Addition polymerization catalysts, processes for their preparation, precursors therefor and methods of use

Abstract: Hafnium, titanium or zirconium coordination complexes comprise a cyclopentadienyl or substituted cyclopentadienyl group forming part of a ring structure in which the metal is both bonded to the (substituted) cyclopentadienyl group by a divalent moiety of specified type containing one or more heteroatoms and held in association with the (substituted) cyclopentadienyl moiety. These complexes form addition polymerization catalysts with activating cocatalysts such as Lewis acids, ammonium salts, oxidizing agents and, especially, aluminum compounds, particularly aluminum trialkyls. Novel polymers, including ElPE resins and pseudo-random copolymers, can be obtained using the catalysts.

Description: The present invention relates to metal coordination complexes. The invention also relates to certain novel addition polymerization catalysts comprising such metal complexes. Furthermore, the invention relates to methods for the polymerization of addition polymerizable monomers and to the resulting polymers. Because of the exposure of the active metal site of the metal coordination complexes of the invention, catalysts resulting therefrom have unique properties. Under certain conditions, the catalysts of the invention are capable of preparing novel olefin polymers having previously unknown properties due to their unique facile abilities to polymerize α-olefins, diolefins, hindered vinylidene aliphatic monomers, vinylidene aromatic monomers and mixtures thereof. Numerous metal coordination complexes are known in the art including such complexes involving monocyclopentadienyl groups and substituted monocyclopentadienyl groups. The present metal coordination complexes differ from those previously known in the art due to the fact that the metal is bound to a cyclopentadienyl or substituted cyclopentadienyl or similar group by both a η 5 -bond and a bridging linkage including other ligands of the metal. Also previously known in the art are transition metal coordination complexes known as tucked complexes. Such complexes are described in Organometallics 6, 232-241 (1987). In US Serial No. 8,800, filed January 30, 1987 (published in equivalent form as EP-A-0277004) there are disclosed certain bis(cyclopentadienyl) metal compounds formed by reacting a bis(cyclopentadienyl) metal complex with salts of Bronsted acids containing a noncoordinating compatible anion. The reference discloses the fact that such complexes are usefully employed as catalysts in the polymerization of olefins. The foregoing catalysts are not considered to be particularly effective olefin polymerization catalysts. Previous attempts to prepare copolymers of vinylidene aromatic monomers and α-olefins, in particular copolymers of styrene and ethylene, have either failed to obtain substantial incorporation of the vinylidene aromatic monomer or else have achieved polymers of low molecular weight. In Polymer Bulletin, 20, 237-241 (1988) there is disclosed a random copolymer of styrene and ethylene containing 1 mole percent styrene incorporated therein. The reported polymer yield was 8.3 x 10 -4 grams of polymer per micromole titanium employed. Thomas Kükenhöhner disclosed, in a thesis entitled "Untersuchungen zur Darstellung Chiraler Organotitan (IV) Verbindung für Enantioselektive Synthesen" submitted in August 1983 to Fachbereich Chemie der Philipps-Universität Marburg, 1-oxy-3-cyclopentadienyl-propane-1,3-diyl titanium (IV) complexes in which the propanediyl moiety is optionally substituted with alkyl. The exemplified complexes are 1-oxy-1-tert. butyl-3-dimethyl-3-cyclopentadienyl-propane-1,3-diyl titanium dihalides, dimethyl and halide methyl. No use is specified for the complexes. J. Okuda (Chem. Ber. 123 (1990) 1649-1651; published August 1990) discloses (tert. butylamido)(dimethyl)(3-tert.butyl-cyclopentadienyl) silane titanium dichloride. No use of the complex is specified. EP-A-0420436 discloses inter alia metal Formula A wherein M is titanium, zirconium or hafnium and is in its highest formal oxidation state (+4, d 0 complex); (C 5 H 5-y-x R x ) is (i) a cyclopentadienyl ring which is substituted with from zero to five substituent groups R, x is 0, 1, 2, 3, 4 or 5 denoting the degree of substitution, and each substituent group R is, independently, a C 1 -C 20 hydrocarbyl radical, a substituted C 1 -C 20 hydrocarbyl radical wherein one or more hydrogen atoms is replaced by a halogen atom, C 1 -C 20 hydrocarbyl-substituted metalloid radical wherein the metalloid is of Group 14 of the periodic Table of the Elements, or a halogen atom or (ii) a cyclopentadienyl ring in which two adjacent R-groups are joined forming a C 4 -C 20 ring to give a saturated or unsaturated polycyclic cyclopentadienyl ligand; (JR' z-1-y ) is a heteroatom ligand in which J is an element with a coordination number of three from Group 15 or an element with a coordination number of two from Group 16 of the Periodic Table of the Elements, and each R' is, independently a C 1 -C 20 hydrocarbyl radical or a substituted C 1 -C 20 hydrocarbyl radical wherein one or more hydrogen atoms is replaced by a halogen atom, and z is the coordination number of the element J; each Q is independently a univalent anionic ligand, provided that where any Q is a hydrocarbyl such Q is different from (C 5 H 5-y-x R x ), or both Q together are a divalent anionic chelating agent; B is a covalent bridging group containing an element of Group 14 or 15 of the Periodic Table of the Elements; L is (i) a Lewis base or (ii) a second transition metal compound of the same type such that the two metal centers M and M' are bridged by Q and Q', wherein M' has the same meaning as M and Q' has the same meaning as Q; w is a number from 0 to 1; and y is 0 or 1 when w is greater than 0 and y is 1 when w is 0. Said metal coordination complexes of EP-A-0420436 are for use with an aluminoxane as a catalyst for olefin polymerization. EP-A-0418044 (published 20th March 1991) discloses inter alia