High-activity polyethylene catalysts

Claim 2

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a slurry of a solid, porous carrier having reactive OH groups in a non-polar liquid with dibutylmagnesium to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with tetrabutoxysilane to form an intermediate of step (ii) (iii) contacting said intermediate of step (ii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said dibutylmagnesium in step (i), said transition metal compound being soluble in said non-polar liquid and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (iv) contacting said transition metal-containing intermediate with an additional quantity of dibutylmagnesium to prepare a catalyst precursor of step (iv); (v) contacting said catalyst precursor of step (iv) with an activating amount of dimethylaluminum chloride, to produce said catalyst.

Claim 3

A catalyst composition for copolymerization of ethylene with an alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a solid, porous carrier having reactive OH groups with a liquid, said liquid containing at least one organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with tetrabutoxysilane to form an intermediate of step (ii) (iii) contacting said intermediate of step (ii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said organomagnesium compound in step (i), said transition metal compound being soluble in said non-polar liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (iv) contacting said transition metal-containing intermediate with an additional quantity of an organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to prepare a catalyst precursor of step (iv); (v) contacting said catalyst precursor of step (iv) with an activating amount of dimethylaluminum chloride.

Claim 4

A catalyst composition for copolymerization of ethylene with an alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a solid, porous carrier having reactive OH groups with a liquid, said liquid containing at least one organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with tetrabutoxysilane to form an intermediate of step (ii) (iii) contacting said intermediate of step (ii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said organomagnesium compound in step (i), said transition metal compound being soluble in said non-polar liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (iv) contacting said transition metal-containing intermediate with an additional quantity of an organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to prepare a catalyst precursor of step (iv); (v) contacting said catalyst precursor of step (iv) with an activating amount of dimethylaluminum chloride.

Claim 5

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps (i) contacting a slurry of a solid, porous carrier having reactive OH groups in a non-polar liquid with dibutylmagnesium to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with at least one compound of the formula (R.sup.1 O).sub.x SiR.sup.2.sub.y wherein x is 1, 2, 3, or 4 and y=4-x; R 1 is a hydrocarbyl group of 1 to 10 carbon atoms; and R 2 is halogen or a hydrocarbyl group of 1 to 10 carbon atoms, or hydrogen to form an intermediate of step (ii) (iii) contacting said intermediate of step (ii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said dibutylmagnesium in step (i), said transition metal compound being soluble in said non-polar liquid and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (iv) contacting said transition metal-containing intermediate with an additional quantity of dibutylmagnesium to prepare a catalyst precursor of step (iv); (v) contacting said catalyst precursor of step (iv) with an activating amount of dimethylaluminum chloride.

Claim 6

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps (i) contacting a slurry of a solid, porous carrier having reactive OH groups in a non-polar liquid with dibutylmagnesium to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with at least one compound of the formula (R.sup.1 O).sub.x SiR.sup.2.sub.y wherein x is 1, 2, 3, or 4 and y=4-x; R 1 is a hydrocarbyl group of 1 to 10 carbon atoms; and R 2 is halogen or a hydrocarbyl group of 1 to 10 carbon atoms, or hydrogen to form an intermediate of step (ii) (iii) contacting said intermediate of step (ii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said dibutylmagnesium in step (i), said transition metal compound being soluble in said non-polar liquid and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (iv) contacting said transition metal-containing intermediate with an additional quantity of dibutylmagnesium to prepare a catalyst precursor of step (iv); (v) contacting said catalyst precursor of step (iv) with an activating amount of dimethylaluminum chloride.

Claim 7

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a slurry of a solid, porous carrier having reactive OH groups in a non-polar liquid with dibutylmagnesium to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with silicon tetrahalide to form an intermediate of step (ii) (iii) contacting said product of step (ii) with tetrabutoxysilane to form an intermediate of step (iii) (iv) contacting said intermediate of step (iii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said dibutylmagnesium in step (i), said transition metal compound being soluble in said non-polar liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (v) contacting said transition metal-containing intermediate with an additional quantity of dibutylmagnesium to prepare a catalyst precursor of step (v); (vi) contacting said catalyst precursor of step (v) with an activating amount of dimethylaluminum chloride.

Claim 8

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a slurry of a solid, porous carrier having reactive OH groups in a non-polar liquid with dibutylmagnesium to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with silicon tetrahalide to form an intermediate of step (ii) (iii) contacting said product of step (ii) with tetrabutoxysilane to form an intermediate of step (iii) (iv) contacting said intermediate of step (iii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said dibutylmagnesium in step (i), said transition metal compound being soluble in said non-polar liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (v) contacting said transition metal-containing intermediate with an additional quantity of dibutylmagnesium to prepare a catalyst precursor of step (v); (vi) contacting said catalyst precursor of step (v) with an activating amount of dimethylaluminum chloride.

