Ziegler transition metal halide catalysts and method therefor

Claim 2

Ziegler transition metal halide catalyst composition comprising a plurality of agglomerated particles having a means particle diameter of from about 10 up to 1,000 microns, each agglomerated particle comprising a web of polytetrafluoroethylene submicroscopic fibers entangled with a plurality of Ziegler transition metal halide catalyst particles, said Ziegler transition metal halide catalyst having the formula: MX.sub.m.χM'R.sub.n X.sub.3-n.yR.sub.n M"X.sub.3-n where χ ranges between 0 to 3.0; m ranges between 2 to 3.5; n ranges between 0 to 3.0; and y ranges between 0 to 1; and R is an alkyl group having 1 to 8 carbons; M is a transition metal from Groups IIIB, IVB and VB of the Periodic Table; M' is an element from Groups IA, IIA and IIIA of the Periodic Table; M" is an element from Groups IA, IIA, IIB and IIIA of the Periodic Table; and X is a halogen from Group VIIA of the Periodic Table.

Claim 3

The composition of claim 1 wherein the mean particle diameter of said agglomerated catalyst composition is from 20 to 1,000 microns.

Claim 4

The composition of claim 1 wherein the mean particle diameter of said agglomerated catalyst composition is from 20 to 50 microns.

Claim 5

The composition of claim 1 wherein said Ziegler transition metal halide catalyst is a reduced TiCl m . χAlR n Cl 3-n .

Claim 6

The composition of claim 4 wherein the Ziegler transition metal halide catalyst is a reduced TiCl 3 .χAlCl 3 , where χ ranges between 0 to 1.5, and being produced from a grinding step.

Claim 7

The composition of claim 4 wherein the Ziegler transition metal halide catalyst is an aluminum alkyl reduced TiCl m .χAlR n Cl 3-n wherein m ranges between 2.0 and 3.5; χ ranges between 0.001 to 1.5; n ranges between 0.01 to 3.

Claim 8

A process for increasing the mean particle size of Ziegler transition metal halide catalysts having the formula: MX.sub.m.χM'R.sub.n X.sub.3-n.yR.sub.n M"X.sub.3-n where χ ranges between 0 to 3.0; m ranges between 2 to 3.5; n ranges between 0 to 3.0; and y ranges between 0 to 1; and R is an alkyl group having 1 to b 8 carbons; M is a transition metal from Groups IIIB, IVB and VB of the Periodic Table; M' is an element from Groups IA, IIA and IIIA of the Periodic Table; M" is an element from Groups IA, IIA, IIB and IIIA of the Periodic Table; and X is a halogen from Group VIIA of the Periodic Table; said process comprising working an effective amount of a polytetrafluoroethylene powder, capable of forming a submicroscopic web upon working at a temperature above that necessary to achieve fibrillation, with said catalyst composition for a period of time sufficient to form a plurality of individual web entrapped catalyst agglomerates.

Claim 9

A process for increasing the mean particle size of Ziegler transition metal halide catalysts having the formula: MX.sub.m.χM'R.sub.n X.sub.3-n.yR.sub.n M"X.sub.3-n where χ ranges between 0 to 3.0; m ranges between 2 to 3.5; n ranges between 0 to 3.0; and y ranges between 0 to 1; and R is an alkyl group having 1 to b 8 carbons; M is a transition metal from Groups IIIB, IVB and VB of the Periodic Table; M' is an element from Groups IA, IIA and IIIA of the Periodic Table; M" is an element from Groups IA, IIA, IIB and IIIA of the Periodic Table; and X is a halogen from Group VIIA of the Periodic Table; said process comprising working an effective amount of a polytetrafluoroethylene powder, capable of forming a submicroscopic web upon working at a temperature above that necessary to achieve fibrillation, with said catalyst composition for a period of time sufficient to form a plurality of individual web entrapped catalyst agglomerates.

Claim 10

The process of claim 7 wherein said fibrillatable polytetrafluoroethylene powder is used as a dry powder.

Claim 11

The process of claim 7 wherein said Ziegler transition metal halide catalyst is a reduced TiCl m . χAlR n Cl 3-n .

Claim 12

The process of claim 7 wherein said Ziegler transition metal halide catalyst is a reduced TiCl 3 . χAlCl 3 , where χ ranges between 0 to 1.5, and being produced from a grinding step.

Claim 13

The process of claim 7 wherein the Ziegler transition metal halide catalyst is an aluminum alkyl reduced TiCl m .χAlR n Cl 3-n wherein m ranges between 2.0 to 3.5; χ ranges between 0.001 to 1.5; n ranges between 0.01 to 3.

Claim 14

The process of claim 7 wherein the grinding is performed for about 1 hour.

Claim 15

A catalyst system for the polymerization of alpha-olefin, said catalyst system comprising an organoaluminum catalyst component and a transition metal halide catalyst component having the formula: MX.sub.m.χM'R.sub.n X.sub.3-n.yR.sub.n M"X.sub.3-n where χ ranges between 0 to 3.0; m ranges between 2 to 3.5; n ranges between 0 to 3.0; and y ranges between 0 to 1; and R is an alkyl group having 1 to 8 carbons; M is a transition metal from Groups IIIB, IVB and VB of the Periodic Table; M' is an element from Groups IA, IIA and IIIA of the Periodic Table; M" is an element from Groups IA, IIA, IIB and IIIA of the Periodic Table; and X is a halogen from Group VIIA of the Periodic Table; said transition metal halide catalyst component comprising a plurality of individual polytetrafluoroethylene web entrapped catalyst agglomerates.

Claim 16

A catalyst system for the polymerization of alpha-olefin, said catalyst system comprising an organoaluminum catalyst component and a transition metal halide catalyst component having the formula: MX.sub.m.χM'R.sub.n X.sub.3-n.yR.sub.n M"X.sub.3-n where χ ranges between 0 to 3.0; m ranges between 2 to 3.5; n ranges between 0 to 3.0; and y ranges between 0 to 1; and R is an alkyl group having 1 to 8 carbons; M is a transition metal from Groups IIIB, IVB and VB of the Periodic Table; M' is an element from Groups IA, IIA and IIIA of the Periodic Table; M" is an element from Groups IA, IIA, IIB and IIIA of the Periodic Table; and X is a halogen from Group VIIA of the Periodic Table; said transition metal halide catalyst component comprising a plurality of individual polytetrafluoroethylene web entrapped catalyst agglomerates.

Claim 17

The catalyst system of claim 13 wherein the mean particle diameter of said web entrapped catalyst agglomerates is from about 20 to 1,000 microns.

Claim 18

The catalyst system of claim 13 wherein the mean particle diameter of said web entrapped catalyst agglomerates is from about 20 to about 50 microns.

Claim 19

The catalyst system of claim 13 wherein said Ziegler transition metal halide catalyst is a reduced TiCl m .χAlR n CL 3-n .

Claim 20

The catalyst system of claim 13 wherein said Ziegler transition metal halide catalyst is a reduced TiCl 3 .χAlCl 3 , where χ ranges between 0 to 1.5, and being produced from a grinding step.

Claim 21

The catalyst system of claim 13 wherein said Ziegler transition metal halide catalyst is an aluminum alkyl reduced TiCl m .χAlR n Cl 3-n wherein m ranges between 2.0 to 3.5; χ ranges between 0.001 to 1.5; n ranges between 0.01 to 3.