catalysts corresponding to Formula B: - CpMX n + A - wherein: Cp is a single η 5 -cyclopentadienyl or η 5 -substituted cyclopentadienyl group optionally covalently bound to M through a substituent; M is hafnium, titanium or zirconium bound in an η 5 bonded mode to the cyclopentadienyl or substituted cyclopentadienyl group; X is independently each occurrence hydride or a moiety selected from halo, alkyl, aryl, silyl, germyl, aryloxy, alkoxy, amide, siloxy and combinations thereof having of up to 20 non-hydrogen atoms, and neutral Lewis base ligands having up to 20 non-hydrogen atoms or optionally one X together with Cp forms a metallocycle with M of up to 20 non-hydrogen atoms; R is alkyl or aryl of up to 10 carbons; n is 1 or 2 depending on the valence of M; and A - is a noncoordinating, compatible anion of a Bronsted acid salt. The present invention provides metal monocyclopentadienyl coordination complexes corresponding to the formula I: wherein: M is hafnium, zirconium or, preferably titanium; Cp* is a cyclopentadienyl or substituted cyclopentadienyl group bound in an η 5 bonding mode to M; Z is SiR* 2 , CR* 2 , SiR* 2 SiR* 2 , CR* 2 CR* 2 , CR*=CR*, CR* 2 SiR* 2 , GeR* 2 , BR*, or BR* 2 ; and R* each occurrence is hydrogen or a moiety selected from alkyl, aryl, silyl, halogenated alkyl, halogenated aryl groups and combinations thereof (e.g. aralkyl, alkaryl, haloalkaryl and haloaralkyl) having up to 20 non-hydrogen atoms, or two or more R* groups from Z or both Y and Z form a fused ring system; X each occurrence is an anionic ligand group or neutral Lewis base ligand group having up to 30 non-hydrogen atoms; n is 1, 2, 3, or 4 depending on the valence of M; and Y is a neutral two electron donor ligand selected from OR*, SR*, NR* 2 , and PR* 2 and bound to M by a coordinate-covalent bond. The metal coordination complexes of the invention are used with an activating cocatalyst in addition polymerizations. Use of the catalysts can provide ElPE polymers which are highly elastic, interpolymers of ethylene and one or more olefins other than ethylene. Further, use of the catalysts can provide pseudo-random interpolymers of an α-olefin, particularly ethylene and a vinylidene aromatic monomer, a hindered aliphatic vinylidene monomer, or a mixture thereof. The complexes of the invention are usefully employed as catalysts for addition polymerization processes to prepare polymers that are useful as molded articles, films for packaging applications, and foams for cushioning applications; and in the modification of synthetic and naturally occurring resins. The complexes may also be used as catalysts for hydrogenations, catalytic cracking processes, and in other industrial applications. The term "activating cocatalyst" as used herein refers to a secondary component of the catalyst able to cause the metal-containing complex to become effective as an addition polymerization catalyst or alternatively to balance the ionic charge of a catalytically activated species. Examples of the foregoing activating cocatalysts for use herein include aluminum compounds containing an Al-O bond such as the alkylaluminoxanes, especially methylalumin-oxane; aluminum alkyls; aluminum halides; aluminum alkylhalides; Lewis acids; ammonium salts; noninterfering oxidizing agents, e.g. silver salts, and ferrocenium ions; and mixtures of the foregoing. Particular techniques for the preparation of aluminoxane type compounds by contacting an aluminum alkyl compound with an inorganic salt containing water of crystallization are disclosed in US-A-4,542,119. In a particularly preferred embodiment an aluminum alkyl compound is contacted with a regeneratable water-containing substance such as hydrated alumina, silica, or other substance. A process for preparing aluminoxane employing such regeneratable substance is disclosed in EP-A-0338,044. Additional suitable activating cocatalysts include compounds corresponding to the formula: AlR n X" 3-n wherein: R is each occurrence C 1-10 alkyl or aralkyl; X" is halogen; and n is 1, 2 or 3. Most preferably such cocatalysts are trialkyl aluminum compounds, particularly triethyl aluminum. "Addition polymerizable monomers" include, for example, ethylenically unsaturated monomers, acetylenic compounds, conjugated or nonconjugated dienes, and polyenes (e.g. C 1 -C 20 polyenes). Preferred monomers include the C 2-10 α-olefins especially ethylene, propylene, isobutylene, 1-butene, 1-hexene, 4-methyl-1-pentene, and 1-octene. Other preferred monomers include styrene, halo- or alkyl substituted styrene, vinyl chloride, acrylonitrile, methyl acrylate, methylmethacrylate, tetrafluoroethylene, methacrylonitrile, vinylidene chloride, vinylbenzocyclobutane, and 1,4-hexadiene. By the term "hindered aliphatic vinylidene compounds" is meant addition polymerizable vinylidene monomers corresponding to the formula: CG 2 =CG'R" wherein R" is an sterically bulky, aliphatic substituent of up to 20 carbons, G independently each occurrence is hydrogen or methyl, and G' independently each occurrence is hydrogen or methyl or alternatively G' and R" together form a ring system. By the term "sterically bulky" is meant that the monomer bearing this substituent is normally incapable of addition polymerization by standard Ziegler-Natta polymerization catalysts at a rate comparable with ethylene polymerizations. Preferred hindered aliphatic vinylidene compounds are monomers in which one of the carbon atoms bearing ethylenic unsaturation is tertiary or quaternary substituted. Examples of such substituents include cyclic aliphatic groups such as cyclohexane, cyclohexene, cyclooctene, or ring alkyl or aryl substituted derivatives thereof, tert-butyl, and norbornyl. Most preferred hindered aliphatic vinylidene compounds are the various isomeric vinyl-ring substituted derivatives of cyclohexene and substituted cyclohexenes, and 5-ethylidene-2-norborn-ene. Especially suitable are 1-, 3-, and 4- vinylcyclohexene. By the term "hindered vinylidene compound" is meant addition polymerizable vinylidene monomers corresponding to the formula: