Mathematical Model of the Ethylene to Propylene Process | Sciact - CRIS-система Института катализа

Mathematical Model of the Ethylene to Propylene Process Научная публикация

Конференция

6th All-Russian Scientific School-Conference for Young Scientists on Chemistry under the Sign of SIGMA: Research, Innovation, Technology
18-20 мая 2020 , Омск

Журнал

AIP Conference Proceedings
ISSN: 0094-243X , E-ISSN: 1551-7616

Вых. Данные

Год: 2020, Том: 2301, Страницы: 020001 Страниц : 5 DOI: 10.1063/5.0034524

Авторы

Buluchevskiy E.A. ¹ , Karpova T.R. ¹ , Belyavskiy A.O. ² , Lavrenov A.V. ¹

Организации

1	Center of New Chemical Technologies BIC, Boreskov Institute of Catalysis, 54, Neftezavodskaya St., Omsk 644040, Russian Federation
2	Omsk State Technical University, Mira Av. 11, Omsk, 644050, Russian Federation

Информация о финансировании (1)

Федеральное агентство научных организаций России

V.46.2.5. (АААА-А17-117021450096-8)

The kinetics of the ethylene to propylene process was studied in a laboratory reactor. Ethylene dimerization was shown to be the limiting stage of the process. By means of calculations using a non-isothermal model, it was found that the adiabatic heating of the bed in the reactor is 350 °C and more, which requires the use of an isothermal reactor. The contact time providing the maximum propylene yield is 6 s at WHSV 1 h-1 and 50° C.

Buluchevskiy E.A. , Karpova T.R. , Belyavskiy A.O. , Lavrenov A.V.
Mathematical Model of the Ethylene to Propylene Process
AIP Conference Proceedings. 2020. V.2301. P.020001. DOI: 10.1063/5.0034524 Scopus РИНЦ CAPlus OpenAlex

Принята к публикации:	26 окт. 2020 г.
Опубликована online:	8 дек. 2020 г.

Scopus:	2-s2.0-85098090282
РИНЦ:	45061912
Chemical Abstracts:	2021:1128854
OpenAlex:	W3111965248

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