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dc.contributor.author | Solovev S.A. | |
dc.contributor.author | Soloveva O.V. | |
dc.contributor.author | Gilmurahmanov B.S. | |
dc.contributor.author | Lamberov A.A. | |
dc.date.accessioned | 2021-02-25T06:52:15Z | |
dc.date.available | 2021-02-25T06:52:15Z | |
dc.date.issued | 2020 | |
dc.identifier.issn | 1742-6588 | |
dc.identifier.uri | https://dspace.kpfu.ru/xmlui/handle/net/161193 | |
dc.description.abstract | © Published under licence by IOP Publishing Ltd. In this work, we carried out a numerical simulation of an industrial reactor of a radial type with a fixed catalyst bed for the process of ethylbenzene to styrene dehydrogenation. We solved the problem in the approximation of two-dimensional axial symmetry. The parameters of the chemically reacting gas mixture movement in the catalyst bed are considered. The reactor zones which have a negative impact on the reaction efficiency have been determined. | |
dc.relation.ispartofseries | Journal of Physics: Conference Series | |
dc.title | Mathematical simulation of the reactor for the ethylbenzene to styrene dehydrogenation reaction | |
dc.type | Conference Paper | |
dc.relation.ispartofseries-issue | 5 | |
dc.relation.ispartofseries-volume | 1679 | |
dc.collection | Публикации сотрудников КФУ | |
dc.source.id | SCOPUS17426588-2020-1679-5-SID85097538580 |