PHOTO-POLYMERIZATION OF VINYL CHLORIDE USING METALLOCENE CATALYSTS

Abstract: A process for polymerizing vinyl chloride monomer in the presence of light. A mixture is formed of liquid vinyl chloride monomer, preferably about 50 to about 125 ppm of a metallocene catalyst, about 1 to about 2000 moles of an aluminum-containing co-catalyst per mole of catalyst, and optionally up to about 500 moles of a Lewis base per mole of aluminum in the co-catalyst. Selected alkyl groups from the aluminum-containing co-catalyst can be placed on the ends of the poly (vinyl chloride) chains.

Description: PHOTO-POLYMERIZA ION OF VINYL CHLORIDE USING METALLOCENE CATALYSTS THIS INVENTION relates to the photopolymerization of vinyl chloride using metallocene catalysts. In particular, it relates to the photopolymerization of vinyl chloride using cyclopentadienyl or cyclopentadienyl-type transition metal catalysts in the presence of an aluminum-containing co-catalyst and an optional base. Vinyl chloride monomer (VCM) is commercially polymerized to produce poly (vinyl chloride) (PVC) using peroxide initiators. Because peroxides are unstable and can even be explosive, they must be handled and stored very carefully at low temperatures, which complicates and adds to the cost of the manufacturing process. Moreover, elevated temperatures are usually required in polymerization reactions initiated by peroxides (50 to 80°C) , which can deteriorate the properties of the product. The free-radical nature of the traditional polymerization process implies that the product properties, such as tacticity, molecular weight, and polydispersity, are not influenced in any way by the structure or composition of the free-radical initiator. We have discovered that vinyl chloride can be polymerized using metallocene catalysts if light is present. We further discovered that the activity of the catalyst can be enhanced by the presence of a co-catalyst and a base. According to this invention there is provided a method of making poly (vinyl chloride) comprising the step of polymerizing vinyl chloride monomer in the presence of light, a metallocene catalyst, and at least 1 mole of an aluminum-containing co-catalyst per mole of said catalyst. The co-catalyst may be considered not to be a catalyst in the strict sense of the word as the co-catalyst can enter into the polymerisation reaction. Preferably the amount of catalyst is at least 2 ppm, advantageously at least 10 ppm, based on monomer weight. A preferred amount of catalyst is about 2 to about 250 ppm, and the most preferred amount of catalyst is about 50 to about 125 ppm. The amount of co-catalyst is preferably about 1 to about 2,000 moles per mole of said catalyst. Preferably said metallocene catalyst has the general formula L\ \ M — (X) where each X is independently selected from halogen, alkyl from Ci to Co/ oxyalkyl or oxyaryl from d to C 30 , or - N(R') 2 , where each R' is independently selected from hydrogen, alkyl from Ci to (Y, aryl from C 6 to Cι 5 , alkaryl from C 7 to C15, and aralkyl from C 7 to Cι 5 , L is a ligand containing a cyclopentadienyl ring or an anionicheterocyclic ring that is isoelectronic with a cyclopentadienyl ring, L' is L or X, and n is 1, 2, or 3. Conveniently L has the formula where each R is independently selected from hydrogensilyl, germyl, cyano, R"OR", or halogen, where R" is a Ci to C 2 o hydrocarbyl group, or two R groups are joined together to form a C 4 to C fa ring, and m is 1 to 5. Thus L may be cyclopentadienyl or indenyl . Alternative!v L is R, where each R is independently selected from hydrogen, silyl, germyl, cyano, R"OR", or halogen, where R" is a Ci to C 2 o hydrocarbyl group, or two R groups are joined together to form a C 4 to C L ring, Ri is hydrogen, N(R') 2/ OR', or R' , each R' is independently selected from halogen, alkyl from Ci to Cio, aryl from C 6 to C] 5 , and aralkyl from C to Cι 5 , and m is 1 to the maximum number of substituents allowable on the ring. Thus L may be borabenzene, boranaphthalene, or boraanthracene . Alternatively again L has the formula: where R 2 is alkyl from Ci to Cι 2 or aryl from C 6 to C12, alkaryl from C G to Cι 2/ aralkyl from C b to d 2/ or Si(R') 3 / R3 is R 2 , halogen, COR' , COOR' , SOR' , or SOOR' , R' is alkyl from Ci to do / aryl from C 6 to C^, alkaryl from C 7 to C15, or aralkyl from C 7 to C 15 , and m is 1 to the maximum number of substituents on the ring. Advantageously the R 2 group on the boron is alkyl from d to d 2 or aryl, R^ group is t- butyl or trimethylsilyl, and the R ^ , group on the ring is hydrogen 01 methyl. In an alternative embodiment L is where R is independently selected from hydrogen, silyl, germyl, cyano, R"OR", or halogen, where R" is a Ci to C ;: hydrocarbyl group, or two R groups are joined together to form a C 4 to C 6 ring, and m is 1 to the maximum number of substituents on the ring, Z is N or P, and m is 1 to the maximum number of substituents on the ring. It is preferred that M is zirconium, titanium or hafnium. In particularly preferred embodiments of the invention said metallocene catalyst is selected from the group consisting of and where tBu is tertiary butyl. Conveniently said aluminum containing co-catalyst has the general formula R"' pAlX' (3 - p) , where R"' is alkyl from to C 5 o X is hydrogen, halogen, alkoxy, phenoxy, amino, imino, amido, or OR"", where R"" is alkyl, aryl, or where R 4 is hydrogen, alkoxy, or alkyl, and p is 1 to 3. Advantageously said aluminium-containing co-catalyst has the general formula -(0-Al-R 5 ) α or (0-Al-R 5 ) q (0-Al-R 6 ) r , where R 5 and R b are independently selected from (Ci to C 50 ) alkyl, and where q+r is 5 to 100. Preferably a Lewis base is also present during the polymerisation step, there being at least about 2 moles of Lewis base per mole of aluminium in said co-catalyst. Considered from another perspective a Lewis base is also present during the polymerisation step, the amount of said Lewis base is up to about 500 moles per mole of aluminium m said co-catalyst. Conveniently the amount of said Lewis base is about 2 to about 300 moles per mole of aluminium said co-catalyst. The preferred Lewis base is tetrahydrofuran . Conveniently at the light is light in the UV or visible region of the spectrum. Advantageously the light is provided from a light source providing at least IW for each 100 ml of the monomer, catalyst and co-catalyst. Preferably the light source provides at least 10W for each 100 ml of the monomer, catalyst and co-catalyst. According to a second aspect of this invention there is provided a method of producing poly (vinyl chloride) chains terminated with alkyl groups comprising (A) preparing a mixture of (1) vinyl chloride monomer; (2) a metallocene catalyst; (3) at least 1 mole per mole of said catalyst of an aluminium-containing said alkyl groups; and (4) about 2 to about 300 moles of a Lewis base per mole of aluminium in said co- catalyst; and (B) exposing said mixture to at least about IW output radiation in the ultraviolet or visible region, whereby said alkyl groups on said aluminum containing co-catalyst are transferred to the ends of said poly (vinyl chloride) chains. The invention relates to polyvinyl chloride when made by a method as described above. According