PROCESS FOR PRODUCING CRYSTALLINE VINYL AROMATIC POLYMERS HAVING A PREDOMINANTLY SYNDIOTACTIC STRUCTURE

Abstract: A process for the production of predominantly syndiotactic vinyl aromatic polymers by polymerizing or copolymerizing vinyl aromatic monomers such as styrene or styrene derivatives in the presence of a catalyst system comprising the product of the reaction between: a) a compound of transition metal (M) containing at least one M-O, M-C, M-N, M-P, M-S or M-halogen bond, and b) an organoaluminium compound containing at least one oxygen atom bound to the aluminium atom or located between two aluminium atoms. Compounds a) and b) can be used as such or supported on a carrier.

Description: The present invention relates to a process for preparing predominantly syndiotactic crystalline vinyl aromatic polymers. More particularly, the present invention relates to a process for preparing crystalline styrene polymers in which the chains are at least mainly in the syndiotactic configuration. As is known, styrene polymers and particularly polystyrene are thermoplastic materials which may show high molecular weights. Its thermal resistance, thermomoldability and excellent insulating properties render polystyrene particularly suitable for the production of extruded articles, molded articles and films to be used mainly in the field of sound and heat insulation, of packing and as dielectric material. Polystyrene can be produced by radical polymerization, anionic polymerization or cationic polymerization. The styrene polymerization conducted by the radical mechanism, either thermally or in the presence of initiators, can be effected by bulk polymerization, emulsion polymerization, suspension polymerization or bulk suspension polymerization. On X-ray analysis, the resulting polymer exhibits a diffraction pattern typical for an amorphous structure, and on ¹H-NMR analysis it exhibits a spectrum with broad bands without peak resolution in the area of the chemical shifts typical for the methine and methylene protons. This is in accordance with a random sequence of monomeric units with different steric configuration (atactic structure). The use of this amorphous polymer is limited by its low glass transition temperature (Tg) of about 100°C. Above this temperature there is a drastic deterioration of the mechanical properties of the polymer. Amorphous polymers are also obtained when styrene polymerization is conducted by cationic and anionic catalysis even if in some cases a prevalent syndiotactic configuration of the carbon atoms in the main chain was found. It is also known that crystalline, mainly isotactic polystyrene can be produced by stereospecific polymerization of styrene. Styrene polymerization, in such case, is carried out in the presence of Ziegler-Natta-type catalysts based on halogenated compounds of transition metals, either as such or supported on magnesium halides, in combination with aluminium alkyls, optionally in the presence of electron donors. A detailed description of this type of polymerization is given in IT-PS- 537 425, US-A-3 161 624 and 2 882 263 and in GB-A-826 021 and 844 944. Polystyrene prepared by means of such types of stereospecific catalysts was obtained for the first time by G. Natta et al (J. Am. Chem. Soc. 1955, 77, 1700) and shows, in the X-ray pattern, diffraction peaks which may be assigned to a structure which is mainly isotactic. On ¹H-NMR analysis, the multiplet assigned to the methylene group is indicative of a non-equivalence of the two protons, what also indicates an isotactic structure (Heatley, F. and Bovey, F.A., Macromolecules (1968), 1, 301). This crystalline, mainly isotactic polymer has not found any industrial use as its crystallization rate is very low. Also known (N. Ishihara et al., Macromolecules (1986), 19, 2464-2465) is a crystalline polystyrene having a low weight average molecular weight (about 82 000) and mainly a syndiotactic structure, as concluded on the basis of the data of X-ray diffraction, infrared spectroscopic analysis, ¹H-NMR and ¹³C-NMR analyses. This polymer shows a high melting point, about 270°C, and a high crystallization rate. The thermal and structural characteristics of this mainly syndiotactic polymer allow retention of the mechanical properties even at higher temperatures than the glass transition temperature (Tg). It is well known, however, that many mechanical properties of polystyrene, such as tensile strength, elongation at break, tenacity and stress-cracking resistance, improve remarkably as the molecular weight increases, while