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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">alternative</journal-id><journal-title-group><journal-title xml:lang="ru">Альтернативная энергетика и экология (ISJAEE)</journal-title><trans-title-group xml:lang="en"><trans-title>Alternative Energy and Ecology (ISJAEE)</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">1608-8298</issn><publisher><publisher-name>Международный издательский дом научной периодики "Спейс</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.15518/isjaee.2023.02.064-081</article-id><article-id custom-type="elpub" pub-id-type="custom">alternative-2196</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>IV. ВОДОРОДНАЯ ЭКОНОМИКА 12. Водородная экономика</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>IV. HYDROGEN ECONOMY. 12. Hydrogen Economy</subject></subj-group></article-categories><title-group><article-title>Моделирование процесса газификации эффлюента темновой ферментации в газогенераторе с нисходящим потоком</article-title><trans-title-group xml:lang="en"><trans-title>Modeling of air gasification from dark fermentation effluent in a downdraft gasifier</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0001-8329-1808</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Ермолаев</surname><given-names>Д. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Ermolaev</surname><given-names>D. V.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Ермолаев Денис Васильевич - кандидат технических наук, старший научный сотрудник лаборатории энергетических систем и технологий.</p><p>420111, Казань, ул. Лобачевского, д. 2/31, а/я 260</p><p>Researcher ID: E-9858-2017, Scopus Author ID: 55232290400</p></bio><bio xml:lang="en"><p>Denis V. Ermolaev - PhD, Leading Researcher, laboratory of Energy Systems and Technologies.</p><p>420111, Kazan, st. Lobachevsky, 2/31, PO Box 190</p></bio><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-9275-332X</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Караева</surname><given-names>Ю. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Karaeva</surname><given-names>J. V.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Караева Юлия Викторовна - кандидат технических наук, ведущий научный сотрудник лаборатории энергетических систем и технологий.</p><p>420111, Казань, ул. Лобачевского, д. 2/31, а/я 260</p><p>Researcher ID: F-6917-2017, Scopus Author ID: 56856782800</p></bio><bio xml:lang="en"><p>Julia V. Karaeva - Leading Researcher, laboratory of Energy Systems and Technologies, PhD, Institute of Power Engineering and Advanced Technologies, FRC Kazan Scientific Center, Russian Academy of Sciences.</p><p>420111, Kazan, st. Lobachevsky, 2/31, PO Box 190</p></bio><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0003-4168-2442</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Тимофеева</surname><given-names>С. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Timofeeva</surname><given-names>S. S.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Тимофеева Светлана Сергеевна - кандидат технических наук, старший научный сотрудник лаборатории энергетических систем и технологий.</p><p>420111, Казань, ул. Лобачевского, д. 2/31, а/я 260</p><p>Researcher ID: AAZ-5531-2020, Scopus Author ID: 56711352400</p></bio><bio xml:lang="en"><p>Svetlana S. Timofeeva - Senior Researcher, laboratory of Energy Systems and Technologies, PhD, Institute of Power Engineering and Advanced Technologies, FRC Kazan Scientific Center, Russian Academy of Sciences.</p><p>420111, Kazan, st. Lobachevsky, 2/31, PO Box 190</p></bio><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-1983-3454</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Ковалев</surname><given-names>А. A.</given-names></name><name name-style="western" xml:lang="en"><surname>Kovalev</surname><given-names>A. A.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Ковалев Андрей Александрович - кандидат технических наук, старший научный сотрудник лаборатории биоэнергетических и сверхкритических технологий.</p><p>109428, Москва, 1-й Институтский проезд, д. 5</p><p>Researcher ID: F-7045-2017, Scopus Author ID: 57205285134</p></bio><bio xml:lang="en"><p>Andrey A. Kovalev - senior researcher of the laboratory of bioenergy and supercritical technologies, PhD, Federal Scientific Agroengineering Center VIM.</p><p>109428, Moscow, 1st Institutskiy Proezd, Building 5</p></bio><xref ref-type="aff" rid="aff-2"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-3603-3686</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Ковалев</surname><given-names>Д. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Kovalev</surname><given-names>D. A.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Ковалев Дмитрий Александрович - кандидат технических наук, заведующий лабораторией биоэнергетических технологий.</p><p>109428, Москва, 1-й Институтский проезд, д. 5</p><p>Researcher ID: K-4810-2015</p></bio><bio xml:lang="en"><p>Dmitry A. Kovalev - PhD, head of the laboratory of bioenergy and supercritical technologies.</p><p>109428, Moscow, 1st Institutskiy Proezd, Building 5</p></bio><xref ref-type="aff" rid="aff-2"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-5457-4603</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Литти</surname><given-names>Ю. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Litti</surname><given-names>Yu. V.</given-names></name></name-alternatives><bio xml:lang="ru"><p>Литти Юрий Владимирович - кандидат биологических наук, заведующий лабораторией микробиологии антропогенных мест обитания.</p><p>119071, Москва, Ленинский проспект, д.33, стр. 2</p><p>Researcher ID: C-4945-2014, Scopus Author ID: 55251689800</p></bio><bio xml:lang="en"><p>Yuriy V. Litti - Candidate of Biological Sciences, Head of Laboratory of Microbiology of Anthropogenic Habitats.