to a further aspect of this invention there is provided a composition comprising vinyl chloride monomer, about 10 to about 250 ppm of a metallocene catalyst, about 1 to about 2000 moles of an aluminum-containing co-catalyst per mole of said catalyst, and up to about 500 moles of a Lewis base per mole of aluminum in said co-catalyst. Conveniently the amount of said catalyst is about 50 to about 125 ppm, the amount of said co-catalyst is about 2 to about 500 moles per mole of said catalyst, and the amount of Lewis base is about 2 to about 300 moles per mole of aluminium in said co-catalyst. PVC made by a method according to this invention has been found to be of superior quality. Nuclear magnetic resonance (NMR) studies of PVC produced by a method according to this invention indicate a substantially lower level of unsaturated end groups compared with polymers made using traditional free radical polymerized PVC. A particular aspect of a preferred method of this invention is the ability of an optional base to enhance the transfer of alkyl groups from the aluminum co-catalyst to the growing polymer macroradical . This has two effects. First, it terminates the growing polymer chain, thereby limiting the molecular weight of the PVC. Thus, it is possible to produce ultra- low molecular weight PVC (i.e., M n <20,000) in bulk at room temperature. Second, it alters the properties of the PVC by placing unique alkyl groups at the ends of the PVC chains. PVC having tailored properties that are unobtainable by other means can therefore be produced by a process in accordance with this invention. In order that the invention may be more readily understood, the invention will now be described, by way of example, with reference to the accompanying drawings in which : Figure 1 is a 13 C nuclear magnetic resonance (NMR) spectrum of PVC prepared by a method according to this invention, Figure 2 shows the relationship between polymerization temperature (°C) and number average molecular weight (M for commercial PVC and PVC prepared by a method according to this invention, Figures 3a and 3b are proton NMR spectra of commercial PVC, Figures 4a and 4b show the spectra of PVC samples prepared by a method according to this invention, and Figure 5 shows the relationship between glass transition temperature (T q in °C) and M„ for commercial PVC samples and for samples prepared by a method according to this invention. In the practice of this invention, vinyl chloride monomer (VCM) is polymerised in the presence of light using a metallocene catalyst and an aluminum-containing co- catalyst . The Metallocene Catalyst The preferred amount of metallocene catalyst is at least 2 ppm, and most preferably about 10 to about 250 ppm (based on monomer weight) as less catalyst is ineffective and mor.e catalyst is unnecessary. The most preferred amount of metallocene catalyst is about 50 to about 125 ppm. Almost any metallocene catalyst can be used in this invention, where "metallocene" means a transition metal pi bonded to at least one cyclopentadienyl group or to a group containing a cyclopentadienyl ring or to a group containing a cyclopentadienyl-type of ring, i.e., a heterocyclic ring that is anionic, has 6 pi electrons for bonding, and is isoelectronic with a cyclopentadienyl ring. A suitable catalyst can have a general formula: where each X is independently selected from halogen, alkyl from Ci to C 3o oxyalkyl or oxyaryl from C, to C 30 / or - N(R') 2 , where each R' is independently selected from hydrogen, alkyl from d to Cm, aryl from C„ to C 15 , alkaryl from C 7 to C ι5 , and aralkyl from C to ds, L is a ligand containing a cyclopentadienyl ring or an anionic heterocyclic ring that is isoelectronic with a cyclopentadienyl ring, L' is L or X, M is a Group IV transition metal, and n, the valency of M minus 2, is 1, 2, or 3. The transition metal is preferably titanium, zirconium, or hafnium because those catalysts are believed to be superior; zirconium is most preferred as zirconium catalysts tend to produce a PVC that is less colored. The X group is preferably halogen or alkyl from Ci to and is most preferably chlorine or methyl as those catalysts are easier to make. The L and L' ligands are preferably independently selected from cyclopentadienyl and indenyl as those catalysts are easier to prepare and have good activity. Examples of L groups include ligands containing (1) a cyclopentadienyl ring, (2) a borabenzene ring, (3) a 1,2- azaborolinyl ring, or (4) a pyrrolyl or phospholyl ring. Cyclopentadienyl Catalysts In certain embodiments L can have the formula: where each R is independently selected from hydrogen, silyl (such as Si(CH 3 ) 3 ), germyl, cyano, R"OR", or halogen, where R" is a Ci to o hydrocarbyl group (such as alkyl, alkenyl, aryl, alkylaryl, or arylalkyl), preferably a d to C 6 group, and x m' is 1 to the maximum number of substituents on the ring. Alternatively, the R group can be a fused C to C 6 ring, with other groups on the two rings optionally substituted with R groups. Examples of alkyl substituted Cp rings include butyl cyclopentadienyl, methyl cyclopentadienyl, and pentamethylcyclopentadienyl (Cp*) and examples of fused ring systems include indenyl and fluorenyl: indenyl fluorenyl Examples of ligands containing fused ring systems include 2- ethylindenyl, tetrahydroindenyl, 2, 2 ' -dimethylfluorenyl, and 2-methylindenyl . Borabenzene Catalysts In alternative embodiments L can contain the group: where Ri is hydrogen, N(R') 2 , OR', or R' and is preferably - N(R') 2 or phenyl, as those catalysts have the best properties; if Rj is -N(R') 2 '/ then R' is preferably methyl. Examples of ligands containig a borabenzene ring include: borap enantlirene Examples of metallocene catalysts containing borabenzene rings include: (1-methyl borabenzene) zirconium trichloride; (1-ethyl borabenzene) zirconium trichloride; (1-tert-butyl borabenzene) zirconium trichloride; (N, N-dιmethyl-1-amιnoborabenzene) zirconium trichloride; (N, N-dιethyl-1-ammoborabenzene) zirconium trichloride; ( 9-mesιtyl-9-boraanthracene) zirconium trichloride; ( 9-phenyl-9-boraanthracene) zirconium trichloride; (9-methyl-9-boraanthracene) zirconium trichloride; (9-ethyl-9-boraanthracene) zirconium trichloride; (N, N-dimethyl-9-amino-9-boraanthracene) zirconium trichloride; (N, -diethyl-9-amino-9-boraanthracene) zirconium trichloride; and (N, N-dimethyl-l-amino-3, 5-dimethyl borabenzene) zirconium trichloride. The preferred borabenzene-containing ligands are borabenzene, boranaphthalene, and boraanthracene because those catalysts are easier to prepare. Azaborolinyl Catalysts Alternatively again L can have the formula: where R 2 is alkyl from Ci to Cι_ or aryl from C 6 to Cι 2 , alkaryl from d to d_/ aralkyl from C 6 to Cι 2 , or Si(R') 3 , R 3 is R 2 , halogen, COR', COOR' , SOR' , or SOOR' , and R' is alkyl from Ci to Cio / aryl from C b to ds/ alkaryl from d to C15, or aralkyl from C 7 to C15. The R_. group on the boron is preferably alkyl from d to C ]2 or aryl, the R 3 group is preferably t-butyl or trimethylsilyl, and the R 2 group on the ring is preferably hydrogen or methyl as those compounds are easier to make. Fused ring systems containing the 1,2- azaborolmyl ring typically contain four to six carbon