Catalysis over activated 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 catalyst comprising a zeolite composition prepared by a method which comprises the steps of (1) compositing a porous crystalline zeolite having an initial silica-to-alumina mole ratio greater than about 100 with alumina, (2) impregnating the composite under a vacuum with an aqueous solution of an alkali metal fluoride, (3) contacting the impregnated composite with a warm aqueous solution of an ammonium salt, and (4) calcining the ammonium salt solution contacted material at a temperature of from about 200° C. to about 600° C.

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 ammonium salt solution is ammonium nitrate.

Claim 5

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 6

The process of claim 4 wherein said zeolite has the structure of ZSM-5 or ZSM-11.

Claim 7

A process for converting a feedstock comprising an alcohol, ether or mixture thereof to conversion products comprising hydrocarbons which comprises contacting said feedstock at conversion conditions with a catalyst comprising a composition prepared by a method which comprises the steps of (1) compositing a porous crystalline zeolite having an initial silica-to-alumina mole ratio greater than about 100 with alumina so that the composite comprises from about 25 weight percent to about 75 weight percent zeolite, (2) extruding the composite to form an extrudate thereof, (3) impregnating the extrudate under a vacuum with an aqueous solution of an alkali metal fluoride, (4) contacting the impregnated extrudate with a warm aqueous solution of an ammonium salt, and (5) calcining the ammonium salt solution contacted material at a temperature of from about 200° C. to about 600° C.

Claim 8

A process for converting a feedstock comprising an alcohol, ether or mixture thereof to conversion products comprising hydrocarbons which comprises contacting said feedstock at conversion conditions with a catalyst comprising a composition prepared by a method which comprises the steps of (1) compositing a porous crystalline zeolite having an initial silica-to-alumina mole ratio greater than about 100 with alumina so that the composite comprises from about 25 weight percent to about 75 weight percent zeolite, (2) extruding the composite to form an extrudate thereof, (3) impregnating the extrudate under a vacuum with an aqueous solution of an alkali metal fluoride, (4) contacting the impregnated extrudate with a warm aqueous solution of an ammonium salt, and (5) calcining the ammonium salt solution contacted material at a temperature of from about 200° C. to about 600° C.

Claim 9

The process of claim 6 wherein said zeolite has an initial silica-to-alumina mole ratio greater than about 500.

Claim 10

The process of claim 6 wherein said ammonium salt solution is ammonium nitrate.

Claim 11

The process of claim 6 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 12

The process of claim 9 wherein said zeolite has the structure of ZSM-5 or ZSM-11.

Claim 13

The process of claim 1 wherein said alkali metal fluoride is selected from the group consisting of lithium fluoride, sodium fluoride, potassium fluoride, rubidium fluoride and cesium fluoride.

Claim 14

The process of claim 6 wherein said alkali metal fluoride is selected from the group consisting of lithium fluoride, sodium fluoride, potassium fluoride, rubidium fluoride and cesium fluoride.

Claim 15

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 16

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 17

The process of claim 6 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 about 0 to about 100.

Claim 18

The process of claim 6 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 19

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 comprising a zeolite composition prepared by a method which comprises the steps of (1) compositing a porous crystalline zeolite having an initial silica-to-alumina mole ratio greater than about 100 and the structure of ZSM-5 with alumina, (2) impregnating the composite under a vacuum with an aqueous solution of an alkali metal fluoride, (3) contacting the impregnated composite with a warm aqueous solution of an ammonium salt, and (4) calcining the ammonium salt solution contacted material at a temperature of from about 200° C. to about 600° C.

Claim 20

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 comprising a zeolite composition prepared by a method which comprises the steps of (1) compositing a porous crystalline zeolite having an initial silica-to-alumina mole ratio greater than about 100 and the structure of ZSM-5 with alumina, (2) impregnating the composite under a vacuum with an aqueous solution of an alkali metal fluoride, (3) contacting the impregnated composite with a warm aqueous solution of an ammonium salt, and (4) calcining the ammonium salt solution contacted material at a temperature of from about 200° C. to about 600° C.

Claim 21

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 comprising a composition prepared by a method which comprises the steps of (1) compositing a porous crystalline zeolite having an initial silica-to-alumina mole ratio greater than about 100 and the structure of ZSM-5 with alumina so that the composite comprises from about 25 weight percent to about 75 weight percent zeolite, (2) extruding the composite to form an extrudate thereof, (3) impregnating the extrudate under a vacuum with an aqueous solution of an alkali metal fluoride, (4) contacting the impregnated extrudate with a warm aqueous solution of an ammonium salt, and (5) calcining the ammonium salt solution contacted material at a temperature of from about 200° C. to about 600° C.

Claim 22

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 comprising a composition prepared by a method which comprises the steps of (1) compositing a porous crystalline zeolite having an initial silica-to-alumina mole ratio greater than about 100 and the structure of ZSM-5 with alumina so that the composite comprises from about 25 weight percent to about 75 weight percent zeolite, (2) extruding the composite to form an extrudate thereof, (3) impregnating the extrudate under a vacuum with an aqueous solution of an alkali metal fluoride, (4) contacting the impregnated extrudate with a warm aqueous solution of an ammonium salt, and (5) calcining the ammonium salt solution contacted material at a temperature of from about 200° C. to about 600° C.