Hydrocracking process using a catalyst selective for making middle distillates
AssigneeUnion Oil Company of California
InventorJohn W. Ward
Life of this patent
Estimating the term…
Loading patent…
AssigneeUnion Oil Company of California
InventorJohn W. Ward
Estimating the term…
A hydrocarbon conversion catalyst useful for converting hydrocarbon feeds to midbarrel products is prepared by extruding a mixture of an inorganic refractory oxide component and a crystalline aluminosilicate zeolite having cracking activity to form extrudates which are broken into particles normally ranging in length between 1/16 and 1/2 inch. The extruded particles are then calcined in the presence of steam at a water vapor partial pressure greater than about 2.0 p.s.i.a., preferably greater than about 5.0 p.s.i.a. The calcination step is carried out in the presence of sufficient steam for a sufficient amount of time at a sufficient temperature to convert the crystalline aluminosilicate zeolite in the extrudates into an ultrahydrophobic zeolite having a unit cell size between about 24.20 and about 24.45 Angstroms and a sorptive capacity for water vapor less than about 5 weight percent of the zeolite at 25.degree. C. and a p/p.degree. value of 0.10.
A hydrocracking process which comprises contacting a hydrocarbon feedstock with a hydrocracking catalyst under hydrocracking conditions in the presence of added hydrogen, wherein said catalyst contains a zeolite having a unit cell size between 24.20 and 24.40 angstroms and is prepared by the process comprising:
A hydrocracking process for producing middle distillate products which comprises contacting a hydrocarbon feedstock with a hydrocracking catalyst in the presence of added hydrogen under hydrocracking conditions, wherein said catalyst comprises a support containing a zeolite having a unit cell size between 24.20 and 24.35 angstroms and a dispersion of silica-alumina in an alumina matrix and said catalyst is prepared by the process comprising:
Dependencies are inferred from the claim text.