Integrated mathematical modeling of catalytic cracking and zeolite-containing catalyst oxidative regeneration; Petroleum Science and Technology; Vol. 38, iss. 12
| Parent link: | Petroleum Science and Technology Vol. 38, iss. 12.— 2020.— [P. 754-762] |
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| Müşterek Yazar: | |
| Diğer Yazarlar: | , , , , , |
| Özet: | 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 |
| Dil: | İngilizce |
| Baskı/Yayın Bilgisi: |
2020
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| Konular: | |
| Online Erişim: | https://doi.org/10.1080/10916466.2020.1779290 |
| Materyal Türü: | Elektronik Kitap Bölümü |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=662863 |
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| 200 | 1 | |a Integrated mathematical modeling of catalytic cracking and zeolite-containing catalyst oxidative regeneration |f G. Yu. Nazarova, E. N. Ivashkina, E. D. Ivanchina [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: 20 tit.] | ||
| 330 | |a 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. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | |t Petroleum Science and Technology | ||
| 463 | |t Vol. 38, iss. 12 |v [P. 754-762] |d 2020 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a catalytic cracking | |
| 610 | 1 | |a hydrodynamics | |
| 610 | 1 | |a kinetics | |
| 610 | 1 | |a regeneration | |
| 610 | 1 | |a thermodynamics | |
| 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 Ivanchina |b E. D. |c chemist |c Professor of Tomsk Polytechnic University, Doctor of technical sciences |f 1951-2022 |g Emilia Dmitrievna |3 (RuTPU)RU\TPU\pers\31274 |9 15452 | |
| 701 | 1 | |a Oreshina |b A. A. |g Aleksandra Aleksandrovna | |
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