IMPROVED OLEFIN ADDITION POLYMERIZATION CATALYST COMPOSITION

Abstract: Catalyst compositions that are highly tolerant of catalyst poisons comprising a cationic or zwitterionic Group 4 metal complex of the constrained geometry type and an organoaluminum hydrocarbyloxide compound according to the formula R<1>2Al(OR<2>), wherein R<1> and R<2> independently each occurence are C1-30 hydrocarbyl, the molar ratio of complex to organoaluminum hydrocarbyloxide compound being from 1:0.1 to 1:100.

Description: IMPROVED OLEF1N ADDITION POLYMERIZATION CATALYST COMPOSITION This invention relates to compositions of matter which are useful as addition polymerization catalysts, to a method for preparing these catalyst compositions and to a method of using these catalyst compositions More particularly, this invention relates to improved olefm polymerization catalyst compositions comprising a Group 4 metal complex and to an improved method for polymerizing addition polymerizable monomers using the same Constrained geometry metal complexes and methods for their preparation are disclosed in EP-A-416,815, EP-A-468,651; EP-A-514,828, EP-A-520,732, WO93/19104, WO95/00526, as well as US-A-5,055,438, US-A-5,057,475, US-A-5,096,867, US-A-5,064,802, and US-A-5, 132,380. In EP-A-418,044, published March 20, 1991and in USP 5,064,802 certain cationic derivatives of the foregoing constrained geometry catalysts that are highly useful as olefm polymerization catalysts are disclosed and claimed In EP-A-520,732, certain borane reaction products of the foregoing constrained geometry catalysts are disclosed and a method for their preparation taught and claimed. In US-A-5, 453,410 combinations of cationic constrained geometry catalysts with an alumoxane were disclosed as suitable olefm polymerization catalysts. For the teachings contained therein, the aforementioned United States Patents and published European Patent Applications (or the equivalent US patent or application) are herein incorporated in their entirety by reference thereto. Although previously known cationic catalysts, especially the cationic catalysts disclosed in the foregoing applications and publications, have excellent activity, they are extremely sensitive to catalyst poisons, such as polar impurities, that may be contained in a polymerization mixture. Because of this fact, catalyst efficiencies and lifetimes have been limited and molecular weights of the resulting polymers have been reduced. It is previously known in the art to utilize adjuvants such as tπalkylboron and tπalkylaluminum compounds to remove catalyst poisons from biscyclopentadienyl containing olefm polymerization catalysts. Disadvantageously however, such adjuvants have proven to be less effective in combating the inhibition of cationic catalysts, especially cationic, constrained geometry catalysts, and when used in the polymerization of olefm monomers, actually may interfere with the desired catalytic process. The previously disclosed US-A-5,453,410 disclosed the combination of an alumoxane adjuvant with a cationic constrained geometry catalyst composition. However, alumoxanes are rather less soluble than is desired in aliphatic hydrocarbon solvents used in common polymerization systems Additionally, alumoxanes are pyrophoπc and are relatively expensive. Thus, it would be desirable to reduce the quantity of alumoxane used in a polymeπzation process or more desirably still, to eliminate use of alumoxanes entirely. Instead it would be desirable to utilize an adjuvant which is not pyrophonc and is more soluble in aliphatic hydrocarbons. Finally, components in polymerization processes or their reaction products ultimately become incorporated into the polymer produced by the polymerization process unless a technique for their removal is available. Alumoxanes are relatively high molecular weight polymeric aluminum oxide compounds. Their presence in residual quantities in the polymerization product is generally not considered to be beneficial to polymer properties, and may actually degrade some polymer properties, particularly polymer clarity. An active component of the polymer catalyst that ultimately may be converted to a beneficial additive, such as an antioxidant, is a particularly desired objective of the present invention. The present investigations have led to certain improved cationic catalyst compositions that are highly active as addition polymerization catalysts, desirably having improved resistance to catalyst poisons, and reduced cost. Moreover, certain of the compositions utilize components that under hydrolysis conditions result in the formation of compounds that are believed to beneficially improve oxidation resistance of the resulting polymers. Since such hydrolysis products can be formed at any time during the polymeπzation process or subsequent handling such beneficial additives are capable of protecting the polymer at a time before addition of conventional additives and antioxidants According to the present invention there is now provided a catalyst composition comprising in combination: a1) a rr^ complex corresporxing to L M)OC ql wherein: M is a metal of Group 4 of the Periodic Table of the Elements having an oxidation state of +2, +3 or +4, bound in an η 5 bonding mode to L; L is a cyclopentadienyl-, indenyl-, tetrahydroindenyl-, fluorenyl-, tetrahydrofluorenyl-, or octahydrofluorenyl- group covalently substituted with at least a divalent moiety, Z, and L further may be substituted with from 1 to 8 substituents independently selected from the group consisting of hydrocarbyl, halo, halohydrocarbyl, hydrocarbyioxy, dihydrocarbylamino, dihydrocarbylphosphino or silyl groups containing up to 20 non-hydrogen atoms, or two such substituents may together form a divalent deπvative; Z is a divalent moiety bound to both L and M via σ-bonds, said Z compnsmg boron, or a member of Group 14 of the Periodic