Process for preparation of syndiotactic vinyl aromatic polymers

Abstract: A process for preparing syndiotactic vinyl aromatic polymers comprising contacting one or more aromatic monomers under polymerization conditions with a catalyst corresponding to the formula: [Cp m MX n X′p]⁺A⁻ wherein: Cp is a single η⁵-cyclopentadienyl or η⁵-­ substituted cyclopentadienyl group; M is a metal of Group 3, 4, 5, 6, 8, 9, 10 or the Lanthanide Series of the Periodic Table; X each occurrence is an inert anionic lignd, with the proviso that at least one X is R; X′ is an inert, neutral, donor ligand; R is hydrocarbyl, silyl, a combination thereof or a substituted derivative thereof having up to 20 carbon, silicon or carbon and silicon atoms; m and p are independently 0 or 1; n is an integer greater than or equal to 1; the sum of m and n is equal to the valence of M; and A⁻ is a noncoordinating, compatible anion of a Bronsted acid salt.

Description: The present invention relates to a process for polymerizing vinyl aromatic monomers, such as styrene, to produce polymers having a high degree of syndiotacticity, and more particularly to a process for preparing polymers of vinyl aromatic monomers having a high degree of syndiotacticity using an alkylaluminoxane-free catalyst. Such polymers may be usefully employed in the preparation of solid objects and articles such as a moldings, films, sheets and foamed objects by molding, casting or the like process. In US-A-4,680,353 there is disclosed a process for the preparation of polymers of vinyl aromatic monomers having a stereoregular structure of high syndiotacticity by the use of certain coordination catalysts. Particularly disclosed were the reaction products of a titanium compound and an organoaluminum compound, especially polymethylaluminoxane. The process disclosed in this patent, however, requires the use of large amounts of the polymethylaluminoxane which is very expensive and difficult to make due to its very complex structure. Also, this process requires an expensive polymer purification system to remove remaining catalyst components due to the use of large amounts of the polymethylaluminoxane. In 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 non-coordinating compatible anion. The reference discloses the fact that such complexes are usefully employed as catalysts in the polymerization of olefins. EP-A-0418044 (published on 20th March 1991 in pursuance of European Patent Application No. 90309962.0 filed 12th September 1990 designating BE, DE, ES, FR, GB, IT, NL & SE and claiming priority from US Patent Applications Nos. 407169 filed 14th September 1989 and 547728 filed 3rd July 1990) discloses addition polymerization catalysts comprising a monocyclopentadienyl or substituted monocyclopentadienyl metal complex containing compound corresponding to the formula: CpMX n + A - wherein: Cp is a single η 5 -cyclopentadienyl or η 5 -substituted cyclopentadienyl group optionally covalently bonded to M through a substituent; M is a metal of Groups 3-10 or the Lanthanide Series of the Periodic Table bound in an η 5 bonding mode to the cyclopentadienyl or substituted cyclopentadienyl group; X each occurrence is hydride or a moiety selected from halo, alkyl, aryl, silyl, germyl, aryloxy, alkoxy, amide, siloxy, and combinations thereof having 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; n is 1 or 2 depending on the valence of M; and A - is a noncoordinating, compatible anion of a Bronsted acid salt. The catalysts of EP-A-0418044 are stated to be of use to polymerize α-olefins and/or acetylenically unsaturated monomers having from 2 to 18 carbon atoms and/or diolefins having from 4 to 18 carbon atoms either alone or in combination. They may also be used to polymerize α-olefins, diolefins and/or acetylenically unsaturated monomers in combination with other unsaturated monomers. In a preferred embodiment the catalysts are employed to prepare copolymers of mixtures of vinyl aromatic monomers with olefins other than a vinyl aromatic monomer, especially copolymers of styrene with ethylene or propylene. EP-A-0416815 (published on 13th March 1991 in pursuance of European Patent Application No. 90309496.9 filed 30th August 1990 designating AT, BE, DE, ES, FR, GB, IT, NL & SE and claiming priority from US Patent Applications Nos. 401344 filed 31st August 1989, 401345 filed 31st August 1989, 428082 filed 27th October 1989, 428283 filed 27th October 1989, 428276 filed 27th October 1989, 436524 filed 14th November 1989, and 545403 filed 3rd July 1990) discloses addition polymerization catalysts comprising (a) a metal coordination complex comprising a metal of Group 3 (other than scandium), 4-10 or the lanthanide series of the Periodic Table of the Elements and a delocalized π-bonded moiety substituted with a constrain-inducing moiety, said complex having a constrained geometry about the metal atom such that the angle at the metal between the centroid of the delocalized, substituted π-bonded moiety and the center of at least one remaining substituent is less than such angle in an comparative complex differing only in that said constrain-inducing substituent is replaced by hydrogen, and provided that for such complexes comprising more than one delocalized, substituted π-bonded moiety, only