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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">10.18412/1816-0387-2017-1-37-45</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-408</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>Ингибирование хинолином реакций гидродесульфуризации и гидрирования на Co(Ni)PMo(W)/Al2O3 катализаторах: влияние состава активной фазы на устойчивость в гидроочистке модельного и нефтяного сырья</article-title><trans-title-group xml:lang="en"><trans-title>Quinoline Inhibiting of Hydrodesulfurization and Hydrogenation Reactions over Co(Ni)PMo(W)/Al2O3 Catalysts: Influence of the Active Phase Composition on the Stability during Hydrotreatment of Model and Oil Feedstock</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>Минаев</surname><given-names>П. П.</given-names></name><name name-style="western" xml:lang="en"><surname>Minaev</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>Коклюхин</surname><given-names>А. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Koklyukhin</surname><given-names>A. 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>Маслаков</surname><given-names>К. И.</given-names></name><name name-style="western" xml:lang="en"><surname>Maslakov</surname><given-names>K. I.</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>Никульшин</surname><given-names>П. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Nikul’shin</surname><given-names>P. A.</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>Самарский государственный технический университет (СамГТУ)</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Samara State Technical University</institution><country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru"><institution>Московский государственный университет им. М.В. Ломоносова (МГУ)</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Moscow State University, Chemical Department</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2017</year></pub-date><pub-date pub-type="epub"><day>31</day><month>05</month><year>2017</year></pub-date><volume>17</volume><issue>1</issue><fpage>37</fpage><lpage>45</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2017</copyright-statement><copyright-year>2017</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/408">https://www.catalysis-kalvis.ru/jour/article/view/408</self-uri><abstract><p>Приготовлены Со(Ni)-PMo(W)/Al2O3 катализаторы с использованием гетерополикислот Кеггина H3PMo(W)12O40 и цитрата кобальта (никеля). Физико-химические свойства катализаторов исследованы методами низкотемпературной адсорбции азота, РФЭС и ПЭМВР. Каталитические свойства определяли в гидроочистке модельного сырья, содержащего дибензотиофен, нафталин и различное количество хинолина (до 1000 ppm азота), а также в процессе гидроочистки прямогонной дизельной фракции и вакуумного газойля. Показано, что состав Со(Ni)-PMo(W)/Al2O3 катализаторов играет решающую роль при гидроочистке сложного углеводородного сырья. Ni-PW/Al2O3 катализатор был более устойчив к азоторганическим ингибиторам, чем Ni(Co)-PMo/Al2O3 образцы, имеющие более реакционноспособные активные центры. В результате гидроочистки вакуумного газойля наибольшую глубину превращения сера-, азотсодержащих соединений и полициклических ароматических углеводородов обеспечил Ni-PW/Al2O3 катализатор.</p></abstract><trans-abstract xml:lang="en"><p>Co(Ni)-PMo(W)/Al2O3 catalysts were prepared using Keggin heteropoly acids H3PMo(W)12O40 and cobalt (nickel) citrate. Physicochemicalproperties of the catalysts were characterized using low-temperature nitrogen adsorption, XPS and HRTEM techniques. Catalytic properties were studied during hydrotreatment of a model feedstock containing dibenzothiophene, naphthalene and quinoline in different proportions (up to 1000 ppm of nitrogen), as well as during hydrotreatment of straight-run diesel fraction and vacuum gasoil. The composition of Со(Ni)-PMo(W)/Al2O3 catalysts was shown to play a crucial role in the hydrotreatment of complex hydrocarbon feedstock. The Ni-PW/Al2O3 catalyst was more stable to organonitrogen inhibitors than Ni(Co)-PMo/Al2O3 bearing more reactive active centers. The highest conversions of sulfur- and nitrogen-containing compounds and polycyclic aromatic hydrocarbons during hydrotreatment of vacuum gasoil were observed with the Ni-PW/Al2O3 catalyst.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>гидроочистка</kwd><kwd>CoMoS</kwd><kwd>NiMoS</kwd><kwd>NiWS</kwd><kwd>гетерополианион</kwd><kwd>дизельное топливо</kwd><kwd>вакуумный газойль</kwd></kwd-group><kwd-group xml:lang="en"><kwd>hydrotreatment</kwd><kwd>CoMoS</kwd><kwd>NiMoS</kwd><kwd>NiWS</kwd><kwd>heteropoly anion</kwd><kwd>diesel fuel</kwd><kwd>vacuum gasoil</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">Stanislaus A., Marafi A., Rana M.S. // Catal. Today. 2010. V. 153. P. 1.</mixed-citation><mixed-citation xml:lang="en">Stanislaus A., Marafi A., Rana M.S. // Catal. Today. 2010. V. 153. 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