Table of the Elements, and optionally, also compnsmg nitrogen, phosphorus, sulfur or oxygen; X is an anionic or dianionic ligand group having up to 60 atoms, exclusive of the class of ligands that are cyclic, delocalized, π-bound ligand groups; X' independently each occurrence is a neutral ligating compound, having up to 20 atoms; p is 0, 1 or 2, and is two less than the formal oxidation state of M, with the proviso that when X is a dianionic iigand group, p is 1 ; and q is O, 1 or 2, a1 ') an activating cocatalyst which forms a cationic derivative of a1); and b) an organoaluminum hydrocarbyloxide compound according to the formula R .AI(OR 2 ), wherein R 1 and R 2 independently each occurrence are C, 30 hydrocarbyl, the molar ratio of a1): b) being from 1 :0.1 to 1 :100; or a catalyst composition comprising in combination a cationic complex, a2) corresponding to the formula: [Z L M * X * p .f A , wherein: M * is a metal of Group 4 of the Periodic Table of the Elements having an oxidation state of +3 or +4, bound in an η bonding mode to L; L is a cyclopentadienyl-, indenyl-, tetrahydroindenyl-, fluorenyl-, tetrahydrofluorenyl-, or octahydrofluorenyl- group covalently substituted with at least a divalent moiety, Z, and L further may be substituted with from 1 to 8 substituents independently selected from the group consisting of hydrocarbyl, halo, halohydrocarbyl, hydrocarbyioxy, dihydrocarbylamino, dihydrocarbylphosphino or silyl groups containing up to 20 non-hydrogen atoms, or two such substituents may together form a divalent derivative; Z is a divalent moiety bound to both L and M * via σ-bonds, said Z comprising boron, or a member of Group 1 of the Periodic Table of the Elements, and also optionally compnsmg nitrogen, phosphorus, sulfur or oxygen; X * is an anionic ligand group having up to 60 atoms, exclusive of the class of ligands that are cyclic, delocalized, π-bouπd ligand groups; p * is 0 or 1 , and is three less than the formal oxidation state of M; and A is an noncoordmating, compatible anion, and b) an organoaluminum hydrocarbyloxide compound according to the formula R 2 AI(OR 2 ), wherein R' and R 2 independently each occurrence are C,. 30 hydrocarbyl the molar ratio of a2): b) being from 1:0.1 to 1 :100. Further according to the present invention there is provided a process for polymerization of addition polymerizable monomers or mixtures thereof compnsmg contacting said monomer or mixture of monomers with a catalyst system compnsmg the above catalyst composition under addition polymeπzation conditions. Preferred addition polymenzable monomers include C 2 20 -olefins Polymers prepared by the foregoing invented process are usefully employed for molding, film, sheet, extrusion foaming and other applications. All references 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 Groups shall be to the Group or Groups as reflected in this Periodic Table of the Elements using the IUPAC system for numbering groups. The compositions of the present invention are believed to exist in the form of a mixture of a cationic species having a charge limited structure corresponding to the formula for a2) and the organoaluminum hydrocarbyloxide, b), or they exist in the form of a mixture of a zwittenonic derivative of the complex of formula a1 ) and the organoaluminum hydrocarbyloxide, b). Fully cationic or partially charge separated metal complexes, that is, zwittenonic metal complexes, have been previously disclosed in USP's 5,470,993 and 5,486,632, the teachings of which are herein incorporated in their entirety by reference. The zwittenonic complexes in particular result from activation of a Group 4 metal diene complex that is in the form of a metallocyclopentene, wherein the metal is in the +4 formal oxidation state, by the use of a Lewis acid activating cocatalyst, especially trιs(perfluoroaryl)boranes. These zwittenonic complexes are believed to correspond to the formula: Z / I L — M + - X** - A wherein: M is a Group 4 metal in the +4 formal oxidation state; L and Z are as previously defined; X" is the divalent remnant of the conjugated diene, X', formed by ring opening at one of the carbon to metal bonds of a metallocyclopentene; and A is the moiety derived from the activating cocatalyst. As used herein, the recitation "noncoordinating, compatible anion" means an anion which either does not coordinate to component a1) or which is only weakly coordinated therewith remaining sufficiently labile to be displaced by an olef . A non-coordinating, compatible anion specifically refers to a compatible 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 said cation thereby forming a neutral four coordinate metallocene and a neutral metal byproduct. "Compatible anions" are anions which are not degraded to neutrality when the initially formed complex decomposes and are noninterfeπng with desired subsequent polymerizations. Preferred X' groups are phosphmes, especially tnmethylphosphine, tπethylphosphine, tπphenylphosphine and bιs(1 ,2-dιmethylphosphιno)ethane, P(OR) 3 , wherein R is as previously defined; ethers, especially tetrahydrofuran; amines, especially pyridine, bipyridine, tetramethylethylenediamine (TMEDA), and triethylamine; olefins; and conjugated dienes having from 4 to 40 carbon atoms Complexes including conjugated diene X' groups include those wherein the metal is in the +2 formal oxidation state. Preferred coordination complexes a1 ) used according to the present invention are complexes corresponding to the formula: wherein: R independently independently each occurrence is a group selected from hydrogen, hydrocarbyl, halohydrocarbyl, silyl, germyl and mixtures thereof, said group containing up to 20 nonhydrogen atoms, and optionally 2 R groups may together form a divalent derivative bound to two positions of a nng; M is titanium, zirconium or hafnium; Z is a divalent moiety or a moiety covalently