atoms. Examples of fused ring structures that can be used include: Examples of metallocene catalysts containing 1,2- azaborolmyl ring include: (l-tert-butyl-2-methyl azaborolmyl) zirconium trichloride; (l-tert-butyl-2-ethyl azaborolmyl) zirconium trichloride; (l-tert-butyl-2-phenyl azaborolmyl) zirconium trichloride; (l-trimethylsilyl-2-methyl azaborolinyl ) zirconium trichloride; ( l-trimethylsilyl-2-phenyl azaborolinyl) zirconium trichloride; and (l-methyl-2-methyl azaborolinyl ) zirconium trichloride Pyrrolyl and Phospholyl Catalysts Alternatively again L can have the structure: where Z is N or P, and is preferably N. Examples include 2- methylpyrrolyl, 3-methylpyrrolyl, 2, 5-dimethylpyrrolyl, 2,5- di-tert-butylpyrrolyl, aryl substituted pyrrolyl rings such as 2-phenylpyrrolyl, 2, 5-diphenylpyrrolyl, indolyl, alkyl substituted indolyls or their phosphoindenyl analogues such as 2-methylindolyl, 2-tert-butylindolyl, 3-butylindolyl, 7- methylindolyl, 4, 7-dimethylindolyl, aryl substituted indolyls such as 2-phenylindolyl, 3-phenylindolyl, 2- naphthylindolyl, isoindolyl, and alkyl and aryl substituted isoindolyls having the formulas: indolyl isoindolyl and carbazolyl and alkyl substituted carbazolyls having the formula : and their phospho analogues. The alkyl and aryl substituents (R) on the pyrrolyl ring-containing ligand are not on the nitrogen atom in the ring but are on the carbon atoms of the ring. Examples of metallocene catalysts containing pyrrolyl or phospholyl rings include: (l-phospha-2, 3, , 5- tetramethylcyclopentadienyl ) zirconium trichloride; ( l-phospha-2, 3,4,5- tetramethylcyclopentadienyl) zirconium trimethyl; ( l-phospha-2, 3, 4 , 5- tetramethylcyclopentadienyl ) zirconium tribenzyl; (l-phospha-2, 3,4,5- tetramethylcyclopentadienyl) zirconium methyldichloride; (l-phospha-2, 3,4,5- tetramethylcyclopentadienyl) zirconium tπhydride; (l-phospha-3, -dιphenylcyclopentadιenyl) zirconium trichloride; (l-phospha-3, 4-dιphenylcyclopentadιenyl ) zirconium trimethyl ; (l-phospha-3, 4-dιphenylcyclopentadιenyl) zirconium tribenzyl; (l-phospha-3, -dιphenylcyclopentadιenyl ) zirconium methyldichloride; (l-phospha-3, 4-dιphenylcyclopentadιenyl ) zirconium trihydride; (l-phospha-3, 4-dιmethylcyclopentadιenyl ) zirconium trichloride; ( 1-phosphamdenyl) zirconium trichloride; ( l-phospha-3-methoxycarbonylcyclopentadιenyl ) zirconium trichloride; (1, 3-dιphospha-4, 5-dιphenylcyclopentadιenyl ) zirconium trichloride; (1,2, -trιphospha-3, 5- diphenylcyclopentadienyl) zirconium trichloride; (1,2,3, 4-tetraphospha-5- phenylcyclopentadienyl) zirconium trichloride; (pentaphosphacyclopentadienyl) zirconium trichloride; (l-phospha-3-benzoyloxycyclopentadienyl) zirconium trichloride; (imidazolyl) zirconium trichloride; (imidazolyl) zirconium trimethyl; (imidazolyl) zirconium tribenzyl; (imidazolyl) zirconium methyldichloride; (imidazolyl) zirconium trihydride; (pyrazolyl) zirconium trichloride; (1, 2, 3-triazolyl) zirconium trichloride; (1, 2, 4-triazolyl) zirconium trichloride; (tetrazolyl) zirconium trichloride; and (pentazolyl) zirconium trichloride. Bridging The L group can be bridged to the L' group with various bridging groups that are known in the art such as methylene, ethylene, 1, 2-phenylene, dimethyl silyl, diphenyl silyl, diethyl silyl, and methyl phenyl silyl. The preferred bridging groups are ethylene and silyl as those catalysts are easier to make. Normally, only a single bridge is used in a catalyst. It is believed that bridging the two ligands changes the geometry around the catalytically active transition metal and improves catalyst activity and other properties, such as comonomer incorporation and thermal stability. Co-catalyst An aluminum-containing co-catalyst is required in the process of this invention. The co-catalyst can be either an alkyl aluminum derivative or an alkyl alummoxane. Alkyl aluminum co-catalysts have the general formula R"'pAlX' (3 _p), where R"' is alkyl from C, to C 50 , X' is hydrogen, halogen, alkoxy, phenoxy, ammo, imino, amido, or OR"", where R"" is alkyl, aryl, or where R 4 is hydrogen, alkoxy, or alkyl, and p is 1 to 3. The trialkyl aluminum co-catalysts can be made by several methods known in the art, such as adding dialkyl aluminum hydrides to olefms, and the Ziegler reaction of isobutyl aluminum with long chain olefms. The other alkyl aluminum co-catalysts are prepared by reaction of the trialkyl aluminum compound with the appropriate alcohol, phenol, am e, or amide derivative. Alkyl aluminoxane co-catalysts have the general formula -(0-Al-R 5 ) η or (0-Al-R 5 ) q (0-Al-R_) r , where R 5 and R 6 are independently selected from Ci to C 50 alkyl, and q+r is 5 to 100. If q+r is less than 5 the co-catalyst is hard to make and if q+r is more than 100 the catalyst becomes insoluble; q+r is preferably about 10 to about 30. The preferred co- catalysts are (0-Al-CH 3 ) q and (0-Al-CH 3 ) q (O-Al-isobutyl) r because they are available commercially. Examples of these co-catalysts include poly (methylaluminoxane) (PMAO) , poly (isobutylaluminoxane) (PBAO) , poly (octylaluminoxane) (POAO) and poly(methyl) (i-butyl) aluminoxane) (MMAO) . The mole ratio of co-catalyst to catalyst is preferably about 1 to about 2000 as at mole ratios less than 1 the co- catalyst is ineffective and mole ratios over 2000 are unnecessary. The amount of co-catalyst used is inversely proportional to the molecular weight (MW) of the resulting PVC (i.e., a higher MW is obtained if less co-catalyst is used and a lower MW is obtained if more co-catalyst is used) . The preferred molar ratio of co-catalyst to catalyst depends on the molecular weight desired and can be in the range of about 2 to about 500 moles per mole of catalyst. The co-catalyst may be considered to be a reactant rather than a catalyst as strictly defined. Base Up to about 500 moles per mole of aluminum in said co- catalyst of a Lewis base can be included, if desired, as part of the catalyst system. The purpose of the Lewis base is to increase the activity of the catalyst, enhance the quality of the PVC produced, and control the molecular weight of the PVC. The presence of the Lewis base lowers the molecular weight of the resultant polymer, probably by facilitating the transfer of alkyl groups from the co- catalyst to the growing polymer chain. Examples of bases that can be used in this invention include oxygen-containing bases, such as ethers (e.g., diethylether, dibutylether, tetrahydrofuran (THF) , and 1 , 2-dimethoxyethane) and esters (e.g., n-butylphthalate, ethylbenzoate, and ethyl p- anisate) , nitrogen-containing bases such as pyridine and tertiary amines (e . g. , triethylamine) , and phosphorus- containing bases, such as phosphines (e.g., triethyl phosphine, tributyl phosphine, and triphenyl phosphine, PPh 3 ) . The amount of base is preferably about 2 to about 300 moles per mole of aluminum in the co-catalyst as less base results in a less active catalyst and lowers the quality of the PVC and more base is unnecessary and usually must be removed from the PVC. Many bases are solvents for this process, and the amount of base used is preferably less than the amount at which it begins to act as a solvent. Polymerization The polymerization proceeds in the presence of light. While