20 to 50 μmol / g and acidity of the OD 300 to 800 zeolite beta with an average crystal size of nanometers; USY zeolite (where wt% of the zeolite beta is less than the wt% of the zeolite USY); Support comprising an amorphous silica-aluminate, and a second support material; And a hydrocracking catalyst comprising a metal of at least one member selected from the group consisting of Group 6 of the periodic table and an element of group 8 to 10 is provided. A method of contacting the hydrocarbon feedstock with the hydrocracking catalyst under hydrocracking conditions for hydrocracking a hydrocarbon feedstock, comprising the step of producing a hydrogenated cracked effluent containing the middle distillate is provided. The method for producing the present hydrocracking catalysts are also provided.