attached to the ring and possessing an electron pair by which it is coordinate-covalently bound to M, said Z compnsmg boron, or a member of Group 14 of the Peπodic Table of the Elements, and also comprising nitrogen, phosphorus, sulfur or oxygen, and having up to 60 non-hydrogen atoms; X and X' are as previously defined; with the proviso that: when p is 2, q is zero, M is in the +3 or +4 formal oxidation state, and X is an anionic ligand selected from the group consisting of halide, hydrocarbyl, hydrocarbyioxy, dι(hydrocarbyl)amιdo, dι(hydrocarbyl)phosphιdo, hydrocarbylsulfido, and silyl groups, as well as halo-, dι(hydrocarbyl)amιno- , hydrocarbyioxy- and dι(hydrocarbyl)phosphιno-substιtuted deπvatives thereof, said X group having up to 20 nonhydrogen atoms, when p is 1 , q is zero, M is in the +3 formal oxidation state, and X is a stabilizing anionic ligand group selected from the group consisting of allyl, 2-(N,N-dιmethyiamιnomethyl)phenyl, and 2- (N,N-dιmethyl)-amιnobenzyl, or M is in the +4 formal oxidation state, and X is a divalent derivative of a conjugated diene, M and X together forming a metallocyclopentene group, and when p is 0, q is 1 , M is in the +2 formai oxidation state, and X" is a neutral, conjugated or nonconjugated diene, optionally substituted with one or more hydrocarbyl groups, said X' having up to 40 carbon atoms and forming a π-complex with M. More preferred coordination complexes a1) used according to the present invention are complexes corresponding to the formula: wherein: R independently each occurrence is hydrogen or C, 6 alkyl; M is titanium; Y is -O-, -S-, -NR * -, -PR * -, -NR * 2 , or -PR%; Z* is SiR* 2 , CR , SιR* 2 SiR , CR CR * 2 , CR * =CR * , CR * 2 SιR * 2 , or GeR * 2 ; R* each occurrence is independently hydrogen, or a member selected from hydrocarbyl, hydrocarbyioxy, silyl, halogenated alkyl, halogenated aryl, and combinations thereof, said R * having up to 20 non-hydrogen atoms, and optionally, two R * groups from Z (when R * is not hydrogen), or an R * group from Z and an R * group from Y form a nng system; with the proviso that: when p is 2, q is zero, M is in the +3 or +4 formal oxidation state, and X is independently each occurrence methyl or benzyl, when p is 1 , q is zero, M is in the +3 formal oxidation state, and X is 2-(N,N- dιmethyl)amιnobenzyl; or M is in the +4 formal oxidation state and X is 1 ,4-butadιenyl, and when p is 0, q is 1 , M is in the +2 formal oxidation state, and X' is 1 ,4-dιpheny ,3-butadιene or 1 ,3-pentadιene The latter diene is illustrative of unsymetncal diene groups that result in production of metal complexes that are actually mixtures of the respective geometrical isomers The complexes can be prepared by use of well known synthetic techniques A preferred process for preparing the metal complexes is disclosed in USSN 8/427,378, filed April 24, 1995, USP 5,491 ,246, the teachings of which are hereby incorporated by reference. The reactions are conducted in a suitable noninterfenng solvent at a temperature from -100 to 300 °C, preferably from -78 to 100 °C, most preferably from 0 to 50 °C. A reducing agent may be used to cause the metal M. to be reduced from a higher to a lower oxidation state. Examples of suitable reducing agents are alkali metals, alkaline earth metals, aluminum and zinc, alloys of alkali metals or alkaline earth metals such as sodium mercury amalgam and sodium potassium alloy, sodium naphthalenide, potassium graphite, lithium alkyls, lithium or potassium alkadienyls, and Gπgnard reagents Suitable reaction media for the formation of the complexes include aliphatic and aromatic hydrocarbons, ethers and cyclic ethers, particularly branched-chain hydrocarbons such as isobutane. butane, pentane, hexane, heptane, octane, and mixtures thereof; cyclic and alicyclic hydrocarbons such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof; aromatic and hydrocarbyl-substituted aromatic compounds such as benzene, toluene, and xylene, C, „ dialkyl ethers, C, dialkyl ether derivatives of (poly)alkylene glycols, and tetrahydrofuran. Mixtures of the foregoing are also suitable. Suitable activating cocatalysts useful in combination with component a1) are those compounds capable of abstraction of an X substituent from a1) to form an inert, noninterfenng counter ion, or that form a zwittenonic derivative of a1 ). Suitable activating cocatalysts for use herein include perfluoπnated tπ(aryl)boron compounds, and most especially tπs(pentafluoro-phenyl)borane; nonpolymeπc, compatible, noncoordinating, ion forming compounds (including the use of such compounds under oxidizing conditions), especially the use of ammonium-, phosphonium-, oxonium-, carbonium-, silylium- or sulfonium- salts of compatible, noncoordinating anions, and ferrocenium salts of compatible, noncoordinating anions. Suitable activating techniques include the use of bulk electrolysis (explained in more detail hereinafter). A combination of the foregoing activating cocatalysts and techniques may be employed as well. The foregoing activating cocatalysts and activating techniques have been previously taught with respect to different metal complexes in the following references: EP-A-277,003, US-A-5,153,157, US-A-5,064,802, EP-A-468.651 , EP-A-520,732, and EP-A-520,732, the teachings of which are hereby incorporated by reference. More particularly, suitable ion forming compounds useful as cocatalysts in one embodiment of the present invention compπse a cation which is a Bronsted acid capable of donating a proton, and a compatible, noncoordinating anion, A . As used herein, the term "noncoordinating" means an anion or substance which either does not coordinate to the Group 4 metal containing precursor complex and the catalytic derivative derived therefrom, or which is only weakly coordinated to such complexes thereby remaining sufficiently labile to be displaced by an olefm. "Compatible anions" are anions which are not degraded to neutrality when the initially formed complex decomposes and are noninterfenng with desired subsequent polymerization or other uses of the complex. Preferred anions are those containing a single coordination complex comprising a charge- bearing metal or metalloid core which anion is capable of balancing the charge of the active catalyst species (the metal cation) which may be formed when the two components are combined. Also, said anion should be sufficiently labile to be displaced by olefmic, diolefinic and acetylenically unsaturated compounds or other neutral Lewis bases such as ethers or nitπles. 