Studies of the externally heat-integrated double distillation columns (EHIDDiC). Asia-Pacific J. Chem. Eng. 2011;6(3):327–337. https://doi.org/10.1002/apj.566</mixed-citation><mixed-citation xml:lang="en">Liu G., Chen Z., Huang K., Shi Z., Chen H., Wang S. Studies of the externally heat-integrated double distillation columns (EHIDDiC). Asia-Pacific J. Chem. Eng. 2011;6(3):327–337. https://doi.org/10.1002/apj.566</mixed-citation></citation-alternatives></ref><ref id="cit67"><label>67</label><citation-alternatives><mixed-citation xml:lang="ru">Huang K., Liu W., Ma J., Wang S. Externally heat-integrated double distillation column (EHIDDiC): basic concept and general characteristics. Ind. Eng. Chem. Res. 2010;49(3): 1333–1350. https://doi.org/10.1021/ie901307j</mixed-citation><mixed-citation xml:lang="en">Huang K., Liu W., Ma J., Wang S. Externally heat-integrated double distillation column (EHIDDiC): basic concept and general characteristics. Ind. Eng. Chem. Res. 2010;49(3): 1333–1350. https://doi.org/10.1021/ie901307j</mixed-citation></citation-alternatives></ref><ref id="cit68"><label>68</label><citation-alternatives><mixed-citation xml:lang="ru">Rudakov D.G., Klauzner P.S., Ramochnikov D.A., Anokhina E.A., Timoshenko A.V. Efficiency of Using Heat Pumps in the Extractive Rectification of an Allyl Alcohol– Allyl Acetate Mixture Depending on the Composition of the Feed. Part 2. Application of Heat Pumps in Column Complexes with Partially Coupled Heat and Material Flows. Theor. Found. Chem. Eng. 2024;58(1):192–201. https://doi.org/10.1134/S0040579524700337</mixed-citation><mixed-citation xml:lang="en">Rudakov D.G., Klauzner P.S., Ramochnikov D.A., Anokhina E.A., Timoshenko A.V. Efficiency of Using Heat Pumps in the Extractive Rectification of an Allyl Alcohol– Allyl Acetate Mixture Depending on the Composition of the Feed. Part 2. Application of Heat Pumps in Column Complexes with Partially Coupled Heat and Material Flows. Theor. Found. Chem. Eng. 2024;58(1):192–201. https://doi.org/10.1134/S0040579524700337</mixed-citation></citation-alternatives></ref><ref id="cit69"><label>69</label><citation-alternatives><mixed-citation xml:lang="ru">Клаузнер П.С., Рудаков Д.Г., Анохина Е.А., Тимошенко А.В. Закономерности применения тепловых насосов в экстрактивной ректификации. Теор. основы хим. технологии. 2022;56(3):313–325. https://doi.org/10.31857/S0040357122030071</mixed-citation><mixed-citation xml:lang="en">KlauznerP.S., RudakovD.G., AnokhinaE.A., TimoshenkoA.V. Application Regularities of Heat Pumps in Extractive Distillation. Theor. Found. Chem. Eng. 2022;56(3):308–320. https://doi.org/10.1134/S0040579522030071 [Original Russian Text: Klauzner P.S., Rudakov D.G., Anokhina E.A., Timoshenko A.V. Application Regularities of Heat Pumps in Extractive Distillation. Teoreticheskie osnovy khimicheskoi tekhnologii. 2022;56(3):313–325 (in Russ.). https://doi.org/10.31857/S0040357122030071 ]</mixed-citation></citation-alternatives></ref><ref id="cit70"><label>70</label><citation-alternatives><mixed-citation xml:lang="ru">Wang Y., Zhang Z., Xu D., Liu W., Zhu Z. Design and control of pressure-swing distillation for azeotropes with different types of boiling behavior at different pressures. J. Process. Control. 2016;42:59–76. https://doi.org/10.1016/j.jprocont.2016.04.006</mixed-citation><mixed-citation xml:lang="en">Wang Y., Zhang Z., Xu D., Liu W., Zhu Z. Design and control of pressure-swing distillation for azeotropes with different types of boiling behavior at different pressures. J. Process. Control. 