Claim 9

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a slurry of a solid, porous carrier having reactive OH groups in a non-polar liquid with dibutylmagnesium to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with silicon tetrahalide to form an intermediate of step (ii) (iii) contacting said product of step (ii) with at least one compound of the formula (R.sup.1 O).sub.x SiR.sup.2.sub.y wherein x is 1, 2, 3, or 4 and y=4-x; R 1 is a hydrocarbyl group of 1 to 10 carbon atoms; and R 2 is halogen or a hydrocarbyl group of 1 to 10 carbon atoms, or hydrogen to form an intermediate of step (iii) (iv) contacting said intermediate of step (iii) 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 OH groups on said carrier prior to reaction with said dibutylmagnesium in step (i), said transition metal compound being soluble in said liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (v) contacting said transition metal-containing intermediate with an additional quantity of dibutylmagnesium to prepare a catalyst precursor of step (v); (vi) contacting said catalyst precursor of step (v) with an activating amount of dimethylaluminum chloride.

Claim 10

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a slurry of a solid, porous carrier having reactive OH groups in a non-polar liquid with dibutylmagnesium to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with silicon tetrahalide to form an intermediate of step (ii) (iii) contacting said product of step (ii) with at least one compound of the formula (R.sup.1 O).sub.x SiR.sup.2.sub.y wherein x is 1, 2, 3, or 4 and y=4-x; R 1 is a hydrocarbyl group of 1 to 10 carbon atoms; and R 2 is halogen or a hydrocarbyl group of 1 to 10 carbon atoms, or hydrogen to form an intermediate of step (iii) (iv) contacting said intermediate of step (iii) 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 OH groups on said carrier prior to reaction with said dibutylmagnesium in step (i), said transition metal compound being soluble in said liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (v) contacting said transition metal-containing intermediate with an additional quantity of dibutylmagnesium to prepare a catalyst precursor of step (v); (vi) contacting said catalyst precursor of step (v) with an activating amount of dimethylaluminum chloride.

Claim 11

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a solid, porous carrier having reactive OH groups with a non-polar liquid containing at least one organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with silicon tetrahalide to form an intermediate of step (ii) (iii) contacting said product of step (ii) with tetrabutoxysilane to form an intermediate of step (iii) (iv) contacting said intermediate of step (iii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said organomagnesium compound in step (i), said transition metal compound being soluble in said liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of transition metal becomes supported on said carrier; and (v) contacting said transition metal-containing intermediate with an additional quantity of least one organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to prepare a catalyst precursor of step (v), (vi) contacting said catalyst precursor of step (v) with an activating amount of dimethylaluminum chloride.

Claim 12

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a solid, porous carrier having reactive OH groups with a non-polar liquid containing at least one organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with silicon tetrahalide to form an intermediate of step (ii) (iii) contacting said product of step (ii) with tetrabutoxysilane to form an intermediate of step (iii) (iv) contacting said intermediate of step (iii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said organomagnesium compound in step (i), said transition metal compound being soluble in said liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of transition metal becomes supported on said carrier; and (v) contacting said transition metal-containing intermediate with an additional quantity of least one organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to prepare a catalyst precursor of step (v), (vi) contacting said catalyst precursor of step (v) with an activating amount of dimethylaluminum chloride.

Claim 13

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a solid, porous carrier having reactive OH groups with a non-polar liquid, said liquid containing at least one organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, wherein said organomagnesium compound is soluble in said non-polar liquid, to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with at least one compound selected from the group consisting of (a) SiCl 4 and (b) a compound of the formula (R.sup.1 O).sub.x SiR.sup.2.sub.y wherein x is 1, 2, 3, or 4 and y=4-x; R 1 is a hydrocarbyl group of 1 to 10 carbon atoms; and R 2 is halogen or a hydrocarbyl group of 1 to lo carbon atoms, or hydrogen to form an intermediate of step (ii); (iii) contacting said intermediate of step (ii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said organomagnesium compound in step (i), said transition metal compound being soluble in said liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (iv) contacting said transition metal-containing intermediate with an additional quantity of R m Mg R' n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to prepare a catalyst precursor of step (iv); (v) contacting said catalyst precursor of step (iv) with an activating amount of dimethylaluminum chloride, to produce said catalyst.