one thereof for each metal atom of the complex is a cyclic, delocalized, substituted π-bonded moiety and (b) an activating cocatalyst. Preferably the delocalized π-bonded moiety is a cyclopentadienyl or substituted cyclopentadienyl group forming a portion of a ring structure wherein the metal is both bonded to an adjacent covalent moiety and is held in association with the delocalized π-bonded moiety through η 5 bonds. The catalysts of EP-A-0416815 are stated to be of use to polymerize α-olefins, diolefins, hindered vinylidene aliphatic monomers, vinylidene aromatic monomers and mixtures thereof. In one embodiment the catalysts are employed to prepare copolymers of mixtures of vinylidene aromatic monomers with α-olefins, especially copolymers of styrene with ethylene. According to the present invention there is now provided a process for preparing a syndiotactic polymer of a vinyl aromatic monomer said process comprising contacting at least one polymerizable vinyl aromatic monomer under polymerization conditions with a catalyst characterized in that the catalyst comprises a metal complex of the formula: [Cp m MX n X' p ] + A - wherein: Cp is a single η 5 -cyclopentadienyl group or a η 5 -substituted cyclopentadienyl group which may optionally also be bonded to M through a substituent; M is a metal of Group 3, 4, 5, 6, 8, 9, 10 or the Lanthanide Series of the Periodic Table; each X independently is an inert anionic ligand or a group of formula R, with the provisio that at least one X is R; X' is an inert, neutral donor ligand; each R independently is hydride, or is hydrocarbyl or silyl, optionally substituted with one or more halogen atoms or alkoxy groups, and having up to 20 carbon and/or silicon atoms; m and p are independently 0 or 1; n is an integer greater than or equal to 1; and the sum of m and n is one less than the valence of M, or when Cp is optionally bonded to M through a substituent, the sum of m and n is two less than the valence of M; and A - is a compatible noncoordinating anion. As used herein, the term "syndiotactic" when used to refer to a polymer, indicates a polymer of which greater than 50 percent and preferably greater that 75 percent of the triads present are syndiotactic, as determined by C 13 nuclear magnetic resonance spectroscopy. Such polymers may be usefully employed in the preparation of articles and objects (e.g., via compression molding, injection molding or other suitable technique) having an extremely high resistance to deformation due to the effects of temperature. Examples of R include aralkyl, alkaryl, haloalkyl, silylalkyl, haloalkyl, haloaryl, haloalkaryl, halosilyl, haloalkarylsilyl, and alkoxyalkyl. The term "inert" means noninterfering with the desired catalyst preparation or with the use of the resulting metal complex containing compound as a polymerization catalyst. Illustrative but nonlimiting examples of X include R, halo, NR 2 , PR 2 , OR, SR, and BR 2 . Illustrative but nonlimiting examples of X' include ROR, RSR, NR 3 , PR 3 , and C 2-20 olefin or diolefins. Such donor ligands are able to form shared electron bonds but not a formal covalent bond. The catalytically effective ingredients of the catalysts used in the present invention are prepared by combining at least two components as hereinafter disclosed. The first component is a derivative of a metal of Group 3, 4, 5, 6, 8, 9, 10 or the Lanthanide Series of the Periodic Table of the Elements containing at least one substituent which will combine with the cation of a second component (described hereinafter) or alternatively which is subject to oxidative activation as hereinafter described. The first component additionally must be capable of forming a cation formally having a coordination number that is one less than its valence. The second component is a salt of noncoordinating compatible anion, in particular a salt of such an anion with a Bronsted acid and or with an oxidizing cation. All reference to the Periodic Table of the Elements herein shall refer to the Periodic Table of the Elements, published and copyrighted by CRC Press, Inc., 1989. Also, any reference to a Group or Series shall be to the Group or Series as reflected in this Periodic Table of the Elements, utilizing the IUPAC system for numbering groups. As used herein, the recitation "noncoordinating, compatible anion" means an anion which either does not coordinate with the first component or a derivative thereof; or which is only weakly coordinated to said component thereby remaining sufficiently labile to be displaced by the vinyl aromatic monomer to be polymerized. The recitation "noncoordinating, compatible anion" specifically refers to an anion which when functioning as a charge balancing anion in the catalyst system of this invention does not transfer an anionic substituent or fragment thereof to the cationic portion of the catalyst. Compatible anions are also anions which are not degraded to neutrality under the reaction conditions of the present invention. Cyclopentadienyl and substituted cyclopentadienyl groups for use according to the present invention are more specifically depicted by the formula: wherein: each R' independently is hydrogen, halogen, R, NR 2 , PR 2 ; OR; SR or BR 2 , wherein R is as previously defined; and R" is