Catalyst composition for polymerizing alpha-olefins

Claim 2

In a process of preparing a supported catalyst composition used in alpha-olefin polymerization reactions comprising contacting a solid porous carrier with a transition metal compound and activating the thus-formed catalyst precursor with a co-catalyst, an improvement wherein the solid, porous carrier has such an average pore diameter that the resulting supported catalyst composition has an average pore diameter of at least about 170 Angstroms.

Claim 3

A process of claim 1 wherein the supported catalyst composition is prepared by: (a) contacting a solid, porous carrier with a magnesium compound; and (b) contacting the product of step (i) with a transition metal compound.

Claim 4

A process of claim 2 wherein the magnesium compound is a halide-containing magnesium compound or an organomagnesium compound.

Claim 5

A process of claim 3 wherein the supported catalyst composition is prepared by a process comprising the steps of: (i) contacting a solid, porous carrier having reactive OH groups with a liquid containing at least one organomagnesium composition having the empirical formula: R.sub.n MgR'.sub.(2-n) where R and R' are the same or different and they are C 1 -C 12 hydrocarbyl groups, provided that R' may also be a halogen, and n is 0, 1 or 2, the number of moles of said organomagnesium composition being in excess of the number of moles of said OH groups on said carrier; (ii) evaporating said liquid from step (i) to produce a supported magnesium composition in the form of a dry, free-flowing powder; and (iii) reacting said powder of step (ii) with at least one transition metal compound in a liquid medium, the number of moles of said transition metal compound being in excess of the number of the OH groups on said carrier prior to the reaction of the carrier with said organomagnesium composition in step (i), said transition metal compound being soluble in said liquid medium, and said supported magnesium composition being substantially insoluble in said liquid medium, whereby a reacted form of transition metal which is insoluble in said liquid medium becomes supported on said carrier.

Claim 6

A process of claim 4 wherein the supported catalyst composition has an average pore diameter of about 170 to about 220 Angstroms.

Claim 7

A process of claim 5 wherein the supported catalyst composition has an average pore diameter of about 175 to about 215 Angstroms.

Claim 8

A process of claim 6 wherein the supported catalyst composition has an average pore diameter of about 211 Angstroms.

Claim 9

A process of claim 7 wherein n is 1.

Claim 10

A process of claim 8 wherein step (i) comprises: (a) slurrying the carrier in a non-Lewis base liquid; and (b) adding to the slurring resulting from step (a) the organomagnesium composition in the form of an ether solution thereof.

Claim 11

A process of claim 9 wherein the ether is tetrahydrofuran.

Claim 12

A process of claim 10 wherein the porous, solid carrier is silica, alumina or combinations thereof.

Claim 13

A process of claim 11 wherein the porous, solid carrier is silica.

Claim 14

A process of claim 12 wherein the transition metal compound is a tetravalent titanium compound.

Claim 15

A process of claim 13 wherein the tetravalent titanium compound is TiCl 4 .

Claim 16

A process of claim 14 wherein, in step (i), the ratio of the number of moles of said organomagnesium composition to the number of moles of the OH groups on said silica is from about 1.1 to about 3.5.

Claim 17

A process a claim 15 wherein in step (i), the ratio of the number of moles of said organomagnesium composition to the number of moles of the OH groups on said silica is about 2.0 to about 3.5.

Claim 18

A process of claim 16 wherein said liquid medium is an alkane, cycloalkane, aromatics or halogenated aromatics.

Claim 19

A process of claim 17 wherein said liquid medium is hexane.

Claim 20

A process of claim wherein, prior to contacting the silica in step (i), it is heated at a temperature of about 750° C. for at least four hours.

Claim 21

A process of claim 19 wherein the organomagnesium composition is ethylmagnesium chloride.

Claim 22

In supported catalyst composition used in alpha-olefin polymerization reactions prepared by a process comprising contacting a solid porous carrier with a transition metal compound and activating the thus-formed catalyst precursor with a co-catalyst, an improvement wherein the solid, porous carrier has such an average pore diameter that the resulting supported catalyst composition has an average pore diameter of at least about 170 Angstroms.

