Catalytic Cracking of Cyclohexane and 1-Hexene Mixtureson Mono-, Bi-, and Tri-Zeolite Catalysts
<sec> —The effects of temperature (540–640°C), weight hour space velocity (1.0–7.0 h<sup>–1</sup>), and steam : raw material ratios (0–2.5) on the yield of C<sub>2</sub>–C<sub>4</sub> olefins, conversion, and octane characteristics in the cracking of a mixture of model hydrocarbons (cyclohexane and 1-hexene) were studied. The influence of the structure of zeolites in mono-, bi-, and tri-zeolite catalysts on the distribution of cracking products was examined. It was found that the combination of catalyst components in bi- and tri-zeolite systems makes it possible to increase the efficiency of the consecutive cracking of hydrocarbons (C<sub>6</sub>–C<sub>12</sub> → C<sub>4</sub>–C<sub>8</sub> → C<sub>3</sub>–C<sub>6</sub> → C<sub>2</sub>–C<sub>4</sub>) according to the following reaction scheme: matrix → ZSM-5 → FER. The maximum total yield of C<sub>2</sub>–C<sub>4</sub> olefins (50.2 wt % at a conversion of 75.5%) was achieved with the use of a bi-zeolite catalyst of ZSM-5 + FER. </sec>