Conversion enhancement of heavy reformates into xylenes by optimal design of a novel radial flow packed bed reactor, applying a detailed kinetic model
•Modeling of a novel radial-flow reactor for upgrading of heavy reformates to xylene.•A new kinetic model involving 18 pseudo-components and 39 reactions.•Applying thermodynamic principles to estimate the reversibility of the reactions.•Applying DE optimization method to optimize the proposed and co...
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Published in | Chemical engineering research & design Vol. 95; pp. 317 - 336 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
Elsevier B.V
01.03.2015
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Subjects | |
Online Access | Get full text |
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