Catalytic conversion of methanol to light olefins

Claim 2

A process for producing a hydrocarbon mixture containing light olefins by contacting a methanol feed with a catalyst consisting essentially of a bound or unbound crystalline aluminosilicate zeolite having a Constraint Index of about 1 to 12 and a silica to alumina molar ratio of at least about 12, said catalyst not being modified by incorporation of essentially any material other than binder into or onto the zeolite, said contacting occurring in a reaction zone under methanol conversion reaction conditions, said process comprising: co-feeding to said reaction zone along with said methanol feed a diluent which provides in said reaction zone an O 2 -containing gas in an amount sufficient to increase the selectivity of the conversion reaction for production of C 2 to C 4 olefins, said amount of O 2 -containing gas being further sufficient to provide a molar ratio of molecular oxygen to methanol of from about 0.01:1 to 0.25:1.

Claim 3

A process according to claim 1 wherein said diluent is selected from molecular oxygen and molecular oxygen admixed with an inert gaseous material.

Claim 4

A process according to claim 2 wherein said zeolite is selected from ZSM-5, ZSM-11, ZSM-12, ZSM-23, ZSM-35, ZSM-38 and ZSM-48.

Claim 5

A process according to claim 3 wherein the weight hourly space velocity of the oxygen-providing diluent ranges from about 10 -6 to 10.

Claim 6

A process according to claim 4 wherein said gaseous diluent comprises air.

Claim 7

A process according to claim 5 wherein said methanol feed is admixed with water present in an amount of from about 1 mol to 10 mols of water per mole of methanol.

Claim 8

A process according to claim 1 wherein said catalyst further comprises a binder for said zeolite material.

Claim 9

A process for producing a hydrocarbon mixture containing light olefins by contacting a methanol feed with a catalyst consisting essentially of a bound or unbound ZSM-5 zeolite, said catalyst not being modified by incorporation of essentially any material other than binder into or onto the zeolite, said contacting occurring in a reaction zone under methanol conversion reaction conditions which include a temperature of from about 200° C. to 500° C., and a reaction zone pressure from about 5 psia to 500 psia, said process comprising: co-feeding to said reaction zone along with said methanol feed a diluent which provides in said reaction zone an O 2 -containing gas in an amount sufficient to increase the selectivity of the conversion reaction for production of C 2 to C 4 olefins, said amount of O 2 -containing gas being further sufficient to provide a molar ratio of molecular oxygen to methanol of from about 0.01:1 to 0.25:1.

Claim 10

A process for producing a hydrocarbon mixture containing light olefins by contacting a methanol feed with a catalyst consisting essentially of a bound or unbound ZSM-5 zeolite, said catalyst not being modified by incorporation of essentially any material other than binder into or onto the zeolite, said contacting occurring in a reaction zone under methanol conversion reaction conditions which include a temperature of from about 200° C. to 500° C., and a reaction zone pressure from about 5 psia to 500 psia, said process comprising: co-feeding to said reaction zone along with said methanol feed a diluent which provides in said reaction zone an O 2 -containing gas in an amount sufficient to increase the selectivity of the conversion reaction for production of C 2 to C 4 olefins, said amount of O 2 -containing gas being further sufficient to provide a molar ratio of molecular oxygen to methanol of from about 0.01:1 to 0.25:1.

Claim 11

A process according to claim 8 wherein said catalyst further comprises a binder for said zeolite material.

Claim 12

A process for producing a hydrocarbon mixture containing light olefins by contacting a methanol feed with a catalyst consisting essentially of an amorphous silica modified, bound or unbound crystalline aluminosilicate zeolite having a Constraint Index of about 1 to 12 and a silica to alumina molar ratio of at least about 12, said catalyst being modified by treatment with a silicone or silane to incorporate amorphous silica with said catalyst, said amorphous silica being essentially the only material other than binder incorporated into or onto said zeolite, said contacting occurring in a reaction zone under methanol conversion reaction conditions, said process comprising: co-feeding to said reaction zone along with said methanol feed a diluent which provides in said reaction zone an O 2 -containing gas in an amount sufficient to increase the selectivity of the conversion reaction for production of C 2 to C 4 olefins, said amount of O 2 -containing gas being further sufficient to provide a molar ratio of molecular oxygen to methanol of from about 0.01:1 to 0.25:1.

Claim 13

A process for producing a hydrocarbon mixture containing light olefins by contacting a methanol feed with a catalyst consisting essentially of an amorphous silica modified, bound or unbound crystalline aluminosilicate zeolite having a Constraint Index of about 1 to 12 and a silica to alumina molar ratio of at least about 12, said catalyst being modified by treatment with a silicone or silane to incorporate amorphous silica with said catalyst, said amorphous silica being essentially the only material other than binder incorporated into or onto said zeolite, said contacting occurring in a reaction zone under methanol conversion reaction conditions, said process comprising: co-feeding to said reaction zone along with said methanol feed a diluent which provides in said reaction zone an O 2 -containing gas in an amount sufficient to increase the selectivity of the conversion reaction for production of C 2 to C 4 olefins, said amount of O 2 -containing gas being further sufficient to provide a molar ratio of molecular oxygen to methanol of from about 0.01:1 to 0.25:1.

Claim 14

A process according to claim 10 wherein said catalyst further comprises a binder for said zeolite material.