CG 2 =CG'R"' wherein R"' is R" or an aryl substituent of up to 20 carbons, and G and G' are as previously defined. For example, in addition to hindered aliphatic vinylidene compounds, hindered vinylidene compounds also include the vinylidene aromatic monomers. By the term "vinylidene aromatic monomers" is meant addition polymerizable compounds corresponding to the formula: CG 2 =C(G)-Ph wherein G independently each occurrence is hydrogen or methyl and Ph is phenyl, or a halo- or C 1-4 alkyl-substituted phenyl group. Preferred vinylidene aromatic monomers are monomers corresponding to the above formula wherein G each occurrence is hydrogen. A most preferred vinylidene aromatic monomer is styrene. By the term "α-olefin" is meant ethylene and the C 3-10 olefins having ethylenic unsaturation in the α-position. Preferred α-olefins are ethylene, propylene, 1-butene, isobutylene, 4-methyl-1-pentene, 1-hexene, and 1-octene, and mixtures thereof. As used herein all reference to the Periodic Table of the Elements and groups thereof shall be to the version of the table published by the Handbook of Chemistry and Physics, CRC Press, 1987, utilizing the IUPAC system for naming groups. Each carbon atom in the cyclopentadienyl radical may be substituted or unsubstituted with the same or a different radical selected from hydrocarbyl radicals, substituted-hydrocarbyl radicals wherein one or more hydrogen atoms is replaced by a halogen atom, hydrocarbyl-substituted metalloid radicals wherein the metalloid is selected from Group 14 of the Periodic Table of the Elements, and halogen radicals. In addition two or more such substituents may together form a fused ring system, for example indenyl or fluorenyl. Suitable hydrocarbyl and substituted-hydrocarbyl radicals, which may be substituted for at least one hydrogen atom in the cyclopentadienyl radical, will contain from 1 to 20 carbon atoms and include straight and branched alkyl radicals, cyclic hydrocarbon radicals, alkyl-substituted cyclic hydrocarbon radicals, aromatic radicals and alkyl-substituted aromatic radicals. Suitable organometalloid radicals include mono-, di- and tri-substituted organometalloid radicals of Group 14 elements wherein each of the hydrocarbyl groups contain from 1 to 20 carbon atoms. More particularly, suitable organometalloid radicals include trimethylsilyl, triethylsilyl, ethyldimethylsilyl, methyldiethylsilyl, phenyldimethylsilyl, methyldiphenylsilyl, triphenylsilyl, triphenylgermyl and trimethylgermyl. Suitable anionic ligand groups, X, are illustratively selected from hydride, halo, alkyl, silyl, germyl, aryl, amide, aryloxy, alkoxy, phosphide, sulfide, acyl, pseudo halides such as cyanide, azide, and acetylacetonate and mixtures thereof. As previously mentioned, the complexes according to the present invention preferably comprise structures having altered or enhanced catalytic activity at the metal site when the complex is combined with a cocatalyst. In this regard electron donating substituents have been found to improve the catalytic properties of the complexes. A preferred metal coordination complex corresponds to Formula II: wherein R' each occurrence is hydrogen or a moiety selected from alkyl, aryl, silyl, germyl, cyano, halo and combinations thereof (e.g. alkaryl, aralkyl, silyl substituted alkyl, silyl substituted aryl, cyanoalkyl, cyanoaryl, haloalkyl, haloaryl, and halosilyl) having up to 20 non-hydrogen atoms, or an adjacent pair of R' groups form a hydrocarbyl ring fused to the cyclopentadienyl moiety; X each occurrence is hydride or a moiety selected from halo, alkyl, aryl, silyl, germyl, aryloxy, alkoxy, amide, siloxy and combinations thereof (e.g. alkaryl, aralkyl, silyl substituted alkyl, silyl substituted aryl, aryloxy alkyl, aryloxyaryl, alkoxyalkyl, alkoxyaryl, amidoalkyl, amidoaryl, siloxyalkyl, siloxyaryl, amidosiloxyalkyl, haloalkyl, and haloaryl) having up to 20 non-hydrogen atoms and neutral Lewis base ligands having up to 20 non-hydrogen atoms; and M, n, Y and Z are as previously defined. It should be noted that whereas Formula I and the following Formulae indicate a cyclic structure for the catalysts, the bond between M and Y is more accurately referred to as a coordinate-covalent bond. Also, it should be noted that the complex may exist as a dimer or higher oligomer. The complexes can be prepared by contacting the metal reactant and a group I metal derivative or Grignard derivative of the cyclopentadienyl compound in a solvent and separating the salt byproduct. Suitable solvents for use in preparing the metal complexes are aliphatic or aromatic liquids such as cyclohexane, methylcyclohexane, pentane, hexane, heptane, tetrahydrofuran, diethyl ether, C 1-4 alkyl ethers of mono- or diethylene glycol, C 1-4 alkyl ethers of mono- or dipropylene glycol, benzene, toluene, xylene, and ethylbenzene, or mixtures thereof. In a preferred embodiment, the metal compound is MX n+1 , ie. M is in a lower oxidation state than in the corresponding compound, MX n+2 and the oxidation state of M in the desired final complex. A noninterfering oxidizing agent may thereafter be employed to raise the oxidation state of the metal. The oxidation is accomplished merely by contacting the reactants utilizing solvents and reaction conditions used in the preparation of the complex itself. By the term "noninterfering oxidizing agent" is meant a compound having an oxidation potential sufficient to raise the metal oxidation state without interfering with the desired complex formation or subsequent polymerization processes. A particularly suitable noninterfering oxidizing agent is AgCl. In order to assist in the handling of the metal compounds employed in the present process corresponding to the formula MX n+2 , it may be beneficial first to form a solid adduct thereof by the use of a suitable coordinating agent according to well known techniques in the art. For example, whereas titanium tetrachloride is a fuming liquid which is difficult to handle, one may first form an adduct of TiCl 4 with an ether, tertiary amine, tertiary phosphine