Catalysis over activated high silica zeolites

Claim 2

A process for converting a feedstock comprising hydrocarbon compounds to conversion products comprising hydrocarbon compounds of lower molecular weight than feed stock hydrocarbon compounds which comprises contacting said feedstock at conversion conditions with a catalyst composition comprising a supported crystalline zeolite having an initial silica-to-alumina mole ratio greater than about 100 prepared by a method which comprises compositing said crystalline zeolite with a support matrix material of alumina, gallia or a combination thereof, calcining the resulting supported zeolite at a temperature of from about 200° C. to about 600° C. for a period of time ranging from about 1 minute to about 48 hours, contacting said calcined supported zeolite with volatile boron fluoride in a dry environment at a temperature of from about 0° C. to about 100° C. until said supported zeolite is saturated with said boron fluoride, purging unreacted boron fluoride from said boron fluoride contacted supported zeolite, hydrolyzing said boron fluoride contacted supported zeolite, and converting said hydrolyzed material to hydrogen form.

Claim 3

The process of claim 1 wherein said zeolite has an initial silica-to-alumina mole ratio greater than about 500.

Claim 4

The process of claim 1 wherein said conversion to the hydrogen form comprises contact of said material with a hydrogen ion precursor solution followed by calcination.

Claim 5

The process of claim 3 wherein said hydrogen ion precursor solution is an ammonium salt solution.

Claim 6

The process of claim 1 wherein said zeolite has the structure of ZSM-5, ZSM-11, ZSM-5/ZSM-11 intermediate, ZSM-12, ZSM-23, ZSM-35, ZSM-38 or ZSM-48.

Claim 7

The process of claim 5 wherein said zeolite has the structure of ZSM-5 or ZSM-11.

Claim 8

The process of claim 1 wherein said volatile boron fluoride contacting is conducted at a temperature of from about ambient to about 50° C.

Claim 9

The process of claim 1 wherein said supported zeolite is in the form of an extrudate.

Claim 10

The process of claim 1 wherein said conversion conditions include a temperature of from about 300° C. to about 800° C., a pressure of from about 0.1 atmosphere to about 35 atmospheres and a weight hourly space velocity of from about 0.1 hr -1 to about 20 hr -1 .

Claim 11

A process for converting a feedstock comprising hydrocarbon compounds to conversion products comprising hydrocarbon compounds of lower molecular weight than feedstock hydrocarbon compounds which comprises contacting said feedstock at conversion conditions with a catalyst composition comprising a supported crystalline zeolite having an initial silica-to-alumina mole ratio greater than 100 and the structure of zeolite ZSM-5 prepared by a method which comprises compositing said crystalline zeolite with a support matrix material of alumina, gallia or a combination thereof, calcining the resulting supported zeolite at a temperature of from about 200° C. to about 600° C. for a period of time ranging from about 1 minute to about 48 hours, contacting said calcined supported zeolite with volatile boron fluoride in a dry environment at a temperature of from about 0° C. to about 100° C. until said supported zeolite is saturated with said boron fluoride, purging unreacted boron fluoride from said boron fluoride contacted supported zeolite, hydrolyzing said boron fluoride contacted supported zeolite, and converting said hydrolyzed material to hydrogen form.

Claim 12

A process for converting a feedstock comprising hydrocarbon compounds to conversion products comprising hydrocarbon compounds of lower molecular weight than feedstock hydrocarbon compounds which comprises contacting said feedstock at conversion conditions with a catalyst composition comprising a supported crystalline zeolite having an initial silica-to-alumina mole ratio greater than 100 and the structure of zeolite ZSM-5 prepared by a method which comprises compositing said crystalline zeolite with a support matrix material of alumina, gallia or a combination thereof, calcining the resulting supported zeolite at a temperature of from about 200° C. to about 600° C. for a period of time ranging from about 1 minute to about 48 hours, contacting said calcined supported zeolite with volatile boron fluoride in a dry environment at a temperature of from about 0° C. to about 100° C. until said supported zeolite is saturated with said boron fluoride, purging unreacted boron fluoride from said boron fluoride contacted supported zeolite, hydrolyzing said boron fluoride contacted supported zeolite, and converting said hydrolyzed material to hydrogen form.

Claim 13

The process of claim 10 wherein said zeolite has an initial silica-to-alumina mole ratio greater than about 500.

Claim 14

The process of claim 10 wherein said conversion to the hydrogen form comprises contact of said material with a hydrogen ion precursor solution followed by calcination.

Claim 15

The process of claim 12 wherein said hydrogen ion precursor solution is an ammonium salt solution.

Claim 16

The process of claim 10 wherein said volatile boron fluoride contacting is conducted at a temperature of from about ambient to about 50° C.

Claim 17

The process of claim 10 wherein said supported zeolite is in the form of an extrudate.

Claim 18

The process of claim 10 wherein said conversion conditions include a temperature of from about 300° C. to about 800° C., a pressure of from about 0.1 atmosphere to about 35 atmospheres and a weight hourly space velocity of from about 0.1 hr -1 to about 20 hr -1 .