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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">10.18412/1816-0387-2017-3-184-200</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-456</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>Перспективы прямой каталитической переработки метана в востребованные химические продукты. Обзор</article-title><trans-title-group xml:lang="en"><trans-title>Potentialities of the Direct Catalytic Processing of Methane into in-Demand Chemicals. Review</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>Пинаева</surname><given-names>Л. Г.</given-names></name><name name-style="western" xml:lang="en"><surname>Pinaeva</surname><given-names>L. 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>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><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>Пармон</surname><given-names>В. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Parmon</surname><given-names>V. N.</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 катализа им. Г.К. Борескова СО РАН, Новосибирск</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Boreskov Institute of Catalysis, Novosibirsk</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2017</year></pub-date><pub-date pub-type="epub"><day>21</day><month>09</month><year>2017</year></pub-date><volume>17</volume><issue>3</issue><fpage>184</fpage><lpage>200</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2017</copyright-statement><copyright-year>2017</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/456">https://www.catalysis-kalvis.ru/jour/article/view/456</self-uri><abstract><p>Проанализированы литературные данные по исследованиям каталитических реакций прямого превращения метана в востребованные химические продукты (Н2, С2+ углеводороды, метанол, формальдегид и более высокие оксигенаты). На настоящий момент процессы на основе этих реакций не реализованы в промышленности. Для каждой из реакций выявлены каталитические системы, на которых достигаются максимальные показатели (прежде всего, выход целевых продуктов), а также определена степень приближения их к уровню, при котором возможна коммерциализация процесса. В ближайшее время наиболее вероятными для опытно-промышленного освоения можно считать процессы получения С2+ и алкилароматических углеводородов путем окислительной конденсации (димеризации) метана и в результате реакции метана с алканами С3–С6 соответственно. Благодаря значительному прогрессу в разработке новых модификаций цеолитов и алюмосиликатов может быть решена проблема, связанная c быстрой дезактивацией катализаторов при получении углеводородов бензиновой фракции метилированием олефинов. Основными ограничениями для реализации процесса пиролиза метана до углерода и Н2 являются недостаточный спрос на получаемые разновидности углеродных материалов, а также низкие прочностные характеристики имеющихся катализаторов в случае проведения процесса в подвижном слое. Для ряда продуктов (метанол, формальдегид) выходы не достигают необходимых для коммерциализации значений, для других (высшие оксигенаможность их получения.</p></abstract><trans-abstract xml:lang="en"><p>Literature data are reviewed in the field of catalytic reaction of the direct transformation of methane into marketable chemicals (H2, C2+ hydrocarbons, methanol, formaldehyde and higher oxygenates). At present the processes based on these reactions are not implemented in industry. Catalytic systems providing achievement of the maximal parameters (in the first, the yields of target products) were identified for each of the reactions, and the proximity to their potential commercialization was determined. The processes of synthesis of C2+ and alkylaromatic hydrocarbons via oxidative condensation (dimerization) of methane and by the reaction of methane with C3–C6 alkanes, respectively, are considered most promising for the semicommercial production in the nearest future. A considerable progress in the development of new zeolite and aluminosilicate modifications makes it possible to solve the problem of the fast catalyst deactivation during olefin methylation to produce hydrocarbons of the gasoline fraction. Implementation of the process of methane pyrolysis to carbon and H2 is mainly limited by insufficient demand for the obtained types of carbon materials and by the low strength of the available catalysts for fixed catalyst bed processes. The yields of a number of products (methanol, formaldehyde) are not as high as the ones required for the process commercialization. As to the other products (higher oxygenates), a general possibility of their synthesis is only so far demonstrated.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>метан</kwd><kwd>катализаторы</kwd><kwd>окисление</kwd><kwd>функционализация</kwd><kwd>димеризация</kwd><kwd>пиролиз</kwd></kwd-group><kwd-group xml:lang="en"><kwd>methane</kwd><kwd>catalysts</kwd><kwd>oxidation</kwd><kwd>functionalization</kwd><kwd>dimerization</kwd><kwd>pyrolysis</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">IHS Chemical Process Economics Program. Report 148B: Synthesis Gas Production from Natural Gas Reforming, by S.N. Naqvi. 2013.</mixed-citation><mixed-citation xml:lang="en">IHS Chemical Process Economics Program. Report 148B: Synthesis Gas Production from Natural Gas Reforming, by S.N. 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