Samara University Repository
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| Title: | Mathematical model of the catalytic isomerization reactor block of the pentane-hexane fraction based on the kinetic model |
| Issue Date: | May-2019 |
| Publisher: | Новая техника |
| Citation: | Faskhutdinov A.G. Mathematical model of the catalytic isomerization reactor block of the pentane-hexane fraction based on the kinetic model / Faskhutdinov A.G., Arefyev I.A. // Сборник трудов ИТНТ-2019 [Текст]: V междунар. конф. и молодеж. шк. "Информ. технологии и нанотехнологии": 21-24 мая: в 4 т. / Самар. нац.-исслед. ун-т им. С. П. Королева (Самар. ун-т), Ин-т систем. обраб. изобр. РАН-фил. ФНИЦ "Кристаллография и фотоника" РАН; [под ред. В.А. Соболева]. - Самара: Новая техника, 2019. – Т. 3: Математическое моделирование физико-технических процессов и систем. - 2019. - С. 359-363. |
| Abstract: | The main schemes for the conversion of the catalytic isomerization of the pentane-hexane fraction, which are probable from the standpoint of thermodynamics, are considered. Based on a literary analysis of possible transformation schemes, the mechanism of the process and based on experimental data, a mathematical model of the reactor unit of the process in UniSim Design was developed and the kinetic parameters were determined. The foundations were laid for the subsequent solution of the tasks of the multi-purpose optimization of the catalytic isomerization process of the pentane-hexane fraction. |
| URI: | http://repo.ssau.ru/jspui/handle/123456789/11388 |
| Appears in Collections: | Информационные технологии и нанотехнологии |
| File | Description | Size | Format | |
|---|---|---|---|---|
| paper56.pdf | Основная статья | 258.69 kB | Adobe PDF | View/Open |
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