when the weight average molecular weight is below 100 000 the values of said properties are unacceptable for a practical industrial utilization. (Encyclopedia of Polymer Science and Technology, vol. 13). For this reason, the commercially available polystyrenes have weight average molecular weights ranging from 200 000 to 300 000. EP-A-210 615 describes styrene polymers having the following repeating unit: with a degree of polymerization of not less than 5, and a stereoregularity which is mainly syndiotactic. EP-A-224 097 claims a process for producing styrene polymers which comprises polymerizing styrene or styrene derivatives by the use of a catalyst comprising: (A) a titanium compound, and (B) a contact product of an organoaluminium compound and a condensation agent. However, those references do not disclose the use of the special titanium compounds described hereinbelow. It has now surprisingly been found that by using particular catalyst systems it is possible to obtain crystalline vinyl aromatic polymers and particularly styrene or styrene derivative polymers having a mainly syndiotactic structure and an average molecular weight higher than 100 000. Thus, the present invention provides crystalline vinyl aromatic polymers and particularly styrene or styrene derivative polymers having a predominantly syndiotactic structure and particularly a regular structure with syndiotactic configuration at least in long portions of the chain and an average molecular weight higher than 100 000. The crystalline polymers with a mainly syndiotactic structure according to the present invention are endowed with improved mechanical properties as compared to the ones of the syndiotactic polystyrene of the art, said mechanical properties being combined with a melting point of about 270°C or even higher and with a high crystallization rate. According to the present invention, the process for preparing crystalline vinyl aromatic polymers, and particularly styrene or styrene derivative polymers, of mainly syndiotactic structure consists in carrying out the polymerization of the vinyl aromatic monomer, and particularly of styrene or styrene derivative, either alone or in admixture with up to 30 % (particularly up to 15 %) of another copolymerizable ethylenically unsaturated monomer, in the presence of catalytic amounts of a catalyst system comprising the product of the reaction between: a) a titanium compound which contains at least one Ti-P or Ti-S bond or which is selected from: bis(methylcyclopentadienyl)titanium dichloride; Ti(OC₆H₅)₄; TiCl₃(OC₄H₉); TiCl₂(OC₄H₉)₂; Ti(OC₂H₅)₃; Ti(OC₃H₇)₃; Ti(O-t-C₄H₉)₄; Ti(OC₄H₉)₃; Ti(OCH₂-CH₂Cl)₄; TiCl₂[OSi(CH₃)₃]₂; (η⁵C₅H₅)₂Ti(C₆H₅)₂; [(η⁵C₅H₅)₂TiCl]₂O; acetylacetonate titanium dichloride; bis-acetylacetonate titanium dichloride; titanium triacetylacetonate; titanium trichloro-p-dodecylbenzene sulphonate; {[(CH₃)₃C]₃C-O-}₂TiCl₂; MgCl₂·2Ti(OC₄H₉)₄; co-ground MgCl₂ + TiCl₄; MgTiCl₆·4CH₃COOC₂H₅; and b) an organoaluminium compound containing at least one oxygen atom bound to the aluminium atom or located between two Al atoms. The titanium compounds are utilizable as such or supported on organic or inorganic carriers, such as for example SiO₂ or Al₂O₃ or Mg halides (e.g. MgCl₂ and MgBr₂). Also the organoaluminium compound can be used as such or supported on the same carriers utilized for the titanium compounds. The catalyst components carried on Mg halides are well known in literature and are described, for example, in US-A-4 298 718 or in GB-A-1 292 853 and 1 305 610 in the name of the applicant hereof, the disclosures of which are explicitly referred to. The molar ratio of Al to Ti is not critical and is in the range from 1 to 1000, preferably from 10 to 200 (e.g. 10 to 20). The concentration of the aluminium compound preferably ranges from 10⁻⁴ to 1, particularly from 10⁻³ to 10⁻¹ mole/liter, based on the reaction mixture. Examples of organoaluminium compounds corresponding to the definition of component b) are: for a straight aluminoxane for a cyclic aluminoxane, wherein n is 0 or an integer from 1 to 40, preferably from 10 to 30; R can be: an alkyl radical containing 1 to 20, preferably 1 to 8 carbon atoms, an aryl radical containing 6 to 20, preferably 6 to 12 carbon atoms, an arylalkyl radical containing 7 to 20, preferably 7 to 12 carbon atoms or a cycloalkyl radical containing 3 to 20, preferably 5 to 8 carbon atoms; a O-R' radical, where R' may be an alkyl radical having 1 to 8, preferably 1 to 4, carbon atoms or an aryl radical having 6 to 20, preferably 6 to 12, carbon