Nitrogen-containing group 13 anionic complexes for olefin polymerization

Claim 2

A process for the preparation of polyolefins from one or more olefinic monomers comprising combining said olefins under olefin polymerization conditions with an organometallic catalyst compound that is activated for olefin polymerization by reaction with a Group 13 element cocatalyst complex comprising at least one halogenated, nitrogen-containing aromatic group ligand.

Claim 3

The process of claim 1 wherein said Group 13 element cocatalyst complex is a neutral, Group 13 three-coordinate Lewis acid compound or ionic salt compound comprising a four-coordinate Group 13 element anionic complex.

Claim 4

The process of claim 1 wherein said organometallic catalyst compound is a Group 3-10 transition metal compound capable of activation for olefin polymerization by ligand abstraction.

Claim 5

The process of claim 3 wherein said transition metal organometallic catalyst compound is a Group 3-6 metallocene compound having the formula: L.sup.A L.sup.B L.sup.C.sub.i MDE where, L A is a substituted or unsubstituted cyclopentadienyl or heterocyclopentadienyl ancillary ligand π-bonded to M; L B is a member of the class of ancillary ligands defined for L A , or is J, a heteroatom ancillary ligand bonded to M; the L A and L B ligands may be covalently bridged together through a Group 14 element linking group; L C i is an optional neutral, non-oxidizing ligand having a dative bond to M (i equals 0 to 3); M is a Group 3-6 transition metal; and, D and E are independently monoanionic labile ligands, each having a σ-bond to M, optionally bridged to each other or to L A or L B , which can be broken for abstraction purposes by said Group 13 element cocatalyst complex and into which a polymerizable monomer or macromonomer can insert for coordination polymerization.

Claim 6

The process of claim 2 wherein said Group 13 element cocatalyst complex is a Lewis acid described by the following formula: R.sub.n M(ArNHal).sub.3-n, where R is a substituted or unsubstituted C 1 to C 30 hydrocarbyl aliphatic or aromatic groups, M is a Group 13 metal or metalloid, ArNHal is a halogenated, nitrogen-containing aromatic ring, polycyclic aromatic ring or aromatic ring assembly, and n=0-2.

Claim 7

The process of claim 2 wherein said Group 13 element cocatalyst complex is an ionic salt represented by the formula: [C].sup.+ [R.sub.n M(ArNHal).sub.4-n ].sup.-, where [C] + is a is a suitable cation, R is a substituted or unsubstituted C 1 to C 30 hydrocarbyl aliphatic or aromatic groups, M is a Group 13 metal or metalloid, ArNHal is a halogenated, nitrogen-containing aromatic ring, polycyclic aromatic ring or aromatic ring assembly, and n=0-3.

Claim 8

The process of claim 1 wherein said olefin polymerization conditions comprise a solution, supercritical pressure, bulk, slurry or gas phase process conducted at reaction temperatures between 30° C.-200° C. and pressures between 0-2000 bar.

Claim 9

The process of claim 7 wherein said process is bulk, slurry or gas phase, and said Group 13 element cocatalyst complex additionally comprises a covalent connecting group linking the Group 13 atom to a metal/metalloid or polymeric support.

Claim 10

The process of claim 8 wherein said support is silica.

Claim 11

The process of claim 8 wherein said support is polymeric.

Claim 12

The process of claim 4 wherein M is titanium and L B is J, a heteroatom ancillary ligand σ-bonded to M.

Claim 13

The process of claim 4 wherein M is zirconium or hafnium and L B is independently a substituted or unsubstituted cyclopentadienyl or heterocyclopentadienyl ancillary ligand π-bonded to M.