Factorial design analysis of parameters for the sorption-enhanced steam reforming of ethanol in a circulating fluidized bed riser using CFD.

The catalyst-to-sorbent ratio (C), the solid flux (D), the riser diameter (A), the inlet temperature (B), and the gas velocity (E) were very highly significant, with P -values < 0.0001, in descending order.

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S1a, † all of the main effects showed a positive trend, except for the inlet temperature (B), according to their coefficients in the regression model.

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