Hydrocracking process

A process of hydrocracking at least one of 2,4-dimethylpentane and 2,2,3-trimethylbutane, comprising:

• contacting a hydrocracking feed stream comprising C5-C12 hydrocarbons in the presence of hydrogen with a hydrocracking catalyst under process conditions including a temperature of 425-580° C., a pressure of 300-5000 kPa gauge and a Weight Hourly Space Velocity of 0.1-30 to produce a hydrocracking product stream;
• wherein the hydrocracking feed stream comprises at least 0.5 wt % of 2,4-dimethylpentane and/or 2,2,3-trimethylbutane, based upon a total weight of the hydrocracking feed stream;
• wherein the hydrocracking catalyst comprises a hydrogenation metal in an amount of 0.01-0.30 wt % with respect to the total catalyst;
• and
• wherein the hydrocracking catalyst comprises a medium pore zeolite having a pore size of 5-6 Å and a silica to alumina molar ratio of 20-75 and a large pore zeolite having a pore size of 6-8 Å and a silica to alumina molar ratio of 10-80, wherein the hydrogenation metal is deposited on the medium pore zeolite and the large pore zeolite.