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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">10.18412/1816-0387-2024-2-59-65</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-1007</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>Co- и Ni-содержащие катализаторы облагораживания тяжелой нефти: влияние этанола на состав и структуру продуктов каталитического крекинга</article-title><trans-title-group xml:lang="en"><trans-title>Co and Ni-containing catalysts for heavy oil refining: the effect of ethanol on the composition and structure of catalytic cracking products</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>Уразов</surname><given-names>Х. Х.</given-names></name><name name-style="western" xml:lang="en"><surname>Urazov</surname><given-names>Kh. Kh.</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>Свириденко</surname><given-names>Н. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Sviridenko</surname><given-names>N. N.</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>Сергеев</surname><given-names>Н. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Sergeev</surname><given-names>N. 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>Акимов</surname><given-names>А. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Akimov</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>Огородников</surname><given-names>В. Д.</given-names></name><name name-style="western" xml:lang="en"><surname>Ogorodnikov</surname><given-names>V. D.</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>Институт химии нефти СО РАН, Томск</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Institute of Petroleum Chemistry SB RAS, Tomsk</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2024</year></pub-date><pub-date pub-type="epub"><day>20</day><month>03</month><year>2024</year></pub-date><volume>24</volume><issue>2</issue><fpage>59</fpage><lpage>65</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2024</copyright-statement><copyright-year>2024</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/1007">https://www.catalysis-kalvis.ru/jour/article/view/1007</self-uri><abstract><p>Исследованы продукты термической переработки тяжелой нефти в присутствии Ni- и Co-содержащих катализаторов, образующихся in situ из смеси соответствующих солей с этанолом. По сравнению с термическим крекингом в каталитическом процессе увеличивается выход светлых фракций с 51 до 63 % и снижается выход кокса с 3 до 2 мас.% В случае смешанного Ni- и Сo-катализатора наблюдаются наименьшие выходы газа (5 мас.%) и кокса (0,1 мас.%). Снижение содержания серы происходит как в продуктах термического крекинга (на 17 %), так и каталитического крекинга (от 12 до 32 отн.%), преимущественно за счет удаления ее в виде газообразных продуктов. Изучены структурно-групповые характеристики усредненных молекул асфальтенов до и после крекинга тяжелой нефти. Методом РФА твердых продуктов крекинга идентифицированы фазы Ni0,96S, Ni9S8 и Co9S8.</p></abstract><trans-abstract xml:lang="en"><p>The study deals with the products of thermal processing of heavy oil in the presence of Ni- and Co-containing catalysts that are formed in situ from the mixture of corresponding salts with ethanol. In comparison with thermal cracking, in the catalytic process the yield of bright fractions increases from 51 to 63 % and the yield of coke decreases from 3 to 2 wt.%. In the case of mixed Ni and Сo catalyst, the least yields of gas (5 wt.%) and coke (0.1 wt.%) are observed. A decrease in the sulfur content occurs in the products of both thermal (by 17 %) and catalytic cracking (from 12 to 32 rel.%) predominantly due to its removal as gaseous products. The structuralgroup characteristics of the averaged asphaltene molecules were studied before and after heavy oil cracking. XRD of solid cracking products was used to identify Ni0.96S, Ni9S8 and Co9S8 phases.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>тяжелая нефть</kwd><kwd>асфальтены</kwd><kwd>сульфид никеля</kwd><kwd>сульфид кобальта</kwd><kwd>этанол</kwd></kwd-group><kwd-group xml:lang="en"><kwd>heavy oil</kwd><kwd>asphaltenes</kwd><kwd>nickel sulfide</kwd><kwd>cobalt sulfide</kwd><kwd>ethanol</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">Hosseinpour M., Fatemi S., Ahmadi S. J., Morimoto M., Akizuki M., Oshima Y., Fumoto E. // Appl. Catal. B. 2018. V. 230. P. 91–101. https://doi.org/10.1016/j.apcatb.2018.02.030</mixed-citation><mixed-citation xml:lang="en">Hosseinpour M., Fatemi S., Ahmadi S. J., Morimoto M., Akizuki M., Oshima Y., Fumoto E. // Appl. Catal. B. 2018. V. 230. 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