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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">10.32362/2410-6593-2017-12-3-33-43</article-id><article-id custom-type="elpub" pub-id-type="custom">chemicallytech-91</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>ENERGy EFFICIENCy OF THE COMPLEX COLUMN FOR THE SEPARATION OF VAPOR CRACkING PRODUCTS UNDER  THE DEPENDING ON FEED COMPOSITION</article-title><trans-title-group xml:lang="ru"><trans-title>ЭНЕРГЕТИЧЕСКАЯ ЭФФЕКТИВНОСТЬ СЛОЖНОЙ КОЛОННЫ ПРИ РАЗДЕЛЕНИИ ПРОДУКТОВ ПИРОЛИЗА В ЗАВИСИМОСТИ ОТ СОСТАВА ПИТАНИЯ</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>Кочарян</surname><given-names>С. О.</given-names></name><name name-style="western" xml:lang="en"><surname>Kocharyan</surname><given-names>S. O.</given-names></name></name-alternatives><bio xml:lang="ru"><p>аспирант кафедры химии и технологии основного органического синтеза</p><p>119571, Россия, Москва, пр-т Вернадского, д. 86</p></bio><bio xml:lang="en"><p>Moscow 119571, Russia</p></bio><email xlink:type="simple">kocharyanso@mitht.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>Рудаков</surname><given-names>Д. Г.</given-names></name><name name-style="western" xml:lang="en"><surname>Rudakov</surname><given-names>D. G.</given-names></name></name-alternatives><bio xml:lang="ru"><p>кандидат технических наук, ассистент кафедры химии и технологии основного органического синтеза</p><p>119571, Россия, Москва, пр-т Вернадского, д. 86</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>Тимошенко</surname><given-names>А. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Timoshenko</surname><given-names>A. V.</given-names></name></name-alternatives><bio xml:lang="ru"><p>доктор технических наук, профессор кафедры химии и технологии основного органического синтеза</p><p>119571, Россия, Москва, пр-т Вернадского, д. 86</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-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>2017</year></pub-date><pub-date pub-type="epub"><day>28</day><month>06</month><year>2017</year></pub-date><volume>12</volume><issue>3</issue><fpage>33</fpage><lpage>43</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Kocharyan S.O., Rudakov D.G., Timoshenko A.V., 2017</copyright-statement><copyright-year>2017</copyright-year><copyright-holder xml:lang="ru">Кочарян С.О., Рудаков Д.Г., Тимошенко А.В.</copyright-holder><copyright-holder xml:lang="en">Kocharyan S.O., Rudakov D.G., Timoshenko A.V.</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/91">https://www.finechem-mirea.ru/jour/article/view/91</self-uri><abstract><p>The dependence of the energy consumption decrease on the different feed composition for the separation of C4+ vapor cracking fraction by means of complex columns implementation is investigated. Distillation sequences consisting of simple columns and partially thermally coupled distillation columns are compared. Cases of direct and indirect separation for all the schemes are considered. In order to reduce capital cost and industrial areas the implementation of dividing wall columns was proposed. These dividing wall columns are the thermodynamic analogs of partially thermally coupled distillation flowsheets. Analysis of temperature, liquid and vapor profiles in the partially thermally coupled distillation sequence revealed that only one column in the original flowsheets requires a structural change when converting it to the partially thermally coupled configuration. It is shown that the complex columns provide energy consumption reduction in the reboilers by 3-60% as compared to conventional distillation schemes.</p></abstract><trans-abstract xml:lang="ru"><p>Исследована зависимость снижения энергетических затрат на разделение смеси C4+ фракций продуктов пиролиза за счет применения сложных колонн для различного состава сырья. Рассмотрено ректификационное разделение как в последовательностях, состоящих из двухотборных колонн, так и в комплексах с частично связанными тепловыми и материальными потоками, полученных на их основе. Для всех вариантов схем исследованы режимы работы по первому и второму заданным разделениям. С целью снижения капитальных затрат и уменьшения занимаемых производственных площадей предложено использование колонн с перегородками, которые являются термодинамическими аналогами комплексов с частично связанными тепловыми и материальными потоками. Изучено распределение температур, потоков жидкости и пара по высоте колонн; на основе этого показано, что при переходе к комплексам с частично связанными тепловыми и материальными потоками только одна из колонн потребует конструктивных изменений. Выявлено, что использование сложных колонн обеспечивает снижение энергозатрат в кипятильниках на 3-60% относительно схем из простых колонн.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>пиролиз</kwd><kwd>ректификация</kwd><kwd>энергосбережение</kwd><kwd>сложные колонны</kwd><kwd>С4-С6 фракции углеводородов</kwd><kwd>С4-С6 hydrocarbon fractions</kwd></kwd-group><kwd-group xml:lang="en"><kwd>vapor cracking</kwd><kwd>distillation</kwd><kwd>energy saving</kwd><kwd>complex column</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">Litvintsev I.Yu. 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