Granted Patent B2

US 7,678,726 · App. 10/568,954 · Granted Mar 16, 2010

Abstract

Claims (48)

1. A supported polymerisation catalyst system prepared by a method consisting essentially of the following steps:

(i) adding a cocatalyst to a porous support,

(ii) mixing a polymerisation catalyst with a polymerisable monomer, and

(iii) contacting together the components resulting from steps (i) and (ii),

wherein the molar ratio of the polymerisable monomer to polymerization catalyst is in the range 1:1 to 250:1.

2. A supported polymerisation catalyst system according to claim 1 wherein the porous support is an inorganic metal oxide.

3. A supported polymerisation catalyst system according to claim 2 wherein the inorganic metal oxide is silica.

4. A supported polymerisation catalyst system according to claim 1 wherein the polymerisable monomer has 2 to 10 carbon atoms.

5. A supported polymerisation catalyst system according to claim 4 wherein the monomer is 1-hexene.

6. A supported polymerisation catalyst system according to claim 1 wherein the polymerisation catalyst is a transition metal compound.

7. A supported polymerisation catalyst system according to claim 6 wherein the transition metal compound is a metallocene.

8. A supported polymerisation catalyst system according to claim 7 wherein the metallocene has the formula

wherein:—

R′ each occurrence is independently selected from the group consisting of hydrogen, hydrocarbyl, silyl, germyl, halo, cyano, and combinations thereof, said R′ having up to 20 nonhydrogen atoms, and optionally, two R′ groups (where R′ is not hydrogen, halo or cyano) together form a divalent derivative thereof connected to adjacent positions of the cyclopentadienyl ring to form a fused ring structure;

X is hydride or a moiety selected from the group consisting of halo, alkyl, aryl, aryloxy, alkoxy, alkoxyalkyl, amidoalkyl, siloxyalkyl having up to 20 non-hydrogen atoms and neutral Lewis base ligands having up to 20 non-hydrogen atoms,

Y is —O—, —S—, —NR*—, —PR*—,

M is hafnium, titanium or zirconium,

Z* is SiR* 2 , CR* 2 , SiR* 2 SiR* 2 , CR* 2 CR* 2 , CR*═CR*, CR* 2 SiR* 2 , or GeR* 2 , wherein:

R* each occurrence is independently hydrogen, or a member selected from the group consisting of hydrocarbyl, silyl, halogenated alkyl, halogenated at, and combinations thereof, said

R* having up to 10 non-hydrogen atoms, and optionally, two R* groups from Z* (when R* is not hydrogen), or an R* group from Z* and an R* group from Y form a ring system, and n is 1 or 2 depending on the valence of M.

9. A supported polymerisation catalyst system according to claim 7 wherein the metallocene has the formula

wherein:—

R′ each occurrence is independently selected from the group consisting of hydrogen, hydrocarbyl, silyl, germyl, halo, cyano, and combinations thereof, said R′ having up to 20 nonhydrogen atoms, and optionally, two R′ groups (where R′ is not hydrogen, halo or cyano) together form a divalent derivative thereof connected to adjacent positions of the cyclopentadienyl ring to form a fused ring structure;

X is a neutral η 4 bonded diene group having up to 30 non-hydrogen atoms, which forms a π-complex with M;

Y is —O—, —S—, —NR*—, —PR*—,

M is titanium or zirconium in the +2 formal oxidation state;

Z* is SiR* 2 , CR* 2 , SiR* 2 SiR* 2 , CR* 2 CR* 2 , CR*═CR*, CR* 2 SiR* 2 , or GeR* 2 , wherein:

R* each occurrence is independently hydrogen, or a member selected from the group consisting of hydrocarbyl, silyl, halogenated alkyl, halogenated aryl, and combinations thereof, said

R* having up to 10 non-hydrogen atoms, and optionally, two R* groups from Z* (when R* is not hydrogen), or an R* group from Z* and an R* group from Y form a ring system.

10. A supported polymerisation catalyst system according to claim 1 wherein the cocatalyst is an aluminoxane, borane or borate.

11. A supported polymerisation catalyst system according to claim 1 wherein the cocatalyst has the formula

(L*—H) + d (A d− )

wherein

L* is a neutral Lewis base

(L*—H) + d is a Bronsted acid

A d− is a non-coordinating compatible anion having a charge of d − , and d is an integer from 1 to 3.

12. A supported polymerisation catalyst system according to claim 11 wherein the cocatalyst comprises a cation and an anon wherein the anion has at least one substituent comprising a moiety having an active hydrogen.

13. A process for the polymerisation of olefin monomers selected from the group consisting of (a) ethylene, (b) propylene (c) mixtures of ethylene and propylene and (d) mixtures of (a), (b) or (c) with one or more other alpha-olefins, said process comprising polymerizing said monomers in the presence of a supported polymerisation catalyst system as claimed in claim 1 .

14. A process for the polymerisation of ethylene or the copolymerisation of ethylene and α-olefins having from 3 to 10 carbon atoms, said process comprising conducting said polymerization or copolymerization under polymerisation conditions in the presence of a polymerisation catalyst system as claimed in claim 1 .

15. A process according to claim 14 wherein the α-olefin is 1-butene, 1-hexene, 4-methyl-1-pentene or 1-octene.

16. A process according to claim 13 performed in the slurry or gas phase.

17. A process according to claim 16 performed in a fluidised bed gas phase reactor.

18. A supported polymerisation catalyst system according to claim 1 wherein the ratio of the polymerisable monomer to polymerization catalyst is in the range 20:1 to 80:1.

19. A process for preparing a supported polymerisation catalyst system comprising the steps of:

(i) adding a cocatalyst to a porous support,

(ii) mixing a polymerisation catalyst with a polymerisable monomer, and

(iii) contacting together the components resulting from steps (i) and (ii),

wherein the molar ratio of the polymerisable monomer to polymerization catalyst is in the range 1:1 to 250:1.

Assignments (16)