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 feedstock hydrocarbon compounds which comprises contacting said feedstock at conversion conditions, including a temperature of from about 100° C. to about 800° C., a pressure of from about 0.1 atmospheres to about 200 atmospheres, a weight hourly space velocity of from about 0.08 hr -1 to about 2000 hr -1 and a hydrogen/feedstock hydrocarbon compound mole ratio of from 0 to about 100, with a catalyst composition comprising a crystalline zeolite having an initial silica:alumina mole ratio greater than about 100:1 prepared by a method which comprises calcining the 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 zeolite with from about 0.1 to about 1 gram of solid aluminum fluoride per gram of zeolite at a temperature of from about 0° C. to about 65° C., and converting said aluminum fluoride contacted zeolite to hydrogen form.

Claim 3

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

Claim 4

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

Claim 5

The process of claim 3 which comprises an additional step of steaming said zeolite subsequent to said contact with a hydrogen ion precursor solution and prior to said calcination.

Claim 6

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

Claim 7

The process of claim 5 wherein said ammonium salt solution is ammonium nitrate.

Claim 8

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 9

The process of claim 7 wherein said zeolite has the structure of ZSM-5 or ZSM-11.

Claim 10

The process of claim 8 which comprises an additional step of hydrolyzing said zeolite subsequent to said aluminum fluoride contacting step.

Claim 11

The process of claim 1 which comprises an additional step of hydrolyzing said zeolite subsequent to said aluminum fluoride contacting step.

Claim 12

The process of claim 1 wherein said aluminum fluoride is provided as a precipitate in solution with said zeolite from the reaction of an aluminum salt and a source of fluoride ions.

Claim 13

The process of claim 1 wherein said catalyst composition is in the form of an extrudate.

Claim 14

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 15

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, including a temperature of from about 100° C. to about 800° C., a pressure of from about 0.1 atmosphere to about 200 atmospheres, a weight hourly space velocity of from about 0.08 hr -1 to about 2000 hr -1 and a hydrogen/feedstock hydrocarbon compound mole ratio of from 0 to about 100, with a catalyst composition comprising a crystalline zeolite having an initial silica:alumina mole ratio greater than about 100:1 and the structure of zeolite ZSM-5 prepared by a method which comprises calcining the 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 zeolite with from about 0.1 to about 1 gram of solid aluminum fluoride per gram of zeolite at a temperature of from about 0° C. to about 650° C., and converting said aluminum fluoride contacted zeolite to hydrogen form.

Claim 16

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, including a temperature of from about 100° C. to about 800° C., a pressure of from about 0.1 atmosphere to about 200 atmospheres, a weight hourly space velocity of from about 0.08 hr -1 to about 2000 hr -1 and a hydrogen/feedstock hydrocarbon compound mole ratio of from 0 to about 100, with a catalyst composition comprising a crystalline zeolite having an initial silica:alumina mole ratio greater than about 100:1 and the structure of zeolite ZSM-5 prepared by a method which comprises calcining the 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 zeolite with from about 0.1 to about 1 gram of solid aluminum fluoride per gram of zeolite at a temperature of from about 0° C. to about 650° C., and converting said aluminum fluoride contacted zeolite to hydrogen form.

Claim 17

The process of claim 14 wherein said zeolite has an initial silica:alumina mole ratio greater than about 500:1.

Claim 18

The process of claim 14 wherein said conversion of said aluminum fluoride contacted zeolite to the hydrogen form comprises contact of said zeolite with a hydrogen ion precursor solution followed by calcination.

Claim 19

The process of claim 16 which comprises an additional step of hydrolyzing said zeolite subsequent to said aluminum fluoride contacting step.

Claim 20

The process of claim 16 which comprises an additional step of steaming said zeolite subsequent to said contact with a hydrogen ion precursor solution and prior to said calcination.

Claim 21

The process of claim 16 wherein said hydrogen ion precursor solution is an ammonium salt solution.

Claim 22

The process of claim 14 wherein said zeolite is in the form of an extrudate.

Claim 23

The process of claim 14 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 24

The process of claim 14 which comprises an additional step of hydrolyzing said zeolite subsequent to said aluminum fluoride contacting step.