Enhancement of Equilibriumshift in Dehydrogenation Reactions Using a Novel Membrane Reactor | Zendy

Shamsuddin Ilias | Zendy; Franklin G. King | Zendy

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Enhancement of Equilibriumshift in Dehydrogenation Reactions Using a Novel Membrane Reactor

Author(s) -

Shamsuddin Ilias,

Franklin G. King

Publication year - 1997

Publication title -

osti oai (u.s. department of energy office of scientific and technical information)

Language(s) - English

Resource type - Reports

DOI - 10.2172/897396

Subject(s) - dehydrogenation , hydrogen , permeation , membrane , mass transfer , membrane reactor , chemical engineering , ceramic , data flow model , flow (mathematics) , materials science , composite number , chemistry , process engineering , catalysis , mechanics , chromatography , engineering , composite material , physics , organic chemistry , biochemistry

A mathematical model is developed to describe the permeation of hydrogen through thin-film palladium ceramic composite membrane in cocurrent flow configuration. Numerical simulation results show that the model under predicts reject composition and over predicts the product purity. These results suggest that the gas phase mass transfer resistance could be important. The difference between the predicted and actual hydrogen composition is less than 12%. Thus the model appears to be adequate for predicting the membrane module performance

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