Improving the Mathematical Model of the Catalytic Reforming Process with a Fixed Catalyst Bed Научная публикация
| Конференция |
XXV Всероссийская конференция по химическим реакторам 08-13 окт. 2023 , Тюмень |
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| Журнал |
Catalysis in Industry
ISSN: 2070-0504 , E-ISSN: 2070-0555 |
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| Вых. Данные | Год: 2025, Том: 17, Номер: 2, Страницы: 162–176 Страниц : DOI: 10.1134/S2070050425700072 | ||||
| Авторы |
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| Организации |
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Реферат:
A mathematical model that adequately describes the process of catalytic reforming—the main industrial technology for obtaining high-octane components of motor fuels in Russia and abroad is presented. The necessity of expanding the existing scheme of transformations of hydrocarbons of the gasoline series to create a model of reforming feedstocks of various origins (gasoline fractions of thermal destructive processes, hydrocracking naphtha, gas condensate) is shown. Based on the results of experimental studies using gas chromatography, as well as the calculations of thermodynamic parameters, an improved formalized reaction scheme has been compiled to take into account into account reactions involving unsaturated hydrocarbons. A kinetic model of the reforming process of the expanded gasoline fraction has been compiled. To describe the kinetic model based on the formalized scheme of hydrocarbon transformations, a matrix method was used, which makes the model more flexible to the composition of the feedstock.
Библиографическая ссылка:
Pchelintseva I.V.
, Ivashkina E.N.
, Chernyakova E.S.
, Tazhmulikov D.B.
, Chyuzlov V.A.
Improving the Mathematical Model of the Catalytic Reforming Process with a Fixed Catalyst Bed
Catalysis in Industry. 2025. V.17. N2. P.162–176. DOI: 10.1134/S2070050425700072 WOS Scopus РИНЦ OpenAlex
Improving the Mathematical Model of the Catalytic Reforming Process with a Fixed Catalyst Bed
Catalysis in Industry. 2025. V.17. N2. P.162–176. DOI: 10.1134/S2070050425700072 WOS Scopus РИНЦ OpenAlex
Оригинальная версия:
Пчелинцева И.В.
, Ивашкина Е.Н.
, Чернякова Е.С.
, Тажмуликов Д.Б.
, Чузлов В.А.
Совершенствование математической модели процесса каталитического риформинга со стационарным слоем катализатора
Катализ в промышленности. 2024. №4. С.78-93. DOI: 10.18412/1816-0387-2024-4-78-93 РИНЦ CAPlus OpenAlex
Совершенствование математической модели процесса каталитического риформинга со стационарным слоем катализатора
Катализ в промышленности. 2024. №4. С.78-93. DOI: 10.18412/1816-0387-2024-4-78-93 РИНЦ CAPlus OpenAlex
Даты:
| Поступила в редакцию: | 16 янв. 2024 г. |
| Принята к публикации: | 6 мар. 2024 г. |
| Опубликована online: | 24 июн. 2025 г. |
Идентификаторы БД:
| Web of science: | WOS:001515178700007 |
| Scopus: | 2-s2.0-105009301978 |
| РИНЦ: | 82565709 |
| OpenAlex: | W4411583824 |