Claim 23

In supported catalyst composition used in alpha-olefin polymerization reactions prepared by a process comprising contacting a solid porous carrier with a transition metal compound and activating the thus-formed catalyst precursor with a co-catalyst, an improvement wherein the solid, porous carrier has such an average pore diameter that the resulting supported catalyst composition has an average pore diameter of at least about 170 Angstroms.

Claim 24

A catalyst composition of claim 21 which is prepared by: (a) contacting a solid, porous carrier with a magnesium compound; and (b) contacting the product of step (i) with a transition metal compound.

Claim 25

A catalyst composition of claim 22 wherein the magnesium compound is a halide-containing magnesium compound or an organomagnesium compound.

Claim 26

A catalyst composition of claim 23 prepared by a process comprising the steps of: (i) contacting a solid, porous carrier having reactive OH groups with a liquid containing at least one organomagnesium composition having the empirical formula: R.sub.n MgR'.sub.(2-n) where R and R' are the same or different and they are C 1 -C 12 hydrocarbyl groups, provided that R' may also be a halogen, and n is 0, 1 or 2, the number of moles of said organomagnesium composition being in excess of the number of moles of said OH groups on said carrier; (ii) evaporating said liquid from step (i) to produce a supported magnesium composition in the form of a dry, free-flowing powder; (iii) reacting said powder of step (ii) with at least one transition metal compound in a liquid medium, the number of moles of said transition metal compound being in excess of the number of the OH groups on said carrier prior to the reaction of the carrier with said organomagnesium composition in step (i), said transition metal compound being soluble in said liquid medium, and said supported magnesium composition being substantially insoluble in said liquid medium, whereby a reacted form of transition metal which is insoluble in said liquid medium becomes supported on said carrier.

Claim 27

A catalyst composition of claim 24 wherein the supported catalyst composition has an average pore diameter of about 170 to about 220 Angstroms.

Claim 28

A catalyst composition of claim 25 wherein the supported catalyst composition has an average pore diameter of about 175 to about 215 Angstroms.

Claim 29

A catalyst composition of claim 26 wherein the supported catalyst composition has an average pore diameter of about 211 Angstroms.

Claim 30

A catalyst composition of claim 27 wherein n is 1.

Claim 31

A catalyst composition of claim 28, wherein said step (i) comprises: (a) slurrying the carrier in a non-Lewis base liquid; and (b) adding to the slurry resulting from step (a) the organomagnesium composition in the form of an ether solution thereof.

Claim 32

A catalyst composition of claim 29 wherein the ether is tetrahydrofuran.

Claim 33

A catalyst composition of claim 30 wherein the porous, solid carrier is silica, alumina or combinations thereof.

Claim 34

A catalyst composition of claim 31 wherein the porous, solid carrier is silica.

Claim 35

A catalyst composition of claim 32 wherein the transition metal compound is a tetravalent titanium compound.

Claim 36

A catalyst composition of claim 33 wherein the tetravalent titanium compound is TiCl 4 .

Claim 37

A catalyst composition of claim 34 wherein, in step (i), the ratio of the number of moles of said organomagnesium composition to the number of moles of the OH groups on said silica is from about 1.1 to about 3.5.

Claim 38

A catalyst composition of claim 35 wherein in step (i), the ratio of the number of moles of said organomagnesium composition to the number of moles of the OH groups on said silica is about 2.0 to about 3.5.

Claim 39

A catalyst composition of claim 36 wherein said liquid medium is alkane, cycloalkane, aromatics or halogenated aromatics.

Claim 40

A catalyst composition of claim 37 wherein said liquid medium is hexane.

Claim 41

A catalyst composition of claim 38 wherein, prior to contacting the silica in step (i), it is heated at a temperature of about 750° C. for at least four hours.

Claim 42

A catalyst composition of claim 39 wherein the organomagnesium composition is ethylmagnesium chloride.