ultraviolet light (UV) can be used, it is not essential for the light to be UV, and visible light is also effective. Any source of light can be used, such as, for example, fluorescent lamps, incandescent lamps, or halogen lamps. However, to obtain significant yields, it is appropriate to use a light source with a radiated output in the UV or visible region of the spectrum of at least IW per 100 ml reaction volume; radiation of at least about 10W is preferred. The polymerization is preferably performed at room temperature, although it can be performed at higher or lower temperatures if desired. No solvent is needed in the process of this invention. The VCM is polymerized as a liquid, which can be achieved by cooling to below -15°C at atmospheric pressure or at higher temperatures under pressure, such as at a pressure of about 345 kPa (about 50 psi) at a temperature of about 20 to about 30°C. The polymerization normally takes about 1 to about 6 hours and is performed in a glass vessel or an opaque vessel fitted with means to permit exposure of the VCM to light. The PVC is produced as a powder which precipitates from the excess VCM. Excess VCM is removed and methanol is added to kill the catalyst and co-catalyst and help precipitate the PVC from the VCM. The solid PVC is isolated by filtration. The following examples further illustrate this invention. All the metallocene complexes used in the examples were either prepared according to literature procedures or purchased from Strem Chemicals, Aldrich Chemical Co., or Boulder Scientific Co. Some of the trialkylaluminum compounds were purchased from Aldrich Chemicals Co., while others were prepared using known procedures. The alkylaluminoxane solutions were purchased from AKZO Inc. VCM was purchased from Aldrich Chemicals and purified by passing the vapors through a calcined (200°C) molecular sieve column. General Polymerization Procedures Method A. A catalyst/co-catalyst/modifier (e.g. Lewis base) mixture was charged to a dry Pyrex 100 ml pressure tube in a dry box. The pressure tube was evacuated, cooled with an ice bath, and pressurized with VCM. After condensation of the required amount of monomer, the closed reactor with the stirred mixture was heated to the required temperature and irradiated with a light source. After a specific reaction time, the excess VCM was removed and the residue quenched with excess methanol. The precipitated PVC was filtered, washed with methanol, and dried. Method B. A dry reactor (100 ml Pyrex pressure tube or 1000 ml borosilicate Buchi reactor) was evacuated, cooled with an ice bath or constant temperature bath, and pressurized with VCM. After condensation of the required amount of monomer, the catalyst/co-catalyst system and the modifier were charged to the closed reactor. The stirred mixture at the required temperature was exposed to a light source. After a specific reaction time, the excess VCM was removed and the residue quenched with excess methanol. The precipitated PVC was filtered, washed with methanol, and dried. Results 1. Metallocenes with poly (alkylaluminoxane) co-catalysts Active catalysts for VCM polymerization were generated from metallocene dichloride precursors and different polyalkylaluminoxane co-catalysts . 1.1 Preliminary studies - Polymerization in dark Initial polymerization reactions were conducted in Pyrex pressure tubes at ambient illumination (fume-hood, no direct light source) and were considered to be "dark" polymerizations, even though no special measures were taken to shield the reaction vessels. Initially, the attempted polymerization of VCM in toluene solution using bis (cyclopentadienyl) zirconium dichloride (see formula 1) or bis (pentamethylcyclopentadienyl) zirconium dichloride (see formula 2) with methylalummoxane did not produce PVC. When the polymerization was conducted m bulk using the metallocenes (formula 1), bis (2-methylmdenyl) zirconium dichloride (formula 3) and rac- (racemic) dimethylsilyl (2- methymdenyl) zirconium dichloride (formula 4) with poly (methylalummoxane) (PMAO) and modified poly (methylalummoxane) (MMAO) some polymerization was observed (Table 1), but the color of the resulting product was usually yellow to dark brown, especially when MMAO was used as the co-catalyst. H NMR spectra of the polymer samples contained intense signals m the area of olefmic protons, indicating that the product was partially dehydrochlormated. However, when a Lewis base, such as tetrahydrofuran (THF) was added to the catalyst system, the dehydrochlormation process was inhibited without influencing significantly the catalyst activity. Apparently, the base coordinates to the metallocenium cation and/or the aluminum atom of the co-catalyst, thereby greatly reducing the Lewis acidity of the catalytic system. The catalysts used had the following formulas: where "tBu" is tertiary butyl. 1.2 Photopolymerization - effect of reaction conditions on activity During preliminary screening experiments, it was observed that the polymer yield significantly increased when the reaction mixture in the Pyrex reactor was illuminated. Data presented in Table 2 indicates that the polymerization of VCM can be efficiently photoinitiated by different light sources in visible and UV area of the spectrum. Further polymerization experiments were conducted using a 200 watt incandescent light bulb as the visible light source. A number of titanium and zirconium metallocene complexes were tested with an MMAO co-catalyst and a THF base in VCM polymerization (Table 3) . The activity of the catalytic systems varied over a broad range, from negligible in case of titanocene dichloride, to reasonably high (more than 130 kg of PVC per mole of transition metal) in case of the "constrained geometry" dimethylsilyl (tetramethylcyclopentadienyl ) (t-butylamido) titanium dichloride complex (formula 5) and ansa-bis ( indenyl ) complex (formula 4) . The indenylzirconium complexes were found to be generally more active with MMAO co-catalyst, and among the various systems examined, the commercially available, silicon-bridged ansa-bis (indenyl) complex (formula 4) had the highest activity. Hence, further studies on catalyst systems were based on the complex in formula 4. Experiments with different levels of catalyst concentrations indicated that the activity (kg PVC/mole of metal) is higher at the lower catalyst level (Table 4) indicating the presence of some kind of bimolecular catalyst deactivation process. All the polyalkylaluminoxane co- catalysts tested with the metallocene complex of formula 4 had comparable activities (Table 5) . The activity of the catalyst system increases only slightly with increasing Zr/Al ratio, as determined in experiments using the formula 4/MMAO/THF catalyst system (Table 6) . As mentioned hereinabove, polymerization of VCM with a catalyst system metallocene/alkylaluminoxane, unmodified with a base, such as THF, produces a yellow, partially dehydrochlorinated PVC. Other bases, such as anisole, triphenylphosphine, triethylamine, and diethyl ether, were also successful in inhibiting the degradation of PVC by the catalyst system. The activity of the catalytic system varied only slightly as a function of the type of base used. An exception was pyridine, which drastically lowered the catalyst activity (Table 7) . Experiments with a THF- modified catalyst system showed that the Al/THF ratio did not influence the polymerization activity significantly (Table 8) and THF can even be used as a solvent. Other solvents, such as toluene or heptane, can also be used without significant changes in the activity of the metallocene-based catalyst (Table 9) . Tables 10 and 11 show the results from large scale polymerization of VCM using a metallocene photoinitiator in a 1L borosilicate glass reactor. 