Manufacture of particulate homopolymers or copolymers of ethylene
AssigneeBASF SE
InventorsRudolf Herbeck, Erich Kolk, Guenther Schweier, Hans Schick, Friedrich Urban
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AssigneeBASF SE
InventorsRudolf Herbeck, Erich Kolk, Guenther Schweier, Hans Schick, Friedrich Urban
Estimating the term…
Particulate polymers of ethylene are prepared by polymerization of ethylene or ethylene/.alpha. -monoalkene mixtures in a dry agitated bed (B) of the particulate polymer by means of a Ziegler/Natta catalyst system consisting of (1) a titanium-containing component and (2) an aluminum-containing component, the said components (1) and (2) being separately fed to the bed (B). Component (1) is a particulate reaction product (U) (of) (1.1) a substance of the formula TiCl.sub.3 . (AlCl.sub.3).sub.n where n is a number equal to from 0 to 0.34, and (1.2) a reaction product (R) of phosgene and a substnace (S) obtained from a substance of the formula Mg.sub.6 . Al.sub.2 . (OH).sub.16 . CO.sub.3 . (H.sub.2 O).sub.4 by calcination (heating), provided that (R) has a chlorine content of from 10 to 76% by weight and (U) has been obtained by milling (1.1) and (1.2) together.
A process for the manufacture of particulate ethylene homopolymers (HP) or ethylene copolymers (CP) containing up to 20% by weight of polymerized units of C.sub.3-8 .alpha.-monoalkene, which polymers have a particle size of from 0.1 to 6 mm and are obtained by polymerization of ethylene or ethylene/C.sub.3-8 .alpha.-monoalkene mixtures in a dry, agitated bed (B) of particulate homopolymer (HP) or copolymer (CP) at temperatures of from 30.degree. to 120.degree.C and pressures of from 1 .times. 10.sup.5 to 2 .times. 10.sup.7 N/m.sup.2 (Pascal) by means of a Ziegler/Natta catalyst system consisting of (1) a titanium-containing component and (2) an aluminum (C.sub.1-8 trialkyl) or aluminum (C.sub.1-8 dialkyl) chloride, provided that (I) the components (1) and (2) of the catalyst system are separately fed to the bed (B) and (II) the atomic ratio of titanium in component (1) to aluminum in component (2) is from 1:0.1 to 1:1,000, wherein the titanium-containing component (1) of the catalyst system is a particulate reaction product (U) having a particle diameter of from 0.1 to 2,000 .mu.m and obtained from
Dependencies are inferred from the claim text.