Mathematical model of the ethylene to propylene process Full article
| Conference |
VI Всероссийская научная молодежная школа-конференция «Химия под знаком СИГМА: исследования, инновации, технологии" 18-20 May 2020 , Омск |
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| Journal |
AIP Conference Proceedings
ISSN: 0094-243X , E-ISSN: 1551-7616 |
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| Output data | Year: 2020, Volume: 2301, Pages: 020001 Pages count : 5 DOI: 10.1063/5.0034524 | ||||
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| Affiliations |
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Funding (1)
| 1 | Ministry of Science and Higher Education of the Russian Federation | 46.2.5 |
Abstract:
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.
Cite:
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 OpenAlex
Mathematical model of the ethylene to propylene process
AIP Conference Proceedings. 2020. V.2301. P.020001. DOI: 10.1063/5.0034524 Scopus РИНЦ OpenAlex
Dates:
| Accepted: | Oct 26, 2020 |
| Published online: | Dec 8, 2020 |
Identifiers:
| Scopus: | 2-s2.0-85098090282 |
| Elibrary: | 45061912 |
| OpenAlex: | W3111965248 |
Citing:
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