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 and many, particularly such compounds containing a single boron atom in the anion portion, are available commercially. Preferably such cocatalysts may be represented by the following general formula: <L * -H) * d (A) d wherein' L * is a neutral Lewis base; (L * -H) * is the conjugate Bronsted acid of L; A d is a noncoordinating, compatible anion having a charge of d-, and d is an integer from 1 to 3. More preferably A d corresponds to the formula: [M'QJ ; wherein- M' is boron or aiummum in the +3 formal oxidation state; and Q independently each occurrence is selected from hydπde, dialkylamido, halide, hydrocarbyl, hydrocarbyloxide, halosubstituted-hydrocarbyl, halosubstituted hydrocarbyioxy, and halo- substituted silylhydrocarbyl radicals (including perhalogenated hydrocarbyl- perhalogenated hydrocarbyioxy- and perhalogenated silylhydrocarbyl radicals), said Q having up to 20 carbons with the proviso that in not more than one occurrence is Q halide. Examples of suitable hydrocarbyloxide Q groups are disclosed in U. S. Patent 5,296,433, the teachings of which are herein incorporated by reference. In a more preferred embodiment, d is one, that is, the counter ion has a single negative charge and is A . Activating cocatalysts compnsmg boron which are particularly useful in the preparation of catalysts of this invention may be represented by the following general formula: (L * - wherein: L * is as previously defined; B is boron in a formal oxidation state of 3, and Q is a hydrocarbyl-, hydrocarbyioxy-, fluorinated hydrocarbyl-, fluonnated hydrocarbyioxy-, or fluonnated silylhydrocarbyl- group of up to 20 nonhydrogen atoms, with the proviso that in not more than one occasion is Q hydrocarbyl Most preferably, Q is each occurrence a fluonnated aryl group, especially, a pentafluorophenyl group Illustrative, but not limiting, examples of boron compounds which may be used as an activating cocatalyst in the preparation of the improved catalysts of this invention are tn-substituted ammonium salts such as. tπmethylammonium tetrakis (pentafluorophenyl) borate, tπethylammonium tetrakιs(pentafluorophenyl) borate, tπpropylammonium tetrakιs(pentafluorophenyl) borate, tπ(n-butyl)ammonιum tetrakιs(pentafiuorophenyl) borate, trι(sec-butyl)ammoπιum tetrakis entaf luorophenyl) borate, N,N-dιmethylanιiιnιum tetrakιs(pentafluorophenyl) borate, N,N-dιmethylanιlιnιum n-butyltπs(pentafiuorophenyl) borate, N,N-dιmethylanιlιnιum benzyltπs(pentafluorophenyl) borate, N,N-dιmethylanιlιnιum tetrakιs(4-(t-butyldιmethylsιlyl)-2, 3, 5, 6-tetrafluorophenyl) borate, N,N-dιmethylanιlιnιum tetrakιs(4-(tnιsopropylsιlyl)-2, 3, 5, 6-tetrafluorophenyl) borate, N,N-dιmethylanιlιnιum pentafluorophenoxytπs(pentafluorophenyl) borate, N.N-diethylanilmium tetrakιs(pentafluorophenyl) borate, N,N-dιmethyl-2,4,6-tπmethylanιlιnιum tetrakιs(pentafiuorophenyl) borate, trimethylammonium tetrakιs(2,3,4,6-tetrafluorophenyl)borate, tnethylammonium tetrakιs(2,3,4,6-tetrafluorophenyl) borate, tπpropylammonium tetrakιs(2,3,4,6-tetrafluorophenyl) borate, tπ(n-butyl)ammonιum tetrakιs(2,3,4,6-tetrafluorophenyl) borate, dιmethyloctadecylammoπιum tetrakιs(2,3,4,6-tetrafluorophenyl) borate, N,N-dιmethylanιiιnιum tetrakιs(2 t 3,4,6-tetrafluorophenyl) borate, N,N-dιethylanιlιnιum tetrakιs(2,3,4,6-tetrafluorophenyl) borate, and N,N-dιmethyl-2,4,6-tπmethylanιlιnιum tetrakιs(2,3,4,6-tetrafluorophenyl) borate; disubstituted ammonium salts such as: dι-(ι-propyl)ammonιum tetrakιs(pentafluorophenyl) borate, and dicyclohexylammonium tetrakιs(pentafluorophenyl) borate; tπsubstituted phosphonium salts such as. tπphenylphosphonium tetrakιs(pentafluorophenyl) borate, tπ(o-tolyl)phosphonιum tetrakιs(pentafluoropheπyl) borate, and trι(2,6-dιmethylphenyl)phosphonιum tetrakιs(pentafluorophenyl) borate, disubstituted oxonium salts such as: diphenyloxonium tetrakιs(pentafiuorophenyl) borate, dι(o-toiyl)oxonιum tetrakιs(pentafluorophenyl) borate, and dι(2,6-dιmethylphenyl)oxonιum tetrakis(pentaf luorophenyl) borate; disubstituted sulfonium salts such as: diphenyisulfomum tetrakιs(pentafluorophenyl) borate, dι(o-tolyl)sulfonιum tetrakιs(pentafluorophenyl) borate, and bιs(2,6-dιmethylphenyl)sulfonιum tetrakιs(pentafluorophenyl) borate. Preferred (L * -H) * cations are N,N-dιmethylanιiιnιum and dimethyloctadecylammonium. Another suitable ion forming, activating cocatalyst comprises a salt of a cationic oxidizing agent and a noncoordinating, compatible anion represented by the formula: (Ox") d (A a ).. wherein: Ox* * is a cationic oxidizing agent having a charge of e+; e is an integer from 1 to 3; and A and d are as previously defined. Examples of cationic oxidizing agents include: ferrocenium, hydrocarbyl-substituted ferrocenium, Ag * or Pb *2 . Preferred embodiments of A d are those anions previously defined with respect to the Bronsted acid containing activating cocatalysts, especially tetrakιs(pentafluorophenyl)borate. Another suitable ion forming, activating cocatalyst comprises a compound which is a salt of a carbenium ion and a noncoordinating, compatible anion represented by the formula: © * A wherein: © * ιs a C 1 40 carbenium ion; and A is as previously defined. A preferred carbenium ion is the tπtyl cation, i.e. tπphenyimethylium. A further suitable ion forming, activating cocatalyst compnses a compound which is a salt of a silylium ion and a noncoordinating, compatible anion represented by the formula: R * 3 Si * A wherein: R'IS C, 10 hydrocarbyl, and A is as previously defined. Preferred sily um salt activating cocatalysts are tπmethylsilyiium tetrakispentafluorophenyl- borate, tπethylsilylium tetrakispentafluorophenylborate and ether substituted adducts thereof Silyhum salts have been previously generically disclosed in J. Chem Soc Chem Comm . 