1.3. Tacticity of PVC The tacticity of PVC was accurately and easily determined using ^-decoupled Y NMR spectra of the polymer. Figure 1 shows the partial spectrum in the methine (CHCl) carbon region for a THF-d 6 solution of a PVC sample made with a new catalyst. It consisted of three well-separated peaks, characteristic of the rr (syndiotactic), mr (atactic) and mm (isotactic) triads. These triad peak areas were used to obtain values for P L , the probability of syndiotactic placement of the monomer unit. This value corresponds to the tacticity of the polymer and was simply obtained from the equation P t = (rr) + 0.5(mr). The tacticity of PVC samples made using radical initiators depends upon the temperature of polymerization. The P L values vary between 0.545 for the polymer made at 90°C and 0.62 for a low temperature product made at -30°C, indicating an increase in the syndiotacticity with decreasing polymerization temperature. Remarkably, the tacticity of polymers photoinitiated by the metallocene catalysts was not sensitive to variation m metallocene structure (Table 2) and is similar to that usually observed in traditional free radical polymerization. 1.4. Molecular Weight Values of number average molecular weight, M n , in Tables 2-9 indicate that the degree of polymerization of VCM in the presence of metallocene photomitiator systems is quite sensitive to variation in catalyst composition. In traditional free-radical polymerization processes the molecular weight of PVC is almost totally dependent on the polymerization temperature (Figure 3) . In general, the molecular weight of our PVC samples was significantly lower than what one might expect with traditional free-radical initiators. Figure 2 gives the relationship between polymerization temperature and molecular weight for commercial PVC (line A), the catalyst of formula (4) with an MMAO co-catalyst in THF (line B) , and the catalyst of formula (4) with an MMAO co-catalyst in anisole (line C) . Besides temperature, the nature of the base used to modify the co-catalyst also exerted a major influence on the molecular weight. When anisole or triphenylphosphine was used as the modifier, ultra-low molecular weight (M n < 20,000) PVC was obtained (Table 7) at ambient temperature in bulk. The intrinsic viscosity of these samples in cyclohexane at 30°C is expected to be less than 0.4 (or K<40) . Polymerization in solvents tended to reduce the molecular weight, apparently through chain transfer to the solvent (Table 9) . Increasing the catalyst concentration also tended to decrease the molecular weight. The polydispersity of the PVC samples (mostly between 2.5 and 3.0) was slightly higher than the values characteristic for traditional free-radical polymerization (2.0 to 2.5). Table 1 VCM Polymerization in Bulk with Metallocene Catalysts in "Dark"." 3 Conditions: a Conditions: 15 ml VCM, Zr = 0.0000038 moles; Al/THF molar ratio =1. b Al/Zr ratio = 156. c Al/Zr ratio = 235. d Polymerization time was 3 hours. Table 2. Effect of light source on vinyl chloride photo ¬ polymerization in bulk with rac-dimethylsilyl (2- methylindenyl) zirconium dichloride (4) /MMAO/THF catalyst system. 3 a Conditions: 15 ml VCM, 0.00000756 moles Zr, Al/Zr ratio = 215, Al/THF mol. ratio = 1, 1 hour, 30 °C Relative ratio of H NMR peak heights of terminal alkyl group at 0.9 ppm to terminal allyl chloride at 4.1 ppm. c 3 hours at 50°C. 3 hours Table 3. Vinyl Chloride Photopolymerization m Bulk with Metallocene /MMAO/THF catalyst system. 3 a Conditions: 15 ml VCM, 0.0000038 moles metallocene, MMAO co-catalyst (AKZO), Al/Zr ratio 215, 0.06 ml THF, 1 hour, 35 °C, 200 W incandescent light source at 5.08 cm (2 inch) distance . Table . Effect of Catalyst Concentration on Vinyl Chloride Photopolymerization in Bulk with rac- Dimethylsilyl (2-methylindenyl) zirconium Dichloride ( ) /MMAO/THF Catalyst System. 3 a Conditions: 15 ml VCM, Al/Zr ratio = 215, Al/THF molar ratio =1, 1 hour, 30 °C, 200 W incandescent light source at 5.08 cm (2 inch) distance. b 2 hours polymerization time. Table Effect of Aluminoxane Co-catalyst on Vinyl Chloride Photopolymerization in Bulk with rac-Dimethylsilyl (2-methylindenyl) zirconium Dichloride (4_) /AO/THF Catalyst System. a Conditions: 15 ml VCM, Zr = 0.0000038; Al/Zr ratio = 215, Al/THF molar ratio =1, 1 hour, 30 °C, 200 incandescent light source at 5.08 cm (2 inch) distance. b Relative ratio of H NMR peak heights of terminal alkyl group at 0.9 or 1.1 ppm to terminal allyl chloride at 4.1 ppm. Table 6. Effect of Al/Zr Ratio on Vinyl Chloride Photopolymerization in Bulk with rac-Dimethylsilyl (2- methylindenyl) zirconium Dichloride ( _) /MMAO/THF Catalyst System. d a Conditions: 15 ml VCM, 0.00000756 moles Zr, Al/THF molar ratio 1, 1 hour, 35 °C, 200 W incandescent light source at 5.08 cm (2 inch) distance . Table Effect of Base on Vinyl Chloride Photopolymerization in Bulk with rac-Dimethylsilyl (2- methylindenyl) zirconium Dichloride (4_) /MMAO/Base Catalyst System. a a Conditions: 15 ml VCM, 0.00000756 moles Zr, Al/Zr ratio = 215, Al/base ratio = 0.5, 1 hour, 35 °C, 200 W incandescent light source at 5.08 cm (2 inch) distance. b Yellow, partially dehydrochlorinated PVC c Al/Anisole = 1. Table 8. Effect of Al/THF Ratio on Vinyl Chloride Photopolymerization in Bulk with rac-Dimethylsilyl (2- methylindenyl) zirconium Dichloride (_) /MMAO/THF Catalyst System. a a Conditions: 15 ml VCM, 0.00000756 moles Zr, Al/Zr ratio = 215, 1 hour, 35 °C, 200 W incandescent light source at 5.08 cm (2 inch) distance. b Yellow, partially dehydrochlorinated PVC c Used 7.5 ml THF as solvent Table Effect of Solvent on Vinyl Chloride Photopolymerization with rac-Dimethylsilyl (2-methylindenyl ; zirconium Dichloride (4) /MMAO/THF Catalyst System. 3 a Conditions: 15 ml VCM, 0.00000756 moles Zr, Al/Zr ratio = 215; if THF is not the solvent, Al/THF ratio = 1, 1 hour, 35 °C, 200 W incandescent light source at 5.08 cm (2 inch) distance . b With 150 W + 125 W lamps, 1 inch distance, 2 hours c 3 hour run Table 10 Photopolymerization of VCM: Scale-up Data for Catalyst System (rac-Dimethylsilyl (2-methylindenyl) zirconium dichloride/MMAO/THF) (Method B) 1) Catalyst MW: 476; MMAO solution (0.73 g/cc) contains 7% Al w/w; A;/Zr mole ratio ≡219 for all runs; temperature = 25°C; pressure = 45 psi; agitation = 500 rp ; time = 4.5 hours . 2) White incandescent light was used for irradiation in runs 7739-14, 17, 21 and 23 (2 x 200W lamps) 2.54 cm (1") from the reactor except in 7739-14 (2.5" away); 100W UV light source at 7.62 cm (3") from reactor was used in run 7739-34. Table 11 Photopolymerization of VCM: Scale-up Data for Catalyst System A2 (rac-Dimethylsilyl (2-methylindenyl) zirconium dichloride/MMAO/Anisole) Catalyst M : 476; MMAO solution (0.73 gle ) contains 7 ! Al w/w; Al/Zr mole ratio ≡219 for all runs. Catalyst solution was added in 4 portions (3.6/3.5/3.5/lml) ; 1st portion added at the beginning and subsequent portions at 1 hour intervals. 