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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">spfp</journal-id><journal-title-group><journal-title xml:lang="ru">Хранение и переработка сельхозсырья</journal-title><trans-title-group xml:lang="en"><trans-title>Storage and Processing of Farm Products</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">2072-9669</issn><issn pub-type="epub">2658-767X</issn><publisher><publisher-name>РОСБИОТЕХ</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.36107/spfp.2023.426</article-id><article-id custom-type="elpub" pub-id-type="custom">spfp-426</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>БИОТЕХНОЛОГИЧЕСКИЕ И МИКРОБИОЛОГИЧЕСКИЕ АСПЕКТЫ</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>BIOTECHNOLOGICAL AND MICROBIOLOGICAL ASPECTS</subject></subj-group></article-categories><title-group><article-title>Определение целесообразности предварительной декатионизации растительного сырья для ферментативной фрагментации протопектинового комплекса</article-title><trans-title-group xml:lang="en"><trans-title>Determination of the Feasibility of Preliminary Decationization of Plant Raw Materials for Enzymatic Fragmentation of the Protopectin Complex</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-0913-5644</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Кондратенко</surname><given-names>Владимир Владимирович</given-names></name><name name-style="western" xml:lang="en"><surname>Kondratenko</surname><given-names>Vladimir V.</given-names></name></name-alternatives><bio xml:lang="ru"><p>SPIN-код: 3383-1774;  Researcher ID: E-3592-2010</p><p> </p><p> </p></bio><email xlink:type="simple">v_kondratenko@vnimi.org</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0001-8237-0774</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Кондратенко</surname><given-names>Татьяна Юрьевна</given-names></name><name name-style="western" xml:lang="en"><surname>Kondratenko</surname><given-names>Tatyana Yu.</given-names></name></name-alternatives><bio xml:lang="ru"><p>SPIN-код: 7558-8832;  Researcher ID: ABF-3810-2022</p></bio><email xlink:type="simple">t.kondratenko@fncps.ru</email><xref ref-type="aff" rid="aff-2"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Всероссийский научно-исследовательский институт молочной промышленности»</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Russian Dairy Research Institute</institution><country>Russian Federation</country></aff></aff-alternatives><aff-alternatives id="aff-2"><aff xml:lang="ru"><institution>Всероссийский научный центр пищевых систем им. В.М. Горбатова</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Russian Research Institute of Canning Technology — branch of Gorbatov&#13;
Research Center for Food Systems 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>30</day><month>06</month><year>2023</year></pub-date><volume>0</volume><issue>2</issue><fpage>118</fpage><lpage>131</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Кондратенко В.В., Кондратенко Т.Ю., 2023</copyright-statement><copyright-year>2023</copyright-year><copyright-holder xml:lang="ru">Кондратенко В.В., Кондратенко Т.Ю.</copyright-holder><copyright-holder xml:lang="en">Kondratenko V.V., Kondratenko T.Y.</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.spfp-mgupp.ru/jour/article/view/426">https://www.spfp-mgupp.ru/jour/article/view/426</self-uri><abstract><sec><title>Введение</title><p>Введение: Использование ферментных препаратов для обработки растительного сырья налагает некоторые ограничения, определяемые структурой молекул ферментов и свойствами среды. Одним из основных лимитирующих факторов является возможное присутствие в среде ингибитора, подавляющего каталитическую активность. Потенциальным ингибитором могут являться катионы поливалентных металлов, поэтому определение целесообразности декатионизации среды перед ферментативной обработкой является актуальным.</p></sec><sec><title>Цель</title><p>Цель: исследования является разработка подхода к определению целесообразности предварительной декатионизации сырья перед ферментативным процессом.