1993, 383-384, as well as Lambert, J. B., et al., Orqanometallics. 1994, 13, 2430-2443 The use of the above siiylium salts as activating cocatalysts for addition polymeπzation catalysts is disclosed and claimed in USSN 08/304,314, filed September 12, 1994, equivalent to WO96/08519. Certain complexes of alcohols, mercaptans, silanols, and oximes with tns(pentafluorophenyl)borane are also effective catalyst activators and may be used according to the present invention. Such cocatalysts are disclosed in US-A- 5,296,433, the teachings of which are herein incorporated by reference. The technique of bulk electrolysis involves the electrochemical oxidation of the metal complex a1) under electrolysis conditions in the presence of a supporting electrolyte comprising a noncoordinating, inert anion to form the cationic complex a2). In the technique, solvents, supporting electrolytes and electrolytic potentials for the electrolysis are used such that electrolysis byproducts that would render the metal complex catalytically inactive are not substantially formed during the reaction. More particularly, suitable solvents are materials that are: liquids under the conditions of the electrolysis (generally temperatures from 0 to 100 °C), capable of dissolving the supporting electrolyte, and inert. "Inert solvents" are those that are not reduced or oxidized under the reaction conditions employed for the electrolysis. It is generally possible in view of the desired electrolysis reaction to choose a solvent and a supporting electrolyte that are unaffected by the electrical potential used for the desired electrolysis. Preferred solvents include difluorobenzene (all isomers), dimethoxyethane (DME), and mixtures thereof. The electrolysis may be conducted in a standard electrolytic cell containing an anode and cathode (also referred to as the working electrode and counter electrode respectively). Suitable materials of construction for the cell are glass, plastic, ceramic and glass coated metal. The electrodes are prepared from inert conductive materials, by which are meant conductive materials that are unaffected by the reaction mixture or reaction conditions. Platinum or palladium are preferred inert conductive matenals. Normally an ion permeable membrane such as a fine glass frit separates the cell into separate compartments, the working electrode compartment and counter electrode compartment. The working electrode is immersed in a reaction medium compnsmg the metal complex to be activated, solvent, supporting electrolyte, and any other materials desired for moderating the electrolysis or stabilizing the resulting complex. The counter electrode is immersed in a mixture of the solvent and supporting electrolyte. The desired voltage may be determined by theoretical calculations or expeπmentally by sweeping the cell using a reference electrode such as a silver electrode immersed in the cell electrolyte The background cell current, the current draw in the absence of the desired electrolysis, is also determined. The electrolysis is completed when the current drops from the desired level to the background level In this manner, complete conversion of the initial metal complex can be easily detected. Suitable supporting electrolytes are salts comprising a cation and a compatible, noncoordinating anion, A-. Preferred supporting electrolytes are salts corresponding to the formula G * A , wherein: G * is a cation which is nonreactive towards the starting and resulting complex, and A is as previously defined. Examples of cations, G\ include tetrahydrocarbyl substituted ammonium or phosphonium cations having up to 40 nonhydrogen atoms Preferred cations are the tetra(n-butylammonιum)- and tetraethylammonium- cations. During activation of the complexes of the present invention by bulk electrolysis the cation of the supporting electrolyte passes to the counter electrode and A- migrates to the working electrode to become the anion of the resulting oxidized product. Either the solvent or the cation of the supporting electrolyte is reduced at the counter electrode in equal molar quantity with the amount of oxidized metal complex formed at the working electrode. Preferred supporting electrolytes are tetrahydrocarbylammonium salts of tetrakιs(perfluoro-aryl) borates having from 1 to 10 carbons in each hydrocarbyl or perfluoroaryl group, especially tetra(n-butylammonιum)tetrakιs- (pentafluorophenyl) borate. A further recently discovered electrochemical technique for generation of activating cocatalysts is the electrolysis of a disilane compound in the presence of a source of a noncoordinating compatible anion All of the foregoing techniques are more fully disclosed and claimed in WO95/00683. In as much as the activation technique ultimately produces a cationic metal complex, the amount of such resulting complex formed dunng the process can be readily determined by measuring the quantity of energy used to form the activated complex in the process. A most preferred activating cocatalyst is tπspentafluoro-phenylborane. The molar ratio of metal complex: activating cocatalyst employed preferably ranges from 1 :10 to 2:1 , more preferably from 1 :5 to 1.5:1 , most preferably from 1 :5 to 1 :1. The organoaluminum hydrocarbyloxide component, component b) of the catalyst composition of the invention preferably