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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">vguit</journal-id><journal-title-group><journal-title xml:lang="ru">Вестник Воронежского государственного университета инженерных технологий</journal-title><trans-title-group xml:lang="en"><trans-title>Proceedings of the Voronezh State University of Engineering Technologies</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">2226-910X</issn><issn pub-type="epub">2310-1202</issn><publisher><publisher-name>VSUET</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.20914/2310-1202-2025-2-126-133</article-id><article-id custom-type="elpub" pub-id-type="custom">vguit-3667</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>Пищевые системы</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>Food systems</subject></subj-group></article-categories><title-group><article-title>Кинетика сушки яблочных выжимок в псевдоожиженном слое</article-title><trans-title-group xml:lang="en"><trans-title>Kinetics of apple pomace drying in fluidised bed</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0009-0007-5931-3545</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Поперечный</surname><given-names>А. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Poperechny</surname><given-names>A. N.</given-names></name></name-alternatives><bio xml:lang="ru"><p>д.т.н., профессор, кафедра оборудования пищевых производств, пр-т Театральный, 28, г. Донецк, 283001, Россия</p></bio><bio xml:lang="en"><p>Dr. Sci. (Engin.), professor, food production equipment department, Teatralny Ave, Donetsk, 283001, Russia</p></bio><email xlink:type="simple">oborud@kaf.donnuet.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/0009-0007-4157-3269</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Байда</surname><given-names>Б. Ю.</given-names></name><name name-style="western" xml:lang="en"><surname>Baida</surname><given-names>B. Y.</given-names></name></name-alternatives><bio xml:lang="ru"><p>старший преподаватель, кафедра холо-дильной и торговой техники имени Осокина В.В., пр-т Театральный, 28, г. Донецк, 283001, Россия</p></bio><bio xml:lang="en"><p>Senior Lecturer, Osokin V.V. refrigeration and trade technolog department, Teatralny Ave, Donetsk, 283001, Russia</p></bio><email xlink:type="simple">bayda.boris@mail.ru</email><xref ref-type="aff" rid="aff-2"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0009-0003-5527-4252</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Плетминцев</surname><given-names>И. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Pletmintsev</surname><given-names>I. A.</given-names></name></name-alternatives><bio xml:lang="ru"><p>магистрант, кафедра оборудования пищевых производств, пр-т Театральный, 28, г. Донецк, 283001, Россия</p></bio><bio xml:lang="en"><p>graduate student, food production equipment department, Teatralny Ave, Donetsk, 283001, Russia</p></bio><email xlink:type="simple">gatbaida@ya.ru</email><xref ref-type="aff" rid="aff-3"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Донецкий национальный университет экономики и торговли им. Михаила Туган-Барановского</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Donetsk National University of Economics and Trade named after Mikhail Tugan-Baranovsky, 28</institution><country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru"><institution>Донецкий национальный университет экономики и торговли им. Михаила Туган-Барановского</institution><country>Russian Federation</country></aff><aff xml:lang="en"><institution>Donetsk National University of Economics and Trade named after Mikhail Tugan-Baranovsky, 28</institution><country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-3"><aff xml:lang="ru"><institution>Донецкий национальный университет экономики и торговли им.Михаила Туган-Барановского</institution><country>Russian Federation</country></aff><aff xml:lang="en"><institution>Donetsk National University of Economics and Trade named after Mikhail Tugan-Baranovsky, 28</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2025</year></pub-date><pub-date pub-type="epub"><day>30</day><month>05</month><year>2025</year></pub-date><volume>87</volume><issue>2</issue><fpage>126</fpage><lpage>133</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Поперечный А.Н., Байда Б.Ю., Плетминцев И.А., 2025</copyright-statement><copyright-year>2025</copyright-year><copyright-holder xml:lang="ru">Поперечный А.Н., Байда Б.Ю., Плетминцев И.А.</copyright-holder><copyright-holder xml:lang="en">Poperechny A.N., Baida B.Y., Pletmintsev I.A.