A Model of Catalytic Cracking: Product Distribution and Catalyst Deactivation Depending on Saturates, Aromatics and Resins Content in Feed; Catalysts; Vol. 11, iss. 6

Dades bibliogràfiques
Parent link:Catalysts
Vol. 11, iss. 6.— 2021.— [701, 17 p.]
Autor corporatiu: Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
Altres autors: 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
Sumari: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.
Idioma:anglès
Publicat: 2021
Matèries:
Accés en línia:http://earchive.tpu.ru/handle/11683/70744
https://doi.org/10.3390/catal11060701
Format: Electrònic Capítol de llibre
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=666790

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200 1 |a A Model of Catalytic Cracking: Product Distribution and Catalyst Deactivation Depending on Saturates, Aromatics and Resins Content in Feed  |f G. Yu. Nazarova, E. N. Ivashkina, E. D. Ivanchina [et al.] 
203 |a Text  |c electronic 
300 |a Title screen 
320 |a [References: 40 tit.] 
330 |a 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. 
338 |b Российский фонд фундаментальных исследований  |d 21-53-10004 
338 |b Российский научный фонд  |d 19-71-10015 
461 |t Catalysts 
463 |t Vol. 11, iss. 6  |v [701, 17 p.]  |d 2021 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
610 1 |a vacuum gasoil 
610 1 |a residues 
610 1 |a coke 
610 1 |a catalyst deactivation 
610 1 |a kinetics 
610 1 |a mathematical model 
610 1 |a вакуумные газойли 
610 1 |a кокс 
610 1 |a дезактивация 
610 1 |a катализаторы 
610 1 |a кинетика 
610 1 |a математические модели 
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701 1 |a Ivashkina  |b E. N.  |c Chemical Engineer  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1983-  |g Elena Nikolaevna  |3 (RuTPU)RU\TPU\pers\31275  |9 15453 
701 1 |a Ivanchina  |b E. D.  |c chemist  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1951-  |g Emilia Dmitrievna  |3 (RuTPU)RU\TPU\pers\31274 
701 1 |a Vosmerikov  |b A. V.  |g Aleksandr Vladimirovich 
701 1 |a Vosmerikova  |b L. N.  |g Lyudmila Nikolaevna 
701 1 |a Antonov  |b A. V.  |c chemist  |c engineer of Tomsk Polytechnic University  |f 1996-  |g Artem Viktorovich  |3 (RuTPU)RU\TPU\pers\47444 
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