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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">10.32362/2410-6593-2016-11-4-15-25</article-id><article-id custom-type="elpub" pub-id-type="custom">chemicallytech-35</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>DISTILLATION OF BINARY TWO-PHASE MIXTURES WITH VARIOUS PHYSICO-CHEMICAL PROPERTIES: NORMAL MODE AND DEVIATIONS FROM IT</article-title><trans-title-group xml:lang="ru"><trans-title>РЕКТИФИКАЦИЯ БИНАРНЫХ ДВУХФАЗНЫХ СМЕСЕЙ РАЗНОЙ ФИЗИКО-ХИМИЧЕСКОЙ ПРИРОДЫ: НОРМАЛЬНЫЙ РЕЖИМ И ОТКЛОНЕНИЯ ОТ НЕГО</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>Серафимов</surname><given-names>Л. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Serafimov</surname><given-names>L. A.</given-names></name></name-alternatives><bio xml:lang="ru"><p>профессор, 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">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>Морозов</surname><given-names>К. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Morozov</surname><given-names>K. A.</given-names></name></name-alternatives><bio xml:lang="ru"><p>аспирант, 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">kamorozov@mitht.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Московский технологический университет (Институт тонких химических технологий)</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Moscow Technological University (Institute of Fine Chemical Technologies)</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2016</year></pub-date><pub-date pub-type="epub"><day>28</day><month>08</month><year>2016</year></pub-date><volume>11</volume><issue>4</issue><fpage>15</fpage><lpage>25</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Serafimov L.A., Morozov K.A., 2016</copyright-statement><copyright-year>2016</copyright-year><copyright-holder xml:lang="ru">Серафимов Л.А., Морозов К.А.</copyright-holder><copyright-holder xml:lang="en">Serafimov L.A., Morozov K.A.</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/35">https://www.finechem-mirea.ru/jour/article/view/35</self-uri><abstract><p>In this article, the normal continuous mode of distillation is considered using an example of binary two-phase mixture distillation. In practice, there are often deviations from the normal mode. It has been proved that the deviation leads to an increase in energy consumption for the ongoing process. In the industry, columns separating binary mixtures are normally the finishing apparatuses in the flow-sheet separation of multicomponent mixtures, which are obtained in the reactor as a result of main reactions as well as by-reactions. The distillation of binary mixtures is relatively simpler than that of multicomponent mixtures. In this regard, the fundamental parts of monographs especially in the thirties-forties of the last century started with the study of binary mixtures, although multicomponent mixtures were the main focus. The aim of analyzing this complex and the highly energy-intensive process is to facilitate the choice of a mathematical model for the process and the determination on its basis variance. Variance is a set of independent variables that allow calculation of a process only after taking into account the number of independent equations related to these variables. A case of deviation from the normal distillation regime where an under-heated liquid enters the column feed has been revised. This leads to an increase in energy consumption during distillation. Key indicators of the normal regime relative to the level of feed and the temperature of the liquid are shown in the text.</p></abstract><trans-abstract xml:lang="ru"><p>Рассмотрено отклонение от нормального режима ректификации в случае подачи в колонну недогретой жидкости. Последнее приводит к завышению энергозатрат на ректификацию. Приводятся основные показатели нормального режима относительно уровня подачи, температуры подаваемой жидкости.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>нормальный режим ректификации</kwd><kwd>проектный расчет</kwd><kwd>виртуальные режимы ректификации</kwd><kwd>специальные режимы ректификации</kwd><kwd>минимальное флегмовое число</kwd><kwd>максимальное паровое число</kwd></kwd-group><kwd-group xml:lang="en"><kwd>normal distillation mode</kwd><kwd>design calculations</kwd><kwd>virtual modes of distillation</kwd><kwd>special modes of distillation</kwd><kwd>minimum reflux ratio</kwd><kwd>maximum boilup ratio</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">Робинзон К.Ш. Основные начала дробной перегонки: пер. с англ. П.И. Котлярова / под ред. И.А. Красуского. 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