Olefin polymerization catalyst system and process for polymerization of olefins

Claim 2

In a process for the polymerization or copolymerization of at least one 1-olefin monomer to produce linear, solid polyolefins of high molecular weight by the use, as polymerization catalyst, of a transition metal composition, in which the transition metal is a metal of Group IV(a) of the Periodic Table of the Elements, the improvements which consists essentially of employing as the transition metal composition a transition metal hydrocarbyl hydride aluminate supported on alumina in which said hydrocarbyl radical is selected from the group consisting of radicals having the structure RCH 2 -- in which R-- is aryl, aralkyl in which no hydride radical is attached to the carbon atom bonded to the methylene group, or tertiary butyl, and in which from about 60% to substantially 100% of the radicals other than aluminate bonded to the transition metal are hydride radicals.

Claim 3

A process according to claim 1 in which the transition metal hydrocarbyl hydride aluminate is zirconium neophyl hydride aluminate.

Claim 4

A process according to claim 1 in which the transition metal hydrocarbyl hydride aluminate is zirconium benzyl hydride aluminate.

Claim 5

A process according to claim 1 in which the olefin monomer consists solely of ethylene.

Claim 6

A process according to claim 1 in which the olefin monomer consists of a mixture of ethylene and propylene in which the mole percent of propylene is greater than 50%.

Claim 7

A process according to claim 1 in which the olefin monomer consists of a mixture of ethylene with up to 15 mole percent of a higher 1-olefin having from 4 to 10 carbon atoms.

Claim 8

A process according to claim 1 in which the olefin monomer consists solely of propylene.

Claim 9

In a continuous solution process for the polymerization of ethylene to produce a linear, solid, crystalline polymer of ethylene in which a solution in an inert hydrocarbon solvent of polymerizable olefins comprising at least 85 mole percent ethylene and from 0 to 15 mole percent of another 1-olefin having from 4 to 10 carbon atoms in the monomer molecule is continuously passed into one or more agitated polymerization zones maintained at a temperature in the range of 130° to 300°C. maintained under a pressure in the range of 500 to 5000 psi, and the solution of reaction products in continuously withdrawn from the polymerization zone to a catalyst deactivation zone where it is continuously mixed with a substance which reacts to deactivate the catalyst and the hot solution of reaction products is continuously passed from the deactivation zone to a product recovery zone where the polymer of ethylene is separated from the solvents and isolated in solid form, the improvement which (comprises) consists essentially of continuously feeding to the polymerization zone as the polymerization initiator a slurry in hydrocarbon medium of a zirconium hydrocarbyl hydride aluminate supported on alumina, said hydrocarbyl radical being selected from the group having the structure R--CH 2 -- in which R-- is aryl, aralkyl in which no hydride radical is attached to the carbon atom bonded to the methylene group, or tertiary butyl, in which the valence of the zirconium is reduced, at least in part, to three, and from about 90% to substantially 100% of the radicals, other than aluminate bonded to zirconium, are hydride radicals, at a rate sufficient to maintain the temperature constant in the reaction zone under adiabatic conditions and such that the molar ratio of polymerizable olefins to zirconium in the polymerization zone is maintained in the range of 35,000-400,000 to 1.

Claim 10

In a continuous solution process for the polymerization of ethylene to produce a linear, solid, crystalline polymer of ethylene in which a solution in an inert hydrocarbon solvent of polymerizable olefins comprising at least 85 mole percent ethylene and from 0 to 15 mole percent of another 1-olefin having from 4 to 10 carbon atoms in the monomer molecule is continuously passed into one or more agitated polymerization zones maintained at a temperature in the range of 130° to 300°C. maintained under a pressure in the range of 500 to 5000 psi, and the solution of reaction products in continuously withdrawn from the polymerization zone to a catalyst deactivation zone where it is continuously mixed with a substance which reacts to deactivate the catalyst and the hot solution of reaction products is continuously passed from the deactivation zone to a product recovery zone where the polymer of ethylene is separated from the solvents and isolated in solid form, the improvement which (comprises) consists essentially of continuously feeding to the polymerization zone as the polymerization initiator a slurry in hydrocarbon medium of a zirconium hydrocarbyl hydride aluminate supported on alumina, said hydrocarbyl radical being selected from the group having the structure R--CH 2 -- in which R-- is aryl, aralkyl in which no hydride radical is attached to the carbon atom bonded to the methylene group, or tertiary butyl, in which the valence of the zirconium is reduced, at least in part, to three, and from about 90% to substantially 100% of the radicals, other than aluminate bonded to zirconium, are hydride radicals, at a rate sufficient to maintain the temperature constant in the reaction zone under adiabatic conditions and such that the molar ratio of polymerizable olefins to zirconium in the polymerization zone is maintained in the range of 35,000-400,000 to 1.

Claim 11

A process according to claim 8 in which the zirconium hydrocarbyl hydride aluminate is zirconium benzyl hydride aluminate.

Claim 12

A process according to claim 8 in which the zirconium hydrocarbyl hydride aluminate is zirconium neophyl hydride aluminate.

Claim 13

A process according to claim 8 in which the polymerizable olefin fed to the polymerization zone is solely ethylene.

Claim 14

A process according to claim 8 in which from 0.001 to 10 moles of H 2 , dissolved in an inert hydrocarbon solvent, per mole of ethylene is simultaneously fed continuously to the polymerization zone to control and limit the molecular weight of the polymer of ethylene produced.