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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">10.18412/1816-0387-2019-1-40-49</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-583</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 ХИМИЧЕСКОЙ И НЕФТЕХИМИЧЕСКОЙ ПРОМЫШЛЕННОСТИ</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>CATALYSIS IN CHEMICAL AND PETROCHEMICAL INDUSTRY</subject></subj-group></article-categories><title-group><article-title>Исследование влияния промотирования катализатора Ni/Al2O3 медью на его активность в процессе гидрообработки сложных эфиров</article-title><trans-title-group xml:lang="en"><trans-title>Studies of the Influence of Promoting the Ni/Al2O3 Catalyst with Copper on the Activity to Hydrotreatment of Esters</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>Кукушкин</surname><given-names>Р. Г.</given-names></name><name name-style="western" xml:lang="en"><surname>Kukushkin</surname><given-names>R. G.</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>Елецкий</surname><given-names>П. М.</given-names></name><name name-style="western" xml:lang="en"><surname>Eletskiy</surname><given-names>P. M.</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>Булавченко</surname><given-names>О. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Bulavchenko</surname><given-names>O. 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>Сараев</surname><given-names>А. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Saraev</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>Яковлев</surname><given-names>В. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Yakovlev</surname><given-names>V. 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">Институт катализа им. Г.К. Борескова СО РАН (ИК СО РАН), Новосибирск; Новосибирский национальный исследовательский государственный университет (НГУ)<country>Россия</country></aff><aff xml:lang="en">Boreskov Institute of Catalysis, Novosibirsk; Novosibirsk State University<country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru">Институт катализа им. Г.К. Борескова СО РАН (ИК СО РАН), Новосибирск<country>Россия</country></aff><aff xml:lang="en">Boreskov Institute of Catalysis, Novosibirsk<country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2019</year></pub-date><pub-date pub-type="epub"><day>17</day><month>01</month><year>2019</year></pub-date><volume>19</volume><issue>1</issue><fpage>40</fpage><lpage>49</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2019</copyright-statement><copyright-year>2019</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/583">https://www.catalysis-kalvis.ru/jour/article/view/583</self-uri><abstract><p>Исследовано влияние состава активного компонента никелевых катализаторов, допированных медью, на их активность и селективность в процессе гидродеоксигенации (ГДО) модельных соединений растительных масел – сложных эфиров – с целью удаления из них кислорода и получения алканов. Показано, что катализаторы Ni/Al2O3, Ni-Cu/Al2O3 проявляют активность в данном процессе. В их присутствии ГДО смеси метилового эфира гексадекановой кислоты и этилового эфира декановой кислоты приводит к образованию алканов ряда С6–С16 и кислородсодержащих продуктов; в газовой фазе обнаружены метан и этан. С уменьшением соотношения Ni : Cu в составе катализатора наблюдается снижение конверсии эфиров и уменьшение способности данных катализаторов к гидрогенолизу связи С–С. Это означает, что внедрение меди может способствовать сохранению углеродного скелета алканов, получаемых в результате ГДО, и снижению количества метана. По данным РФА, внедрение меди в состав катализатора Ni/Al2O3 приводит к образованию твердых растворов состава Ni1–xCux. По данным РФЭС, увеличение содержания меди в составе катализатора Ni-Cu/Al2O3 приводит к уменьшению соотношения Ni : Cu на поверхности образца.</p></abstract><trans-abstract xml:lang="en"><p>The influence of the composition of the active component of copper-doped nickel catalysts on the activity and selectivity to hydrodeoxygenation (HDO) of model vegetable oils (esters) to eliminate oxygen and produce alkanes was studied. The Ni/Al2O3 andNi-Cu/Al2O3 catalysts were shown to be active to this process. They catalyzed HDO of a mixture of methyl ester of hexadecane acid and ethyl ester of decane acid to produce C6–C16 alkanes and oxygen-containing compounds, methane and ethane being detected in the gas phase. A decrease in the Ni/Cu ratio in the catalyst led to a decrease in the ester conversion and in the catalyst activity to hydrogenolysis of C–C bonds. Hence, the introduction of copper may favor preservation of the carbon skeleton of HDO-produced alkanes and a decrease in the methane yield. XRD studies revealed the formation of solid solutions Ni1–xCux upon addition of copper to the Ni/Al2O3 catalyst. From XPS data, an increase in the copper proportion in the Ni-Cu/Al2O3 catalyst resulted in a decrease in the Ni/Cu ration on the catalyst surface.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>гидродеоксигенация</kwd><kwd>биотопливо</kwd><kwd>углеводородное топливо</kwd><kwd>растительные масла</kwd></kwd-group><kwd-group xml:lang="en"><kwd>hydrodeoxygenation</kwd><kwd>biofuel</kwd><kwd>hydrocarbon fuel</kwd><kwd>vegetable oil</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">Organization of the Petroleum Exporting Countries. 2017 OPEC World Oil Out- look. October 2017. 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