or other basic nonprotic compound. The resulting solids may be more easily handled. A preferred coordinating adduct is tetrahydrofuran. The reactions employed in preparing the metal complex may be conducted either heterogeneously or homogeneously. That is, the various reactants or the resulting product need not be substantially soluble in the solvent mixture. Generally the reactants are contacted under an inert atmosphere for a time from several minutes to several days. Agitation may be employed if desired. The temperature of the reaction is generally from -90°C to 150°C, preferably from -20°C to 70°C. Suitable catalysts for use according to the present invention are prepared by combining the metal coordination compound and activating cocatalyst compound in any order and in any suitable manner. Preferably the ratio of the coordination complex and cocatalyst on a molar basis is from 1:0.1 to 1:10,000. It will, of course, be appreciated that the catalyst system may also be formed in situ if the components thereof are added directly to the polymerization process and a suitable solvent or diluent, including condensed monomer, is used in said polymerization process. Suitable solvents include toluene, ethylbenzene, alkanes and mixtures thereof. In certain cases the catalysts may be isolated from solution and retained under inert atmosphere prior to use. The catalysts' components are sensitive to both moisture and oxygen and should be handled and transferred in an inert atmosphere such as nitrogen, argon or helium or under vacuum. The polymerization is usually conducted according to known techniques for Ziegler-Natta or Kaminsky-Sinn type polymerizations. That is, the monomer(s) and catalyst are contacted at a temperature from -30°C to 250°C, at reduced, elevated or atmospheric pressures. The polymerization is conducted under an inert atmosphere which may be a blanketing gas such as nitrogen, argon, hydrogen, or ethylene, or under vacuum. Hydrogen may additionally be utilized in the control of molecular weight through chain termination as is previously known in the art. The catalyst may be used as is or supported on a suitable support such as alumina, MgCl 2 or silica to provide a heterogeneous supported catalyst. A solvent may be employed if desired. Suitable solvents include toluene, ethylbenzene, and excess vinylidene aromatic or olefin monomer. The reaction may also be conducted under solution or slurry conditions, in a suspension utilizing a perfluorinated hydrocarbon or similar liquid, in the gas phase, ie. utilizing a fluidized bed reactor, or in a solid phase powder polymerization. A catalytically effective amount of the present catalyst and cocatalyst are any amounts that successfully result in formation of polymer. Such amounts may be readily determined by the routine experimentation by the skilled artisan. Preferred amounts of catalyst and cocatalyst are sufficient to provide an equivalent ratio of addition polymerizable monomer:catalyst of from 1 x 10 10 :1 to 100:1, preferably from 1 x 10 8 :1 to 500:1, most preferably 1 x 10 6 :1 to 1000:1. The cocatalyst is generally utilized in an amount to provide an equivalent ratio of cocatalyst:catalyst from 10,000:1 to 0.1:1, preferably from 1,000:1 to 1:1. It is to be understood that the metal complex may undergo various transformations or form intermediate species prior to and during the course of a polymerization. Thus other precursors could possibly be conceived to achieve the same catalytic species as are herein envisioned without departing from the scope of the present invention. The resulting polymeric product is recovered by filtering or other suitable technique. Additives and adjuvants may be incorporated in the polymers of the present invention in order to provide desirable characteristics. Suitable additives include pigments, UV stabilizers, antioxidants, blowing agents, lubricants, plasticizers, photosensitizers, and mixtures thereof. In the preparation of copolymers containing vinylidene aromatic or hindered aliphatic vinyl monomers it is desirable that a comonomer that is an α-olefin that is not particularly sterically hindered also be employed. Without wishing to be bound by any particular theory of operation, it is believed this is because the active site becomes crowded with the incorporation of the hindered vinyl compound making it unlikely that another hindered vinyl compound could enter into the polymerization as the next monomer in the sequence. After the incorporation of one or more olefins other than a hindered vinyl compound the active site once again becomes available for inclusion of a hindered vinyl monomer. On a limited basis however, the vinylidene aromatic monomer or sterically hindered vinyl monomer may insert into the polymer chain in reverse order, ie. so as to result in two methylene groups between the substituted polymer backbone moiety. Preferably such polymers possess a Mw of greater than 13,000, more preferably greater than 20,000 and most preferably greater than 30,000. Also preferably such polymers possess a melt index (I 2 ), ASTM D-1238 Procedure A, condition E, of less than 125, more preferably from 0.01 - 100 and most preferably from 0.1 to 10. Due to the use of the previously mentioned catalyst system comprising a coordination complex of the invention, copolymers may be prepared that incorporate relatively bulky or hindered monomers in substantially random manner at low concentrations, and at higher concentrations according to an ordered insertion logic. The copolymers of α-olefins, especially ethylene and a hindered aliphatic vinylidene compound or vinylidene aromatic monomer can further be described as "pseudo-random". That is, the copolymers lack well defined blocks of either monomer, however the respective monomers are limited to insertion according to certain rules. These rules were deduced from certain experimental details resulting from an analysis of the polymers. The polymers were analyzed by 13 C NMR spectroscopy at 130°C with a Varian VXR-300 spectrometer at 75.4 MHz. Samples of 