Prediction of residue coke content and operating modes of regenerator in the catalytic cracking technology

מידע ביבליוגרפי
Parent link:Petroleum Science and Technology
Vol. 38, iss. 24.— 2020.— [P. 1017-1025]
מחבר תאגידי: Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
מחברים אחרים: Nazarova G. Yu. Galina Yurievna, Ivashkina E. N. Elena Nikolaevna, Shafran T. A. Tatjyana Aleksandrovna, Oreshina A. A. Aleksandra Aleksandrovna, Seytenova G. Zh. Gayni Zhumagalievna
סיכום:Title screen
This work is aimed at predicting the amount of residue coke and the temperature of operating mode of the regenerator, depending on the initial technological conditions of the process during regeneration of catalyst coked at various degrees (0.4–0.6% wt.). Numerical studies were performed using a mathematical model that takes into account the physicochemical regularities of the regeneration process for zeolite-containing catalysts and making it possible to predict not only the amount of the residual coke and the flue gas composition of regeneration, but also the temperature in the regeneration zone. It has been stated that when changing the amount of coke on the coked catalyst from 0.4 to 0.6% wt., the regeneration temperature must be maintained in the range of 673.8–712.8 C to achieve the degree of coke conversion at the level of 92% and to prevent the irreversible deactivation of the catalyst.
Режим доступа: по договору с организацией-держателем ресурса
שפה:אנגלית
יצא לאור: 2020
נושאים:
גישה מקוונת:https://doi.org/10.1080/10916466.2020.1825966
פורמט: אלקטרוני Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=663238

MARC

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200 1 |a Prediction of residue coke content and operating modes of regenerator in the catalytic cracking technology  |f G. Yu. Nazarova, E. N. Ivashkina, T. A. Shafran [et al.] 
203 |a Text  |c electronic 
300 |a Title screen 
320 |a [References: 26 tit.] 
330 |a This work is aimed at predicting the amount of residue coke and the temperature of operating mode of the regenerator, depending on the initial technological conditions of the process during regeneration of catalyst coked at various degrees (0.4–0.6% wt.). Numerical studies were performed using a mathematical model that takes into account the physicochemical regularities of the regeneration process for zeolite-containing catalysts and making it possible to predict not only the amount of the residual coke and the flue gas composition of regeneration, but also the temperature in the regeneration zone. It has been stated that when changing the amount of coke on the coked catalyst from 0.4 to 0.6% wt., the regeneration temperature must be maintained in the range of 673.8–712.8 C to achieve the degree of coke conversion at the level of 92% and to prevent the irreversible deactivation of the catalyst. 
333 |a Режим доступа: по договору с организацией-держателем ресурса 
461 |t Petroleum Science and Technology 
463 |t Vol. 38, iss. 24  |v [P. 1017-1025]  |d 2020 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
610 1 |a mathematical modeling 
610 1 |a optimization 
610 1 |a regeneration 
610 1 |a residue coke 
610 1 |a математическое моделирование 
610 1 |a оптимизация 
610 1 |a регенерация 
701 1 |a Nazarova  |b G. Yu.  |c chemist  |c assistant of Tomsk Polytechnic University  |f 1990-  |g Galina Yurievna  |3 (RuTPU)RU\TPU\pers\35588  |9 18757 
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 Shafran  |b T. A.  |g Tatjyana Aleksandrovna 
701 1 |a Oreshina  |b A. A.  |g Aleksandra Aleksandrovna 
701 1 |a Seytenova  |b G. Zh.  |g Gayni Zhumagalievna 
712 0 2 |a Национальный исследовательский Томский политехнический университет  |b Инженерная школа природных ресурсов  |b Отделение химической инженерии  |3 (RuTPU)RU\TPU\col\23513 
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