Olefin oligomerization catalysts, their production and use

Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – Polymers from only ethylenic monomers or processes of...

Reexamination Certificate

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C526S133000, C526S134000, C526S165000, C526S352000, C585S521000, C585S523000, C585S525000, C585S527000

Reexamination Certificate

active

06531555

ABSTRACT:

FIELD OF THE INVENTION
This invention relates to a new family of olefin, in particular ethylene oligomerization catalysts based upon phenoxide complexes of transition metals and methods for their use.
BACKGROUND OF THE INVENTION
Alpha-olefins, especially those containing 4 to about 20 carbon atoms, are important items of commerce, with about 1.5 million tons reportedly being produced in 1992. The alpha-olefins are used as intermediates in the manufacture of detergents, as monomers (especially in linear low density polyethylene), and as intermediates for many other types of products. As a consequence, improved methods of making these compounds are of interest.
Most commercially produced alpha-olefins are made by the oligomerization of ethylene, catalyzed by various types of compounds, see for instance B. Elvers, et al., Ed. Ullmann's Encyclopedia of Industrial Chemistry, Vol. A13, VCH Verlagsgesellschaft mbH, Weinheim, 1989, p. 243-247 and 275-276, and B. Cornils, et al., Ed., Applied Homogeneous Catalysis with Organometallic Compounds, A Comprehensive Handbook, Vol. 1, VCH Verlagsgesellschaft mbH, Weinheim, 1996, p. 245-258. The major types of commercially used catalysts are alkylaluminum compounds, certain nickel-phosphine complexes, and a titanium halide with a Lewis acid such as AlCl
3
. In all of these processes significant amounts of branched and/or internal olefins and/or diolefins, are produced. Since in most instances these are undesired, and often difficult to separate from the desired linear alpha-olefins, minimization of these byproducts is desirable.
Examples of new ethylene oligomerization catalysts which produce high purity alpha-olefins have recently appeared. Brookhart recently developed iron-based catalysts, which produce either high molecular weight HDPE or high purity &agr;-olefins, depending on the extent of steric effects of ligand substituents. (Small, B. L.; Brookhart, M.
J. Am. Chem. Soc.
1998, 120, 7143; U.S. Pat. No. 6,103,946.) These iron-based ethylene oligomerization catalysts exhibit very high catalytic activities and produce highly pure alpha-olefins. However, use of these catalysts to produce alpha-olefin comonomers in situ for polymerization by, for example, metallocene catalysts, could be confounded by potential incompatibilities between the iron and metallocene catalysts.
Bazan utilized electronic control of molecular weight in his studies with Zr-boratabenzene catalysts. (Rogers, J. S.; Bazan, G. C.; Sperry, C. K.
J. Am. Chem. Soc.
1997, 119, 9305.) B-Ph boratabenzene complexes were observed to produce polyethylene, but the less electron-rich B-OMe boratabenzene analog catalyzed ethylene oligomerization. By incorporating an electron withdrawing substituent on boron, the electrophilicity of the catalyst was increased which resulted in an increased &bgr;-H elimination rate and lower molecular weight product. Like the Brookhart Fe catalyst, Bazan's boratabenzene catalyst exhibits extremely high selectivity for &agr;-olefin production. The catalytic activity of the boratabenzene-Zr catalyst is much lower than that required for commercial operation in a tandem oligomerization/polymerization process using a metallocene polymerization catalyst.
Transition metal complexes of salicylimine ligands have recently been reported which are extremely active polymerization catalysts. Grubbs et al (Organometallics, Vol 17, 1988 page 3149-3151; WO 98/42664) disclose that nickel (II) salicylaldiminato complexes, combined with B(C
6
F
5
)
3
, reacted with ethylene to form polyethylene with MW=49,500.
Ethylenebis(salicylideneiminato)zirconium dichloride combined with methyl alumoxane deposited on a support and unsupported versions were used to polymerize ethylene by Repo et al in Macromolecules 1997, 30, 171-175.
EP 241,560 A1 (Sumitomo) discloses alkoxide ligands in transition metal catalyst systems.
EP 0 874 005 A1 discloses salicylimine compounds for use as polymerization catalysts.
WO 00/37512 discloses a family of olefin polymerization catalysts based upon phenoxide complexes of transition metals.
In all of the above cases, salicylimine transition metal complexes reacted with ethylene to produce polyethylene, not ethylene oligomers or alpha-olefins. Described herein is a new class of salicylimine-based ethylene oligomerization catalysts having high activity and high selectivity for alpha-olefin. One application of these catalysts is their use in a mixed catalyst system which produces linear low density polyethylene (LLDPE) using only ethylene feedstock.
SUMMARY OF THE INVENTION
This invention relates to a process to produce alpha-olefins comprising contacting ethylene with a catalyst system comprising an activator and one or more metal catalyst compounds represented by the following formula:
wherein
R
3
, R
4
, R
5
, R
8
, R
9
and R
10
may each independently be hydrogen, a halogen, a heteroatom containing group or a C
1
to C
100
group, provided that at least one of these groups has a Hammett &sgr;
p
value (Hansch, et al Chem. Rev. 1991, 91, 165) greater than 0.20;
R
2
and R
7
may each independently be alkyl, aryl or silyl groups preferably tertiary alkyl, tertiary silyl or aryl groups;
R
1
and R
6
may each independently be an alkyl group, an aryl group, an alkoxy group, or an amino group, preferably a C
1
to C
5
primary alkyl group;
N is nitrogen;
H is hydrogen;
O is oxygen;
M is a group 4 transition metal; and
each X may each independently be an anionic ligand such as halide, alkyl, aryl, hydride, carboxylate, alkoxide or amide, or a dianionic ligand, such as a dialkoxide or diamide.
These catalyst compounds may be activated with activators including alkyl aluminum compounds (such as diethylaluminum chloride), alumoxanes, modified alumoxanes, non-coordinating anions, non-coordinating group 13 metal or metalliod anions, boranes, borates and the like.
This invention further relates to the production of polymer by introducing ethylene, a polymerization catalyst and a catalyst system as described above into a polymerization reactor. Preferably the polymer produced is an ethylene homopolymer or an ethylene co-polymer.


REFERENCES:
patent: 6410664 (2002-06-01), Bansleben et al.
patent: 0 241 560 (1986-10-01), None
patent: 0 874 005 (1998-10-01), None
patent: WO 98/42664 (1998-10-01), None
patent: WO 00/37512 (2000-06-01), None
Rogers, J. S., et al.Ethoxyboratabenzene Zirconium Complexes: Catalysts for &agr;-Olefin Production, J. Am. Chem. Soc. 1997, 119, 9305-9306.
Wang, et al.,Neutral Nickel(II)-Based Catalysts for Ethylene Polymerization, Organometallics, 1998, 17, 3149-3151.
Repo et al.,Ethylenebis(salicylindeneiminato)zirconium Dichloride: Crystal Structure and Use as a Heterogeneous Catalyst in the Polymerization of Ethylene, Macromolecules 1997, 30, 171-175.

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