Preparation of homopolymers of ethene and copolymers of ethene with higherα-monolefins using a Ziegler catalyst system

Claim 2

A process for the preparation of copolymers of ethylene with minor amounts of C 3 -C 8 -α-monoolefins by polymerization of the monomers at from 50° to 125° C. and under a pressure of from 5 to 60 bar, the improvement which comprises using a Ziegler catalyst system comprising (1) a transition metal catalyst component, (2) an organoaluminum catalyst component of the formula AIR.sub.3 where R is C 2 -C 8 -alkyl, and (3) an organohalogen catalyst component (cocatalyst), selected from the group consisting of those of the formulae CFCl 3 , CCl 4 , CHCl 3 , CH 2 Cl 2 , CF 2 Cl 2 , CH 2 ═CH--CH 2 Cl, CCl 2 ═CCl--CCl 3 , CH.tbd.C--CH 2 Cl, α-chlorotoluene, α,α-dichlorotoluene, α,α,α-trichlorotoluene, methyl perchlorocrotonate and n-butyl 2,3, 4, 4-tetrachlorobut-2-enoate

Claim 3

with the provisos that the atomic ratio of the transition metal from the catalyst component (1) to aluminum from the catalyst component (2) is from 1:0.2 to 1:50, and the molar ratio of the organoaluminum catalyst component (2) to the organohalogen catalyst component (3) is from 1:0.01 to 1:10, wherein the transition metal catalyst component (1) used is a solid-phase product (VI), obtained by a method in which (1.1) first (1.1.1) a finely divided, porous silicon dioxide (I), which has a particle diameter of from 1 to 400 μm, a pore volume of from 1 to 2.5 cm 3 /g and a specific surface area of from 200 to 400 m 2 / g and (1.1.2) a solution (II), as obtained on combining (11a) 100 parts by weight of a saturated alicyclic oxahydrocarbon of 1 oxa oxygen atom and 4 to 6 carbon atoms an (11b) from 1 to 50 parts by weight of a mixture of (11b1) 100 molar parts of a vanadium trihalide/alcohol complex of the formula VY 3 .nZ-OH, wherein Y is chlorine, n is from 1 to 6, and Z is an alkyl of not more than 6 carbon atoms, (IIb2) from 0.5 to 100 molar parts of a titanium trichloride or of a titanium trihalide/alcohol complex of the formula TiY 3 .nZOH, where Y is chlorine, n is from 1 to 6 and Z is an alkyl of not more than 4 carbon atoms and (IIb3) from 3 to 200 molar parts of a zirconium tetrachloride, are brought into contact with one another to form a suspension (III), with the proviso that the weight ratio of silicon dioxide (I) to transition metal composition (IIb) is from 1:0.2 to 1:1.5, the suspension (III) is evaporated to dryness at below 160° C. and above the melting point of the oxahydrocarbon (IIa) used, a solid-phase intermediate (IV) being formed, and (1.2) thereafter (1.2.1) the solid-phase intermediate (IV) obtained from stage (1.1) and (1.2.2) a solution, in an organic solvent, of an aluminum compound (V) of the formula AIR.sub.m X.sub.3-m where X is chlorine, R is C 2 -C 8 -alkyl, and m is the number 2, are brought into contact with one another to form a suspension, with the proviso that the weight ratio of the solid-phase intermediate (IV) to the aluminum compound (V) is from 1:0.1 to 1:1, and the resulting suspended solid-phase product (VI) is the transition metal catalyst component (1).

Claim 4

with the provisos that the atomic ratio of the transition metal from the catalyst component (1) to aluminum from the catalyst component (2) is from 1:0.2 to 1:50, and the molar ratio of the organoaluminum catalyst component (2) to the organohalogen catalyst component (3) is from 1:0.01 to 1:10, wherein the transition metal catalyst component (1) used is a solid-phase product (VI), obtained by a method in which (1.1) first (1.1.1) a finely divided, porous silicon dioxide (I), which has a particle diameter of from 1 to 400 μm, a pore volume of from 1 to 2.5 cm 3 /g and a specific surface area of from 200 to 400 m 2 / g and (1.1.2) a solution (II), as obtained on combining (11a) 100 parts by weight of a saturated alicyclic oxahydrocarbon of 1 oxa oxygen atom and 4 to 6 carbon atoms an (11b) from 1 to 50 parts by weight of a mixture of (11b1) 100 molar parts of a vanadium trihalide/alcohol complex of the formula VY 3 .nZ-OH, wherein Y is chlorine, n is from 1 to 6, and Z is an alkyl of not more than 6 carbon atoms, (IIb2) from 0.5 to 100 molar parts of a titanium trichloride or of a titanium trihalide/alcohol complex of the formula TiY 3 .nZOH, where Y is chlorine, n is from 1 to 6 and Z is an alkyl of not more than 4 carbon atoms and (IIb3) from 3 to 200 molar parts of a zirconium tetrachloride, are brought into contact with one another to form a suspension (III), with the proviso that the weight ratio of silicon dioxide (I) to transition metal composition (IIb) is from 1:0.2 to 1:1.5, the suspension (III) is evaporated to dryness at below 160° C. and above the melting point of the oxahydrocarbon (IIa) used, a solid-phase intermediate (IV) being formed, and (1.2) thereafter (1.2.1) the solid-phase intermediate (IV) obtained from stage (1.1) and (1.2.2) a solution, in an organic solvent, of an aluminum compound (V) of the formula AIR.sub.m X.sub.3-m where X is chlorine, R is C 2 -C 8 -alkyl, and m is the number 2, are brought into contact with one another to form a suspension, with the proviso that the weight ratio of the solid-phase intermediate (IV) to the aluminum compound (V) is from 1:0.1 to 1:1, and the resulting suspended solid-phase product (VI) is the transition metal catalyst component (1).

Claim 5

The process of claim 1 wherein component IIa is tetrahydrofuran; in component IIb1 n is 3 or 4; and in component IIb2 n is 3 or 4.

Claim 6

The process of claim 1 wherein component (IIb2) consists solely of a titanium trihalide/alcohol complex of the formula TiY 3 -nZOH, where Y is chlorine, n is from 1 to 6, and Z is an alkyl of not more than 4 carbon atoms.