Development of a Mathematical Model of the Vacuum Oil Distillates Hydrocracking Process Taking into Account Catalyst Deactivation by Coke; Petroleum and Coal; Vol. 63, iss. 4
| Parent link: | Petroleum and Coal Vol. 63, iss. 4.— 2021.— [P. 988-993] |
|---|---|
| Autor corporatiu: | Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии |
| Altres autors: | Belinskaya N. S. Natalia Sergeevna, Afanasjeva D. A. Darjya Aleksandrovna, Bykova V. V. Violetta Vitaljevna, Kosten M. S. Mikhail Sergeevich |
| Sumari: | Title screen A mathematical model of the vacuum oil distillates hydrocracking process, which takes into account catalyst deactivation by coke, was developed. The mathematical model was implemented in the form of a computer modelling system. Using the developed computer modelling system, predictive calculations of the decrease in the catalyst activity during the working cycle were carried out for various compositions of the feedstock. The influence of the ratio Hydrogen-containing gas / Feedstock on the rate of catalyst deactivation during the working cycle was shown. |
| Idioma: | anglès |
| Publicat: |
2021
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| Matèries: | |
| Accés en línia: | https://www.vurup.sk//wp-content/uploads/2022/01/PC-X_Belinskaya_81.pdf |
| Format: | Electrònic Capítol de llibre |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=668041 |
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