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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">10.18412/1816-0395-2016-5-40-46</article-id><article-id custom-type="elpub" pub-id-type="custom">ekip-734</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 гидроочистки 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</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>05</month><year>2016</year></pub-date><volume>20</volume><issue>5</issue><fpage>40</fpage><lpage>46</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/734">https://www.ecology-kalvis.ru/jour/article/view/734</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>Content of catalytic cracking gasoline (GCC) in Russian blended gasoline is greater than 30 %. The most of sulfur in blended gasoline comes from GCC, while permitted sulfur content in commercial gasoline of Euro 5 standard is 10 ppm. High sulfur content of the GCC makes it impossible to use them without prior hydrotreating, inevitably reducing the octane number of gasoline. The nature of sulfur compounds that make the major contribution to the octane number was considered. An overview of modern technological processes and catalysts for hydrotreating of GCC was made. It was shown that modern gasoline desulfurization were based on pre-fractionation and separate purification of heavy and light fractions that made them technologically complicated and energy-intensive. Boreskov Institute of Catalysis together with AO “Gazpromneft-MNPZ” developed the catalyst and a single stage hydrotreating process of GCC. Developed catalyst provides selective hydrotreating of all GCC fractions without prefractionation to obtain gasoline with a sulfur content of no more than 10 ppm, and octane number loss not more than 1 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>catalytic cracking gasoline</kwd><kwd>selective hydrotreating</kwd><kwd>hydrotreating catalyst</kwd><kwd>motor 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">Siddiqui M.A.B., Aitani A.M. FCC Gasoline Sulfur Reduction by Additives: A Review // Pet. Sci. Technol. 2007. Vol. 25. P.299-313.</mixed-citation><mixed-citation xml:lang="en">Siddiqui M.A.B., Aitani A.M. 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