200 to 250 mg polymer were dissolved in 15 mL of hot o-dichlorobenzene/1,1,2,2-tetrachloroethane-d 2 (approximately 70/30, v/v) which was approximately 0.05 M in chromium (III) tris(acetylacetonate) and a portion of the resulting solution was added to a 10 mm NMR tube. The following parameters and conditions were used: spectral width, 16,500 Hz; acquisition time 0.090 s; pulse width, 36°; delay, 1.0 s with the decoupler gated off during the delay,; FT size 32K; number of scans, >30,000; line broadening, 3Hz. Spectra, as recorded were referenced to tetrachloroethane-d 2 (δ 73.77 ppm, TMS scale). Therefor, without wishing to be bound by any particular theory, the results of the foregoing experimental procedures indicate that a particular distinguishing feature of pseudo-random copolymers is the fact that all phenyl or bulky hindering groups substituted on the polymer backbone are separated by 2 or more methylene units. In other words, the polymers comprising a hindered monomer of the present invention can be described by the following general formula (using styrene as the hindered monomer for illustration): where j, k, and l ≥ 1 In further explanation of the foregoing experimental and theoretical results, and without wishing to be bound by any particular theory it can be concluded that during the addition polymerization reaction employing the present catalysts, if a hindered monomer is inserted into the growing polymer chain, the next monomer inserted must be ethylene or a hindered monomer which is inserted in an inverted or "tail-to-tail" fashion. This is illustrated below for a hindered vinyl monomer where M is the catalyst metal center, HG is a hindering group, and P is the growing polymer chain: During the polymerization reaction, ethylene may be inserted at any time. After an inverted or "tail-to-tail" hindered monomer insertion, the next monomer must be ethylene, as the insertion of another hindered monomer at this point would place the hindering substituent closer together than the minimum separation as described above. A consequence of these polymerization rules is the catalysts of this invention do not homopolymerize styrene to any appreciable extent, while a mixture of ethylene and styrene is rapidly polymerized and may give high styrene content (up to 50 mole percent styrene) copolymers. As a further illustration of the description of the α-olefin/hindered monomer copolymer of the present invention, a computer model of the polymerization reaction was used to calculate the expected 13 C NMR spectrum of the polymer product. The computer program utilized a random number generator to select either α-olefin or hindered monomer to be inserted into a growing polymer chain, then calculated the number of each type of 13 C NMR signals resulting from that insertion. Polymers were computer generated by repeating this process for 10,000 or more monomer insertions, and the resulting calculated 13 C NMR spectrum was compared to actual experimental 13 C NMR spectra for pseudo-random ethylene/styrene copolymers of the invention. Computer simulations of the polymer and resulting 13 C NMR spectra of the calculated pseudo-random ethylene/styrene copolymers were performed using the constraint that if styrene monomer were inserted into the growing polymer chain, the next monomer inserted must be ethylene or a styrene which is inserted in an inverted or "tail-to-tail" fashion. Optimum fits between experimental and calculated spectra were obtained if approximately 15 percent of the styrene insertions are in the "tail-to-tail" manner. The observed and calculated 13 C NMR spectra for such pseudo-random ethylene/styrene copolymers containing 1.4, 4.8, 9.0, 13, 37, and 47 mole percent styrene are shown in Figures 1-6. In each case, the observed and calculated spectra are in excellent agreement. Computer simulation of the polymer and resulting 13 C NMR spectra of completely random α-olefin/hindered monomer copolymers were then performed using no constraints on hindered monomer insertion. In other words, the hindered monomer was allowed to insert into the growing polymer chain after a previous hindered monomer insertion if the random number generator selected hindered monomer as the next monomer to be inserted. The calculated spectra for these completely random copolymers do not agree with the observed 13 C NMR spectra, as shown in Figure 7 for a 37 mole percent styrene containing ethylene/styrene copolymer. Prior to polymerization according to the present process the monomers and solvents, if any, may be purified by vacuum distillation, and/or contacted with molecular sieves, silica, or alumina to remove impurities. In addition, reactive blanking agents, such as trialkyl-aluminum compounds, alkali metals and metal alloys, especially Na/K, may be used to remove impurities. Suitable vinylidene aromatic monomers which may be employed according to the present invention include styrene as well as α-methyl styrene, the C 1 -C 4 alkyl- or phenyl-ring substituted derivatives of styrene, such as ortho-, meta-, and para-methylstyrene, or mixtures thereof, the ring halogenated styrenes, vinylbenzocyclobutanes, and divinylbenzene. A preferred vinylidene aromatic monomer is styrene. In the polymerization of vinylidene aromatic monomers or hindered aliphatic vinylidene compounds and olefins the monomers are preferably combined in a proportion so as to achieve a vinylidene aromatic monomer (or hindered aliphatic vinylidene compound) content of at least 1.0 mole percent in the resulting polymer more preferably from 1.5 to less than 50 mole percent, highly preferably 5.0 to 48 mole percent, and most preferably from more than 8.0 up to 47 mole percent. Preferred operating conditions for such polymerization reactions are pressures from atmospheric to 1000 atmospheres (0.1 MPa to 100 MPa) and temperatures from 30°C to 200°C. Polymerizations at temperatures above the autopolymerization temperature of the respective monomers may contain small amounts of homopolymer polymerization products resulting from free radical polymerization. Certain