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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="en"><front><journal-meta><journal-id journal-id-type="publisher-id">chemicallytech</journal-id><journal-title-group><journal-title xml:lang="en">Fine Chemical Technologies</journal-title><trans-title-group xml:lang="ru"><trans-title>Тонкие химические технологии</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">2410-6593</issn><issn pub-type="epub">2686-7575</issn><publisher><publisher-name>MIREA – Russian Technological University (RTU MIREA).</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.32362/2410-6593-2025-20-6-540-554</article-id><article-id custom-type="edn" pub-id-type="custom">NAQGZO</article-id><article-id custom-type="elpub" pub-id-type="custom">chemicallytech-2333</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="en"><subject>CHEMISTRY AND TECHNOLOGY OF ORGANIC SUBSTANCES</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="ru"><subject>ХИМИЯ И ТЕХНОЛОГИЯ ОРГАНИЧЕСКИХ ВЕЩЕСТВ</subject></subj-group></article-categories><title-group><article-title>Synthesis of methanol from gaseous products of pyrolysis of sewage sludge</article-title><trans-title-group xml:lang="ru"><trans-title>Синтез метанола из газообразных продуктов пиролиза осадка сточных вод</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0003-2023-6806</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Ларина</surname><given-names>О. М.</given-names></name><name name-style="western" xml:lang="en"><surname>Larina</surname><given-names>O. M.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Ларина Ольга Михайловна, к.т.н., старший научный сотрудник</p><p>Scopus Author ID 57190050879, ResearсherID D-3336-2014</p><p>125412, Россия, Москва, ул. Ижорская, д. 13, стр. 2</p></bio><bio xml:lang="en"><p>Olga M. Larina, Cand. Sci. (Eng.), Senior Researcher</p><p>Scopus Author ID 57190050879, ResearсherID D-3336-2014</p><p>13-2, Izhorskaya ul., Moscow, 125412</p></bio><email xlink:type="simple">olga.m.larina@ihed.ras.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-8437-1532</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Лищинер</surname><given-names>И. И.</given-names></name><name name-style="western" xml:lang="en"><surname>Lishchiner</surname><given-names>I. I.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Лищинер Иосиф Израилевич, к.х.н., старший научный сотрудник</p><p>Scopus Author ID 6507439331, ResearсherID J-7291-2018</p><p>125412, Россия, Москва, ул. Ижорская, д. 13, стр. 2</p></bio><bio xml:lang="en"><p>Iosif Iz. Lishchiner, Cand. Sci. (Chem.), Senior Researcher</p><p>Scopus Author ID 6507439331, ResearсherID J-7291-2018</p><p>13-2, Izhorskaya ul., Moscow, 125412</p></bio><email xlink:type="simple">lii48@bk.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0001-6081-926X</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Малова</surname><given-names>О. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Malova</surname><given-names>O. V.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Малова Ольга Васильевна, к.х.н., старший научный сотрудник</p><p>Scopus Author ID 57190617511, ResearсherID J-7261-2018</p><p>125412, Россия, Москва, ул. Ижорская, д. 13, стр. 2</p></bio><bio xml:lang="en"><p>Olga V. Malova, Cand. Sci. (Chem.), Senior Researcher</p><p>Scopus Author ID 57190617511, ResearсherID J-7261-2018</p><p>13-2, Izhorskaya ul., Moscow, 125412</p></bio><email xlink:type="simple">mov58rus@yandex.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-7424-5137</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Фалеева</surname><given-names>Ю. М.</given-names></name><name name-style="western" xml:lang="en"><surname>Faleeva</surname><given-names>Yu. M.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Фалеева Юлия Михайловна, научный сотрудник</p><p>ResearсherID AAY-2189-2021</p><p>125412, Россия, Москва, ул. Ижорская, д. 13, стр. 2</p></bio><bio xml:lang="en"><p>Yulia M. Faleeva, Researcher</p><p>ResearсherID AAY-2189-2021</p><p>13-2, Izhorskaya ul., Moscow, 125412</p></bio><email xlink:type="simple">faleeva.julia@mail.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Объединенный институт высоких температур Российской академии наук (ОИВТ РАН)</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Joint Institute for High Temperatures of the Russian Academy of Sciences (JIHT RAS)</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2025</year></pub-date><pub-date pub-type="epub"><day>15</day><month>01</month><year>2026</year></pub-date><volume>20</volume><issue>6</issue><fpage>540</fpage><lpage>554</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Larina O.M., Lishchiner I.I., Malova O.V., Faleeva Y.M., 2026</copyright-statement><copyright-year>2026</copyright-year><copyright-holder xml:lang="ru">Ларина О.М., Лищинер И.И., Малова О.В., Фалеева Ю.М.</copyright-holder><copyright-holder xml:lang="en">Larina O.M., Lishchiner I.I., Malova O.V., Faleeva Y.M.</copyright-holder><license xml:lang="ru" license-type="creative-commons-attribution" xlink:href="https://creativecommons.org/licenses/by/4.0/" xlink:type="simple"><license-p>Данная работа распространяется под лицензией Creative Commons Attribution 4.0.</license-p></license><license xml:lang="en" license-type="creative-commons-attribution" xlink:href="https://creativecommons.org/licenses/by/4.0/" xlink:type="simple"><license-p>This work is licensed under a Creative Commons Attribution 4.0 License.