Experimental and simulation studies of the production of renewable hydrogen through ethanol steam reforming in a large-scale catalytic membrane reactor
Ethanol steam reforming was studied in a catalytic membrane reactor (CMR).
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A CFD simulation model showed 91% accuracy compared to experimental data.
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An experimental hydrogen production rate of 0.38 g per hour was obtained.
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The effect of operating conditions on the reactor performance was determined.
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Hydrogen production in the CMR was enhanced by 122% over fixed bed production.
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