Polymerization method

Claim 1

The method of making polymers of ethylene comprising polymerizing said ethylene under polymerizing conditions with a catalyst prepared by the consecutive steps of: (1) reacting in a liquid hydrocarbon slurry at a temperature of between ambient and about 150° C. a finely divided, difficulty reducible, porous calcined support comprising silica or alumina, said hydrocarbon having between about 4 to 8 carbon atoms, with (2) a magnesium compound of the formula MgR 2 wherein R is an alkyl group and said compound is essentially free of aluminum alkyls, the molar ratio of said magnesium compound to the surface hydroxyls of said calcined support being between about 0.25-3/1, then reacting, at a temperature of about 90°-100° C. the resulting product with (3) a primary hydrocarbyl alcohol, the molar ratio of said alcohol to the magnesium in the reaction product of step (2) being from about 0.5 to about 3 to 1, then reacting in a hydrocarbon slurry at about 90-150° C. the product of this with (4) titanium tetrachloride without first removing unreacted alcohol from the product of (3), the molar ratio of said titanium tetrachloride to said alcohol being between about 1-10/1 and the molar ratio of said titanium tetrachloride to said magnesium compound being between about 0.5-4/1 (5) removing essentially all unreacted components and by-products from the reactions of steps (1), (2), (3) and (4) by washing with a dry hydrocarbon liquid or gas at temperatures between ambient to about 150° C., followed by (6) activating the resulting reaction product by treating in the substantial absence of air with a cocatalyst that is either hydrogen or a Group IA, IIA, IIIA or IIB organometallic compound or mixture of two or more of these.

Claim 2

The method of making polymers of ethylene comprising polymerizing said ethylene under polymerizing conditions with a catalyst prepared by the consecutive steps of: (1) reacting in a liquid hydrocarbon slurry at a temperature of between ambient and about 150° C. a finely divided, difficulty reducible, porous calcined support comprising silica or alumina, said hydrocarbon having between about 4 to 8 carbon atoms, with (2) a magnesium compound of the formula MgR 2 wherein R is an alkyl group and said compound is essentially free of aluminum alkyls, the molar ratio of said magnesium compound to the surface hydroxyls of said calcined support being between about 0.25-3/1, then reacting, at a temperature of about 90°-100° C. the resulting product with (3) a primary hydrocarbyl alcohol, the molar ratio of said alcohol to the magnesium in the reaction product of step (2) being from about 0.5 to about 3 to 1, then reacting in a hydrocarbon slurry at about 90-150° C. the product of this with (4) titanium tetrachloride without first removing unreacted alcohol from the product of (3), the molar ratio of said titanium tetrachloride to said alcohol being between about 1-10/1 and the molar ratio of said titanium tetrachloride to said magnesium compound being between about 0.5-4/1 (5) removing essentially all unreacted components and by-products from the reactions of steps (1), (2), (3) and (4) by washing with a dry hydrocarbon liquid or gas at temperatures between ambient to about 150° C., followed by (6) activating the resulting reaction product by treating in the substantial absence of air with a cocatalyst that is either hydrogen or a Group IA, IIA, IIIA or IIB organometallic compound or mixture of two or more of these.