a group of the formula R' as defined above or a divalent group of from 2 to 7 nonhydrogen atoms that is covalently bonded to M. Preferably, R' is alkyl or haloalkyl of up to 6 carbons, and preferably R" is alkyl or haloalkyl of up to 6 carbons or C 2-5 oxyalkylene or alkylene. Illustrative, but not limiting examples of metal derivatives (first components) which may be used in the preparation of the compounds of this invention are derivatives of titanium, zirconium, hafnium, chromium, and lanthanum. More preferably such metal derivative compounds are those having organyl substituents that are either devoid of reactive hydrogens or wherein potentially reactive hydrogens are protected by bulky protecting groups. Illustrative, but not limiting examples of suitable metal derivative compounds include: tetranorbornenyl titanium, tetrabenzyl zirconium, tetraneopentyl titanium, (cyclopentadienyl)dimethyl(isopropoxy)titanium, (cyclopentadienyl)dibenzyl(isopropoxy)titanium, (cyclopentadienyl)dibenzyl(phenoxy)zirconium, (cyclopentadienyl)dibenzyl(isopropoxy)hafnium, (cyclopentadienyl)dimethylzirconium chloride, (cyclopentadienyl)methylyttrium chloride, bis(phenoxy)di(trimethylsilyl)zirconium, phenoxytrimethylzirconium, bis(2,6-diisopropyl-4-methyl)phenoxy)dibenzyltitanium, bis(2,4,6-trimethylphenoxy)dibenzyltitanium, tri(tertiary butyl)siloxytrimethyl zirconium, bismethoxy-di(phenylmethyl)titanium, bis(2,4,6-trimethylphenoxy) dibenzyltitanium, triphenoxybenzyltitanium, bis(2,4,6-trimethylphenoxy)propylscandium, butoxytris((trimethylsilyl)methyl)zirconium, dimethoxydimethylzirconium, 4-(1-methyl-1-(4-methoxyphenyl)ethyl)phenoxy tribenzyl titanium, dinorborneyldichlorotitanium, tribenzyltitanium hydride, cyclopentadienyltribenzylzirconium, cyclopentadienyltribenzyltitanium, cyclopentadienyltrimethyltitanium, cyclopentadienyltrimethylzirconium, cyclopentadienyltrineopentyltitanium, cyclopentadienyltri(diphenylmethyl)zirconium, cyclopentadienyltriphenylzirconium, cyclopentadienyltrineopentylzirconium, cyclopentadienyldi(m-tolyl)zirconium, cyclopentadienyldi(p-tolyl)zirconium, cyclopentadienyltrimethyltitanium hydride, and cyclopentadienyltridiphenylmethylzirconium; hydrocarbyl-substituted cyclopentadienyl compounds such as pentamethylcyclopentadienyltrimethylzirconium, ethylcyclopentadienyltrimethylzirconium, pentamethylcyclopentadienyltribenzylzirconium, n-butylcyclopentadienyltrineopentyltitanium, (t-butylcyclopentadienyl)tri(trimethylsilyl)zirconium, cyclohexylcyclopentadienyldimethylzirconium, (pentamethylcyclopentadienyl)dimethylzirconium chloride, indenyldibenzyltitanium chloride, (pentamethylcyclopentadienyl)diisopropoxyhafnium chloride, (benzylcyclopentadienyl)di(m-tolyl) titanium chloride, (diphenylcyclopentadienyl)dinorborneylzirconium chloride, methylcyclopentadienyltriphenylzirconium, tetraethylcyclopentadienyltribenzylzirconium, propylcyclopentadienyltrimethylzirconium, propylcyclopentadienyltrimethylzirconium, (n-butylcyclopentadienyl) dimethyl(n-butoxy)titanium, cyclopentadienyldiphenylisopropoxyzirconium, cyclohexylmethylcyclopentadienyltribenzylzirconium, cyclohexylmethylcyclopentadienyltrimethylzirconium, cyclopentadienylzirconium dihydride, benzylcyclopentadienyldimethylhafnium, indenyltribenzylzirconium, trimethylsilylcyclopentadienyltrimethylzirconium, trimethylgermylcyclopentadienyl)trimethyltitanium, trimethylstannylcyclopentadienyltribenzylzirconium, (pentatrimethylsilyl)cyclopentadienyltrimethylzirconium, trimethylsilylcyclopentadienyltrimethylzirconium, penta(trimethylsilyl)cyclopentadienyltribenzyltitanium, trimethylgermylcyclopentadienyltriphenylhafnium, cyclopentadienylbis(p-tolyl)scandium, cyclopentadienyldibenzylchromium, pentamethylcyclopentadienylbis(trimethylsilylmethyl)yttrium, pentamethylcyclopentadienylbis(trimethylsilylmethyl)scandium, and pentamethylcyclopentadienylbis(trimethylsilyl)lanthanum; halogen-substituted cyclopentadienyl compounds such as trifluoromethylcyclopentadienyltrimethylzirconium, trifluoromethylcyclopentadienyltrinorborneylzirconium, and trifluoromethylcyclopentadienyltribenzylzirconium; silyl-substituted (cyclopentadienyl)metal compounds such as cyclopentadienyltrimethylsilylzirconium, and cyclopentadienyltri(phenyldimethylsilyl)zirconium. Preferred components are titanium or zirconium compounds. Compounds useful as a second component in the preparation of the catalyst used in this invention may, in one embodiment, comprise a cation, which is a Bronsted acid capable of donating a proton, and a compatible, noncoordinating anion. In another embodiment such compounds comprise an oxidizing cation and a compatible, noncoordinating anion. Preferred anions are those containing a single coordination complex comprising a charge-bearing metal or metalloid core which anion is relatively large (bulky), capable of stabilizing the active catalyst species (the Group 3, 4, 5, 6, 8, 9, 10 or Lanthanide Series cation) formed when the two components are combined, and which will be sufficiently labile to be displaced by the polymerizable vinyl aromatic monomer. The term "metalloid", as used herein, includes non-metals such as boron, and phosphorus which exhibit semi-metallic characteristics. Suitable metals, include, but are not limited to, aluminum, gold, and platinum. Suitable