1.5. Nature of end groups Proton NMR spectra of commercial PVC in THF-d 8 and CD 2 C1 2 , shown Figures 3a and 3b, respectively, contains a number of signals corresponding to the end groups and irregularities discussed heremabove. Figure 4a and 4b show the spectra in THF-d 8 and CD 2 C1 2 , respectively, of a PVC sample made m the photopolymerization process initiated with the catalytic system, formula (4_) /MMAO/anisole . The major difference between these spectra and those in Figure 3 is the presence of intensive doublets at 0.9 ppm corresponding to isopropyl groups. Multiplets m the region of 1.4-2.0 ppm Figure 4b appear to correspond to the methylene and methme protons in an end group such as CHCl-CH^-CH (CH 3 ) 2 • The ratio of the intensities I (0.9) /I (4.1 ) of the isopropyl doublet at 0.9 ppm to the doublet at around 4.1 ppm is 4.0, which is therefore a rough estimate of the ratio of isobutyl end groups to unsaturated end groups in the PVC produced by the photopolymerization. This observation in combination with the fact that the molecular weight of the PVC made with the metallocene photoinitiated system was much lower than that characteristic for the traditional free-radical PVC, implies that there is an initiation and chain transfer mechanism involving the alkyl groups of the aluminum co-catalysts. The data in Table 6, indicating that the relative number of alkyl end-groups increased when the Al/Zr ratio increased, also supports this idea. When PMAO or POAO was used as the co-catalyst, the NMR spectra of the polymer samples showed the incorporation of the corresponding alkyl groups into the chain, most likely as end ("starting") groups. Another notable difference between the traditional polymer samples and those made using the formula (4_) /MMAO/anisole catalyst system is the low level or apparent absence of saturated chloromethyl branches or end- groups in the new polymer. 1.6. Glass transition temperature Differential scanning calorimetry (DSC) was used to determine the glass transition temperature (T g ) of the PVC samples. Commercial PVC has a T y of about 85°C, and the value is influenced by the polymerization temperature. The Tg value also could be a reflection of changes in syndio- tacticity/crystallinity and/or Mn of the polymer. In Figure 5, line A shows the T CJ values as a function of Mn for commercial PVC samples (Aldrich standard samples with inherent viscosity 0.51, 1.02 and 1.6), and line B (solid square anisole, hollow square in THF) shows the T g values for some experimental resms photopolymerized by a method according to this invention. The new polymer samples made by a method according to this invention appear to have a slightly higher glass transition temperature than commercial PVC at the same M r , values, but both types of PVC samples show similar trends in T ς /M n dependence. 1.7. Product morphology The PVC samples made by the photopolymerization process are powdery materials. A scanning electron micrograph of the product obtained by photopolymerization in bulk using the catalyst system, formula (4_) /MMAO/anisole at 23°C (blade agitator at 500 rpm) shows that the samples are loose agglomerates of 0.3-0.5 micron size particles. 2. Metallocenes with Trialkylaluminum and Modified Analogues as Catalysts 2.1 Polymerizations in "Dark" Preliminary "dark" experiments were carried out with zirconocene dichloride (1_) under ambient light m a fumehood where the lights were turned off. Under these conditions, the yield of PVC and catalyst activity was generally low. Based on experience with the "dark" polymerizations with the bridged bis (indenyl) catalyst {_ ) , it was found that the addition of a coordinating base to the reaction system generally gave PVC with improved yield and substantially less discoloration. During this investigation it was found that the addition of the base 2 ' -hydroxyacetophenone afforded higher yields of PVC. Several "dark" experiments were conducted using different aluminum co-catalysts, such as trimethylaluminum, triethylaluminum, triisobutylaluminum, trioctylaluminum, diethylaluminum hydride, diethylaluminum ethoxide, and diethylaluminum chloride in combination with 2' -hydroxyacetophenone . It was found that the yield of PVC was the highest when trioctylaluminum in combination with 2' -hydroxyacetophenone in a 1:2 molar ratio, respectively, was used as the co-catalyst. Some other systems, notably, diethylaluminum hydride, also showed good activity. In order to verify the necessity for having illumination to polymerize VCM, we carried out the process with the same catalyst system after taking precautions to completely exclude the ambient light that was used in the "dark" experiments. Only a trace amount of PVC resulted. This clearly demonstrated that light was necessary for polymerizing VCM with the catalyst system of this invention. Subsequent experiments showed that if the reaction mixture was illuminated with light, the yield of PVC increased dramatically. The potential of this novel photopolymerization process was tested using the best candidate, 1:2 (octyl) 44/2 ' -hydroxyacetophenone . This catalyst system differs from the one used in the study with the silicon-bridged catalyst {_ ) (Section 1) in one major respect, viz., the co-catalyst. In the case of catalyst 4_, catalyst activation was achieved with methylalummoxane, whereas with catalyst _1, activation was achieved with trioctylaluminum modified with 2 ' -hydroxyacetophenone . 2.2 Photopolymerization Effect of Reaction Variables on Activity and Polymer Properties Various experiments were carried out to determine the effect of reaction variables on catalyst activity and the nature the PVC produced. In all cases, the co-catalyst was either trioctylaluminum or a base-modified version thereof. The effect of changing the light source was investigated by using incandescent lamps of varying power, and the results are shown Table 12. Catalyst activity was directly proportional to intensity of light incident on the Carius tube reactor. The M r was inversely proportional to light intensity at the reactor. Hence, M n decreased m the reverse order relative to catalyst activity. When toluene was used as a co-solvent, catalyst activity was generally higher than that observed in bulk reactions but M n dropped drastically. Proton NMR spectra of the PVC produced clearly showed the presence of the octyl group with the terminal methyl group appearing as a triplet. The relative ratio of alkyl end groups (resulting from trioctylaluminum) , to terminal allyl chloride group was generally higher in the bulk reactions than in the toluene-containing runs. Table 12. Effect of Light Source on Vinyl Chloride Photopolymerization with bis (Cyclopentadienyl) zirconium Dich loride (1) /1:2 (Octyl) 3 Al/2' -Hydroxyacetophenone Catalyst System. 