Zeolite treating process

Claim 2

The process of treating a charge dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 selected from the group consisting of (i) an ammonium form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, (ii) a hydrogen form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, and (iii) a metal exchanged dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 and a Lattice Constant of about 24.30 A-24.50 A which charge is characterized by the presence of Secondary Pores of diameter of about 100 A-600 A which comprises contacting said charge zeolite with acidic medium at 75° F.-140° F. for 0.5-6 hours thereby converting said charge zeolite into an acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, and (v) a Surface Silicon to Aluminum Atom Ratio of about 24-45; and recovering said acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, and (v) a Surface Silicon to Aluminum Atom Ratio of about 24-45.

Claim 3

The process of treating a charge dealuminated Y-zeolite as claimed in claim 1 wherein said charge zeolite is an ammonium form dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120.

Claim 4

The process of treating a charge dealuminated Y-zeolite as claimed in claim 1 wherein said charge zeolite is a hydrogen form dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120.

Claim 5

The process of treating a charge dealuminated Y-zeolite as claimed in claim 1 wherein said charge zeolite is a metal exchanged dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120.

Claim 6

The process of treating a charge dealuminated Y-zeolite as claimed in claim 1 wherein said contacting with acidic medium is carried out at ambient temperature.

Claim 7

The process of treating a charge dealuminated Y-zeolite as claimed in claim 1 wherein said acidic medium is an aqueous solution of an organic acid.

Claim 8

The process of treating a charge dealuminated Y-zeolite as claimed in claim 1 wherein said acidic medium is an aqueous solution of an inorganic acid.

Claim 9

The process of treating a charge dealuminated Y-zeolite as claimed in claim 1 wherein said acidic medium is an aqueous solution of nitric acid, carried out for about 2-6 hours.

Claim 10

The process of treating a charge dealuminated Y-zeolite in hydrogen form having a silica to alumina mole ratio of about 10-120 and a lattice constant of about 24.30 A-24.50 A which comprises contacting said charge zeolite with an acidic medium at 75° F.-140° F. for 0.5-6 hours thereby converting said charge zeolite into an acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 100 A-325 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, and (v) a Surface Silicon to Aluminum Atom Ratio of about 24-45; and recovering said acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, and a Surface Silicon to Aluminum Atom Ratio of about 24-45.

Claim 11

The process of treating a charge dealuminated Y-zeolite in hydrogen form having a silica to alumina mole ratio of about 10-120 and a lattice constant of about 24.30 A-24.50 A which comprises contacting said charge zeolite with an acidic medium at 75° F.-140° F. for 0.5-6 hours thereby converting said charge zeolite into an acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 100 A-325 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, and (v) a Surface Silicon to Aluminum Atom Ratio of about 24-45; and recovering said acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, and a Surface Silicon to Aluminum Atom Ratio of about 24-45.

Claim 12

A novel acidified dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 selected from the group consisting of (i) an ammonium form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, (ii) a hydrogen form of having a silica to alumina mole ratio of about 10-120, and (iii) a metal exchanged dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, (v) a surface Silicon to Aluminum Atom Ratio of about 24-45, and (vi) an Acid Site Density of about 1-5 cc NH 3 /g cat.

Claim 13

A novel acidified dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 selected from the group consisting of (i) an ammonium form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, (ii) a hydrogen form of having a silica to alumina mole ratio of about 10-120, and (iii) a metal exchanged dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, (v) a surface Silicon to Aluminum Atom Ratio of about 24-45, and (vi) an Acid Site Density of about 1-5 cc NH 3 /g cat.

Claim 14

A novel catalyst comprising an acidified dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 selected from the group consisting of (i) an ammonium form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, (ii) a hydrogen form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, and (iii) a metal exchanged dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A--24 33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, (v) a surface Silicon to Aluminum Atom Ratio of about 20-50, and (vi) an Acid Site Density of about 1-5 cc NH 3 /g cat; (i) a binder; and (ii) a catalytic metal.

Claim 15

A novel catalyst comprising an acidified dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 selected from the group consisting of (i) an ammonium form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, (ii) a hydrogen form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, and (iii) a metal exchanged dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A--24 33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, (v) a surface Silicon to Aluminum Atom Ratio of about 20-50, and (vi) an Acid Site Density of about 1-5 cc NH 3 /g cat; (i) a binder; and (ii) a catalytic metal.

Claim 16

A novel catalyst comprising (i) an acidified zeolite prepared from a charge zeolite selected from the group consisting of (i) an ammonium form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, (ii) a hydrogen form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, and (iii) a metal exchanged dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 and a Lattice Constant of about 24.30 A-24.50 A which acidified zeolite charge is characterized by the presence of Secondary Pores of diameter of about 100 A-600 A which has been prepared by the process which comprises contacting said charge zeolite with acidic medium at 75° F.-140° F. for 0.5-6 hours thereby converting said charge zeolite into an acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.114-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, and (v) a Surface Silicon to Aluminum Atom Ratio of about 24-45; and recovering said acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, and (v) a Surface Silicon to Aluminum Atom Ratio of about 24-45 ii; a binder; (iii) at least one Group VIB metal; and (iv) at least one non-noble Group VIII metal.

Claim 17

A novel catalyst comprising (i) an acidified zeolite prepared from a charge zeolite selected from the group consisting of (i) an ammonium form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, (ii) a hydrogen form of dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120, and (iii) a metal exchanged dealuminated Y-zeolite having a silica to alumina mole ratio of about 10-120 and a Lattice Constant of about 24.30 A-24.50 A which acidified zeolite charge is characterized by the presence of Secondary Pores of diameter of about 100 A-600 A which has been prepared by the process which comprises contacting said charge zeolite with acidic medium at 75° F.-140° F. for 0.5-6 hours thereby converting said charge zeolite into an acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.114-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, (iv) a Secondary Pore Diameter of about 100 A-600 A, and (v) a Surface Silicon to Aluminum Atom Ratio of about 24-45; and recovering said acidified zeolite characterized by (i) an increased Secondary Pore Volume of about 0.14-0.20 cc/g, (ii) a decreased Lattice Constant of about 24.23 A-24.33 A, (iii) a Secondary Pore Mode of about 115 A-145 A, and (v) a Surface Silicon to Aluminum Atom Ratio of about 24-45 ii; a binder; (iii) at least one Group VIB metal; and (iv) at least one non-noble Group VIII metal.