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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">10.18412/1816-0387-2020-1-40-49</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-671</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>Иcпользование микроканального реактора для оптимизации получения хлоридов 1-алкил-3-метилимидазолия</article-title><trans-title-group xml:lang="en"><trans-title>The use of a microchannel reactor for optimizing the production of 1-alkyl-3-methylimidazolium chlorides</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>Клименко</surname><given-names>А. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Klimenko</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>Андреев</surname><given-names>Д. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Andreev</surname><given-names>D. V.</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>Приходько</surname><given-names>С. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Prikhod’ko</surname><given-names>S. 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>Грибовский</surname><given-names>А. Г.</given-names></name><name name-style="western" xml:lang="en"><surname>Gribovsky</surname><given-names>A. G.</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>Макаршин</surname><given-names>Л. Л.</given-names></name><name name-style="western" xml:lang="en"><surname>Makarshin</surname><given-names>L. L.</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>Адонин</surname><given-names>Н. Ю.</given-names></name><name name-style="western" xml:lang="en"><surname>Adonin</surname><given-names>N. Yu.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-2"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Институт катализа им. Г.К. Борескова СО РАН (ИК СО РАН), Новосибирск</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Boreskov Institute of Catalysis SB RAS, Novosibirsk</institution><country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru"><institution>Институт катализа им. Г.К. Борескова СО РАН (ИК СО РАН), Новосибирск; Новосибирский национальный исследовательский государственный университет (НГУ)</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Boreskov Institute of Catalysis SB RAS, Novosibirsk; Novosibirsk State University</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2020</year></pub-date><pub-date pub-type="epub"><day>22</day><month>01</month><year>2020</year></pub-date><volume>20</volume><issue>1</issue><fpage>40</fpage><lpage>49</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2020</copyright-statement><copyright-year>2020</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/671">https://www.catalysis-kalvis.ru/jour/article/view/671</self-uri><abstract><p>Возможность использования микроканальных проточных реакторов для получения кинетических и технологических параметров процесса синтеза ионной жидкости 1-бутил-3-метилимидазолия хлорида (BMIMCl) была продемонстрирована на примере реакции 1-метилимидазола (MIm) с 1-хлорбутаном в отсутствие растворителей. BMIMCl был получен с высокой селективностью и удельной производительностью в проточном микроканальным реакторе при температурах 120–180 °C и временах контакта 2–45 мин при давлении 20 бар. Положительный результат достигается благодаря ламинарному профилю потока и равномерному распределению концентрации реагентов по сечению микроканалов. Исследование кинетики процесса с помощью проточного микроканального реактора позволило обнаружить переход реакции в режим диффузионного торможения при температуре выше 150 °С. На основании полученных кинетических данных синтеза BMIMCl были разработаны методики получения хлоридов 1-этил-3-метилимидазолия и 1-гексил-3-метилимидазолия (соответственно EMIMCl и HMIMCl) в условиях микроканального проточного реактора. Подход, предложенный в этой статье, представляет интерес для разработки проточных и периодических установок для малотоннажного производства солей диалкилимидазолия, аммония и пиридиния путем кватернизации соответствующих алкилхлоридов и азотсодержащих оснований.</p></abstract><trans-abstract xml:lang="en"><p>The possibility to use microchannel flow reactors for obtaining kinetic and technological parameters of the synthesis of 1-butyl-3-methylimidazolium chloride (BMIMCl) ionic liquid was demonstrated for the reaction of 1-methylimidazole (MIm) with 1-chlorobutane in the absence of solvents. BMIMCl was produced with high selectivity and specific output in a microchannel flow reactor at temperatures 120–180 °C and contact times 2-45 min at a pressure of 20 bar. The positive result is obtained due to the laminar profile of the flow and a uniform distribution of the reagents’ concentration over the microchannel cross-section. Investigation of the process kinetics in a microchannel flow reactor made it possible to reveal that the reaction moves to the diffusion resistance mode at a temperature above 150 °C. The kinetic data obtained for the BMIMCl synthesis were used to develop methods for the production of 1-ethyl-3-methylimidazolium and 1-hexyl-3-methylimidazolium chlorides (EMIMCl and HMIMCl, respectively) under the conditions of a microchannel flow reactor. The approach suggested in this paper is of interest for the development of flow and batch setups for a small-tonnage production of dialkylimidazolium, ammonium and pyridinium salts by quaternization of the corresponding alkyl chlorides and nitrogen-containing bases.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>ионная жидкость</kwd><kwd>1-алкил-3-метилимидазолий хлорид</kwd><kwd>BMIMC</kwd><kwd>реакция кватернизации</kwd><kwd>проточный микроканальный реактор</kwd></kwd-group><kwd-group xml:lang="en"><kwd>ionic liquid</kwd><kwd>1-alkyl-3-methylimidazolium chloride</kwd><kwd>BMIMCl</kwd><kwd>quaternization reaction</kwd><kwd>microchannel flow reactor</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">Elements of the Business of Chemistry, 2017.</mixed-citation><mixed-citation xml:lang="en">Elements of the Business of Chemistry, 2017.</mixed-citation></citation-alternatives></ref><ref id="cit2"><label>2</label><citation-alternatives><mixed-citation xml:lang="ru">Specialty chemicals market to reach $1.79 trillion by 2025. 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