3 a Conditions (unless otherwise stated): 15 ml VCM, 0.0000036 moles Zr, Al/Zr ratio = 16, Al/2' -hydroxyacetophenone mol. ratio = 0.5, 1 hour, 30 °C b Relative ratio of ] H NMR peak heights of terminal alkyl group to terminal allyl chloride group. c With 15 mL toluene as co-solvent d In bulk Variation in the structure of the metallocene resulted quite a wide variation m catalytic activity. Results are shown m Table 13. Among the systems examined, the most active catalysts were zirconocene dichloride (1_) (> 160 Kg PVC/g mole Zr) and the silicon-bridged bis-mdenyl zirconium dichloride (4_) (> 190 Kg PVC/g mole Zr) . The other systems were only moderately active. The M n m all cases was sharply lower, by a factor of about 2-3, than those polymers obtained when MMAO was used as the co- catalyst (Compare Tables 3 and 13) . Only minor differences in the relative intensities of the terminal alkyl and allyl chloride groups were seen m the proton NMR spectra of the PVC produced from these reactions. The effect of catalyst concentration was examined with toluene as the solvent. At relatively lower catalyst concentrations, there appeared to be an increase in catalyst activity upon increasing the amount of the catalyst. However, at much higher concentrations, catalyst activity fell sharply (See Table 14), perhaps due to a bimolecular deactivation similar to that proposed earlier for the metallocene _. As mentioned hereinabove, the alkyl end groups observed the PVC were believed to come from chain transfer of the alkyl group from the alkylalummum to the growing PVC chain. Hence, it was thought that if the Al/Zr ratio was increased, more efficient chain transfer would occur, such that the growing PVC chain would be terminated at a shorter chain length. This would result in a lower molecular weight for PVC with enhanced intensity for the alkyl end group in the H NMR spectrum. This trend was indeed observed when the Al/Zr ratio was increased from 16 to 128 in bulk polymerization (Table 15), where M r , decreased from 27,800 to 17,100, and the relative ratio of terminal alkyl to terminal allyl chloride peak intensity increased. Table 13 Vinyl Chloride photopolymerization in Bulk with Metallocene /l : 2 (Octyl) ^Al/2' - Hydroxyacetophenone Catalyst a Conditions: 15 ml VCM, 0.0000036 moles metallocene, 2:1 molar ratio of 2' -hydroxyacetophenone/ (Oct) τ l co-catalyst, Al/Zr ratio 16, 1 hour, 30 °C, 2 X 200 W incandescent light source at 5.08 cm (2 inch) distance. b Relative ratio of l U NMR peak heights of terminal alkyl group to terminal allyl chloride group. Table 14 Effect of Catalyst Concentration on Vinyl Chloride Photopolymerization with bis (Cyclopentadienyl ) zircoum Dichloride (1_) /1:2 (Octyl) _Al/2' -Hydroxyacetophenone Catalyst System. 3 a Conditions: 15 ml VCM, 15 mL toluene, Al/Zr ratio = 16, Al/2' -hydroxyacetophenone molar ratio =1, 1 hour, 30 °C, 200 W incandescent light source at 5.08 cm (2 inch) distance. Table 15 Effect of Al/Zr Ratio on Vinyl Chloride Photopolymerization with bis (Cyclopentadienyl) zirconium Dichloride (_1) /1:2 (Oct) 3 Al/2' -Hydroxyacetophenone Catalyst System. 3 a Conditions (unless otherwise stated): 15 ml VCM, 0.00000756 moles Zr, Al/THF molar ratio 1, 1 hour, 35 °C, 200 incandescent light source at 2 inch distance) With 15 mL toluene as solvent c In bulk from 4.87 to 5.43. When toluene was used as a solvent at Al/Zr ratio of 128, the M„ dropped further to 9,500, which is due to an additional pathway for chain transfer to the solvent. Also, catalyst activity increased significantly with a decreasing Al/Zr ratio. Since the molecular weight of the PVC and control of its end groups are influenced by the chain transfer ability of the alkylaluminum compound, a series of different bases, capable of coordinating with the alkylaluminum compound, were examined to determine their effect on VCM polymerization. Trioctylaluminum was chosen as the base co- catalyst and zirconocene dichloride (1_) as the catalyst. Modification was done in two broad ways. In one case, different bases were added to trioctylaluminum, and in the other, different bases were added to the 1:2 complex of trioctylaluminum and 2 ' -hydroxyacetophenone . In both cases, profound differences were found for catalyst activity and molecular weight. The results are shown in Table 16. Trioctylaluminum by itself was not a good co-catalyst, having an activity of only about 48.6 Kg/g mole Zr. Bases based on phenols were examined. It appears that compounds related to 2' -hydroxyacetophenone, such as 2 ' -hydroxy-3- phenylpropiophenone (Table 16), that have protons alpha to the carbonyl group greatly increase the catalyst activity. A H NMR study of the interaction of 2' -hydroxyacetophenone with isobutylalummum (chosen instead of (octyl) 3 A1 for ease of interpretation of spectra) m toluene-d 8 showed the presence of all three possible products resulting from protonolysis of 1,2 or all 3 C-Al bonds. A similar process should be occurring m the case of (octyl) 3 A1. Clearly, for chain transfer to occur, there has to be at least one octyl group on the aluminum. Remarkably, 1, 3-dιcarbonyl compounds related to acetylacetone rendered the co-catalyst inactive. The addition of simple Lewis bases such as anisole and PPh 3 gave comparable moderate activity. However, the molecular weight dropped sharply with PPh 3 as compared to anisole. The addition of Lewis bases to the 1:2 complex of (octyl) ;j l and 2' -hydroxyacetophenone generally resulted in good catalyst activity. With the exception of PPh 3 , the molecular weight was relatively unaffected by the addition of the Lewis base. It appears that addition of triphenylphosphme increases the chain transfer ability of the co-catalyst and lowers the molecular weight of PVC significantly. A similar trend was seen earlier with the base-modified system comprising the bridged catalyst (4) with MMAO co-catalyst. When the solvent is capable of facilitating chain transfer from the octylalummum, tnere was generally an increase in catalyst activity (Table 17) with a concomitant decrease m molecular weight. In heptane, the molecular weight was significantly higher than in toluene or THF. Increasing the amount of VCM used in the bulk phase photopolymerization increases the molecular weight of PVC (Table 18). The drop in catalyst activity upon going from 15 mL VCM to 7-8 mL VCM is perhaps due to greater catalyst deactivation at the relatively higher Zr-concentration by some bimolecular process. Table 16 Effect of Bases on Vinyl Chloride Photopolymerization with bis (cyclopentadienyl) -zirconium Dichloride (l)/(Oct) 3 Al Catalyst System. a Conditions (unless otherwise stated) : 15 L VCM, 10 mL toluene, 0.0000036 moles Zr, Al/Zr ratio = 16, Al/Modifier ratio = 0.5, 1 hour, 35°C, 150 W incandescent lamp at 5.08 cm (2") distance) . b In bulk. With 200 W lamp at 5.08 cm (2") distance. c Al/Base mole ratio = 1 d Al/Anisole mole ratio = 0.5 e Al/Base mole ratio = 2 £ With 1:2 complex of (Oct) 44/2 ' -hydroxyacetophenone; 200 W incandescent lamp at 5.08 cm (2") distance. 9 Al/THF mole ratio = 0.1 Table 17 Effect of Solvent on Vinyl Chloride Photopolymerization with bis (Cyclopentadienyl) zirconium Dichloride (_1) /l : 2 (Oct) 3 Al/2' -Hydroxyacetophenone Catalyst System. 3 3 Conditions (unless otherwise stated) : 15 ml VCM, 15 L solvent, 0.0000036 moles Zr, Al/Zr ratio = 16, 1 hour, 35 °C, 200 W incandescent light source at 5.08 cm (2 inch) distance . b In bulk. Table 18 Effect of Amount of VCM on Vinyl Chloride Photopolymerization with bis (cyclopentadienyl ) zirconimdichlo ride (1) /l : 2 (Oct ) 3 Al/2' -Hydroxyacetophenone catalyst system. 3 3 Conditions (unless otherwise stated): 0.0000036 moles Zr, Al/Zr ratio = 16, 1 hour, 30 °C, 2 X 200 W incandescent light source at 5.08 cm (2 inch) distance. b With 1 X 200W incandescent bulb. 59 SUBSTITUTE SHEET (RULE 23)