of the polymers prepared according to the present invention, especially copolymers of ethylene and an α-olefin other than ethylene, are characterized by unique rheological properties. In particular, it has been found that the polymers (hereinafter called Elastic Polyethylenes or ElPEs) are less Newtonian than conventionally prepared linear polyethylene resins of similar olefin content. The polymers also have higher elastic modulus particularly at high melt indices compared to such conventional polymers. This property makes the resin especially useful in the formation of films, foams and fabricated articles, for example by blow molding techniques. The above phenomenon is more particularly defined by reference to Figure 8 wherein complex viscosity, η* measured in poise at 190°C, is plotted as a function of shear rate, ω, measured in radians per second for a typical ElPE copolymer of ethylene and 1-octene according to the invention. The slope of this curve indicates the melt is highly non-Newtonian. The actual values of η* and ω utilized in the graph are: η* ω η* ω η* ω 1.962x10 5 0.01000 3.230x10 4 0.2512 1.088x10 4 6.310 1.511x10 5 0.01585 2.713x10 4 0.3981 9.336x10 3 10.000 1.115x10 5 0.02512 2.293x10 4 0.6310 7.964x10 3 15.850 8.292x10 4 0.03981 1.966x10 4 1.0000 6.752x10 3 25.120 6.322x10 4 0.06310 1.701x10 4 1.5850 5.677x10 3 39.810 4.920x10 4 0.10000 1.464x10 4 2.5120 4.721x10 3 63.100 3.956x10 4 0.15850 1.265x10 4 3.9810 3.854x10 3 100.000 Also plotted in Figure 8 is the tan δ value of the same ElPE polymer. This value is unitless and is calculated by dividing the viscous modulus value by the elastic modulus. The actual values of tan δ and ω utilized in the graph are: tan δ ω tan δ ω tan δ ω 0.5526 0.01000 1.243 0.2512 1.718 6.310 0.5231 0.01585 1.381 0.3981 1.677 10.000 0.5771 0.02512 1.543 0.6310 1.620 15.850 0.6597 0.03981 1.615 1.0000 1.552 25.120 0.7971 0.06310 1.690 1.5850 1.475 39.810 0.9243 0.10000 1.729 2.5120 1.398 63.100 1.080 0.15850 1.737 3.9810 1.315 100.000 For improved performance in melt blowing applications preferably the tan δ value is from 0.1 to 3.0 for shear rates between 0.01-100 radian/sec. A further property of ElPE polymers is illustrated by reference to Figure 9. The elastic modulus in dynes/cm 2 , G', at 0.1 radian/sec., and 190°C for several ethylene/1-octene ElPE resins is plotted as a function of melt index. The values of melt index and elastic modulus utilized in the graph are as follows: Melt Index Elastic Modulus Melt Index Elastic Modulus Melt Index Elastic Modulus 0.10 98760 3.34 4381 18.42 9669 0.15 35220 5.34 5858 31.2 4516 0.18 35920 6.38 10480 31.53 5012 0.22 14270 10.12 5276 31.69 3238 0.45 11140 10.66 6222 41.02 2972 1.72 3003 16.28 2697 - - 2.46 10620 16.32 6612 - - Typical properties of η* and ω for a conventionally prepared polyethylene resin are provided in Figure 10 for comparison purposes. It is readily seen that ElPE resins are characterized by high elastic modulus in the melt. In particular, ElPE resins have a melt index ((I 2 ), ASTM D-1238 Procedure A, condition E), less than 200, preferably less than 125, most preferably less than 50 and an elastic modulus greater than 1000 dyne/cm 2 , more preferably greater than 2000 dyne/cm 2 . All of the foregoing rheological measurements are performed by standard techniques such as are disclosed in H. A. Barnes et al., Introduction to Rheology, Elsevier, publishing, Inc., 1989. Densities normally range from 0.85 to 0.97 g/ml, preferably from 0.89-0.97 g/ml. Molecular weight distributions (Mw/Mn) are greater than 2.0, preferably from 3.0-10.0. Typically melting points range from 50°C to 135°C. Preferred polymers additionally demonstrate properties of homogeneous polymers as defined in US-A-3,645,992, ie. ethylene copolymers having substantially random comonomer distribution within a given molecule and substantially the same ethylene/comonomer ratio between molecules. Polymers produced at elevated polymerization temperatures, especially temperatures greater than 130°C, may exhibit a heterogeneous melt curve. The polymers of the invention are further marked by high clarity. In particular the polymers have better optical properties, especially lower haze than typical ethylene polymers, making them especially well suited for film and injection molding applications. In addition those polymers comprising an olefin and a vinylidene aromatic monomer, especially ethylene and styrene, have surprisingly been found to possess elastomeric properties. Thus, such polymers are uniquely suited for use in applications for thermoplastic elastomers such as impact modification of thermoplastic and thermosetting polymers including bitumens; adhesives; and elastomeric moldings. The polymers of the invention may be modified by typical grafting, crosslinking, hydrogenation, functionalizing, or other reactions well known to those skilled in the art. With particular regard to the polymers comprising vinylidene aromatic, vinylcyclohexene, or 1,4-hexadiene functionality, the same may be readily sulfonated or chlorinated to provide functionalized derivatives according to established techniques. Additionally, the vinylcyclohexene based polymers are readily crosslinkable by reaction of the unsaturated ring functionality. The polymers of the present invention, whether or not further modified, may be blended with synthetic or natural polymers to provide blends having desirable properties. In particular polyethylene, ethylene/α-olefin copolymers, polypropylene, polystyrene, styrene/ acrylonitrile copolymers (including rubber modified derivatives thereof), syndiotactic polystyrene, polycarbonate, polyamide, aromatic polyester, polyisocyanate, polyurethane, polyacrylonitrile, silicone, and polyphenyleneoxide polymers may be blended with the polymeric compositions of the present invention. The polymeric modifier is utilized in amounts from 0.1 to 99.0 preferably 0.5 to 50 weight percent. In a highly preferred embodiment of the invention the polymers containing ethylene and styrene are elastomeric as defined in the definition