Catalysis over activated high silica zeolites

Claim 2

A process for converting a feedstock comprising an alcohol, ether or mixture thereof to conversion product comprising hydrocarbons which comprises contacting said feedstock at conversion conditions with a catalystt 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 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 organic compound mole ratio of from 0 to about 100.

Claim 11

The process of claim 1 wherein said conversion conditions include a temperature of from about 275° C. to about 600° C., a pressure of from about 0.5 atmosphere to about 50 atmospheres and a liquid hourly space velocity of from about 0.5 to about 100.

Claim 12

A process for converting a feedstock comprising an alcohol, ether or mixture thereof to conversion product comprising hydrocarbons 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

A process for converting a feedstock comprising an alcohol, ether or mixture thereof to conversion product comprising hydrocarbons 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 14

The process of claim 11 wherein said zeolite has an initial silica-to-alumina mole ratio greater than about 500.

Claim 15

The process of claim 11 wherein said conversion to the hydrogen form comprises contact of said material with a hydrogen ion precursor solution followed by calcination.

Claim 16

The process of claim 13 wherein said hydrogen ion precursor solution is an ammonium salt solution.

Claim 17

The process of claim 11 wherein said volatile boron fluoride contacting is conducted at a temperature of from about ambient to about 50° C.

Claim 18

The process of claim 11 wherein said supported zeolite is in the form of an extrudate.

Claim 19

The process of claim 11 wherein said conversion conditions include 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 organic compound mole ratio of from 0 to about 100.

Claim 20

The process of claim 11 wherein said conversion conditions include a temperature of from about 275° C. to about 600° C., a pressure of from about 0.5 atmosphere to about 50 atmospheres and a liquid hourly space velocity of from about 0.5 to about 100.