Hydrocarbon treating catalyst

Claim 2

A catalyst comprising: (a) particles of a crystalline aluminosilicate zeolite; (b) particles of a substantially catalytically inert inorganic oxide having a size of less than about 10 microns in diameter, and (c) a catalytic inorganic oxide matrix, said inert inorganic oxide having initially a surface area greater than 200 square meters per gram and having at least 0.2 cubic centimeter of its pore volume in pores having diameters ranging from about 90 to about 200 Angstroms.

Claim 3

The catalyst of claim 1 wherein at least about 50 percent of said particles of a substantially inert inorganic oxide have a size of less than about 5 microns in diameter.

Claim 4

The catalyst of claim 1 wherein at least about 50 percent of said particles of substantially catalytically inert inorganic oxide have a size of less than about 2 microns in diameter.

Claim 5

The catalyst of claim 1 wherein said particles of zeolite have a size ranging from about 0.1 to about 10 microns.

Claim 6

The catalyst of claim 1 wherein said zeolite comprises from about 0.1 to about 40 weight percent, said substantially catalytically inert inorganic oxide comprises from about 5 to about 40 weight percent, and said catalytic inorganic oxide matrix comprises from about 40 to about 90 weight percent, all said weights being based on the total catalyst.

Claim 7

The catalyst of claim 1 wherein said zeolite comprises from about 5 to about 20 weight percent, said substantially catalytically inert inorganic oxide comprises from about 10 to about 30 weight percent and said catalytic inorganic oxide matrix comprises from about 50 to about 80 weight percent, all said weights being based on the total catalyst.

Claim 8

The catalyst of claim 1 wherein said substantially inert inorganic oxide is selected from the group consisting of alumina, silica, titania, zirconia, magnesia and mixtures thereof.

Claim 9

The catalyst of claim 1 wherein said substantially catalytically inert inorganic oxide comprises a porous alumina.

Claim 10

The catalyst of claim 1 wherein said matrix comprises silica-alumina.

Claim 11

The catalyst of claim 1 wherein said zeolite has a uniform pore diameter ranging from about 6 to about 15 Angstroms and wherein the silica to alumina ratio of said zeolite is greater than 3.

Claim 12

A process for the preparation of a catalyst, which comprises: (a) blending an inorganic oxide hydrogel with particles of a crystalline, aluminosilicate zeolite and particles of a substantially catalytically inert inorganic oxide, said particles of inert inorganic oxide having a size of less than about 10 microns in diameter and having a surface area greater than 200 square meters per gram and having at least 0.2 cubic centimeter per gram of its pore volume in pores having diameters ranging from about 90 to about 200 Angstroms; (b) recovering the solids from said blend; (c) washing with a liquid medium the solids of step (b) substantially free of extraneous metal salts; (d) separating the washed solids from said liquid medium; (e) drying the separated solids resulting from step (d) to a moisture content ranging from about 8 to about 15 weight percent, and (f) recovering a catalyst comprising particles of said zeolite and particles of said inert inorganic oxide dispersed as discrete particles in an inorganic oxide matrix.

Claim 13

A process for the preparation of a catalyst, which comprises: (a) blending an inorganic oxide hydrogel with particles of a crystalline, aluminosilicate zeolite and particles of a substantially catalytically inert inorganic oxide, said particles of inert inorganic oxide having a size of less than about 10 microns in diameter and having a surface area greater than 200 square meters per gram and having at least 0.2 cubic centimeter per gram of its pore volume in pores having diameters ranging from about 90 to about 200 Angstroms; (b) recovering the solids from said blend; (c) washing with a liquid medium the solids of step (b) substantially free of extraneous metal salts; (d) separating the washed solids from said liquid medium; (e) drying the separated solids resulting from step (d) to a moisture content ranging from about 8 to about 15 weight percent, and (f) recovering a catalyst comprising particles of said zeolite and particles of said inert inorganic oxide dispersed as discrete particles in an inorganic oxide matrix.

Claim 14

In the process of claim 11, the additional step of steam-treating said catalyst for a time sufficient to produce a catalyst having at least about 0.4 cubic centimeters of its pore volume in pores having diameters greater than 90 Angstroms.

Claim 15

The process of claim 11 wherein said substantially catalytically inert inorganic oxide comprises alumina and wherein said inorganic oxide matrix comprises amorphous silica-alumina.

Claim 16

The process of claim 11 wherein at least about 50 percent of said inert inorganic oxide particles have a size of less than about 5 microns in diameter.

Claim 17

The process of claim 11 wherein said zeolite particles have a size ranging from about 0.1 to about 10 microns in diameter.

Claim 18

The catalyst of claim 1 wherein said catalyst has at least 0.4 cubic centimeter per gram of its pore volume in pores of greater than 90 Angstroms in diameter.