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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">10.18412/1816-0387-2015-4-42-48</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-290</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>Микро- и микро-мезопористые цеолитные катализаторы в синтезе пиридинов</article-title><trans-title-group xml:lang="en"><trans-title>Zeolite Catalysts with Various Pore Structures in the Synthesis of Pyridines</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>Григорьева</surname><given-names>Н. Г.</given-names></name><name name-style="western" xml:lang="en"><surname>Grigorieva</surname><given-names>N. G.</given-names></name></name-alternatives><email xlink:type="simple">ngg-ink@mail.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>Филиппова</surname><given-names>Н. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Filippova</surname><given-names>N. A.</given-names></name></name-alternatives><email xlink:type="simple">FNA1690@gmail.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>Травкина</surname><given-names>О. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Travkina</surname><given-names>O. S.</given-names></name></name-alternatives><email xlink:type="simple">simchanka@mail.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>Хазипова</surname><given-names>А. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Khazipova</surname><given-names>A. N.</given-names></name></name-alternatives><email xlink:type="simple">kutepoff@inbox.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>Кутепов</surname><given-names>Б. И.</given-names></name><name name-style="western" xml:lang="en"><surname>Kutepov</surname><given-names>B. I.</given-names></name></name-alternatives><email xlink:type="simple">kutepoff@inbox.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Институт нефтехимии и катализа РАН, г. Уфа</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Institute of Petrochemistry and Catalysis, RAS, Ufa</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2015</year></pub-date><pub-date pub-type="epub"><day>26</day><month>01</month><year>2016</year></pub-date><volume>15</volume><issue>4</issue><fpage>42</fpage><lpage>48</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2016</copyright-statement><copyright-year>2016</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/290">https://www.catalysis-kalvis.ru/jour/article/view/290</self-uri><abstract><p>Разработка катализаторов на основе модифицированных цеолитов с микро- или микро-мезопористой структурой, а также мезопористых металлосиликатов направлена на создание высокоселективных способов получения пиридина и алкилпиридинов. Впервые осуществлен гетерогенно-каталитический синтез пиридина и метилпиридинов взаимодействием этанола с формальдегидом и аммиаком в присутствии каталитических систем, представляющих собой микропористые цеолиты Y, Beta, ZSM-12 и ZSM-5 в Н-форме, а также гранулированный цеолит Y с комбинированной микро-, мезо- и макропористой структурой (НY-МММ). Последний наиболее эффективен для синтеза пиколинов, селективность их образования составляет 46–63 % при конверсии этанола 70–80 %. Среди микропористых катализаторов наиболее активными являются глубоко декатионированные цеолиты Н-Y и Н-Beta. Основными продуктами реакции на катализаторах H-Beta и H-ZSM-5 являются пиридин (до 50 %) и пиколины (до 40 %), на Н-Y и Н-ZSM-12 – пиколины (45–52 %) и лутидины (19–25 %). Для цеолита H-Y-МММ установлено влияние реакционных условий на конверсию этанола и состав пиридинов.</p></abstract><trans-abstract xml:lang="en"><p>Development of catalysts based on modified zeolites with a micro- or micro-meso-porous structure and mesoporous metallosilicates is aimed at creating of highly selective methods for producing pyridine and alkylpyridines. A heterogeneous catalytic synthesis of pyridine and methylpyridines was first done via the reaction of ethanol with ammonia and formaldehyde in the presence of the following catalyst systems: microporous zeolites Y, Beta, ZSM-12 and ZSM-5 in the H form, and a granulated Y zeolite with a combined micro-, meso-, and macro-porous structure (HY-MMM). The last is the most effective for the synthesis of picolines: the selectivity toward their formation is 46–63 % at an ethanol conversion of 70–80 %. Among the microporous catalysts, the most active are the highly decationized zeolites H-Y and H-Beta. The main reaction products on the catalysts H-Beta and H-ZSM-5 are pyridine (up to 50 %) and picolines (up to 40 %), while on the catalysts H-Y and H-ZSM-12, the main product are picolines (45–52 %) and lutidines (19–25 %). For zeolite HY-MMM, the influence of reaction conditions on the conversion of ethanol and the composition of pyridines is studied.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>пиридин</kwd><kwd>пиколины</kwd><kwd>лутидины</kwd><kwd>микро- и микро-мезопористые цеолиты</kwd></kwd-group><kwd-group xml:lang="en"><kwd>pyridine</kwd><kwd>picolines</kwd><kwd>lutidines</kwd><kwd>micro- and micro-meso-porous zeolites</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">Golunski S.E., Jacson D. // Applied Catalysis. 1986. 23. P. 1–14.</mixed-citation><mixed-citation xml:lang="en">Golunski S.E., Jacson D. // Applied Catalysis. 1986. 23. 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