</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.vestnik-vsuet.ru/vguit/article/view/3667">https://www.vestnik-vsuet.ru/vguit/article/view/3667</self-uri><abstract><p>Цель исследования – обоснование режимов сушки гранулированных яблочных выжимок в псевдоожиженном слое и оценка кинетики процесса. Эксперимент выполнен на лабораторной установке с прозрачной сушильной камерой, диафрагмой для измерения расхода воздуха, U-образным микроманометром, хромель-копелевыми термопарами и потенциометром. Контролировались температуры на входе и выходе, в толще слоя и в частицах; скорость потока измерялась анемометром. Исходные образцы имели влагосодержание около 250%, конечная влажность доводилась до 8–10%. Съём кривых выполнялся по результатам периодического взвешивания с шагом 2 мин. Получены кривые влагосодержания и скорости сушки при температурах 70–100 °C и при разных тепловых нагрузках. Процесс протекает в два периода: постоянной и падающей скорости. Переходная «критическая точка» фиксируется при влагосодержании около 100%. Продолжительность периода постоянной скорости составляет около 70% общей длительности. Установлены гидродинамические параметры псевдоожижения: устойчивый режим слоя наблюдается при скорости воздуха более 2,5 м/с; характерные скорости для гранул диаметром 5 мм составляют: начало кипения 2,0 м/с, витание 3,5 м/с, вынос из слоя 3,7 м/с. При влагосодержании выше 260% устойчивое псевдоожижение не формируется. Сушка в псевдоожиженном слое обеспечивает существенную интенсификацию: максимальная скорость в первом периоде выше в 3–10 раз по сравнению с неподвижным слоем; длительность процесса меньше в 4–8 раз; удельный расход воздуха ниже примерно в 1,5 раза. Применение виброкипящего слоя повышает однородность псевдоожижения и допускает работу при повышенных скоростях воздуха. Рекомендованы режимы: температура сушильного агента 70–100 °C; скорость воздуха свыше 2,5 м/с; доведение конечной влажности до 8–10%; хранение готового продукта при относительной влажности воздуха не выше 75%.</p></abstract><trans-abstract xml:lang="en"><p>The aim of the study is the substantiation of drying regimes for granulated apple pomace in a fluidized bed and the assessment of the kinetics of the process. The experiment was performed on a laboratory setup with a transparent drying chamber, a diaphragm for measuring air flow rate, a U-tube micro-manometer, chromel–copel thermocouples, and a potentiometer. Temperatures at the inlet and outlet, within the bed and in the particles, were monitored; the flow velocity was measured by an anemometer. The initial samples had a moisture content of about 250%, the final moisture was reduced to 8–10%. The recording of the curves was carried out based on periodic weighing at 2-min intervals. Curves of moisture content and drying rate were obtained at temperatures 70–100 °C and at different heat loads. The process proceeds in two periods: a constant-rate period and a falling-rate period. The transitional “critical point” is fixed at a moisture content of about 100%. The duration of the constant-rate period is about 70% of the total duration. Hydrodynamic parameters of fluidization were established: a stable bed regime is observed at an air velocity greater than 2.5 m/s; the characteristic velocities for granules with a diameter of 5 mm are: onset of bubbling 2.0 m/s, free floating 3.5 m/s, carryover from the bed 3.7 m/s. At a moisture content above 260% stable fluidization is not formed. Drying in a fluidized bed provides substantial intensification: the maximum rate in the first period is 3–10 times higher compared with a fixed bed; the process duration is lower by 4–8 times; the specific air consumption is lower by approximately 1.5 times. The use of a vibro-fluidized bed increases the uniformity of fluidization and allows operation at elevated air velocities. The recommended regimes are: drying-agent temperature 70–100 °C; air velocity above 2.5 m/s; achievement of final moisture 8–10%; storage of the finished product at a relative air humidity not higher than 75%.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>яблочные выжимки</kwd><kwd>псевдоожиженный слой</kwd><kwd>кинетика сушки</kwd><kwd>кривые сушки</kwd><kwd>скорость сушки</kwd><kwd>критическая точка сушки</kwd><kwd>гидродинамическое сопротивление</kwd><kwd>скорость псевдоожижения</kwd><kwd>тепловая нагрузка</kwd><kwd>влагосодержание</kwd></kwd-group><kwd-group xml:lang="en"><kwd>apple pomace</kwd><kwd>fluidized bed</kwd><kwd>drying kinetics</kwd><kwd>drying curves</kwd><kwd>drying rate</kwd><kwd>critical point of drying</kwd><kwd>hydrodynamic resistance</kwd><kwd>fluidization velocity</kwd><kwd>heat load</kwd><kwd>moisture content</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">Шишацкий Ю.И., Толстов С.А., Дерканосова А.А. и др. 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