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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">10.32362/2410-6593-2016-11-3-47-57</article-id><article-id custom-type="elpub" pub-id-type="custom">chemicallytech-29</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>The multivariate calculation of material balances of flowsheets for separating ternary mixtures of different physical-chemical nature</article-title><trans-title-group xml:lang="ru"><trans-title>ПОЛИВАРИАНТНОСТЬ РАСЧЕТА МАТЕРИАЛЬНЫХ БАЛАНСОВ СХЕМ РАЗДЕЛЕНИЯ ТРЕХКО МПОНЕНТНЫХ СМЕСЕЙ РАЗЛИЧНОЙ ФИЗИКО-ХИМИЧЕСКОЙ ПРИРОДЫ</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><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>доцент, кафедра химии и технологии основного органического синтеза</p><p> </p></bio><bio xml:lang="en"><p>Moscow, 119571 Russia</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"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Аблизин</surname><given-names>М. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Ablizin</surname><given-names>M. A.</given-names></name></name-alternatives><bio xml:lang="ru"><p>студент, кафедра химии и технологии основного органического синтеза</p><p>Москва, 119571 Россия</p></bio><bio xml:lang="en"><p>Moscow, 119571 Russia</p></bio><email xlink:type="simple">noemail@neicon.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Маевский</surname><given-names>М. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Mayevskiy</surname><given-names>M. A.</given-names></name></name-alternatives><bio xml:lang="ru"><p>студент, кафедра химии и технологии основного органического синтеза</p></bio><bio xml:lang="en"><p>Moscow, 119571 Russia</p></bio><email xlink:type="simple">noemail@neicon.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Фролкова</surname><given-names>А. К.</given-names></name><name name-style="western" xml:lang="en"><surname>Frolkova</surname><given-names>A. K.</given-names></name></name-alternatives><bio xml:lang="ru"><p>зав.кафедрой, кафедра химии и технологии основного органического синтеза </p><p>Москва, 119571 Россия</p></bio><bio xml:lang="en"><p>Moscow, 119571 Russia</p></bio><email xlink:type="simple">noemail@neicon.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff xml:lang="ru" id="aff-1"><institution>Московский технологический университет (Институт тонких химических технологий)</institution><country>Russian Federation</country></aff><pub-date pub-type="collection"><year>2016</year></pub-date><pub-date pub-type="epub"><day>28</day><month>06</month><year>2016</year></pub-date><volume>11</volume><issue>3</issue><fpage>47</fpage><lpage>57</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Frolkova A.V., Ablizin M.A., Mayevskiy M.A., Frolkova A.K., 2016</copyright-statement><copyright-year>2016</copyright-year><copyright-holder xml:lang="ru">Фролкова А.В., Аблизин М.А., Маевский М.А., Фролкова А.К.</copyright-holder><copyright-holder xml:lang="en">Frolkova A.V., Ablizin M.A., Mayevskiy M.A., Frolkova A.K.</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/29">https://www.finechem-mirea.ru/jour/article/view/29</self-uri><abstract><p>An approach to the determination of free variables required for calculating the material balance of the flowsheet of ternary mixtures separation is presented. Phase diagrams of the considered ternary systems are characterized by the presence of a two-phase splitting area and by the presence of different amounts of azeotropes (classes 3.1.0, 3.1.1, 3.2.1 and 3.3.1). For all the systems flowsheets containing three rectification columns and a florentine vessel for separation were suggested. The multivariance of the solution of the balance problem was shown. The approach was illustrated by the example of real ternary systems characterized by different phase diagrams (methanol - chloroform - water, butyl alcohol - water - toluene, nitromethane - hexane - water). The parameters of the rectification columns were presented.</p></abstract><trans-abstract xml:lang="ru"><p>В работе описан подход к определению свободных переменных, необходимых для расчета материального баланса комплекса разделения трехкомпонентных расслаивающихся смесей. Показана поливариантность решения балансовой задачи. Подход проиллюстрирован на примере реальных трехкомпонентных систем, характеризующихся различными фазовыми портретами.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>разделительный комплекс</kwd><kwd>ректификация</kwd><kwd>расслаивание</kwd><kwd>материальный баланс</kwd></kwd-group><kwd-group xml:lang="en"><kwd>rectification</kwd><kwd>separation flowsheet</kwd><kwd>splitting</kwd><kwd>material balance</kwd></kwd-group></article-meta></front><back><ref-list><title>References</title><ref id="cit1"><label>1</label><citation-alternatives><mixed-citation xml:lang="ru">Гиббс Д. В. Термодинамика, статистическая механика. М.: Наука, 1982. 384 с.</mixed-citation><mixed-citation xml:lang="en">Gibbs D.V. Termodinamika, statisticheskaya mekhanika (Thermodynamics, statistical mechanics). M.: Nauka, 1982. 384 p.</mixed-citation></citation-alternatives></ref><ref id="cit2"><label>2</label><citation-alternatives><mixed-citation xml:lang="ru">Seader J. D., Henley E. Separation process principles. 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