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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">655604</article-id><article-id pub-id-type="doi">10.31857/S0028242123040123</article-id><article-id pub-id-type="edn">OQDXIX</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">Hydrogenation of Acetylene over Pd–Ag/Sibunit Catalysts: Effect of the Deposition Sequence of Active Component Precursors</article-title><trans-title-group xml:lang="ru"><trans-title>Гидрирование ацетилена на катализаторе Pd-Ag/cибунит: влияние последовательности нанесения предшественников активного компонента</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author"><name-alternatives><name xml:lang="en"><surname>Yurpalova</surname><given-names>D. V.</given-names></name><name xml:lang="ru"><surname>Юрпалова</surname><given-names>Д. В.</given-names></name></name-alternatives><email>omsk-glyzdova@mail.ru</email><xref ref-type="aff" rid="aff1"/></contrib><contrib contrib-type="author"><name-alternatives><name xml:lang="en"><surname>Afonasenko</surname><given-names>T. N.</given-names></name><name xml:lang="ru"><surname>Афонасенко</surname><given-names>Т. 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>Trenikhin</surname><given-names>M. V.</given-names></name><name xml:lang="ru"><surname>Тренихин</surname><given-names>М. 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>Leont'eva</surname><given-names>N. N.</given-names></name><name xml:lang="ru"><surname>Леонтьева</surname><given-names>Н. 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>Arbuzov</surname><given-names>A. B.</given-names></name><name xml:lang="ru"><surname>Арбузов</surname><given-names>А. Б</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>Temerev</surname><given-names>V. L.</given-names></name><name xml:lang="ru"><surname>Темерев</surname><given-names>В. Л</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>Shlyapin</surname><given-names>D. A.</given-names></name><name xml:lang="ru"><surname>Шляпин</surname><given-names>Д. А</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">Center of New Chemical Technologies BIC, Boreskov Institute of Catalysis</institution></aff><aff><institution xml:lang="ru">Центр новых химических технологий ИК СО РАН, Институт катализа СО РАН</institution></aff></aff-alternatives><pub-date date-type="pub" iso-8601-date="2023-07-15" publication-format="electronic"><day>15</day><month>07</month><year>2023</year></pub-date><volume>63</volume><issue>4</issue><issue-title xml:lang="en">NO4 (2023)</issue-title><issue-title xml:lang="ru">№4 (2023)</issue-title><fpage>582</fpage><lpage>594</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/655604">https://journals.eco-vector.com/0028-2421/article/view/655604</self-uri><abstract xml:lang="en"><p>The study investigates interactions between palladium and silver in Pd–Ag bimetallic catalysts supported on a mesoporous carbon material Sibunit and, in particular, the dependence of these interactions on the deposition sequence of the metal precursors. Using XRD and TEM results, it was shown that impregnating the support with an aqueous solution that contained nitrate salts of both metals, followed by hydrogen treatment at 500°C, generates uniformly sized Pd0.6Ag0.4 particles (dav = 5.6 nm). These particles exhibit high selectivity (79%) in the reaction of acetylene hydrogenation to ethylene. The catalysts synthesized by sequential impregnation of the support with solutions of Pd and Ag nitrates interleaved with heat treatment in H2 exhibited a lower selectivity (68–73%) due to the formation of particles non-uniform both in composition and size (about 4 to 60 nm). The IR spectroscopy data suggest this effect is presumably associated with the removal of O-containing functional groups from the carbon surface during the reduction of the supported precursor. Given that O-groups act as anchoring sites for the precursors of active components and suppress the ability of Sibunit to reduce metals from their salt solutions, the subsequent deposition of the second metal salt causes a non-uniform distribution of this metal on the surface and the generation of larger particles.</p></abstract><trans-abstract xml:lang="ru"><p>Изучено взаимодействие между палладием и серебром в биметаллических Pd-Ag-катализаторах, нанесенных на мезопористый углеродный материал сибунит, в зависимости от последовательности нанесения предшественников металлов. Методами РФА и ПЭМ показано, что пропитка носителя водным раствором, содержащим нитратные соли обоих металлов, с последующей обработкой водородом при 500°С приводит к формированию однородных по размеру частиц Pd<sub>0.6</sub>Ag<sub>0.4 </sub>( d <sub>ср </sub>= 5.6 нм), которые проявляют высокую селективность (79%) в реакции гидрирования ацетилена в этилен. Катализаторы, приготовленные путем последовательной пропитки носителя растворами нитратов палладия и серебра с промежуточным прокаливанием в H<sub>2</sub>, менее селективны (68-73%) вследствие образования частиц разнородных по составу и размерам (от ~4 до 60 нм). На основании данных ИК-спектроскопии предполагается, что данный эффект связан с удалением О-содержащих функциональных групп с поверхности углеродного материала в ходе восстановительной обработки нанесенного предшественника. О-группы выступают центрами закрепления предшественников активного компонента и снижают способность сибунита восстанавливать металлы из растворов их солей, поэтому последовательное нанесение соли второго металла приводит к его неравномерному распределению по поверхности и образованию более крупных частиц.</p></trans-abstract><kwd-group xml:lang="en"><kwd>bimetallic catalysts</kwd><kwd>Pd–Ag</kwd><kwd>Sibunit carbon support</kwd><kwd>selective hydrogenation of acetylene</kwd></kwd-group><kwd-group xml:lang="ru"><kwd>биметаллические катализаторы</kwd><kwd>углеродный носитель сибунит</kwd><kwd>селективное гидрирование ацетилена</kwd></kwd-group></article-meta></front><body></body><back><ref-list><ref id="B1"><label>1.</label><mixed-citation>Dehghani O., Rahimpour M.R., Shariati A. An experimental approach on industrial Pd-Ag supported α-Al2O3 catalyst used in acetylene hydrogenation process: mechanism, kinetic and catalyst decay // Processes. 2019. V. 7. 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