atoms; or halogen (preferably F, Cl or Br) provided that not all radicals R are halogen or O-R'. R can be the same or different in the various positions of the above cited components (A) and (B). Representative examples are linear methylaluminoxane with n = 20; cyclic methylaluminoxane with n = 20. These aluminium compounds can be used either alone or blended with aluminium trialkyls AlR"₃ or aluminium alkyl halides AlR"₂X and AlR"X₂, wherein the alkyl groups R" contain preferably 1 to 8 carbon atoms and may be the same or different and X may be the same or different and represent F, Cl, Br and J, particularly Cl and Br. The polymerization of vinylaromatic monomers, according to both the continuous and the discontinuous process, can be carried out in bulk, in suspension, in solution or in bulk-suspension. The polymerization temperature is preferably in the range of from -80°C to +200°C, most preferably from -20°C to +100°C. The molecular weight of the polymer can be adjusted by using the techniques which are usually adopted in the Ziegler-Natta catalysis, for example by addition of hydrogen. The modalities concerning the addition of the various catalyst system components, of the monomer and of the solvent, if any, are not critical. The term "vinylaromatic polymers", whenever used in the present description and in the claims, comprises styrene polymers, styrene derivative polymers and the related copolymers containing up to 30 % by weight of another copolymerizable, ethylenically unsaturated monomer, suitably of general formula: CH₂ = CH - R₃ wherein R₃ is hydrogen or an aliphatic group containing 1 to 6, preferably 1 to 4, carbon atoms; an aryl group containing 6 to 20, preferably 6 to 12, carbon atoms; an aryl group substituted with alkyl or halogen radicals in the nucleus and containing altogether 6 to 30,preferably 6 to 18 carbon atoms, or a cycloaliphatic group, optionally alkyl- or halogen-substituted, containing altogether 3 to 20, preferably 5 to 12, carbon atoms. These styrene derivatives include alkylstyrene, halogenated styrene, vinyl-naphthalene and vinyltetrahydro-naphthalene containing from 9 to 12 carbon atoms in the molecule. Representative examples of styrene derivatives are alpha- or beta-vinyl naphthalene, 1,2,3,4-tetrahydro-6-vinyl naphthalene, styrene ring substituted with one or more (up to 5) alkyl groups containing from 1 to 4 carbon atoms and/or with one or more (up to 5) halogen atoms, such as chlorine. The term ring substituted styrene includes first of all and preferably p-methyl-styrene even if other alkyl derivatives may be used with the same results. Typical examples of ring substituted styrene are: methylstyrene,ethylstyrene, butylstyrene, p-tert-butylstyrene, and dimethylstyrene, chlorostyrene, bromostyrene and fluorostyrene, chloromethylstyrene, alkoxystyrene, preferably C₁₋₄ alkoxystyrene, such as methoxystyrene, carboxymethylstyrene (e.g. acetoxymethylstyrene), alkyletherstyrene, alkylsilylstyrene, vinylbenzenesulfonic acid esters, and vinylbenzyldialkoxy phosphide. The crystalline styrene or styrene derivative polymers having a mainly syndiotactic structure, obtained by the process of the present invention, were characterized by the following properties and by using the methods indicated hereinbelow: a) Residue of the extraction with methylethyl ketone (MEK), carried out in a Kumagawa extractor for 24 hours. b) Weight average molecular weight , ( M w ), determined by gel permeation chromatography (G.P.C.) carried out with a Waters apparatus 150 ALC-GPC in ortho-dichlorobenzene (ODCB) at 135°C. Instrument calibration was obtained by using standard samples of atactic polystyrene of known molecular weight (Waters Associates Inc.). c) Melting point (M.P., determined by means of a differential calorimeter, model Perkin-Elmer DSC 7, as the temperature corresponding to the maximum of the endothermal peak, at a scanning rate of 40°C/min. d) Intrinsic Viscosity , determined in tetrahydronaphthalene at 135°C. e) Crystallinity of the polymer residue of MEK , determined after melting and solidification by means of X-ray diffraction, with the powder method, by verifying in the pattern the presence of sharp reflexes typical of the crystalline substances. The values of the interplanar distances corresponding to said reflexes were determined with an error of ± 0.1 Å. f) Syndiotacticity of the polymers , determined by ¹H-NMR or ¹³C-NMR analysis, carried out on a BRUKER AM-300 instrument, in orthodichlorobenzene at 125°C, using hexamethyldisiloxane as standard. The following examples