Kinetic modeling of isobutane dehydrogenation over Ga2O3/Al2O3 catalyst
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DOI: 10.1016/j.cej.2019.122741
Abstract: Abstract Kinetic modeling was done for isobutane dehydrogenation using an alumina supported gallia catalyst in a fixed bed reactor at atmosphere pressure, 520–580 °C and a short residence time (ca. 0.06–0.3 s). A complex reaction network was… read more here.
Keywords: kinetic modeling; isobutane dehydrogenation; isobutane; modeling isobutane ... See more keywords