corresponds to the formula R^AIOR 2 wherein R 1 is C 3 6 secondary or tertiary alkyl, most preferably isopropyl, isobutyl or tert-butyl; and R 2 is a C 12 30 alkaryl radical or aralkyl radical, most preferably, 2,6-dι(t-butyl)-4-methylphenyl, 2,6-dι(t-butyl)-4-methyltolyl, 2,6-dι(ι-butyl)-4- methylphenyl, or 4-(3 , ,5 , -dιtertιarybutyltolyl)-2,6-dιtertιarybutylphenyl. The molar ratio of metal complex (component a1 ) or a2)) to component b) employed in the present invention preferably ranges from 1 :1 to 1 100, more preferably from 1 -1 to 1 :20, highly preferably from 1 :1 to 1 :10, and most preferably from 1 :1 to 1 :5 The process may be used to polymerize ethylenically unsaturated monomers having from 2 to 20 carbon atoms either alone or in combination. Preferred monomers include monovinylidene aromatic monomers, 4-vιnylcyclohexene, vinylcyclohexane, norbornadiene and C 3 10 aliphatic α- olefms (especially ethylene, propylene, isobutylene, 1-butene, 1 -hexene, 3-methyl-1 -pentene, 4- methyl-1 -pentene, and 1 -octene), C 4 40 dienes, and mixtures thereof. Of the dienes typically used to prepare EPDMs, the particularly preferred dienes are 1 ,4-hexadιene (HD), 5-ethylιdene-2-norbornene (ENB), 5-vιnylιdene-2-norbornene (VNB), 5-methylene-2-norbomene (MNB), and dicyclopentadiene (DCPD). The especially preferred dienes are 5-ethylιdene-2-norbornene (ENB) and 1 ,4-hexadιene (HD). Most preferred monomers are ethylene, mixtures of ethylene, propylene and ethyhdenenorbornene, or mixtures of ethylene and a C 4 β α-olefin, especially 1 -octene. In general, the polymerization may be accomplished at conditions well known in the prior art for Ziegler-Natta or Kaminsky-Sinn type polymeπzation reactions, that is, temperatures from 0-250 °C, preferably 30 to 200 °C and pressures from atmospheric to 30,000 atmospheres or higher Suspension, solution, slurry, gas phase, solid state powder polymerization or other process condition may be employed if desired. A support, especially silica, alumina, or a polymer (especially poly(tetrafluoroethylene) or a polyolefm) may be employed, and desirably is employed when the catalysts are used m a gas phase polymerization process. The support is preferably employed in an amount to provide a weight ratio of catalyst (based on metal):support f rom 1 :100,000 to 1 10, more preferably from 1 :50,000 to 1 :20, and most preferably from 1 10,000 to 1 :30. In most polymeπzation reactions the molar ratio of catalyst:polymeπzable compounds employed is from 10 12 1 to 10 ' : 1 , more preferably from 10 9 - 1 to 10 5 : 1 Suitable solvents for polymeπzation are inert liquids. Examples include straight and branched-chain hydrocarbons such as isobutane, butane, pentane, hexane, heptane, octane, and mixtures thereof; cyclic and aiicyciic hydrocarbons such as cyclohexane, cycloheptane, methylcyclohexane, methyicycloheptane, and mixtures thereof; perfiuoπnated hydrocarbons such as perfluoπnated C 4 10 alkanes, and the like and aromatic and alkyl-substituted aromatic compounds such as benzene, toluene, xylene, ethylbenzene and the like. Suitable solvents also include liquid olefins which may act as monomers or comonomers including ethylene, propylene, butadiene, cyclopentene, 1 -hexene, 1 -hexane, 4-vιπylcyclohexene, vinylcyclohexane, 3-methyl-1 -pentene, 4-methyl-1 -pentene, 1 ,4-hexadιene, 1 -octene, 1-decene, styrene, divinylbenzene, allylbenzene, vinyltoluene (including all isomers alone or in admixture), and the iike. Mixtures of the foregoing are also suitable. The catalysts may be utilized in combination with at least one additional homogeneous or heterogeneous polymerization catalyst in separate reactors connected in seπes or in parallel or in a single reactor to prepare polymer blends having desirable properties. An example of such a process is disclosed in WO 94/00500, as well as USSN 08/10958, filed January 29. 1993, equivalent to W094/17112, the teachings of which are hereby incorporated by reference herein. Utilizing the catalyst compositions of the present invention copolymers having high comonomer incorporation and correspondingly low density, yet having a low melt index may be readily prepared. That is, high molecular weight polymers are readily attained by use of the present catalysts even at elevated reactor temperatures. This result is highly desirable because the molecular weight of α-olefin copolymers can be readily reduced by the use of hydrogen or similar chain transfer agent, however increasing the molecular weight of α-olefin copolymers is usually only attainable by reducing the polymerization temperature of the reactor. Disadvantageously, operation of a polymerization reactor at reduced temperatures significantly increases the cost of operation since heat must be removed from the reactor to maintain the reduced reaction temperature, while at the same time heat must be added to the reactor effluent to vaporize the solvent. In addition, productivity is increased due to improved polymer solubility, decreased solution viscosity, and a higher polymer concentration. Utilizing the present catalyst compositions, α-olefin homopolymers and copolymers having densities from 0.85 g/cm 3 to 0.96 g/cm 3 , and melt flow rates from 0.001 to 10.0 dg/min are readily attained in a high temperature process. The catalyst compositions of the present invention are particularly advantageous for the production of ethylene homopolymers and ethylene/α-olefin copolymers having high levels of long chain branching. The use of the catalyst compositions of the present invention in continuous polymerization processes, especially continuous solution polymerization processes, allows for elevated reactor temperatures which favor the formation of vinyl terminated polymer chains that may be incorporated into a growing polymer, thereby giving a long chain branch. The use of the present catalyst compositions advantageously allows for the economical production of ethylene/α-olefin copolymers having processability similar to high pressure, free radical produced low density polyethylene. The present catalysts system may be advantageously employed to prepare olefin polymers having improved processing properties by polymeπzing ethylene alone or ethylene/α-olefin mixtures with low levels of a "H" branch inducing diene, such as norbornadiene, 1 ,7-octadiene, or 1 ,9- decadiene. The unique combination of elevated reactor temperatures, high molecular weight (or low melt indices) at high reactor temperatures and high comonomer reactivity advantageously allows for the economical production of polymers having excellent physical properties and processability. Preferably such polymers compπse ethylene, a C .