2016;42:59–76. https://doi.org/10.1016/j.jprocont.2016.04.006</mixed-citation></citation-alternatives></ref><ref id="cit71"><label>71</label><citation-alternatives><mixed-citation xml:lang="ru">Luyben W.L. Control comparison of conventional and thermally coupled ternary extractive distillation processes. Chem. Eng. Res. Des. 2016;106:253–262. https://doi.org/10.1016/j.cherd.2015.11.021</mixed-citation><mixed-citation xml:lang="en">Luyben W.L. Control comparison of conventional and thermally coupled ternary extractive distillation processes. Chem. Eng. Res. Des. 2016;106:253–262. https://doi.org/10.1016/j.cherd.2015.11.021</mixed-citation></citation-alternatives></ref><ref id="cit72"><label>72</label><citation-alternatives><mixed-citation xml:lang="ru">Gil I.D., Gómez J.M., Rodríguez G. Control of an extractive distillation process to dehydrate ethanol using glycerol as entrainer. Comput. Chem. Eng. 2012;39:129–142. https://doi.org/10.1016/j.compchemeng.2012.01.006</mixed-citation><mixed-citation xml:lang="en">Gil I.D., Gómez J.M., Rodríguez G. Control of an extractive distillation process to dehydrate ethanol using glycerol as entrainer. Comput. Chem. Eng. 2012;39:129–142. https://doi.org/10.1016/j.compchemeng.2012.01.006</mixed-citation></citation-alternatives></ref><ref id="cit73"><label>73</label><citation-alternatives><mixed-citation xml:lang="ru">Qin J., Ye Q., Xiong X., Li N. Control of benzene-cyclohexane separation system via extractive distillation using sulfolane as entrainer. Ind. Eng. Chem. Res. 2013;52(31):10754–10766. https://doi.org/10.1021/ie401101c</mixed-citation><mixed-citation xml:lang="en">Qin J., Ye Q., Xiong X., Li N. Control of benzene-cyclohexane separation system via extractive distillation using sulfolane as entrainer. Ind. Eng. Chem. Res. 2013;52(31):10754–10766. https://doi.org/10.1021/ie401101c</mixed-citation></citation-alternatives></ref><ref id="cit74"><label>74</label><citation-alternatives><mixed-citation xml:lang="ru">Wei H.-M., Wang F., Zhang J.-L., Liao B., Zhao N., Xiao F., Wei W., Sun Y. Design and control of dimethyl carbonate-methanol separation via pressure-swing distillation. Ind. Eng. Chem. Res. 2013;52(33):11463–11478. https://doi.org/10.1021/ie3034976</mixed-citation><mixed-citation xml:lang="en">Wei H.-M., Wang F., Zhang J.-L., Liao B., Zhao N., Xiao F., Wei W., Sun Y. Design and control of dimethyl carbonate-methanol separation via pressure-swing distillation. Ind. Eng. Chem. Res. 2013;52(33):11463–11478. https://doi.org/10.1021/ie3034976</mixed-citation></citation-alternatives></ref><ref id="cit75"><label>75</label><citation-alternatives><mixed-citation xml:lang="ru">Fan Z., Zhang X., Cai W., Wang F. Design and control of extraction distillation for dehydration of tetrahydrofuran. Chem. Eng. Technol. 2013;36(5):829–839. https://doi.org/10.1002/ceat.201200611</mixed-citation><mixed-citation xml:lang="en">Fan Z., Zhang X., Cai W., Wang F. Design and control of extraction distillation for dehydration of tetrahydrofuran. Chem. Eng. Technol. 2013;36(5):829–839. https://doi.org/10.1002/ceat.201200611</mixed-citation></citation-alternatives></ref></ref-list><fn-group><fn fn-type="conflict"><p>The authors declare that there are no conflicts of interest present.</p></fn></fn-group></back></article>