of an elastomeric substance by ASTM Special Technical Bulletin No. 184 as a substance that can be stretched at room temperature to twice its length and will return to its original length upon release. In addition to modification of synthetic thermoplastics the present polymers are also usefully employed as modifiers for asphalt or bitumen compositions. Desirably the polymers of styrene/ethylene are utilized in this manner. The term "bitumen" can generally be defined as mixtures of hydrocarbons of natural or pyrogenous origin or combinations of both, frequently accompanied by their non-metallic derivatives, which may be gaseous, liquid, semi-solid or solid, and which are usually soluble in carbon disulfide. For the purposes of the present invention, bitumen of a liquid, semi-solid or solid nature may be utilized. From a commercial standpoint, bitumen is generally restricted to asphalts and tars and pitches. A listing of various bituminous materials which can be utilized in the present invention include the following: I. Asphalts 1. Petroleum Asphalts A. Straight-reduced asphalts 1. Atmospheric or reduced-pressure reduction 2. Solvent precipitated, as with propane B. Thermal asphalts, as residues from cracking operations on petroleum stocks C. Air-blown asphalts 1. Straight-blown 2. "Catalytic"-blown 2. Native Asphalts A. With mineral content below 5 percent 1. Asphaltites such as gilsonite, graphamite, and glance pitch 2. Bermudez and other natural deposits B. With mineral content over 5 percent 1. Rock asphalts 2. Trinidad and other natural deposits II. Tars and Derivatives 1. Residua from coke-oven-dried coal tars A. Coal tars reduced to float grades, as RT (road tar) grades for paving purposes B. Coal-tar pitches, with reduction carried out to softening-point grades 2. Residua from other pyrogenous distillates as from water-gas, wood, peat, bone, shale, rosin, and fatty acid tars. As can be readily appreciated by those skilled in the art, the weight average molecular weight of the various bitumens can vary over a very wide range, for example such as from 500 to 10,000. Additionally, the softening point of the various types of asphalt will also vary such as from 50°F to 400°F (10°C to 205°C). Of the many types of asphalts which may be utilized, petroleum, and native are desired, with petroleum being preferred. Of the petroleum asphalts, the thermal asphalts are preferred. The amount of bitumen utilized in the compositions of the invention preferably ranges from 65 to 99 parts by weight with preferred amounts ranging from 80 to 98 parts by weight. Having described the invention the following example is provided as further illustration and s not to be construed as limiting. Unless stated to the contrary parts and percentages are based on weight. Example 1 Preparation of (Tetramethyl-η 5 -cyclopentadienyl)dimethyl(1-methylethoxy)silanetitanium trichloride (a) (Tetramethylcyclopentadienyl)dimethyl(1-methylethoxy)-silane To 1.0 g (4.8 mmol) (tetramethylcyclopentadiene)dimethylsilyl chloride in 10 mL toluene was added 0.38 mL (5.0 mmol) 2-propanol followed by 0.66 mL (4.7 mmol) triethylamine. The mixture was filtered and the solids washed with mixed C 6 alkane solvent. The wash and the filtrate were combined and concentrated under reduced pressure to give a pale yellow liquid. 1 H NMR (benzene-d 6 ) δ 3.85 (heptet, 1, J = 6.0), 2.9 (s, 1.1), 2.03 (s, 5.7), 1.8 (s, 6.3), 1.10 (d, 6.3, J = 6.0), -0.02 (s, 5.0). (b) Potassium (dimethyl(1-methylethoxy)silyl)-tetramethyl-cyclopentadienide) To 0.51 g (2.1 mmol) (tetramethylcyclopentadienyl)-dimethyl(1-methylethoxy)silane in toluene was added 0.33 g (2.5 mmol) potassium benzide. The solution was filtered after 3 days and the solvent was removed under reduced pressure to give an oil. The oil was washed with pentane. Residual pentane was removed under reduced pressure to give an orange glassy solid. 1 H NMR (THF-d 8 ) δ 3.89 (heptet, 1, J = 6.1), 2.00 (s,6.1), 1.87 (s, 5.7), 1.05 (d, 5.1, J = 6.1), 0.22 (s, 4.4). (c) (Tetramethyl-η 5 -cyclopentadienyl)dimethyl(1-methylethoxy)silanetitanium trichloride To 0.42 g (1.1 mmol) TiCl 3 ·3THF in 50 mL THF was added dropwise 0.83 mmol potassium (dimethyl(1-methylethoxy)-silyl)tetramethylcyclopentadienide) in 15 mL THF. One hour after addition was complete 0.2 g (1.3 mmol) AgCl was added. The resulting mixture was stirred for 18 h. The solvent was removed under reduced pressure and the residue extracted with pentane. The pentane extracts were filtered, combined, and evaporated to a red oil. The red oil was slurried in pentane and the mixture was filtered. The filtrate was stored art -30°c for 3 weeks which resulted in the precipitation of an orange solid. The solution was decanted from the solid. 1 H NMR (benzene-d 6 ) δ 3.8(heptet, 1, J = 6.0), 2.35 (s, 6.9), 1.86 (s, 7.4), 1.04 (d, 7.1, J = 6.0), 0.45(s, 6.7) .00(s), 1.97 (s), 0.35 (s).

Claims: A metal monocyclopentadienyl coordination complex corresponding to the formula I: wherein: M is hafnium, zirconium or titanium; Cp* is a cyclopentadienyl or substituted cyclopentadienyl group bound in an η 5 bonded mode to M; X each occurrence is an anionic ligand group or neutral Lewis base ligand group having up to 30 non-hydrogen atoms; n is 1, 2, 3 or 4 depending on the valence of M; and Y is a neutral two electron donor ligand selected from OR*, SR*, NR* 2 and PR* 2 and bound to M by a coordinate-covalent bond; Z is SiR* 2 , CR* 2 , SiR* 2 SiR* 2 , CR* 2 CR* 2 , CR*=CR*, CR* 2 SiR* 2 , GeR* 2 , BR*, or BR* 2 ; and R* each occurrence is hydrogen or a moiety selected from alkyl, aryl, silyl, halogenated alkyl, halogenated aryl groups, and combinations thereof having up to 20 non-hydrogen atoms or two or more R* groups from Z or both Y and Z form a fused ring system. A metal coordination complex as claimed in Claim 1, wherein n is 1, 2 or 3 depending on the valence of M. A metal coordination complex as claimed in Claim 1 or Claim 2, wherein M is titanium. A metal coordination complex as claimed in Claim 1 or Claim 2, wherein the substituted cyclopentadienyl