Manufacture of olefin polymers

Claim 1

A process for the manufacture of a homopolymer or copolymer of an α-monoolefin of 2 to 10 carbon atoms by polymerizing the monomer or monomers at a temperature of from 30° to 200° C. and a pressure of from 0.1 to 200 bars, by means of a Ziegler catalyst system comprising (1) a catalyst component containing titanium and/or vanadium and (2) a metal compound of the general formula MeA.sub.m-n X.sub.n where Me is aluminum, magnesium or zinc, A is a hydrocarbon radical of 1 to 12 carbon atoms, X is chlorine, bromine, iodine or hydrogen m is the valency of the metal Me and n is a number from 0 to m-1, the atomic ratio of transition metal in catalyst component (1) to metal (Me) in catalyst component (2) being from 1:0.1 to 1:500, wherein the catalyst component (1), containing titanium and/or vanadium, is the solid-phase product (VII) which has been obtained by first (1.1) bringing a finely divided porous inorganic oxidic material (I), which has a particle diameter of from 1 to 1,000μ, a pore volume of from 0.3 to 3 cm 3 /g, and a surface area of from 100 to 1,000 m 2 /g, and which has the formula SiO 2 , into contact with an aluminum compound (II) dissolved in an organic solvent and having the general formula AlB.sub.3-p Y.sub.p where B is hydrocarbon radical of 1 to 12 carbon atoms, Y is chlorine, bromine, iodine, hydrogen or OR, R is a hydrocarbon radical of 1 to 12 carbon atoms and p is a number from 0 to 3, to form a solid-phase product (III), the weight ratio of the inorganic oxidic material (I) employed to the aluminum compound (II) employed being from 1:0.05 to 1:10, and then (1.2) bringing the solid-phase product (III) obtained from stage (1.1) into contact with a magnesium compound (IV), dissolved in an organic solvent, to form a solid-phase product (V), the weight ratio of solid-phase product (III) employed to magnesium compound (IV) employed being from 1:0.01 to 1:0.25, the magnesium compound (IV) being a manasseite of the formula Mg 6 .Al 2 .(OH) 16 .CO 3 .4H 2 O and further being brought to a chlorine content of from 50 to 75 percent by weight by halogenation with phosgene, and finally (1.3) bringing the solid-phase product (V) obtained from stage (1.2) into contact with a solid or liquid transition metal compound (VI) dissolved in an organic solvent, or a liquid transition metal compound (VI) without solvent, the transition metal being titanium and/or vanadium, to form a solid-phase product (VII), the weight raio of solid-phase product (V) employed to transition metal in the transition metal compound (VI) employed being from 1:0.01 to 1:20.