As a result of investigating low temperature isomerization of n -hexane at 130, 140, 150, 160°C in a flow reactor with a fixed bed of catalyst of the Al 2 O 3 /ZrO 2 /SO 4 /Pt type a ratio of components in the catalyst system was selected and process conditions were defined, which allow to obtain highly branched high-octane isomers with a yield of up to 40% relative to a transformed raw material. A kinetic model of the process was proposed and kinetic parameters were calculated.
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Chuparev et al. (2014) studied this question.
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