</p><p>119071, Moscow, Leninsky Prospekt, 33, building 2</p></bio><xref ref-type="aff" rid="aff-3"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Институт энергетики и перспективных технологий ФИЦ Казанский научный центр РАН</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Institute of Power Engineering and Advanced Technologies, FRC Kazan Scientific Center, Russian Academy of Sciences</institution><country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru"><institution>Федеральный научный агроинженерный центр ВИМ</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Federal Scientific Agroengeneering Сenter VIM</institution><country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-3"><aff xml:lang="ru"><institution>ФИЦ Биотехнологии РАН</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Federal Research Center "Fundamentals of Biotechnology" of the Russian Academy of Sciences</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2023</year></pub-date><pub-date pub-type="epub"><day>28</day><month>03</month><year>2023</year></pub-date><volume>0</volume><issue>2</issue><fpage>64</fpage><lpage>81</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Международный издательский дом научной периодики "Спейс, 2023</copyright-statement><copyright-year>2023</copyright-year><copyright-holder xml:lang="ru">Международный издательский дом научной периодики "Спейс</copyright-holder><copyright-holder xml:lang="en">Международный издательский дом научной периодики "Спейс</copyright-holder><license xlink:href="https://www.isjaee.com/jour/about/submissions#copyrightNotice" xlink:type="simple"><license-p>https://www.isjaee.com/jour/about/submissions#copyrightNotice</license-p></license></permissions><self-uri xlink:href="https://www.isjaee.com/jour/article/view/2196">https://www.isjaee.com/jour/article/view/2196</self-uri><abstract><p>В работе представлены результаты исследования численного моделирования процесса газификации в газогенераторе с нисходящим потоком для получения синтез - газа с высоким содержанием водорода. Впервые исследована возможность применения эффлюента темновой ферментации в качестве сырья для термохимической конверсии с использованием в качестве окислителя - воздуха в соотношениях окислитель/топливо 0,45, 0,55 и 0,65. Моделирование процесса газификации осуществлялось в программном комплексе Comsol Multiphysics. В результате численных исследований были получены значения концентраций основных компонентов синтез - газа. Выход синтез - газа при воздушной газификации составил 1,8 м3/кг сухого вещества. При этом теплота сгорания генерируемого газа варьируется от 3,1 до 3,9 МДж/м3 при молярном отношении водорода к углекислому газу, находящемся в диапазоне от 3,1 до 3,9. Максимальный удельный вес водорода в составе синтез - газа, равный 26,94 %, достигается при соотношении окислитель/топливо, равном 0,45. Эффективность получения водорода варьируется в диапазоне от 23,8 до 27,3 %. Тепловая мощность, которую можно получить из синтез – газа, соответствует 47 – 59 кВт. Эффективность преобразования углерода составляет 23,6 – 28,8 %. На основании конструкционного расчета были получены основные геометрические параметры газогенератора с нисходящим потоком. Газогенератор предназначен для получения синтез - газов из эффлюентов анаэробной ферментации. Получение требуемых значений концентраций необходимых компонентов газа будет осуществляться путем варьирования расхода газифицирующего агента, а также комбинирования соотношений окислитель/топливо. Данное исследование позволит расширить знания в области комплексных технологий получения водорода из органических отходов, сочетающих биологические и термохимические методы.</p></abstract><trans-abstract xml:lang="en"><p>The paper presents the results of numerical simulation of the gasification process in a downdraft gasifier to produce syngas with high hydrogen content. For the first time the possibility of using dark fermentation digestate as a feedstock for thermochemical conversion using air as an oxidizer at equivalence ratio ER of 0.45, 0.55 and 0.65 was investigated. Modeling of the gasification process was carried out in the software package Comsol Multiphysics. As a result of numerical studies, the concentrations of the main components of the syngas were obtained. The syngas yield at air gasification was 1.8 m3/kg. At the same time the combustion heat of the generated gas varies from 3.1 to 3.9 MJ/m3 with the molar ratio MR being in the range from 3.1 to 3.9. The maximum specific gravity of hydrogen in the composition of syngas, equal to 26.94%, is achieved at ER = 0.45. The hydrogen production efficiency HPE ranges from 23.8 to 27.3 %. The thermal power that can be obtained from the syngas corresponds to 47 to 59 kW. Carbon conversion efficiency CCE is 23.6 - 28.8 %. The basic geometric parameters of downdraft gasifier were obtained based on the design calculation. The apparatus is designed to produce syngas from digestates of anaerobic fermentation. Obtaining the required concentrations of the necessary gas components will be done by varying the flow rate of the gasifying agent as well as by combining the ER. This study will increase knowledge in the field of complex technologies combining biological and thermochemical methods.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>воздушная газификация</kwd><kwd>газогенератор с нисходящим потоком</kwd><kwd>эффлюент</kwd><kwd>темновая ферментация</kwd><kwd>водород</kwd><kwd>синтез-газ</kwd></kwd-group><kwd-group xml:lang="en"><kwd>air gasification</kwd><kwd>downflow gas generator</kwd><kwd>effluent</kwd><kwd>dark fermentation</kwd><kwd>hydrogen</kwd><kwd>synthesis gas</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">Kevin C., Abdoulaye D., Faisal K. 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