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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">ekip</journal-id><journal-title-group><journal-title xml:lang="ru">Экология и промышленность России</journal-title><trans-title-group xml:lang="en"><trans-title>Ecology and Industry of Russia</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">1816-0395</issn><issn pub-type="epub">2413-6042</issn><publisher><publisher-name>ООО "Калвис"</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.18412/1816-0395-2016-6-50-53</article-id><article-id custom-type="elpub" pub-id-type="custom">ekip-744</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>АНАЛИЗ. МЕТОДИКИ. ПРОГНОЗЫ</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>ANALYSIS. METHODS. PROGNOSIS</subject></subj-group></article-categories><title-group><article-title>Катализаторы и процессы селективной гидроостки бензина каталитического крекинга</article-title><trans-title-group xml:lang="en"><trans-title>Catalysts and Selective Hydrotreating Processes of Catalytic Cracking Gasoline</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>Носков</surname><given-names>А. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Noskov</surname><given-names>A. S.</given-names></name></name-alternatives><bio xml:lang="ru"><p>д-р техн. наук, заместитель директора по научной работе</p></bio><bio xml:lang="en"><p>Dr. Sci., Deputy Director for Science</p></bio><email xlink:type="simple">podpiska@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>Климов</surname><given-names>О. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Klimov</surname><given-names>O. V.</given-names></name></name-alternatives><bio xml:lang="ru"><p>канд. хим. наук, ст. науч. сотрудник</p></bio><bio xml:lang="en"><p>Ph.D. (Chemistry), Senior researcher</p></bio><email xlink:type="simple">podpiska@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>Надеина</surname><given-names>К. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Nadeina</surname><given-names>K. A.</given-names></name></name-alternatives><bio xml:lang="ru"><p>канд. хим. наук, мл. науч. сотрудник</p></bio><bio xml:lang="en"><p>Ph.D. (Chemistry), Junior researcher fellow</p></bio><email xlink:type="simple">podpiska@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>Перейма</surname><given-names>В. Ю.</given-names></name><name name-style="western" xml:lang="en"><surname>Pereima</surname><given-names>V. Yu.</given-names></name></name-alternatives><bio xml:lang="ru"><p>мл. науч. сотрудник</p></bio><bio xml:lang="en"><p>Junior researcher fellow</p></bio><email xlink:type="simple">podpiska@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Институт катализа им. Г. К. Борескова СО РАН, г. Новосибирск</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Boreskov Institute of Catalysis, the RAS Siberian branch</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2016</year></pub-date><pub-date pub-type="epub"><day>29</day><month>06</month><year>2016</year></pub-date><volume>20</volume><issue>6</issue><fpage>50</fpage><lpage>53</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; ООО "Калвис", 2016</copyright-statement><copyright-year>2016</copyright-year><copyright-holder xml:lang="ru">ООО "Калвис"</copyright-holder><copyright-holder xml:lang="en">ООО "Калвис"</copyright-holder><license xlink:href="https://www.ecology-kalvis.ru/jour/about/submissions#copyrightNotice" xlink:type="simple"><license-p>https://www.ecology-kalvis.ru/jour/about/submissions#copyrightNotice</license-p></license></permissions><self-uri xlink:href="https://www.ecology-kalvis.ru/jour/article/view/744">https://www.ecology-kalvis.ru/jour/article/view/744</self-uri><abstract><p>В российских компаундированных автобензинах  содержание бензинов каталитического крекинга (БКК) превышает 30 %, при этом большая часть серы из разрешённых по стандарту Евро-5 десяти ppm поступает в товарные бензины именно с БКК. Высокое содержание серы в БКК делает невозможным их использование без предварительной гидроочистки, неизбежно снижающей октановое число бензинов. Рассмотрена природа серосодержащих соединений и соединений, вносящих основной вклад в октановое число. Проведен обзор современных технологических процессов и катализаторов гидроочистки БКК. Показано, что современные процессы обессеривания бензинов основаны на предварительном фракционировании и раздельной очистке тяжелой и лёгкой фракций,  что делает их технологически сложными и энергоемкими. Институтом катализа им. Г.К. Борескова СО РАН совместно с АО «Газпромнефть-МНПЗ» разработаны катализатор и процесс селективной одностадийной гидроочистки БКК. Разработанный катализатор позволяет проводить селективную гидроочистку всей фракции БКК без предварительного фракционирования с получением бензина с содержанием серы не более 10 ppm и падением октанового числа не более чем на 1 пункт.</p></abstract><trans-abstract xml:lang="en"><p>In Russian blended gasoline content of gasoline catalytic cracking (GCC) is greater than 30 %, with most the sulfur of from the permitted standard Euro 5 ten ppm in commercial gasoline was with GCC. The high sulfur content of the GCC makes it impossible to use them without prior hydrotreating, inevitably reducing the octane rating of gasoline. There was considered the nature of sulfur compounds making the major contribution in the octane rating. There was providing overview modern technological processes and catalysts for hydrotreating of GCC. There was shown that modern gasoline desulfurization based on pre-fractionation and separate purification of heavy and light fractions, which makes them technologically complex and energy intensive. Boreskov Institute of Catalysis together with JSC “Gazpromneft-MOR” developed of catalyst and a single stage hydrotreating process of GCC. Developed catalyst allows the selective hydrotreating all GCC fractions without pre-fractionation obtain gasoline with a sulfur content of no more than 10 ppm, and drop the octane rating of not more than one point.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>бензин каталитического крекинга</kwd><kwd>селективная гидроочистка</kwd><kwd>катализатор гидроочистки</kwd><kwd>моторные топлива</kwd><kwd>технологии</kwd></kwd-group><kwd-group xml:lang="en"><kwd>gasoline of catalytic cracking</kwd><kwd>selective hydrotreating</kwd><kwd>catalyst of hydrotreating</kwd><kwd>road fuels</kwd><kwd>technologies</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">Dong Hai-Ming, Qu Yun, Li-Lin S. Application of Prime-G+ Technology in FCC Naphtha Hy-drodesulfurisation Unit // Pet. Process. Petrochem. 2012. Vol. 43. 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