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- W2471127935 abstract "In this work the kinetic model for the bio-ethanol steam reforming over a Cu-Ni-K/γ-Al 2O3 catalyst was developed, using a hybrid between experimental results obtained in a fixed bed microreactor 1 and an integration-optimization procedure. The whole mathematical model was implemented over professional software for validate the range of 2 to 9 mols of water/ethanol (rae) in the inlet flow (Fea) and a temperature of 300°C, and also captures the effect of the H2O/EtOH molar ratio and the feed flow by means of empiric equations, through the influence that this operational factors have in the kinetic parameters, assuming that the controlling step for the process is the mass transfer. The whole mathematical system is used in the optimization of a commercial reactor design by the UCLV and UBA." @default.
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- W2471127935 date "2006-01-01" @default.
- W2471127935 modified "2023-09-27" @default.
- W2471127935 title "KINETIC MODEL FOR THE ECOLOGICAL HYDROGEN PRODUCTION VIA ETHANOL STEAM REFORMING" @default.
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