metalloids include, but are not limited to, boron, phosphorus, and silicon. Compounds containing anions which comprise coordination complexes containing a single metal or metalloid atom are, of course, well known. In light of this, salts containing anions comprising a coordination complex containing a single boron atom are preferred. Preferably, second components useful in the preparation of the catalysts used in this invention may be represented by the following general formulas: (L-H) + [A]- or Ox + [A * ] - wherein: L is a neutral Lewis base; (L-H) + is a Bronsted acid; [A]- is a compatible, noncoordinating anion; Ox + is an organic or metallic oxidizing cation; and [A*] - is a compatible, noncoordinating, inert, anion. By the term "inert" as employed above is meant that A* of formula (II) comprises an anion which is a single coordination complex comprising a plurality of lipophilic radicals covalently coordinated to and shielding a central formally charge-bearing metal or metalloid atom, which anion is bulky and stable under the oxidation and subsequent polymerization conditions, and which anion is compatible with and noncoordinating towards the resulting polymerization catalyst. The anion is employed only to provide charge balance without interfering with the oxidizing ability of Ox + . Anions comprising boron which are particularly useful as [A * ] - may be represented by the following general formula: [BX 1 X 2 X 3 X 4 ] - wherein: B is boron in a valence state of 3; X 1 to X 4 are the same or different nonreactive, organyl or silyl radicals containing from 1 to 20 carbon or silicon atoms. In addition two or more of X 1 to X 4 may be linked to each other through a stable bridging group. Preferably X 1 to X 4 lack reactive hydrogen moieties. That is, the radicals are either devoid of hydrogen, contain only hydrogen in nonactivated positions or contain sufficient steric hinderence to protect potentially active hydrogen sites. Examples of suitable radicals for X 1 to X 4 are perfluorinated hydrocarbyl radicals containing from 1 to 20 carbon atoms, 3,4,5-trifluorophenyl, and 3,4-di(trifluoromethyl)phenyl. A most highly preferred compatible, non-coordinating, inert, anion for use in compounds corresponding to formula (II) is tetra(pentafluorophenyl)borate. Suitable oxidizing cations include organic and inorganic cations having sufficient electronegativity to oxidize the metal derivatives. Organic oxidizing cations for use in the compounds corresponding to formula (II) include ferrocenium ions, indenium ions and cationic derivatives of substituted ferrocene, and indene. Suitable metallic oxidizing cations include Ag +1 , Pd +2 , Pt +2 , Hg +2 , Hg 2 +2 , Au + and Cu + . The process of the invention involves a molecular oxidation. The Group 3, 4, 5, 6, 8, 9, 10 or Lanthanide metal is previously fully oxidized. Highly preferred oxidizing cations have an oxidation potential of at least + 0.20 volt and preferably at least + 0.25 volt. Most highly preferred oxidizing cations are ferrocenium and Ag +1 cations. Without wishing to be bound by any particular theory of operation it is believed that the oxidizing cation causes the molecular oxidation of the metal derivative, and in the process becomes a neutral species. The oxidized metal derivative loses a hydrogen or hydrocarbyl radical (·R) by a unimolecular elimination reaction. Two or more such radicals form a hydrogen molecule or a neutral organic species of the formula R(R x ) where x is an integer. These byproducts are neutral or noninterfering with any subsequent polymerization reaction and may also be removed from the reaction mixture. The preparation technique is analogous to that previously disclosed by R. Jordan, et al., J. A. C. S., 109, 4111-4113 (1987). Illustrative, but not limiting, examples of oxidizing agents according to formula (II) are ferrocenium tetra(pentafluorophenyl)borate, gold (I) tetrakis 3,4,5-trifluorophenyl borate, silver tetra(pentafluorophenyl) borate, and 1,1'-dimethylferrocenium tetrakis 3,5-bistrifluoromethylphenyl borate. Returning to above formula (I), preferably A - corresponds to the formula: [M'Q n' ] - wherein: M' is a metal or metalloid selected from Groups 5-15 of the Periodic Table of the Elements; each Q independently is hydride, dialkylamido, halide, alkoxide, aryloxide, hydrocarbyl, or substitutedhydrocarbyl containing up to 20 carbon atoms with the proviso that in not more than one occurrence is Q halide; and n' is an integer from 2 to 8. Second components comprising boron are particularly useful in the preparation of catalysts of formula (I) and may be represented by the following general formula: [L-H] + [BQ 4 ] - wherein: L is a neutral Lewis base; [L-H] + is a Bronsted acid; B is boron in a valence state of 3; and Q is as previously defined. Illustrative, but not limiting, examples of boron compounds which may be used as a second component in formula (I) are trialkyl-substituted ammonium salts such as triethylammonium tetraphenylborate, tripropylammonium tetraphenylborate, tri(n-butyl)ammonium tetraphenylborate, trimethylammonium tetra(p-tolylborate), tributylammonium tetrakis-pentafluorophenylborate, tripropylammonium tetrakis-2,4-dimethylphenylborate, tributylammonium tetrakis-3,5-dimethylphenylborate, and