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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="ru"><front><journal-meta><journal-id journal-id-type="publisher-id">catal</journal-id><journal-title-group><journal-title xml:lang="ru">Катализ в промышленности</journal-title><trans-title-group xml:lang="en"><trans-title>Kataliz v promyshlennosti</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">1816-0387</issn><issn pub-type="epub">2413-6476</issn><publisher><publisher-name>LLC "KALVIS"</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.18412/1816-0387-2024-2-51-58</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-1006</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="ru"><subject>КАТАЛИЗ В ХИМИЧЕСКОЙ И НЕФТЕХИМИЧЕСКОЙ ПРОМЫШЛЕННОСТИ</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>CATALYSIS IN CHEMICAL AND PETROCHEMICAL INDUSTRY</subject></subj-group></article-categories><title-group><article-title>Вариация формы каталитических блоков в процессе автотермического риформинга гексадекана, пропана и метана методом математического моделирования</article-title><trans-title-group xml:lang="en"><trans-title>Variation of the shapes of catalytic blocks in the autothermal reforming of hexadecane, propane and methane using mathematical modeling</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>Зажигалов</surname><given-names>С. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Zazhigalov</surname><given-names>S. V.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.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>Шилов</surname><given-names>В. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Shilov</surname><given-names>V. A.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-2"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Загоруйко</surname><given-names>А. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Zagoruiko</surname><given-names>A. N.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.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>Снытников</surname><given-names>П. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Snytnikov</surname><given-names>P. V.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Институт катализа им. Г.К. Борескова СО РАН (ИК СО РАН), Новосибирск</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Boreskov Institute of Catalysis, Novosibirsk</institution><country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru"><institution>Институт катализа им. Г.К. Борескова СО РАН (ИК СО РАН), Новосибирск; Новосибирский государственный университет (НГУ)</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Boreskov Institute of Catalysis, Novosibirsk; Novosibisk State University</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2024</year></pub-date><pub-date pub-type="epub"><day>20</day><month>03</month><year>2024</year></pub-date><volume>24</volume><issue>2</issue><fpage>51</fpage><lpage>58</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2024</copyright-statement><copyright-year>2024</copyright-year><copyright-holder xml:lang="ru">LLC "KALVIS"</copyright-holder><copyright-holder xml:lang="en">LLC "KALVIS"</copyright-holder><license xlink:href="https://www.catalysis-kalvis.ru/jour/about/submissions#copyrightNotice" xlink:type="simple"><license-p>https://www.catalysis-kalvis.ru/jour/about/submissions#copyrightNotice</license-p></license></permissions><self-uri xlink:href="https://www.catalysis-kalvis.ru/jour/article/view/1006">https://www.catalysis-kalvis.ru/jour/article/view/1006</self-uri><abstract><p>Проведено математическое моделирование автотермического риформинга гексадекана, пропана и метана на каталитических блоках разной геометрической формы. Было показано, что выпуклая в сторону набегающего реакционного потока форма блока может повысить максимальную температуру в лобовой зоне, в то время как вогнутая форма способствует более равномерному распределению температуры по всей длине каталитического слоя. В работе также было исследовано влияние реакционной скорости потока на изменение температурного градиента, что впоследствии может быть использовано для предотвращения образования локальных перегревов и дезактивации катализатора. Полученные результаты могут служить основой для будущих исследований в области автотермического риформинга и оптимизации геометрических параметров катализаторов конверсии углеводородных топлив в синтез-газ.</p></abstract><trans-abstract xml:lang="en"><p>In this work, mathematical modeling of the autothermal reforming of hexadecane, propane and methane on catalytic blocks of different geometric shapes was carried out. It was shown that the convex shape of the block towards the oncoming reaction flow can increase the maximum temperature in the frontal zone, while the concave shape contributes to a more uniform temperature distribution along the entire length of the catalytic layer. The work also investigated the effect of the reaction flow rate on the change in the temperature gradient, which can subsequently be used to prevent the formation of hot spots and catalyst deactivation. The results obtained can serve as the basis for future research in the field of autothermal reforming and optimization of the geometric parameters of catalysts for the conversion of hydrocarbon fuels into synthesis gas.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>автотермический риформинг</kwd><kwd>математическое моделирование</kwd><kwd>оптимизация геометрии</kwd><kwd>дизель</kwd><kwd>метан</kwd><kwd>пропан</kwd><kwd>водород</kwd><kwd>структурированный катализатор</kwd></kwd-group><kwd-group xml:lang="en"><kwd>autothermal reforming</kwd><kwd>math modeling</kwd><kwd>geometry optimization</kwd><kwd>diesel</kwd><kwd>methane</kwd><kwd>propane</kwd><kwd>hydrogen</kwd><kwd>structured catalyst</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">Rahim Malik F., Yuan H. B., Moran J. C., Tippayawong N. 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