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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">10.18412/1816-0387-2026-2-85-93</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-1257</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 НЕФТЕПЕРЕРАБАТЫВАЮЩЕЙ ПРОМЫШЛЕННОСТИ</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>СATALYSIS IN PETROLEUM REFINING INDUSTRY</subject></subj-group></article-categories><title-group><article-title>Сульфидные NiMo/цеолит-Al2O3-катализаторы для гидроочистки сырья, включающего в себя хлорсодержащее термолизное масло</article-title><trans-title-group xml:lang="en"><trans-title>NiMo/zeolite-Al2O3 sulfide catalysts for hydrotreating feedstocks including chlorine-containing thermolysis oil</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>Богомолова</surname><given-names>Т. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Bogomolova</surname><given-names>T. S.</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>Крестьянинова</surname><given-names>В. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Krestyaninova</surname><given-names>V. S.</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>Романова</surname><given-names>Т. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Romanova</surname><given-names>T. S.</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>Мухачёва</surname><given-names>П. П.</given-names></name><name name-style="western" xml:lang="en"><surname>Mukhacheva</surname><given-names>P. P.</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>Саломатина</surname><given-names>А. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Salomatina</surname><given-names>A. A.</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>Надеина</surname><given-names>К. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Nadeina</surname><given-names>K. A.</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>Ватутина</surname><given-names>Ю. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Vatutina</surname><given-names>Yu. 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>Климов</surname><given-names>О. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Klimov</surname><given-names>O. 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">Институт катализа им. Г.К. Борескова СО РАН, Новосибирск<country>Россия</country></aff><aff xml:lang="en">G.K. Boreskov Institute of Catalysis of the Siberian Branch of the Russian Academy of Science<country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru">Институт катализа им. Г.К. Борескова СО РАН, Новосибирск; Новосибирский институт органической химии им. Н.Н. Ворожцова СО РАН, Новосибирск<country>Россия</country></aff><aff xml:lang="en">G.K. Boreskov Institute of Catalysis of the Siberian Branch of the Russian Academy of Science; N.N. Vorozhtsov Novosibirsk Institute of Organic Chemistry of the Siberian Branch of the Russian Academy of Science<country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2026</year></pub-date><pub-date pub-type="epub"><day>30</day><month>03</month><year>2026</year></pub-date><volume>26</volume><issue>2</issue><fpage>85</fpage><lpage>93</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2026</copyright-statement><copyright-year>2026</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/1257">https://www.catalysis-kalvis.ru/jour/article/view/1257</self-uri><abstract><p>Последние годы ознаменовались не только широким применением пластика во многих отраслях промышленности, но и ростом актуальности переработки и поиска альтернативных методов утилизации пластиковых отходов. В работе предложено внедрение продукта переработки пластиков в гидроочистку традиционных нефтяных фракций. Проведено исследование влияния использования моно- (Y/ZSM-23) и бицеолитных (Y+ZSM-23) сульфидных NiMo-катализаторов на процесс гидроочистки сырья, в состав которого входит хлорсодержащее термолизное масло. Показано, что все синтезированные катализаторы обеспечивают конверсию хлорсодержащих соединений выше 92 %. Обнаружено, что цеолитсодержащие катализаторы в процессе гидроочистки оказывают влияние на фракционный состав полученных гидрогенизатов за счет реакций крекинга и изомеризации, способствуя увеличению выхода светлых фракций. Показано, что катализатор на основе цеолита Y демонстрирует перспективу его применения благодаря высокой активности в превращении гетероатомных соединений и высококипящих н-алканов.</p></abstract><trans-abstract xml:lang="en"><p>Recent years have seen not only by the widespread use of plastics in many industries but also by the growing importance of recycling and the search for alternative methods for plastic waste disposal. The work proposes the integration of plastic refining products into the hydrotreating process of traditional petroleum fractions. The effect of mono- (Y/ZSM-23) and bi-zeolite (Y+ZSM-23) sulfide NiMo catalysts on the hydrotreating process of feedstock comprising chlorine-containing thermolysis oil is studied. It is shown that all synthesized catalysts provide conversion of chlorine-containing compounds above 92%. It is found that zeolite-containing catalysts in the hydrotreating process affect the fractional composition of the obtained products due to cracking and isomerization reactions, contributing to an increase in the yield of light fractions. It is shown that the catalyst based on zeolite Y demonstrates the potential for its application due to its high activity in the conversion of heteroatomic compounds and high-boiling n-alkanes.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>переработка пластика</kwd><kwd>термолизное масло</kwd><kwd>гидроочистка</kwd><kwd>цеолит Y</kwd><kwd>цеолит ZSM-23</kwd><kwd>NiMo-сульфиды</kwd></kwd-group><kwd-group xml:lang="en"><kwd>plastic refining</kwd><kwd>thermolysis oil</kwd><kwd>hydrotreating</kwd><kwd>zeolite Y</kwd><kwd>zeolite ZSM-23</kwd><kwd>NiMo sulfides</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">Brandrup J., Bittner M., Michaeli W., Menges G. Recycling and recovery of plastics. Munich: Hanser, 1996.</mixed-citation><mixed-citation xml:lang="en">Brandrup J., Bittner M., Michaeli W., Menges G. Recycling and recovery of plastics. 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