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Wärmeübergang und Kinetik bei der Methan Reformierung mit H2_{2}O-CO2_{2} Gemischen in EVA I

Abstract

The synthesis of alcohols requires a special synthesis gas, which cannot be produced by steam reforming of natural gas, as it was done in EVA I before. The required low H2_{2}/C0 ratios down to 1 in the synthesis gas could be adjust by addition of CO2_{2} to the feed mixture of natural gas and steam. About half of the CO2_{2} is converted to CO by the shift reaction. The experimental heat transfer and kinetic data are in good agreement with correlations used for the reforming process without CO2_{2} addition

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