Integrated mathematical modeling of catalytic cracking and zeolite-containing catalyst oxidative regeneration; Petroleum Science and Technology; Vol. 38, iss. 12

Integrated mathematical modeling of catalytic cracking and zeolite-containing catalyst oxidative regeneration; Petroleum Science and Technology; Vol. 38, iss. 12

Détails bibliographiques
Parent link:	Petroleum Science and Technology Vol. 38, iss. 12.— 2020.— [P. 754-762]
Collectivité auteur:	Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
Autres auteurs:	Nazarova G. Yu. Galina Yurievna, Ivashkina E. N. Elena Nikolaevna, Ivanchina E. D. Emilia Dmitrievna, Oreshina A. A. Aleksandra Aleksandrovna, Vymyatnin E. K. Evgeny Konstantinovich, Burumbaeva G. R. Galiya Rashidovna
Résumé:	Title screen The work is aimed at establishing the thermodynamic, kinetic and hydrodynamic regularities of the vacuum gas oil catalytic cracking and the zeolite-containing catalysts regeneration, which served as a catalytic cracking reactor mathematical model development basis. The prediction calculations ensured the catalyst circulation ratio optimization depending on the catalyst flow temperature after regeneration. To maintain the gasoline fraction maximum yield (58.47 and 58.38?wt%) it is necessary to keep the catalyst circulation ratio at the level of 6 and 9.5 tonscat/tonsfeed if the catalyst flow temperature after regeneration are 700 and 650?°C, respectively. Режим доступа: по договору с организацией-держателем ресурса
Langue:	anglais
Publié:	2020
Sujets:	электронный ресурс труды учёных ТПУ catalytic cracking hydrodynamics kinetics regeneration thermodynamics
Accès en ligne:	https://doi.org/10.1080/10916466.2020.1779290
Format:	Électronique Chapitre de livre
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=662863

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