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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">10.18412/1816-0387-2025-2-79-86</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-1160</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>Паровая конверсия метанола в водородсодержащий газ на нанесенных Pt-содержащих катализаторах</article-title><trans-title-group xml:lang="en"><trans-title>Methanol Steam Reforming to Hydrogen-Containing Gas over Supported Platinum-Containing Catalysts</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>Кузнецова</surname><given-names>А. Д.</given-names></name><name name-style="western" xml:lang="en"><surname>Kuznetsova</surname><given-names>A. D.</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>Рогожников</surname><given-names>В. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Rogozhnikov</surname><given-names>V. N.</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>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-2"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Бадмаев</surname><given-names>С. Д.</given-names></name><name name-style="western" xml:lang="en"><surname>Badmaev</surname><given-names>S. D.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-2"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru">Институт катализа СО РАН, Новосибирск; Новосибирский государственный университет<country>Россия</country></aff><aff xml:lang="en">Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, Novosibirsk; Novosibirsk State University<country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru">Институт катализа СО РАН, Новосибирск<country>Россия</country></aff><aff xml:lang="en">Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, Novosibirsk<country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2025</year></pub-date><pub-date pub-type="epub"><day>28</day><month>03</month><year>2025</year></pub-date><volume>25</volume><issue>2</issue><fpage>79</fpage><lpage>86</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2025</copyright-statement><copyright-year>2025</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/1160">https://www.catalysis-kalvis.ru/jour/article/view/1160</self-uri><abstract><p>Изучены и сопоставлены свойства нанесенных Pt-содержащих гранулированных (Pt/Ce0,75Zr0,25O2) и блочных структурированных (Pt/Ce0,75Zr0,25O2 /η-Al2O3/FeCrAl) катализаторов в отношении реакции паровой конверсии метанола в синтез-газ для питания твердо- оксидных топливных элементов. Сравнительные исследования показали, что активная Pt/Ce0,75Zr0,25O2 система более эффективно работает на блочном структурированном носителе. В частности, катализатор 0,15 мас.% Pt/8 мас.% Ce0,75Zr0,25O2 /6 мас.% η-Al2O3/FeCrAl при атмосферном давлении, температуре 400 °С, скорости подачи реакционной смеси (30 об.% СН3ОН, 35 об.% Н2О, 35 об.% N2) 60 л/(гкат·ч) обеспечивает полную конверсию метанола в синтез-газ с суммарным содержанием Н2 и СО ~60 об.% и производительность по синтез-газу ~85 л (Н2+СО)/(гкат · ч).</p></abstract><trans-abstract xml:lang="en"><p>The catalytic properties of supported Pt-containing granular (Pt/Ce0.75Zr0.25O2) and structured (Pt/Ce0.75Zr0.25O2-δ/η-Al2O3/FeCrAl) catalysts for methanol steam reformong to syngas were studied and compared. Comparative studies prove that the active Pt/Ce0.75Zr0.25O2 system in the structured catalyst operates more efficiently than in the granular catalyst. In particular, the structured catalyst 0.15 wt. % Pt/8 wt. % Ce0.75Zr0.25O2-δ/6 wt. % η-Al2O3/FeCrAl at atmospheric pressure, temperature 400 °C, and the reaction mixture (30 vol. % CH3OH, 35 vol. % H2O, 35 vol. % N2) feed rate of 60 L/(gcat·h), provided complete conversion of methanol to syngas with a total H2 and CO content of ~60 vol. % and syngas productivity of ~85 L(H2+CO)/(gcat·h).</p></trans-abstract><kwd-group xml:lang="ru"><kwd>метанол</kwd><kwd>паровая конверсия</kwd><kwd>синтез-газ</kwd><kwd>платина</kwd><kwd>нанесенные катализаторы</kwd><kwd>блочные структурированные носители</kwd><kwd>FeCrAl</kwd></kwd-group><kwd-group xml:lang="en"><kwd>methanol steam reforming</kwd><kwd>syngas</kwd><kwd>platinum</kwd><kwd>supported catalysts</kwd><kwd>structured supports</kwd><kwd>FeCrAl</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">Агарков Д.А., Бредихин С.И. 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