Claims: CLAIMS 1. A method of making poly (vinyl chloride) comprising the step of polymerizing vinyl chloride monomer in the presence of light, a metallocene catalyst, and at least 1 mole of an aluminum-containing co-catalyst per mole of said catalyst. 2. A method according to Claim 1 wherein the amount of the catalyst is at least 2 ppm based on monomer weight. 3. A method according to Claim 1 wherein the amount of the catalyst is at least 10 ppm based on monomer weight. 4. A method according to Claim 1 wherein the amount of the catalyst is about 2 to about 250 ppm. 5. A method according to Claim 1 wherein the amount of the catalyst is about 50 to about 125 ppm. 6. A method according to any one of Claims 1 to 5 wherein the amount of co-catalyst is about 1 to about 2,000 moles per mole of said catalyst. A method according to any one of the preceding Claims wherein said metallocene catalyst has the general formula L' \ M ■ (x>. / where each X is independently selected from halogen, alkyl from Ci to C 30 , oxyalkyl or oxyaryl from d to do, or - N(R') 2/ where each R' is independently selected from hydrogen, alkyl from C 2 to Cio aryl from d to C 15 , alkaryl from to Cι 5 , and aralkyl from d to C15, L is a ligand containing a cyclopentadienyl ring or an anionic heterocyclic ring that is isoelectronic with a cyclopentadienyl ring, L' is L or X, and n is 1, 2, or 3. A method according to Claim 7 wherein L has the formula where each R is independently selected from hydrogen, silyl, germyl, cyano, R"OR", or halogen, where R" is a Ci to o hydrocarbyl group, or two R groups are joined together to form a to C, ring, and m is 1 to 5. 9. A method according to Claim 7 where L is cyclopentadienyl or indenyl. 10. A method catalyst according to Claim 7 where L is R. where each R is independently selected from hydrogen, silyl, germyl, cyano, R"OR", or halogen, where R" is a Ci to do hydrocarbyl group, or two R groups are joined together to form a to C 6 ring, R ! is hydrogen, N(R') 2 , OR' , or R' , each R' is independently selected from halogen, alkyl from Ci to Cio, aryl from C 6 to C 15 , and aralkyl from C 7 to C15, and m is 1 to the maximum number of substituents allowable on the ring. 11. A method according to Claim 7 wherein L is borabenzene, boranaphthalene, or boraanthracene . 2. A method according to Claim 7 wherein L has the formula : where R 2 is alkyl from d to 2 or aryl from C 6 to C 12 , alkaryl from to C1 2 , aralkyl from to C 2 , or Si(R') 3 , R 3 is R 2 , halogen, COR', COOR' , SOR' , or SOOR' , R' is alkyl from d to do aryl from C 6 to C 15 , alkaryl from C 7 to C15, or aralkyl from C to C 1 5, and m is 1 to the maximum number of substituents on the ring. 13. A method according to Claim 12 wherein the R 2 group on the boron is alkyl from C 3 to C 12 or aryl, R 3 group is t-butyl or trimethylsilyl, and the R 3 group on the ring is hydrogen or methyl. 14. A method according to Claim 7 wherein L is where R is independently selected from hydrogen, silyl, germyl, cyano, R"OR", or halogen, where R" is a Ci to d,, hydrocarbyl group, or two R groups are joined together to form a d to C,-, ring, and m is 1 to the maximum number of substituents on the ring, Z is N or P, and m is 1 to the maximum number of substituents on the ring. 15. A method according to any one of Claims 7 to 14 wherein M is zirconium, titanium, or hafnium. 16. A method according to any one of the preceding Claims wherein said metallocene catalyst is selected from the group consisting of and where tBu is tertiary butyl. 17. A method according to any one of the preceding Claims wherein said aluminum containing co-catalyst has the general formula R"' ,A1X' { 3 - μ) , where R"' is alkyl from d to C 50/ X is hydrogen, halogen, alkoxy, phenoxy, amino, imino, amido, or OR"", where R"" is alkyl, aryl, or where R 4 is hydrogen, alkoxy, or alkyl, and p is 1 to 3. 18. A method according to any one of Claims 1 to 16 wherein said aluminum- containing co-catalyst has the general formula -(0-Al-R 5 ) η or (0-Al-R 5 ) q (0-Al-R 6 ) _, where R 5 and R 6 are independently selected from (Ci to do) alkyl, and where q+r is 5 to 100. 19. A method according to any one of the preceding Claims wherein a Lewis base is also present during the polymerisation step, there being at least about 2 moles of Lewis base per mole of aluminium m said co- catalyst . 20. A method according to any one of Claims 1 to 18 wherein a Lewis base is also present during the polymerisation step, the amount of said Lewis base is up to about 500 moles per mole of aluminium m said co-catalyst. 21. A method according to Claim 19 or 20 wherein the amount of said Lewis base is about 2 to about 300 moles per mole of alummiumm said co-catalyst. 22. A method according to any one of Claims 19 to 21 wherein said Lewis base is tetrahydrofuran . 23. A method according to any one of the preceding Claims wherein the light is light in the UV or visible region of the spectrum. 24. A method according to Claim 23 wherein the light is provided from a light source providing at least IW for each 100 ml of the monomer, catalyst and co-catalyst. 25. A method according to Claim 24 wherein the light source provides at least 10W for each 100 ml of the monomer, catalyst and co-catalyst. 26. A method of producing poly (vinyl chloride) chains terminated with alkyl groups comprising (A) preparing a mixture of (1) vinyl chloride monomer; (2) a metallocene catalyst; (3) at least 1 mole per mole of said catalyst of an aluminium-containing said alkyl groups; and (4) about 2 to about 300 moles of a Lewis base per mole of aluminium m said co- catalyst; and (B) exposing said mixture to at least about IW output radiation in the ultraviolet or visible region, whereby said alkyl groups on said aluminum containing co-catalyst are transferred to the ends of said poly(vmyl chloride) chains. 27. Polyvinvyl chloride when made by a method according to any one of the preceding Claims. 28. A composition comprising vmyl chloride monomer, about 10 to about 250 ppm of a metallocene catalyst, about 1 to about 2000 moles of an aluminum-containing co- catalyst per mole of said catalyst, and up to about 500 moles of a Lewis base per mole of aluminum m said co- catalyst . 29. A composition according to Claim 28 wherein the amount of said catalyst is about 50 to about 125 ppm, the amount of said co-catalyst is about 2 to about 500 moles per mole of said catalyst, and the amount of Lewis base is about 2 to about 300 moles per mole of aluminum in said co-catalyst.

Inventors: COCOMAN MARY K, KRISHNAMURTI RAMESH, NAGY SANDOR M, OPALINSKI WALTER M, SMOLKA THOMAS F, COCOMAN, MARY, K., KRISHNAMURTI, RAMESH, NAGY, SANDOR, M., OPALINSKI, WALTER, M., SMOLKA, THOMAS, F.
Applicants: OCCIDENTAL CHEM CO, OCCIDENTAL CHEMICAL CORPORATION
Application year: 1998
Main classification: C08F114
IPC codes: C08F2, C08F4, C08F114