are given to illustrate the present invention, without being, however, a limitation thereof. Example 1 (Control) Into a glass reactor having an internal volume of 100 ml and being equipped with a stirrer there were placed, in an inert atmosphere and at 20°C: 252 mg of methylaluminoxane (A) 10 ml of toluene 34 mg of Ti (OC₄H₉)₄. After 5 minutes, 30 ml of styrene passed through an alumina column and distilled over LiAlH₄ were added. Within 30 minutes the temperature was brought to 50°C and polymerization was conducted for 4 hours. After this period of time, the polymer was coagulated with methanol, acidified with hydrochloric acid and repeatedly washed with methanol. After drying there were obtained 16 g of polymer (corresponding to a conversion of 59 %) showing a residue to MEK, a weight average molecular weight and a melting point as listed in the following Table. On X-ray analysis, the residue of the extraction with MEK exhibited, after melting and solidification, reflexes of relatively high intensity corresponding to interplanar distances of 13.1 Å, 7.6 Å, 6.46 Å, 4.37 Å and 2.58 Å. The ¹H-NMR pattern of the polymer showed chemical shifts of the methine and methylene protons, respectively centered at 1.9 and 1.4 ppm, as illustrated in Fig. 1. (A) Methylaluminoxane was prepared as follows: Into a three-neck flask having an internal volume of 500 ml, equipped with a dropping funnel, a stop cock and a magnetic stirrer, there were placed 37.1 g of Al₂(SO₄)₃.18H₂O and 250 ml of toluene in a nitrogen atmosphere. 50 ml of Al(CH₃)₃ were placed into the dropping funnel and were added under stirring within 30 minutes. The reaction was carried out at 60°C for 3 hours. The aluminium sulphate was filtered off from the suspension and the solvent was removed. 15.5 g of a solid white product were obtained. Example 2 Example 1 was repeated, using: 263 mg of methylaluminoxane, 10 ml of toluene, 13 mg of MgCl₂.2Ti(OC₄H₉)₄, prepared by reacting 0.79 g of MgCl₂ and 5.7 ml of Ti(OC₄H₉)₄ at 140°C for 4 hours and cooling to room temperature. The amount of polymer obtained, the residue of MEK extraction, the weight average molecular weight and the melting point are given in the Table. The X-ray diffraction pattern and the ¹H-NMR pattern were similar to those of Example 1. Example 3 Example 1 was repeated, using: 261 mg of methylaluminoxane, 15 ml of toluene, 11 mg of TiAc₂Cl₂ (*). The amount of polymer obtained, the residue of MEK extraction, the weight average molecular weight and the melting point are reported in the Table. The X-ray diffraction pattern and the ¹H-NMR pattern were similar to those of Example 1. (*) Ac = Acetylacetonate. Example 4 Example 1 was repeated, using: 230 mg of methylaluminoxane 10 ml of toluene 12 mg of TiAc₃. (*) Amount of obtained polymer, residue of MEK extraction, weight average molecular weight and melting point are reported in the Table. The X-ray diffraction pattern and the ¹H-NMR pattern were similar to those of Example 1. (*) Ac = Acetylacetonate. Example 5 Example 1 was repeated, using: 130 mg of methylaluminoxane, 20 ml of toluene, 18 mg of Ti(OC₂H₅)₃, prepared as described by E. ALBIZZATI et al. in Inorg. Chim. Acta (1986), 120, 197. Amount of polymer obtained, residue of MEK extraction, weight average molecular weight and melting point are reported in the Table. The X-ray diffraction pattern and the ¹H-NMR pattern are similar to those of Example 1. Example 6 Example 1 was repeated, using: 170 mg of methylaluminoxane, 10 ml of toluene, 95 mg of co-ground MgCl₂ + TiCl₄ (*). Amount of polymer obtained, residue of MEK extraction, weight average molecular weight and melting point are reported in the Table. The X-ray diffraction pattern and the ¹H-NMR pattern were similar to those of Example 1. (*) Catalyst component obtained by co-grinding MgCl₂ and TiCl₄ in a vibrating mill in amounts such as to result in a Ti content of 2 % by weight. Example 7 Example 1 was repeated, using: 130 mg of methylaluminoxane, 15 ml of toluene, 25 mg of MgTiCl₆.4CH₃COOC₂H₅, prepared according to GB-A-1 502 567. Amount of polymer obtained, residue of MEK extraction, weight average molecular weight and melting point are reported in the Table. The X-ray diffraction pattern and the ¹H-NMR pattern were similar to those of Example 1. Example 8 Example 1 was repeated, using: 100 mg of methylaluminoxane, 10 ml of toluene, 8 mg of Cl₂Ti(tritox)₂ (*). Amount of polymer obtained, residue of MEK extraction, weight average molecular weight and melting point are reported in the Table. The X-ray diffraction pattern and the ