Hydrocracking with a middle distillate catalyst

Details Hydrocracking with a middle distillate catalyst Hydrocracking with a middle distillate catalyst

B - Operations, Transporting

01

J

B01J 29/08 (2006.01) B01J 29/16 (2006.01) C10G 47/16 (2006.01)

Patent

CA 2140647

The selectivity of a midbarrel hydrocracking process for middle distillates is significantly increased by using a catalyst con- taining an amorphous silica-magnesia component in combination with a Y zeolite having a unit cell size below 24.45 angstroms and/or a water vapor sorptive capacity less than 10 weight percent at 25°C and a p/po value of 0.1. LZ-10 zeolite is a preferred zeolite for use in the catalyst.

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