∞ α-olefin and a "H"-branching comonomer. Preferably, such polymers are produced in a solution process, most preferably a continuous solution process. The present catalyst composition is particularly useful in the preparation of EP and EPDM copolymers in high yield and productivity. The process employed may be either a solution or slurry process both of which are previously known in the art. Kammsky, Poly Sci.. Vol. 23, pp. 2151 -64 (1985) reported the use of a soluble bιs(cyclopentadιenyl) zirconium dimethyl-alumoxane catalyst system for solution polymerization of EP and EPDM elastomers. USP 5,229,478 disclosed a slurry polymerization process utilizing similar bιs(cyciopentadιenyi) zirconium based catalyst systems. Similar polymerization conditions are used with the present catalyst composition. The teachings of the foregoing US patents are herein incorporated by reference. The catalyst composition may be prepared as a homogeneous catalyst by addition of the requisite components to a solvent in which polymerization will be carried out by solution polymerization procedures. The catalyst system may also be prepared and employed as a heterogeneous catalyst by adsorbing the requisite components on a catalyst support material such as silica gel, alumina or other suitable inorganic support material. When prepared in heterogeneous or supported form, it is preferred to use silica as the support material. The heterogeneous form of the catalyst system is employed in a slurry polymeπzation. As a practical limitation, slurry polymerization takes place in liquid diluents in which the polymer product is substantially insoluble Preferably, the diluent for slurry polymerization is one or more hydrocarbons with less than 5 carbon atoms If desired, saturated hydrocarbons such as ethane, propane or butane may be used in whole or part as the diluent. Likewise the α-olefin monomer or a mixture of different α-olefin monomers may be used in whole or part as the diluent. Most preferably the diluent comprises in at least major part the α-olefin monomer or monomers to be polymeπzed. In contrast, solution polymeπzation conditions utilize a solvent for the respective components of the reaction, particularly the EP or EPDM polymer. Preferred solvents include mineral oils and the various hydrocarbons which are liquid at reaction temperatures. Illustrative examples of useful solvents include alkanes such as pentane, iso-pentane, hexane, heptane, octane and nonane, as well as mixtures of alkanes including kerosene and Isopar E™, available from Exxon Chemicals Inc , cycloalkanes such as cyclopentane and cyclohexane; and aromatics such as benzene, toluene, xylenes, ethylbenzene and diethylbenzene. At ail times, the individual ingredients as well as the recovered catalyst components must be protected from oxygen and moisture. Therefore, the catalyst components and catalysts must be prepared and recovered in an oxygen and moisture free atmosphere. Preferably, therefore, the reactions are performed in the presence of an dry, inert gas such as, for example, nitrogen. As previously mentioned however, should some hydrolysis occur, the preferred catalyst composition includes organoaluminum hydrocarbyloxide compounds that result in formation of hindered phenolic compounds, especially 2,6-dι(t-butyl)-4-methyl-phenol. Generally the polymerization process is earned out with a differential pressure of ethylene of from about 10 to about 1000 psi (70 to 7000 kPa), most preferably from about 40 to about 400 psi (30 to 300 kPa). The polymeπzation is generally conducted at a temperature of from 25 to 200 °C, preferably from 75 to 170 °C, and most preferably from greater than 95 to 140 °C The polymeπzation may be carried out as a batchwise or a continuous polymerization process A continuous process is preferred, in which event catalyst, ethylene, α-olefin, and optionally solvent and diene are continuously supplied to the reaction zone and polymer product continuously removed therefrom. The skilled artisan will appreciate that the invention disclosed herein may be practiced in the absence of any component which has not been specifically disclosed. The following examples are provided as further illustration of the invention and are not to be construed as limiting. Unless stated to the contrary ail parts and percentages are expressed on a weight basis. Examples 1-8 A stirred 3.8 liter reactor was charged with 1440 g of Isopar-E™ mixed alkanes solvent (available from Exxon Chemicals Inc.) and 126 g of 1 -octene comonomer. Hydrogen was added as a molecular weight control agent by differential pressure expansion from a 75 mL addition tank at 25 psi (2070 kPa). The reactor was heated to the polymeπzation temperature of 130 S C and saturated with ethylene at 450 psig (3.1 MPa). Approximately 2.0 μmol each of (t-butyiamιdo)dι-methyl(η 5 - tetramethyicyciopentadιeπyl)sιlanetιtaπιum (II) η 4 -1 ,3-pentadιene and tnspentafluorophenylborane cocatalyst as 0.005 M solutions in toluene were premixed in a drybox with a variable amount of one of several organoaluminum hydrocarbyloxide compounds to