A Model of Catalytic Cracking: Product Distribution and Catalyst Deactivation Depending on Saturates, Aromatics and Resins Content in Feed; Catalysts; Vol. 11, iss. 6
| Parent link: | Catalysts Vol. 11, iss. 6.— 2021.— [701, 17 p.] |
|---|---|
| Corporate Author: | Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии |
| Other Authors: | Nazarova G. Yu. Galina Yurievna, Ivashkina E. N. Elena Nikolaevna, Ivanchina E. D. Emilia Dmitrievna, Vosmerikov A. V. Aleksandr Vladimirovich, Vosmerikova L. N. Lyudmila Nikolaevna, Antonov A. V. Artem Viktorovich |
| Summary: | Title screen The problems of catalyst deactivation and optimization of the mixed feedstock become more relevant when the residues are involved as a catalytic cracking feedstock. Through numerical and experimental studies of catalytic cracking, we optimized the composition of the mixed feedstock in order to minimize the catalyst deactivation by coke. A pure vacuum gasoil increases the yields of the wet gas and the gasoline (56.1 and 24.9 wt%). An increase in the ratio of residues up to 50% reduces the gasoline yield due to the catalyst deactivation by 19.9%. However, this provides a rise in the RON of gasoline and the light gasoil yield by 1.9 units and 1.7 wt% Moreover, the ratio of residue may be less than 50%, since the conversion is limited by the regenerator coke burning ability. |
| Language: | English |
| Published: |
2021
|
| Subjects: | |
| Online Access: | http://earchive.tpu.ru/handle/11683/70744 https://doi.org/10.3390/catal11060701 |
| Format: | Electronic Book Chapter |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=666790 |
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