The limiting process in steam methane reforming with gas diffusion into a porous catalytic wall in a flow reactor
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Type
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Journal
Article
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Author
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Motohiro
Saito
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Author
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Junichi
Kojima
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URL
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Volume
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40
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Issue
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29
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Pages
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8844-8855
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Publication
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International
Journal of Hydrogen Energy
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Date
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August
3, 2015
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Abstract
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Transport
phenomena for a reaction in a channel with a catalytic wall are important,
not only in the gas phase but also within the catalyst layer. The research
described here provides a direct method for obtaining the reaction rate of
steam methane reforming by taking into account the internal diffusion of the
porous catalyst on the channel wall. In an experiment with various
thicknesses of nickel-based catalyst, researchers observed the limiting modes
by means of the concentrations at the interface between the gas flow and the
catalyst layer.
According to interpretation of the experimental results using one-dimensional diffusion equation perpendicular to the flow direction, researchers observed a power-law-type reaction rate with an upper limit to be appropriate for explaining the region where the reaction was saturated. They offer a versatile criterion for the rate-limiting condition through an analytical discussion based on dimensionless numbers. |
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