Author:
Solovev S A,Soloveva O V,Gilmurahmanov B Sh,Lamberov A A
Abstract
Abstract
In this work, we performed mathematical modeling of internal elements for mixing the reaction flows. The reactor of the dehydrogenation of ethylbenzene to styrene process was studied. A variant of a radial type reactor in which the gas flow is from the bottom up is considered. Ethylbenzene and steam were selected as components for mixing. Ethylbenzene is supplied to the mixer at a temperature of about 600°C, and steam at a temperature of about 700°C. Three design cases for the internal devices of the mixer are considered. The analysis of the gas mixture parameters, such as volume fraction and average temperature, at the outlet of the mixer was carried out. The cases with the best mixing of the components are determined.
Cited by
2 articles.
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1. Mathematical simulation of the reactor for the ethylbenzene to styrene dehydrogenation reaction;Journal of Physics: Conference Series;2020-11-01
2. Numerical Investigation of the Catalyst Granule Shapes Influence on Dehydrogenation Reaction;International Scientific Conference Energy Management of Municipal Facilities and Sustainable Energy Technologies EMMFT 2019;2020-08-18