Metal complexes as catalyst component for olefin polymerization

Details Metal complexes as catalyst component for olefin polymerization Metal complexes as catalyst component for olefin polymerization

2001-08-09

2004-07-13

Rabago, Roberto (Department: 1713)

Synthetic resins or natural rubbers -- part of the class 520 ser

Synthetic resins

Polymers from only ethylenic monomers or processes of...

C526S113000, C526S114000, C526S115000, C526S129000, C526S134000, C526S169100, C526S171000, C526S172000, C502S103000, C502S117000, C502S118000, C502S120000, C502S150000, C502S155000, C502S162000, C502S167000

Reexamination Certificate

active

06762258

ABSTRACT:

BACKGROUND OF THE INVENTION
The present invention relates to transition metal complex compounds, to polymerisation catalysts based thereon and to their use in the polymerisation and copolymerisation of olefins.
The use of certain transition metal compounds to polymerise 1-olefins, for example, ethylene, is well established in the prior art. The use of Ziegler-Natta catalysts, for example, those catalysts produced by activating titanium halides with organometallic compounds such as triethylaluminium, is fundamental to many commercial processes for manufacturing polyolefins. Over the last twenty or thirty years, advances in the technology have led to the development of Ziegler-Natta catalysts which have such high activities that olefin polymers and copolymers containing very low concentrations of residual catalyst can be produced directly in commercial polymerisation processes. The quantities of residual catalyst remaining in the produced polymer are so small as to render unnecessary their separation and removal for most commercial applications. Such processes can be operated by polymerising the monomers in the gas phase, or in solution or in suspension in a liquid hydrocarbon diluent. Polymerisation of the monomers can be carried out in the gas phase (the “gas phase process”), for example by fluidising under polymerisation conditions a bed comprising the target polyolefin powder and particles of the desired catalyst using a fluidising gas stream comprising the gaseous monomer. In the so-called “solution process” the (co)polymerisation is conducted by introducing the monomer into a solution or suspension of the catalyst in a liquid hydrocarbon diluent under conditions of temperature and pressure such that the produced polyolefin forms as a solution in the hydrocarbon diluent. In the “slurry process” the temperature, pressure and choice of diluent are such that the produced polymer forms as a suspension in the liquid hydrocarbon diluent. These processes are generally operated at relatively low pressures (for example 10-50 bar) and low temperature (for example 50 to 150° C.).
Commodity polyethylenes are commercially produced in a variety of different types and grades. Homopolymerisation of ethylene with transition metal based catalysts leads to the production of so-called “high density” grades of polyethylene. These polymers have relatively high stiffness and are useful for making articles where inherent rigidity is required. Copolymerisation of ethylene with higher 1-olefins (eg butene, hexene or octene) is employed commercially to provide a wide variety of copolymers differing in density and in other important physical properties. Particularly important copolymers made by copolymerising ethylene with higher 1-olefins using transition metal based catalysts are the copolymers having a density in the range of 0.91 to 0.93. These copolymers which are generally referred to in the art as “linear low density polyethylene” are in many respects similar to the so called “low density” polyethylene produced by the high pressure free radical catalysed polymerisation of ethylene. Such polymers and copolymers are used extensively in the manufacture of flexible blown film.
In recent years the use of certain metallocene catalysts (for example biscyclopentadienylzirconiumdichloride activated with alumoxane) has provided catalysts with potentially high activity. However, metallocene catalysts of this type suffer from a number of disadvantages, for example, high sensitivity to impurities when used with commercially available monomers, diluents and process gas streams, the need to use large quantities of expensive alumoxanes to achieve high activity, and difficulties in putting the catalyst on to a suitable support.
Patent Application WO98/27124 published on Jun. 25, 1998 discloses that ethylene may be polymerised by contacting it with certain iron or cobalt complexes of selected 2,6-pyridinecarboxaldehydebis(imines) and 2,6-diacylpyridinebis(imines).
An object of the present invention is to provide a novel catalyst suitable for polymerising monomers, for example, olefins, and especially for polymerising ethylene alone or for copolymerising ethylene with higher 1-olefins. A further object of the invention is to provide an improved process for the polymerisation of olefins, especially of ethylene alone or the copolymerisation of ethylene with higher 1-olefins to provide homopolymers and copolymers having controllable molecular weights. For example, using the catalysts of the present invention there can be made a wide variety of polyolefins such as, for example, liquid polyolefins, oligomers, linear alpha-olefins, resinous or tacky polyolefins, solid polyolefins suitable for making flexible film and solid polyolefins having high stiffness.
SUMMARY OF THE INVENTION
The present invention provide nitrogen containing transition metal complexes having the following Formula.
wherein
M is Fe[II], Fe[III], Ni[II], Co[I], Co[II], Co[III], V[III], Mn[I], Mn[II], Mn[III], Mn[IV], Ru[II], Ru[III] or Ru[IV]; Pd[II], V[III], V[IV] or V[V].
X represents an atom or group covalently or ionically bonded to the transition metal M;
R is independently selected from hydrogen, halogen, hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl or substituted heterohydrocarbyl;
Z is a bridging group comprising a donor atom of N, P or S or alternatively is a neutral group comprising a C
1
-C
4
alkylene group, a silyl or germyl group, and
n=an integer to satisfy the valency of M.


REFERENCES:
patent: 6133387 (2000-10-01), Xu et al.
patent: 6239237 (2001-05-01), Xu et al.
patent: WO 98/30609 (1998-07-01), None
M. Witt, et al., “Synthesis and Structural Characterization of P-Functionalized Metallacyclophosphazenes”, Chemical Abstracts, 127:116633d, Columbus, Ohio, US, vol. 127, No. 8, p. 1273 (1997).
M. W. Avis et al., “Reactions of bis(iminophosphoranes with palladium(II) dichloride: metal-induced tautomerization orthopalladation and unexpected platinum-assisted [2 + 2] cycloaddition of an aryl-nitrile, with a phosphinimine moiety”, Journal of Organometallic Chemistry 527, pp. 263-276, (1997).
M. Rietzel, et al., “Formation of Spirocyclic Imidophosphinato Complexes: Crystal Structures of [V(OPPh2NPPh2O)2O] and [Mo(NPPh2NPPh2O)2Cl2]”, J. Chem. Soc. Dalton Trans., pp. 1285-1290, (1991).
H. W. Roesky, et al., “A Volatile Cyclic Metallaphosphazene; Preparation and X-Ray Structure of [(CF3)2PN]2NVCl2”, J. Chem. Soc., Chem. Commun., pp., 366-367, (1989).

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