group is cyclopentadienyl substituted by one or more C 1-20 hydrocarbyl, C 1-20 halohydrocarbyl, halogen or C 1-20 hydrocarbyl-substituted Group 14 metalloid or is indenyl, tetrahydroindenyl, fluorenyl or octahydrofluorenyl. A metal coordination complex as claimed in any one of the preceding claims, wherein each X is selected from hydride, halo, alkyl, silyl, germyl, aryl, amide, aryloxy, alkoxy, siloxy, phosphide, sulfide, acyl, cyanide, azide, acetylacetonate and combinations thereof. A metal coordination complex as claimed in Claim 1 corresponding to Formula II: wherein R' each occurrence is hydrogen or a moiety selected from alkyl, aryl, silyl, germyl, cyano, halo, or a combination thereof having up to 20 non-hydrogen atoms or an adjacent pair of R' groups form a hydrocarbyl ring fused to the cyclopentadienyl moiety; X each occurrence is hydride or a moiety selected from halo, alkyl, silyl, germyl, aryl, amide, aryloxy, alkoxy, siloxy and combinations thereof having up to 20 non-hydrogen atoms and neutral Lewis base ligands having up to 20 non-hydrogen atoms; and M, n, Y and Z are as defined in Claim 1. A metal coordination complex as claimed in Claim 6, wherein M is titanium. A metal coordination complex as claimed in Claim 1 or Claim 6, wherein Y is NR* 2 . A metal coordination complex as claimed in Claim 1 or Claim 6, wherein Y is OR*. A metal coordination complex as claimed in Claim 6, wherein R' each occurrence is hydrogen or alkyl or R' on the cyclopentadienyl moiety form a hydrocarbyl ring fused to the cyclopentadienyl moiety. A metal coordination complex as claimed in Claim 1 or Claim 6, wherein X is alkyl. A metal coordination complex as claimed in Claim 1 or Claim 6, wherein X is halo. A metal coordination complex as claimed in Claim 1 or Claim 6, wherein X is aralkyl. A metal coordination complex as claimed in Claim 1 or Claim 6, wherein Z is SiR* 2 . A metal coordination complex as claimed in Claim 1 or Claim 6, wherein n is 1. A metal coordination catalyst as claimed in Claim 1 or Claim 6, wherein n is 2. A metal coordination catalyst as claimed in Claim 1 or Claim 6, wherein n is 3. A metal coordination catalyst as claimed in Claim 1 or Claim 6, wherein R* is hydrogen or alkyl. (Tetramethyl-η 5 -cyclopentadienyl)-dimethyl(1-methylethoxy)silane titanium trichloride. A catalyst useful in addition polymerizations comprising a) a metal coordination complex as claimed in any one of Claims 1 to 19, and b) an activating cocatalyst. A catalyst as claimed in Claim 20, wherein said activating cocatalyst comprises an aluminum compound. A catalyst as claimed in Claim 20, wherein said aluminum compound is an alkylaluminoxane. A catalyst as claimed in Claim 20, wherein said aluminum compound is not an alkylaluminoxane. A catalyst as claimed in Claim 21, wherein said aluminum compound is an alkylaluminoxane, aluminum alkyl, aluminum halide, or aluminum alkylhalide. A catalyst as claimed in Claim 20, wherein the activating cocatalyst is selected from compounds corresponding to the formula: AlR n X" 3-n wherein: R is each occurrence C 1-10 alkyl or aralkyl; X" is halogen; and n is 1, 2 or 3. A process for preparing a catalyst as claimed in Claim 20, comprising contacting a complex as defined in any one of Claims 1 to 19 with an activating cocatalyst. A process for preparing a catalyst as claimed in Claim 26, wherein the activating cocatalyst is as defined in any one of Claims 20 to 25. An addition polymerization process for preparing a polymer by contacting one or more addition polymerizable monomers with a catalyst under addition polymerization conditions characterized in that the catalyst is as defined in any one of Claims 20 to 25. A process as claimed in Claim 28, wherein the addition polymerizable monomers are selected from ethylenically unsaturated monomers, acetylenic compounds, conjugated or nonconjugated dienes, and polyenes having from 2 to 20 carbons. A process as claimed in Claim 29, wherein an alpha olefin is copolymerized with a vinylidene aromatic or hindered aliphatic vinyl monomers. A process as claimed in Claim 30, wherein ethylene is copolymerized with styrene or vinylcyclohexene. A process for preparing a copolymer of a hindered aliphatic vinylidene monomer and an alpha-olefin wherein the hindered aliphatic vinylidene monomer is contacted with the alpha-olefin under polymerization conditions in the presence of a catalyst comprising a) a metal coordination complex as defined in any one of Claims 1 to 19 b) an activating cocatalyst. A process as claimed in Claim 32, wherein the activating cocatalyst is as defined in any one of Claims 21 to 25. A process as claimed in Claim 32 or Claim 33, wherein the hindered aliphatic vinylidene monomer is one in which the carbon atoms bearing ethylenic unsaturation is tertiary or quaternary substituted. A process as claimed in Claim 34, wherein said carbon atom is substituted by a cyclic aliphatic group. A process as claimed in Claim 35, wherein the hindered aliphatic vinylidene monomer is 1-, 3- or 4-vinylcyclohexene or 5-ethylidene-2-norbornene. A process as claimed in any one of Claims 28 to 36, wherein the catalyst is formed in situ. A heterogeneous supported catalyst comprising a metal coordination complex corresponding to the Formula I as defined in Claim 1 and an activity cocatalyst. A heterogeneous supported catalyst as claimed in Claim 38, wherein the metal coordination complex is as defined in any one of Claims 2 to 8. A heterogeneous supported catalyst as claimed in Claim 39, wherein the support is selected from alumina, MgCl 2 and silica.

Inventors: KNIGHT GEORGE W, LAI SHIH-YAW, NICKIAS PETER N, ROSEN ROBERT K, SCHMIDT GREGORY F, STEVENS JAMES C, TIMMERS FRANCIS J, WILSON DAVID R, KNIGHT, GEORGE W., LAI, SHIH-YAW, NICKIAS, PETER N., ROSEN, ROBERT K., SCHMIDT, GREGORY F., STEVENS, JAMES C., TIMMERS, FRANCIS J., WILSON, DAVID R.
Applicants: DOW CHEMICAL CO, THE DOW CHEMICAL COMPANY
Application year: 1990
Main classification: C07F17
IPC codes: C07F9, C07F7, C08L23, C08L25, C08F4, C08F210, C08F110, C08F10, C08F8, C07F17, C07F5