</p></sec><sec><title>Материалы и методы</title><p>Материалы и методы: В качестве субстрата использовали негранулированный сухой немелассированный свекловичный жом. Ферментативную обработку проводили гомоферментным препаратом рамногалактуронан лиазного действия в концентрации 0,00,0,05, 0,1, 0,2, 0,4 и 0,8 % от массы сухого субстрата. Предварительную обработку набухшего сырья поводили 0,00, 0,20, 0,50 и 0,91 ед. от 2,87 % водного раствора комплексона (ЭДТА). Фактором отклика была удельная электрическая проводимость. Ферментативный процесс проводили при температуре 45 °С течение 8 часов. Аппроксимацией экспериментальных данных для каждого варианта исследований получали математическое описание динамик ферментативного процесса.</p></sec><sec><title>Результаты</title><p>Результаты: По характеру зависимости обратных кинетических показателей было установлено, что в пределах каждой концентрации ферментного препарата значение асимптотического темпа процесса Vmax = const, а константа Михаэлиса Km непрерывно увеличивается. Для комплексной оценки исследуемых динамик была разработана система критериев, включающая критерий изменчивости константы Михаэлиса Q (Km), дискретный критерий оптимальности Z, комплексный критерий оптимальности декатионизации F и критерий оценки Q, сопровождаемые 4 постулируемыми условиями оптимизации.</p></sec><sec><title>Выводы</title><p>Выводы: В результате разработанная система критериев позволяет решать сразу три задачи — определение целесообразности предварительной декатионизации, оптимальные концентрации комплексона и гомоферментного препарата.</p></sec></abstract><trans-abstract xml:lang="en"><sec><title>Introduction</title><p>Introduction: The use of enzyme preparations for processing plant raw materials imposes some restrictions determined by the structure of enzyme molecules and the properties of the medium. One of the main limiting factors is the possible presence of an inhibitor in the medium that suppresses catalytic activity. Polyvalent metal cations can be a potential inhibitor, therefore, determining the expediency of decationization of the medium before enzymatic treatment is relevant.</p></sec><sec><title>Purpose</title><p>Purpose: The aim of the work is to develop an approach to determining the feasibility of preliminary decationization of raw materials before the enzymatic process.</p></sec><sec><title>Materials and Methods</title><p>Materials and Methods: Non-granulated dry non-massaged beet pulp was used as a substrate. Enzymatic treatment was carried out with a homoenzyme preparation of rhamnogalacturonan lyase action at a concentration of 0.00, 0.05, 0.1, 0.2, 0.4 and 0.8 % by weight of the dry substrate. The pretreatment of the swollen raw materials was carried out by 0.00, 0.20, 0.50 and 0.91 units of 2.87 % aqueous solution of complexon. The response factor was electrical conductivity. The enzymatic process was carried out at a temperature of 45 °C for 8 hours. By approximating the experimental data for each research variant, a mathematical description of the dynamics of the enzymatic process was obtained.</p></sec><sec><title>Results</title><p>Results: By the nature of the dependence of the inverse kinetic parameters, it was found that within each concentration of the enzyme preparation, the value of the asymptotic rate of the process Vmax = const, and the Michaelis constant Km continuously increases. For a comprehensive assessment of the studied dynamics, a system of criteria was developed, including the criterion of variability of the Michaelis constant Q (Km), the discrete optimality criterion Z, the complex optimality criterion of decationization F and the evaluation criterion Q, accompanied by 4 postulated optimization conditions.</p></sec><sec><title>Conclusions</title><p>Conclusions: As a result, the developed system of criteria makes it possible to solve three tasks at once – determining the feasibility of pre-decationization, optimal concentrations of complexon and homoenzyme preparation. </p></sec></trans-abstract><kwd-group xml:lang="ru"><kwd>ферментативная активность</kwd><kwd>фрагментация</kwd><kwd>протопектиновый комплекс</kwd><kwd>ингибирование</kwd><kwd>декатионизация</kwd><kwd>растительное сырьё</kwd></kwd-group><kwd-group xml:lang="en"><kwd>enzymatic activity</kwd><kwd>fragmentation</kwd><kwd>protopectin complex</kwd><kwd>inhibition</kwd><kwd>decationization</kwd><kwd>vegetable raw materials</kwd></kwd-group><funding-group><funding-statement xml:lang="ru">Всероссийский научный центр пищевых систем им. 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