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] |
|---|---|
| Körperschaft: | |
| Weitere Verfasser: | , , , |
| Zusammenfassung: | 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. |
| Sprache: | Englisch |
| Veröffentlicht: |
2021
|
| Schlagworte: | |
| Online-Zugang: | https://www.vurup.sk//wp-content/uploads/2022/01/PC-X_Belinskaya_81.pdf |
| Format: | Elektronisch Buchkapitel |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=668041 |
| Zusammenfassung: | 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. |
|---|