Simulation and optimization of axial-flow and radial-flow reactors for dehydrogenation of ethylbenzene into styrene based on a heterogeneous kinetic model
•Low pressures have great impact on styrene conversion (yield) and selectivity.•Optimal inlet temperatures are increasing from the first to the last catalyst bed.•Radial-flow reactors are a better alternative than axial-flow when optimized.•It was obtained simultaneously styrene conversion of 76.5%...
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Published in | Chemical engineering science Vol. 244; p. 116805 |
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Main Authors | , , |
Format | Journal Article |
Language | English |
Published |
Elsevier Ltd
23.11.2021
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Subjects | |
Online Access | Get full text |
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