triethylammonium tetrakis-(3,5-ditrifluoromethylphenyl)borate. Also suitable are N,N-dialkyl anilinium salts such as N,N-dimethylanilinium tetraphenylborate, N,N-diethylanilinium tetraphenylborate, and N,N-2,4,6-pentamethylanilinium tetraphenylborate; dialkyl ammonium salts such as di-[i-propyl)ammonium tetrakispentafluorophenylborate, and dicyclohexylammonium tetraphenylborate; and triaryl phosphonium salts such as triphenylphosphonium tetraphenylborate, tri(methylphenyl)phosphonium tetrakis-pentafluorophenylborate, and tri(dimethylphenyl)phosphonium tetraphenylborate. In general, the catalyst can be prepared by combining the two components in a suitable solvent at a temperature of from -100°C to 300°C. The catalyst system can also form 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. It is, however, preferred to form the catalyst in a separate step in a suitable solvent prior to adding the same to the polymerization step. The catalysts' components are generally sensitive to both moisture and oxygen and should be handled and transferred in an inert atmosphere such as nitrogen, argon or helium. As previously indicated, the improved catalyst of the present invention will, preferably, be prepared in a suitable solvent or diluent. Suitable solvents or diluents include straight and branched-chain hydrocarbons such as C 6-12 alkanes (eg. hexane, heptane, and octane); C 6-12 cyclic and alicyclic hydrocarbons such as cyclohexane, cycloheptane, methylcyclohexane, and methylcycloheptane and C 6-12 aromatic and alkyl-substituted aromatic compounds such as benzene, toluene, xylene, and decalin, and mixtures thereof. The catalysts may be employed as homogeneous catalysts or supported on the surface of a suitable support such as alumina or silica. In general, catalysts according to the present invention can be selected so as to produce polymer products that will be free of certain trace metals generally found in polymers produced with Ziegler-Natta type catalysts containing cocatalysts such as aluminum or magnesium based compounds. In a highly preferred embodiment of the present invention Cp is pentamethylcyclopentadiene, m is zero or one, M is titanium or zirconium, n is two or three, p is zero, X is R or OR, and A is tetrakis-pentafluorophenyl borate. In a most preferred embodiment X is C 1-20 alkyl, aryl, aralkyl, phenoxyalkoxy and m is 0 or 1. Suitable vinyl aromatic monomers which can be polymerized in the process of the present invention include those represented by the formula: wherein each R is independently hydrogen; an aliphatic, cycloaliphatic or aromatic hydrocarbon group having from 1 to 10, more suitably from 1 to 6, most suitably from 1 to 4, carbon atoms; or a halogen atom. Examples of such monomers include, styrne, chlorostyrene, p-methylstyrene, n-butyl styrene, and p-vinyl toluene with styrene being especially suitable. Copolymers of styrene and the above vinyl aromatic monomers other than styrene can also be prepared. The polymerization may be conducted under slurry, bulk or suspension polymerization conditions or other suitable reaction conditions including solid, powdered reaction conditions. The polymerization can be conducted at temperatures of from 0°C to 160°C, preferably from 25°C to 100°C, more preferably from 30°C to 80°C, for a time sufficient to produce the desired polymer. Typical reaction times are from one minute to 100 hours, preferably from 1 to 10 hours. The optimum reaction time or reactor residence time will vary depending upon the temperature, solvent and other reaction conditions employed. The polymerization can be conducted at subatmospheric pressure as well as superatmospheric pressure, suitably at a pressure within the range of 1 to 500 psig (100 kPa-3,400 kPa). The use of ambient or low pressures, e.g., 1-5 psig (100-130 kPa) is preferred in view of lower capital and equipment costs. The polymerization may be conducted in the presence of an inert diluent or solvent or in the absence thereof, i.e., in the presence of excess monomer. Examples of suitable diluents or solvents include C 6-20 aliphatic, cycloaliphatic, aromatic and halogenated aliphatic or aromatic hydrocarbons, as well as mixtures thereof. Preferred diluents comprise the C 6-10 alkanes, toluene and mixtures thereof. A particularly desirable diluent for the polymerization is iso-octane, iso-nonane or blends thereof such as Isopar-E®, available from Exxon Chemical Company. Suitable amounts of solvent are employed to provide a monomer concentration from 5 percent to 100 percent by weight. The molar ratio of the vinyl aromatic monomer to the catalyst (in terms of metal) may range from 100:1 to 500,000:1, preferably from 3,500:1 to 200,000:1. In the case of using a solvent, the catalyst may be used at a concentration with the range from 10 -7 to 10 -1 moles per liter of solvent. As in other similar polymerizations it is highly desirable that the monomers and solvents employed be of sufficiently high purity that catalyst deactivation does not occur. Any suitable technique for monomer purification such as devolatilization at reduced pressures, contacting with molecular sieves or high surface area alumina, or deaeration may be employed. In addition a small amount of an aluminum trialkyl compound or similar scavenger may