</license-p></license></permissions><self-uri xlink:href="https://www.finechem-mirea.ru/jour/article/view/2333">https://www.finechem-mirea.ru/jour/article/view/2333</self-uri><abstract><p>Objectives. To study the influence of compositional variability (different ash and organic matter contents) of sewage sludge on the characteristics of synthesis gas (syngas) and to determine the yield of products in the entire chain of conversion of sewage sludge to methanol through the stage of syngas production by two-stage pyrolysis.Methods. Syngas was produced by a two-stage pyrolysis method. After heating sewage sludge from 20 to 1000°C in an oxygen-free medium, heterogeneous thermal cracking of the volatile products was carried out in a biochar medium at 1000°C. The syngas was converted to methanol on a CuZnAl catalyst in an isothermal flow heat-pipe reactor at a feedstock feed rate of 600 h−1, an internal reactor pressure of 5 MPa, and temperatures in the catalyst bed of 205, 215, and 225°C. The resultant syngas having a CO2 content of less than 0.5 vol % and a H 2/CO ratio of 1.8 was used as feedstock for methanol production.Results. The experimental studies of syngas production from sewage sludge demonstrated the active formation of syngas during twostage pyrolysis in the temperature range of 140–600°C regardless of the ash content of the sludge. The H2/CO ratio in the syngas produced by two-stage pyrolysis of sewage sludge was shown to depend on the H/O atomic ratio in the sludge composition. Crude methanol was obtained at maximum yield and purity at a temperature of 225°C in the catalyst bed. The overall conversion of carbon monoxide was 43.6%.Conclusions. Variability in the composition of sewage sludge significantly influences quantitative parameters to a large extent in terms of the specific volume yield of syngas and insignificantly terms of its composition. No qualitative influence was exerted by the difference in the types of sewage sludge on syngas production. The experimental studies showed that 1 kg of sewage sludge with a relative moisture content up to 5 wt % can produce 1.1 nm3 of syngas and a further 220 g of pure methanol.</p></abstract><trans-abstract xml:lang="ru"><p>Цели. Исследовать влияние непостоянства состава (различное содержание зольности и органической части) осадка сточных вод (ОСВ) на характеристики синтез-газа, определить выход продуктов во всей цепочке превращений осадка сточных вод в метанол через стадию производства синтез-газа методом двухстадийного пиролиза.Методы. Синтез-газ был получен методом двухстадийного пиролиза, заключающимся в нагреве ОСВ от 20 до 1000°C в бескислородной среде с последующим термическим гетерогенным крекингом летучих продуктов в среде биоугля при температуре 1000°C. Конверсия синтез-газа в метанол проходила на CuZnAl-катализаторе в проточном изотермическом реакторе на тепловых трубах с объемной скоростью подачи сырья 600 ч−1, при давлении внутри реактора 5 МПа, температурах в слое катализатора 205, 215 и 225°C. В качестве сырья для производства метанола был использован синтез-газ с содержанием СО2 менее 0.5 об. % и отношением Н2/СО, равным 1.8.Результаты. Результаты экспериментальных исследований процесса получения синтез-газа из ОСВ установили, что независимо от величины зольности осадка, активное образование синтез-газа при двухстадийном пиролизе происходило в интервале температур 140–600°C. Отношение Н2/СО в синтез-газе, произведенным методом двухстадийного пиролиза ОСВ, зависело от атомного отношения Н/О в составе осадка. Максимальный выход и чистота метанола-сырца были получены при температуре в слое катализатора равной 225°С. Общая конверсия оксида углерода составила 43.6%.Выводы. Непостоянство состава ОСВ влияло на количественные показатели в значительной степени по удельному объемному выходу синтез-газа и незначительно по его составу. Качественно на протекание процесса получения синтез-газа различие в видах ОСВ влияния не оказывало. Результаты экспериментальных исследований показали, что из 1 кг ОСВ с относительной влажностью до 5 мас. % может быть произведено 1.1 нм3 синтез-газа и далее 220 г чистого метанола.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>садок сточных вод</kwd><kwd>синтез-газ</kwd><kwd>метанол</kwd><kwd>двухстадийный пиролиз</kwd><kwd>термический крекинг</kwd><kwd>каталитическая конверсия</kwd><kwd>жидкие моторные топлива</kwd></kwd-group><kwd-group xml:lang="en"><kwd>sewage sludge</kwd><kwd>syngas</kwd><kwd>methanol</kwd><kwd>two-stage pyrolysis</kwd><kwd>thermal cracking</kwd><kwd>catalytic conversion</kwd><kwd>liquid motor fuels</kwd></kwd-group><funding-group><funding-statement xml:lang="ru">Работа выполнена при финансовой поддержке Министерства науки и высшего образования Российской Федерации (государственное задание № 075–00270-24–00)</funding-statement><funding-statement xml:lang="en">This work was supported by the Ministry of Science and Higher Education of the Russian Federation (State Assignment No. 075–00270-24–00).</funding-statement></funding-group></article-meta></front><back><ref-list><title>References</title><ref id="cit1"><label>1</label><citation-alternatives><mixed-citation xml:lang="ru">Pachauri R.K., Meyer L.A. 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