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<article 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" xmlns:ali="http://www.niso.org/schemas/ali/1.0/" article-type="research-article" dtd-version="1.2" xml:lang="en"><front><journal-meta><journal-id journal-id-type="publisher-id">Petroleum Chemistry</journal-id><journal-title-group><journal-title xml:lang="en">Petroleum Chemistry</journal-title><trans-title-group xml:lang="ru"><trans-title>Нефтехимия</trans-title></trans-title-group></journal-title-group><issn publication-format="print">0028-2421</issn><issn publication-format="electronic">3034-5626</issn><publisher><publisher-name xml:lang="en">The Russian Academy of Sciences</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="publisher-id">655588</article-id><article-id pub-id-type="doi">10.31857/S002824212305009X</article-id><article-id pub-id-type="edn">RZUFEH</article-id><article-categories><subj-group subj-group-type="toc-heading" xml:lang="en"><subject>Articles</subject></subj-group><subj-group subj-group-type="toc-heading" xml:lang="ru"><subject>Статьи</subject></subj-group><subj-group subj-group-type="article-type"><subject>Research Article</subject></subj-group></article-categories><title-group><article-title xml:lang="en">Рt/SAPO-11 Catalytic Systems Differing in Acidity and Secondary Pore Structure in n-Hexadecane Hydroisomerization</article-title><trans-title-group xml:lang="ru"><trans-title>Каталитические системы Pt/SAPO-11 с различными кислотностью и вторичной пористой структурой в гидроизомеризации <italic>н</italic>-гексадекана</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author"><name-alternatives><name xml:lang="en"><surname>Agliullin</surname><given-names>M. R.</given-names></name><name xml:lang="ru"><surname>Аглиуллин</surname><given-names>М. Р.</given-names></name></name-alternatives><email>maratradikovich@mail.ru</email><xref ref-type="aff" rid="aff1"/></contrib><contrib contrib-type="author"><name-alternatives><name xml:lang="en"><surname>Serebrennikov</surname><given-names>D. V.</given-names></name><name xml:lang="ru"><surname>Серебренников</surname><given-names>Д. В.</given-names></name></name-alternatives><email>petrochem@ips.ac.ru</email><xref ref-type="aff" rid="aff1"/></contrib><contrib contrib-type="author"><name-alternatives><name xml:lang="en"><surname>Khazipova</surname><given-names>A. N.</given-names></name><name xml:lang="ru"><surname>Хазипова</surname><given-names>А. Н.</given-names></name></name-alternatives><email>petrochem@ips.ac.ru</email><xref ref-type="aff" rid="aff1"/></contrib><contrib contrib-type="author"><name-alternatives><name xml:lang="en"><surname>Malunov</surname><given-names>A. I.</given-names></name><name xml:lang="ru"><surname>Малунов</surname><given-names>А. И.</given-names></name></name-alternatives><email>petrochem@ips.ac.ru</email><xref ref-type="aff" rid="aff1"/></contrib><contrib contrib-type="author"><name-alternatives><name xml:lang="en"><surname>Dement'ev</surname><given-names>K. I.</given-names></name><name xml:lang="ru"><surname>Дементьев</surname><given-names>К. И.</given-names></name></name-alternatives><email>petrochem@ips.ac.ru</email><xref ref-type="aff" rid="aff2"/></contrib><contrib contrib-type="author"><name-alternatives><name xml:lang="en"><surname>Kutepov</surname><given-names>B. I.</given-names></name><name xml:lang="ru"><surname>Кутепов</surname><given-names>Б. И.</given-names></name></name-alternatives><email>petrochem@ips.ac.ru</email><xref ref-type="aff" rid="aff1"/></contrib></contrib-group><aff-alternatives id="aff1"><aff><institution xml:lang="en">Institute of Petrochemistry and Catalysis, Ufa Federal Research Center, Russian Academy of Sciences</institution></aff><aff><institution xml:lang="ru">Институт нефтехимии и катализа УФИЦ РАН</institution></aff></aff-alternatives><aff-alternatives id="aff2"><aff><institution xml:lang="en">Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences</institution></aff><aff><institution xml:lang="ru">Институт нефтехимического синтеза им. А.В. Топчиева РАН</institution></aff></aff-alternatives><pub-date date-type="pub" iso-8601-date="2023-09-15" publication-format="electronic"><day>15</day><month>09</month><year>2023</year></pub-date><volume>63</volume><issue>5</issue><issue-title xml:lang="en">NO5 (2023)</issue-title><issue-title xml:lang="ru">№5 (2023)</issue-title><fpage>709</fpage><lpage>719</lpage><history><date date-type="received" iso-8601-date="2025-02-11"><day>11</day><month>02</month><year>2025</year></date></history><permissions><copyright-statement xml:lang="en">Copyright ©; 2023, Russian Academy of Sciences</copyright-statement><copyright-statement xml:lang="ru">Copyright ©; 2023, Российская академия наук</copyright-statement><copyright-year>2023</copyright-year><copyright-holder xml:lang="en">Russian Academy of Sciences</copyright-holder><copyright-holder xml:lang="ru">Российская академия наук</copyright-holder></permissions><self-uri xlink:href="https://journals.eco-vector.com/0028-2421/article/view/655588">https://journals.eco-vector.com/0028-2421/article/view/655588</self-uri><abstract xml:lang="en"><p>SAPO-11 molecular sieve samples differing in the acid properties, crystal morphology and size, and secondary pore structure characteristics were obtained by crystallization of reaction gels with the SiO2/Al2O3 molar ratios of 0.1 and 0.3, prepared using aluminum isopropoxide or boehmite as an aluminum source. Platinum (0.5 wt %) was deposited onto the molecular sieves prepared, and the catalytic properties of the resulting samples in n-hexadecane hydroisomerization were studied. The hydrocarbon conversion on these samples varies from 76.8 to 87.7 wt %, and the isoparaffin formation selectivity, from 76.7 to 91.2 wt %.</p></abstract><trans-abstract xml:lang="ru"><p>Кристаллизацией реакционных гелей с мольными соотношениями SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>, равными 0.1 и 0.3, приготовленных с использованием в качестве источника алюминия изопропоксида или бёмита, получены образцы молекулярного сита SAPO-11, различающиеся кислотными свойствами, морфологией, размерами кристаллов, характеристиками вторичной пористой структуры. Каталитические свойства синтезированных образцов после нанесения на них 0.5 мас. % Pt изучены в реакции гидроизомеризации н -гексадекана. Установлено, что конверсия углеводорода на этих образцах изменяется от 76.8 до 87.7 мас %, а селективность образования изо -парафинов - от 76.7 до 91.2 мас %.</p></trans-abstract><kwd-group xml:lang="en"><kwd>n-paraffin hydroisomerization</kwd><kwd>bifunctional catalysts</kwd><kwd>zeolites</kwd><kwd>silicoaluminophosphate molecular sieves</kwd></kwd-group><kwd-group xml:lang="ru"><kwd>гидроизомеризация н-парафинов</kwd><kwd>бифункциональные катализаторы</kwd><kwd>цеолиты</kwd><kwd>силикоалюмофосфатные молекулярные сита</kwd></kwd-group></article-meta></front><body></body><back><ref-list><ref id="B1"><label>1.</label><mixed-citation>Akhmedov V.M., Al-Khowaiter S.H. Recent advances and future aspects in the selective isomerization of high n-alkanes // Catalysis Reviews. 2007. V. 49. P. 33-139. https://doi.org/10.1080/01614940601128427</mixed-citation></ref><ref id="B2"><label>2.</label><mixed-citation>Wang W., Wu W., Liu C.-J. 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