be added to the reaction mixture to protect the catalyst from deactivation by contaminants in the reaction mixture. Purification of the resulting polymer to remove entrained catalyst may also be desired by the practitioner. Purification of the resulting polymer prepared by the process of this invention is much easier than a conventional process since the process of this invention does not use polyalkylaluminoxane which is used in large quantities as cocatalyst in the conventional process. Entrained catalyst may generally be identified by residues of ash on pyrolysis of the polymer that are attributable to catalyst metal values. A suitable technique for removing such compounds is by solvent extraction, e.g., extraction utilizing hot, high boiling chlorinated solvents, acids or bases such as caustic followed by filtration. Having described the invention, the following examples are provided as further illustrative and are not to be construed as limiting. Unless stated to the contrary, all parts and percentages are based on weight. Example 1 Preparation of Catalyst In a flask, 0.10 gm of pentamethylcyclopentadienyltitanium trimethyl was added to a suspension of 0.343 gm of tri(ethyl)ammonium tetra(pentafluorophenyl)borate in 10 ml of toluene at room temperature. The obtained mixture was allowed to stir for 10 hours, and then heated to 45°C for one hour. No precipitate was observed since the mixture was a very dark solution. The toluene solvent was stripped off in-vacuo thereby leaving a black solid. This solid was washed 3 times with 5 ml of petroleum ether and dried in-vacuo . The product comprised a composition having a structure as identified by 13 C NMR of the formula: [Cp*TiMe 2 ] + [B(C 6 F 5 ) 4 ] - Preparation of Syndiotactic Polystyrene A dry 20 ml vial was charged with 0.025 gm (28 umole) of the above catalyst and then 10.0 gm (102.9 mmol) of styrene was added. The vial was capped with a PTFE coated septum and a metal crimp cap, and shaken until most of the catalyst was dissolved. The vial was placed in a 70°C water bath for 3 hours and then the vial was taken out from the water bath and the polymerization was stopped by the addition of methanol. The off-white, insoluble product was washed with methanol and dried in-vacuo to obtain 3.32 gm of a resultant polymer. The resultant polymer was insoluble in methylene chloride or other common solvents for atactic polystyrene. The resultant polystyrene had a melting point of 268°C (by DSC) and syndiotacticity of greater than 95 percent by 13 C analysis. The polymer had a weight average molecular weight (Mw) of 382,000. Examples 2-11 The reaction conditions of Example 1 were substantially repeated excepting that various catalysts and reactant ratios were employed. Accordingly, a dry 20 ml vial was charged with the catalyst further described in Table I. Styrene was added, the vial was capped with a PTFE coated septum and a metal crimp cap, and shaken until the mixture had mostly dissolved or the mixture gelled, rendering further mixing impossible. The vial was placed in a 70°C water bath for 3 hours and then the vial was taken out from the water bath and the polymerization stopped by the addition of methanol. The off white, insoluble polymer was washed with methanol and dried in-vacuo . In all cases the polymer was insoluble in methylene chloride and other common solvents for atactic polystyrene. Crystalline melting points were determined by differential scanning calorimetry, DSC. Syndiotacticities were determined by 13 C NMR analysis. Results are contained in Table I. Example Complex Mole Ratio Sty:Ti Temp °C Time h % Yield % Syndio DSC °C Mw x 10 3 2 CMTTB 3700:1 RT 4.0 10.4 >95 263 544 3 CBTTB 7500:1 70 1.5 24.1 >95 270 --- 4 CBTTB 7500:1 70 4.0 38.0 >95 269 --- 5 CBTTB 7500:1 70 4.0 4.5 -- 260 --- 6 CBTTB 7500:1 70 4.0 1.4 -- 267 --- 7 CBTTB 10000:1 70 2.0 20.9 -- 270 584 8 CSTTB 7500:1 70 1.5 8.6 -- 270 340 9 CTBOMB 10000:1 70 2.0 10.0 -- 270 --- 10 CBTTB 10000:1 70 2.0 49.8 -- 266 --- 11 CBTTB 10000:1 70 2.0 32.9 -- 265 --- Examples 12-15 The reaction conditions of Example 1 were substantially repeated excepting that an aluminum trialkyl compound was also present in the reaction mixture. Accordingly, a dry 20 ml vial was charged with the catalyst further described in Table II. (The catalysts were prepared according to the technique of Example 1 or (in Example 15) by contacting in equimolar quantities monocyclopentadienyltitaniumtribenzyl with ferrocenium tetra(pentafluorophenyl)borate in toluene.) To a second vial styrene and an aluminum trialkyl compound (in 1M toluene solution) were combined. This solution was added to the vial containing the titanium complex, capped with a PTFE coated septum and a metal crimp cap, and shaken until the mixture had mostly dissolved or the mixture gelled rendering further mixing impossible. The vial was placed in a 70°C water bath for 2 hours and then the vial was taken out from the water bath and the polymerization stopped by the addition of methanol. The off white, insoluble polymer was washed with methanol and dried in-vacuo . In all cases the polymer was insoluble in methylene chloride and other common solvents for atactic polystyrene. Crystalline melting points were determined by differential scanning