be tested, and transferred to a catalyst addition tank and injected into the reactor over approximately a four minute peπod. The organoaluminum hydrocarbyloxide compounds used were diethylalumiuum ethoxide (DEAL-E), dnsobutylaluminum ethoxide (DiBAL-E), diisobutylalumiuπ n-butoxide (DiBAL-B), and diisobutylaluminum (2,6-dι(t-butyl)-4-methy!phenoxιde (DiBAL-BOT) All of the organoaluminum hydrocarbyloxide compounds were obtained from Akzo Chemicals Inc. The polymerization conditions were maintained for 10 minutes with ethylene on demand. The resulting solution was removed from the reactor, and a hindered phenol antioxidant (Irganox™ 1010 from Ciba Geigy Corporation) was added to the resulting solution. Polymers formed were dπed in a vacuum oven set at 120 S C for about 20 hours. Results are contained in Table 1. Table 1 Run Aluminum cmDd. AI:Ti' Efficiency 2 1 DEAL-E 2.5 694,000 2 " 10 615,000 3 DiBAL-B 2.5 556,000 4 " 10 535,000 5 DiBAL-E 2.5 814,000 6 " 10 829,000 7 DiBAL-BOT 2.5 1 ,155,000 8 10 1 ,234,000 9 * none 0 <500,000 alumιnum:tιtanιum molar ratio g ethylene consumed/ g titanium comparative, not an example of the invention

Claims: CLAIMS: 1 ■ A catalyst composition comprising in combination: a1) a rτιetal αxτ lex coπBspondng^^ L M V wherein: M is a metal of Group 4 of the Periodic Table of the Elements having an oxidation state of +2, +3 or +4, bound in an η bonding mode to L; L is a cyclopentadienyl-, indenyl-, tetrahydroindenyl-, fluoreπyl-, tetrahydrofluorenyl-, or octahydrofluorenyl- group covalently substituted with at least a divalent moiety, Z, and L further may be substituted with from 1 to 8 substituents independently selected from the group consisting of hydrocarbyl, halo, halohydrocarbyl, hydrocarbyioxy, dihydrocarbylamino, dihydrocarbylphosphino or silyl groups containing up to 20 non-hydrogen atoms, or two such substituents may together form a divalent derivative; Z is a divalent moiety bound to both L and M via σ-bonds, said Z comprising boron, or a member of Group 14 of the Periodic Table of the Elements, and optionally, also comprising nitrogen, phosphorus, sulfur or oxygen; X is an anionic or dianionic ligand group having up to 60 atoms, exclusive of the class of ligands that are cyclic, delocalized, π-bound ligand groups; X' independently each occurrence is a neutral ligating compound, having up to 20 atoms; p is 0, 1 or 2, and is two less than the formal oxidation state of M, with the proviso that when X is a dianionic ligand group, p is 1 ; and q is 0, 1 or 2; a1') an activating cocatalyst which forms a cationic derivative of a1 ); and b) an organoaluminum hydrocarbyloxide compound according to the formula R 1 2 AI(OR 2 ), wherein R 1 and R 2 independently each occurrence are C,. 30 hydrocarbyl, the molar ratio of a1): b) being from 1 :0.1 to 1 :100; or a catalyst composition compnsing in combination a cationic complex, a2) corresponding to the formula: [Z L M * X * P I A, wherein: M* is a metal of Group 4 of the Periodic Table of the Elements having an oxidation state of +3 or +4, bound in an η 5 bonding mode to L; L is a cyclopentadienyl-, mdenyl-, tetrahydromdenyl-, fluorenyl-, tetrahydrofiuorenyl-, or octahydrofluorenyl- group covalently substituted with at least a divalent moiety, Z, and L further may be substituted with from 1 to 8 substituents independently selected from the group consisting of hydrocarbyl, halo, halohydrocarbyl, hydrocarbyioxy, dihydrocarbylamino, dihydrocarbylphosphino or silyl groups containing up to 20 non-hydrogen atoms, or two such substituents may together form a divalent derivative; Z is a divalent moiety bound to both L and M * via σ-bonds, said Z comprising boron, or a member of Group 14 of the Periodic Table of the Elements, and also optionally comprising nitrogen, phosphorus, sulfur or oxygen; X * is an anionic ligand group having up to 60 atoms, exclusive of the class of ligands that are cyclic, delocalized, π-bound ligand groups; p* is 0 or 1 , and is three less than the formal oxidation state of M; and A is an noncoordinating, compatible anion, and b) an organoaluminum hydrocarbyloxide compound according to the formula R' 2 AI(OR ), wherein R and R independently each occurrence are C, ^ hydrocarbyl the molar ratio of a2): b) being from 1 :0.1 to 1 :100. 2. A catalyst composition according to claim 1 wherein the organoaluminum hydrocarbyloxide component, component b) corresponds to the formula R 2 AIOR wherein R 1 is C 3 6 secondary or tertiary alkyl; and R 2 is a C 12 30 alkaryl or aralkyl radical. 3. A catalyst composition according to claim 2 wherein the organoaluminum hydrocarbyloxide component is 2,6-dι(t-butyl)-4-methylphenyl, 2,6-dι(t-butyl)-4-methyltolyl, 2,6-dι(ι- butyl)-4-methylphenyl, or 4-(3',5'-dιtertιarybutyltolyl)-2,6-dιtertιarybutyi-phenyl. 4 A catalyst composition according to claim 1 wherein the molar ratio of metal complex (component a1 ) or a2)) to component b) is from 1 :1 to 1 :50. 5. A catalyst composition according to claim 1 wherein the activating cocatalyst is tnspentafluorophenylborane. 6. A process for polymenzation of addition polymerizable monomers or mixtures thereof compnsmg contacting said monomer or mixture of monomers with a catalyst system compnsmg the catalyst composition of claim 1 under addition polymenzation conditions. 7 The process of claim 6 wherein the addition polymenzable monomer is a C 2 20 α-olefin or a mixture thereof. 8. The process of claim 7 wherein the molar ratio of metal complex, component a1 ) or a2), to component b) is from 1 :1 to 1 :50.

Inventors: ROSEN ROBERT K, STEVENS JAMES C, TRACY JOHN C, ROSEN, ROBERT, K., STEVENS, JAMES, C., TRACY, JOHN, C.
Applicants: DOW CHEMICAL CO, ROSEN ROBERT K, STEVENS JAMES C, TRACY JOHN C, ROSEN, ROBERT, K., STEVENS, JAMES, C., THE DOW CHEMICAL COMPANY, TRACY, JOHN, C.
Application year: 1996
Main classification: C08F10
IPC codes: C08F4, C08F10, C08F210