Claim 14

A catalyst composition for copolymerization of ethylene with alpha-olefins, to produce LLDPE resin products of a bimodal molecular weight distribution, having a relatively low molecular weight component and a relatively high molecular weight component, wherein the catalyst is prepared by a process which comprises the steps of: (i) contacting a solid, porous carrier having reactive OH groups with a non-polar liquid, said liquid containing at least one organomagnesium compound having the empirical formula R.sub.m MgR'.sub.n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, wherein said organomagnesium compound is soluble in said non-polar liquid, to form a product of step (i) which contains said carrier and incorporated therein a source of magnesium; (ii) contacting said product of step (i) with at least one compound selected from the group consisting of (a) SiCl 4 and (b) a compound of the formula (R.sup.1 O).sub.x SiR.sup.2.sub.y wherein x is 1, 2, 3, or 4 and y=4-x; R 1 is a hydrocarbyl group of 1 to 10 carbon atoms; and R 2 is halogen or a hydrocarbyl group of 1 to lo carbon atoms, or hydrogen to form an intermediate of step (ii); (iii) contacting said intermediate of step (ii) with at least one transition metal compound in a non-polar liquid medium, the number of moles of said transition metal compound being in excess of the number of OH groups on said carrier prior to reaction with said organomagnesium compound in step (i), said transition metal compound being soluble in said liquid, and said magnesium-containing carrier being substantially insoluble in said liquid medium, whereby a reacted form of the transition metal becomes supported on said carrier; and (iv) contacting said transition metal-containing intermediate with an additional quantity of R m Mg R' n where R and R' are the same or different C 1 -C 12 alkyl groups, and m+n=2, to prepare a catalyst precursor of step (iv); (v) contacting said catalyst precursor of step (iv) with an activating amount of dimethylaluminum chloride, to produce said catalyst.

Claim 15

The catalyst of claim 7, wherein the silane compound is selected from the group consisting of Si(OR) 4 and Si(R'O) x (R'").sub.(4-x) wherein each of R and R" is a C 1 -C 10 hydrocarbyl group, wherein R'" is chlorine, or a C 1 -C 10 hydrocarbyl group or hydrogen and x=1, 2 or 3.

Claim 16

The catalyst of claim 7, wherein the said hydrocarbyl group is selected from the group consisting of alkyl, aryl, arylalkyl, alkenyl and arylalkenyl groups and contains 1 to 10 carbon atoms.

Claim 17

The catalyst of claim 9, wherein said hydrocarbyl group contains 2 to 6 carbon atoms.

Claim 18

The catalyst of claim 10, wherein said silane compound is selected from the group consisting of tetramethoxysilane, dimethoxydimethylsilane, tetraethoxysilane, triethoxyethylsilane, diethoxydiethylsilane, chlorotriethoxysilane, phenyltriethoxysilane, ethoxytriethylsilane, tetraisopropoxysilane, diisopropoxydiisopropylsilane, tetrapropoxysilane, dipropoxydipropylsilane, tetrabutoxysilane, dibutoxydibutylsilane, diethoxydiphenylsilane, phenoxytrimethylsilane, tetraphenoxysilane, triethoxyphenylsilane, tetrakis(2-methoxyethoxy) silane, tetrakis(2-ethylhexoxy) silane, and tetraallyloxysilane.

Claim 19

The catalyst of claim 11, wherein said silane compound is selected from the group consisting of tetraethoxysilane, chlorotriethoxysilane, phenyltriethoxysilane, tetrakis(2-ethylhexoxy)silane, tetraallyloxysilane and tetrabutoxysilane.

Claim 20

The catalyst composition of claim 12 wherein, in step (i), the ratio of the number of moles of said organomagnesium compound to the number of moles of said OH groups on said solid porous carrier is from about 1.1 to about 2.5, wherein in step (ii) the molar ratio of the silane compound to Mg fixed on the solid carrier after the first treatment with an organomagnesium compound is 0.30 to 1.40.

Claim 21

The catalyst of claim 13, wherein, in step (i), the ratio of the number of moles of said organomagnesium compound to the number of moles of OH groups on said solid porous carrier is from about 1.0 to about 2.5.

Claim 22

A catalyst composition of claim 14, wherein, in step (i), the ratio of the number of moles of said organomagnesium compound to the number of moles of OH groups on said solid porous carrier is from about 1.1 to about 1.8.

Claim 23

The catalyst of claim 15, wherein the molar ratio of dimethylaluminum chloride to the transition metal ranges from 1 to 500.

Claim 24

The catalyst of claim 16, wherein the transition metal is provided as a tetravalent titanium compound.

Claim 25

The catalyst of claim 17, wherein the transition metal compound is titanium tetrachloride.

Claim 26

A catalyst which consists of the catalyst of claim 1.

Claim 27

A catalyst which consists of the catalyst of claim 2.

Claim 28

A catalyst which consists of the catalyst of claim 3.

Claim 29

A catalyst which consists of the catalyst of claim 4.

Claim 30

A catalyst which consists of the catalyst of claim 5.

Claim 31

A catalyst which consists of the catalyst of claim 6.

Claim 32

A catalyst which consists of the catalyst of claim 7.