calorimetry, DSC. Syndiotacticities were determined by C 13 NMR analysis. Results are contained in Table II. Example Complex Mole Ratio Styrene:Al:Ti Temp °C Time h % Yield % Syndio DSC °C Mw x 10 3 12 CTBB 10000:20:1 70 2 29.4 --- 266 287 13 CTBB 10000:18:1 70 1.5 76.2 --- 269 92 14 CTBB 65000:9:1 70 1.5 26.6 --- 270 690 15 CTBB 39000:20:1 70 1.5 67.2 --- 269 604 Example 16 In an argon atmosphere dry box, a dry 20 ml vial was charged with 2.2 mg (4.4 µmol) of bis(2,4,6 trimethylphenoxy)dibenzyltitanium and 3.8 mg (4.4 µmol) of ferrocenium tetra(pentafluorophenyl) boron. To this was added 1 ml of dry, degassed toluene. The mixture was allowed to interact while being stirred for ~30 minutes, after which time a dark insoluble, oily product had formed. Styrene was added to the flask (10 ml, 87.4 mmol) the vial was capped with a PTFE coated septum and a metal crimp cap, shaken until most of the complex had dissolved and then placed in a 70°C water bath for 1.5 hours. The vial was removed from the water bath and the polymerization stopped by the addition of 2 ml of methanol. The off white, insoluble polymer was dried in-vacuo to obtain 0.34 gms of a resultant polymer. The polymer was insoluble in methylene chloride, MEK or other common solvents for atactic polystyrene, and had a crystalline melting point of 259°C, which is consistent with a polymer having >90 percent syndiotacticity. Examples 17-22 Pentamethylcyclopentadienyltribenzyltitanium Tetra(pentafluorophenyl)borate catalyzed polymerization of p-methylstyrene and t-butylstyrene In an argon atmosphere dry box, a dry 20 ml vial was charged with a calculated amount of dried, degassed monomer to provide the monomer molar ratios indicated in Table III. The vial was capped with PTFE coated septum and a metal crimp clamp, then removed from the dry box. To this vial was added via syringe, 205 ul of a 0.0055 M catalyst solution consisting of the reaction product derived from pentamethylcyclopentadienetribenzyl titanium, decamethylferrocenium tetra(pentafluorophenyl) borate and 5 equivalents of triisobutyl aluminum in toluene at room temperature. The vial was then placed in a 70°C water bath for 1 hour. Polymerization was stopped by the addition of methanol. The polymer was washed with methanol and dried under reduced pressure. Crystalline melting points were determined by differential scanning calorimetry, DSC. Results are contained in Table III. Ex. Monomer Ratio pMeSt:Al:Ti Percent conv DSC °C 17 p-methylstyrene 67,400:5:1 50.3 169, 198 18 p-methylstyrene 120,200:5:1 14.1 167, 196 19 p-methylstyrene/-styrene (9.5/90.5) 78,000:5:1 55.0 238 20 t-butylstyrene 49,100:5:1 69.4 310 21 t-butylstyrene 125,700:5:1 64.8 310 22 t-butylstyrene/-styrene (10.1/89.9) 76,000:5:1 56.6 ---

Claims: Claims for the following Contracting States : AT, BE, DE, ES, FR, GB, IT, NL, SE A process for preparing a syndiotactic polymer of a vinyl aromatic monomer said process comprising contacting one or more polymerizable vinyl aromatic monomers in the absence of other copolymerizable monomers under polymerization conditions with a catalyst characterized in that the catalyst comprises a metal complex of the formula: [Cp m MX n X' p ] + A - wherein: Cp is a single η 5 -cyclopentadienyl group which may optionally also be bonded to M through a substituent; M is a metal of Group 3, 4, 5, 6, 8, 9, 10 or the Lanthanide Series of the Periodic Table; each X independently is an inert anionic ligand or a group of formula R, with the proviso that at least one X is R; X' is an inert, neutral donor ligand; each R independently is hydride, or is hydrocarbyl or silyl, optionally substituted with one or more halogen atoms or alkoxy groups, and having up to 20 carbon and/or silicon atoms; m and p are independently 0 or 1; n is an integer greater than or equal to 1, the sum of m and n is one less than the valence of M, or when Cp is optionally bonded to M through the substituent, the sum of m and n is two less than the valence of M; and A - is a compatible noncoordinating anion. A process according to Claim 1, wherein the monomer is contacted with the catalyst at a temperature from 0°C to 160°C. A process according to Claim 1 or Claim 2, wherein the molar ratio of the vinyl aromatic monomer to the catalyst ranges from 100:1 to 500,000:1. A process according to any one of the preceding claims, wherein the vinyl aromatic polymer is represented by the formula: wherein each R is independently hydrogen; an aliphatic, cycloaliphatic or aromatic hydrocarbon group having from 1 to 10 carbon atoms; or a halogen atom. A process according to Claim 4, wherein the vinyl aromatic monomer is styrene. A process according to any one of the preceding claims, wherein m is 1 and the optionally substituted cyclopentadienyl group has the formula: wherein: each R' independently is hydrogen, halogen, R, NR 2 , PR 2 , OR, SR or BR 2 , wherein R is as defined in Claim 1; and R" is a group of the formula R' as defined above or a divalent group of from 2 to 7 nonhydrogen atoms that is covalently bonded to M. A process according to Claim 6, wherein R' is alkyl or haloalkyl of up to 6 carbons, and R" is alkyl or haloalkyl of up to 6 carbons or C 2-5 oxyalkylene or alkylene. A process according to any one of the preceding claims, wherein A - is