An acetone−butanol−ethanol (ABE) mixture, containing 62.9 wt % n-butanol, 29.3 wt % acetone, and 7.8 wt % ethanol, can be produced from biomass through the well-established ABE fermentation process using genetically modified Clostridium acetobutylicum. In this work, the catalytic dehydration reactions of the ABE mixture are studied to deoxygenate the mixture. A feed of the ABE mixture was preheated and pumped through a catalytic packed bed tubular reactor in a continuous process at pressures of 3−13 bar. Experiments were run at different operating temperatures and feed flow rates to observe the effect on the dehydration products, which are mixtures of three phases: (1) a gas phase consisting of light hydrocarbons and carbon dioxide, (2) an organic liquid phase consisting of heavy hydrocarbons, and (3) an aqueous phase with dissolved oxygenated hydrocarbons. The products were analyzed and compared to those from the dehydration of pure n-butanol, acetone, and ethanol feedstocks. The conversion is examined on two different catalysts: an alumina (γ-Al 2 O 3 ) and a zeolite (ZSM-5). The dehydration products from the ABE mixture are mostly unsaturated hydrocarbon chains in the range of C 2 −C 16 . On the basis of the higher heating values (HHV) of the liquid products and infrared spectra of the gas products, it can be concluded that the products from the ABE feedstock are different from those from the individual components, which suggests a cross reactivity of the components during the reaction. HHV of the liquid product increases with a decrease in the feed flow rate, and the γ-Al 2 O 3 catalyst is better than ZSM-5 for getting a good conversion of ABE in terms of liquid product energy content at a moderate reaction time.