represented by the following general formula: [BX 1 X 2 X 3 X 4 ] - wherein: B is boron in a valence state of 3; X 1 to X 4 are the same or different nonreactive, organyl or silyl radicals containing from 1 to 20 carbon or silicon atoms or two or more of X 1 to X 4 are linked to each other through a stable bridging group. A process according to Claim 8, wherein X 1 to X 4 are perfluorinated hydrocarbyl radicals containing from 1 to 20 carbon atoms, 3,4,5-trifluorophenyl, and 3,4-di(trifluoromethyl)phenyl. A process according to any one of the preceding claims, wherein M is titanium or zirconium. A process according to any one of the preceding claims, wherein Cp is pentamethylcyclopentadiene. A process according to any one of the preceding claims, wherein each X independently is R or OR, where R is as defined in Claim 1. A process according to any one of the preceding claims, wherein A is tetrakis-pentafluorophenyl borate. A process according to Claim 13, wherein Cp is pentamethylcyclopentadiene, m is 0 or 1, M is titanium or zirconium, n is two or three, p is zero, X is R or OR, wherein R is as defined in Claim 1. A process according to Claim 14, wherein X is C 1-20 alkyl, aryl, aralkyl, phenoxyalkoxy and m is 0 or 1. Claims for the following Contracting States : CH, LI A process for preparing a syndiotactic polymer of a vinyl aromatic monomer said process comprising contacting a polymerizable vinyl aromatic monomer under polymerization conditions with a catalyst characterized in that the catalyst comprises a metal complex of the formula: [Cp m MX n X' p ] + A - wherein: Cp is a single η 5 -cyclopentadienyl group which may optionally also be bonded to M through a substituent; M is a metal of Group 3, 4, 5, 6, 8, 9, 10 or the Lanthanide Series of the Periodic Table; each X independently is an inert anionic ligand or a group of formula R, with the proviso that at least one X is R; X' is an inert, neutral donor ligand; each R independently is hydride, or is hydrocarbyl or silyl, optionally substituted with one or more halogen atoms or alkoxy groups, and having up to 20 carbon and/or silicon atoms; m and p are independently 0 or 1; n is an integer greater than or equal to 1, the sum of m and n is one less than the valence of M, or when Cp is optionally bonded to M through the substituent, the sum of m and n is two less than the valence of M; and A - is a compatible noncoordinating anion. A process according to Claim 1, wherein one or more polymerizable vinyl aromatic monomers are polymerized in the absence of other copolymerizable monomers. A process according to Claim 1 or Claim 2, wherein the monomer is contacted with the catalyst at a temperature from 0°C to 160°C. A process according to any one of the preceding claims, wherein the molar ratio of the vinyl aromatic monomer to the catalyst ranges from 100:1 to 500,000:1. A process according to any one of the preceding claims, wherein the vinyl aromatic polymer is represented by the formula: wherein each R is independently hydrogen; an aliphatic, cycloaliphatic or aromatic hydrocarbon group having from 1 to 10 carbon atoms; or a halogen atom. A process according to Claim 5, wherein the vinyl aromatic monomer is styrene. A process according to any one of the preceding claims, wherein m is 1 and the optionally substituted cyclopentadienyl group has the formula: wherein: each R' independently is hydrogen, halogen, R, NR 2 , PR 2 , OR, SR or BR 2 , wherein R is as defined in Claim 1; and R" is a group of the formula R' as defined above or a divalent group of from 2 to 7 nonhydrogen atoms that is covalently bonded to M. A process according to Claim 7, wherein R' is alkyl or haloalkyl of up to 6 carbons, and R" is alkyl or haloalkyl of up to 6 carbons or C 2-5 oxyalkylene or alkylene. A process according to any one of the preceding claims, wherein A - is represented by the following general formula: [BX 1 X 2 X 3 X 4 ] - wherein: B is boron in a valence state of 3; X 1 to X 4 are the same or different nonreactive, organyl or silyl radicals containing from 1 to 20 carbon or silicon atoms or two or more of X 1 to X 4 are linked to each other through a stable bridging group. A process according to Claim 9, wherein X 1 to X 4 are perfluorinated hydrocarbyl radicals containing from 1 to 20 carbon atoms, 3,4,5-trifluorophenyl, and 3,4-di(trifluoromethyl)phenyl. A process according to any one of the preceding claims, wherein M is titanium or zirconium. A process according to any one of the preceding claims, wherein Cp is pentamethylcyclopentadiene. A process according to any one of the preceding claims, wherein each X independently is R or OR, where R is as defined in Claim 1. A process according to any one of the preceding claims, wherein A is tetrakis-pentafluorophenyl borate. A process according to Claim 14, wherein Cp is pentamethylcyclopentadiene, m is 0 or 1, M is titanium or zirconium, n is two or three, p is zero, X is R or OR, wherein R is as defined in Claim 1. A process according to Claim 15, wherein X is C 1-20 alkyl, aryl, aralkyl, phenoxyalkoxy and m is 0 or 1.

Inventors: CAMPBELL RICHARD E JR, CAMPBELL, RICHARD E. JR.
Applicants: DOW CHEMICAL CO, THE DOW CHEMICAL COMPANY
Application year: 1990
Main classification: C08F12
IPC codes: C08F4, C08F12, C08F10, C08F112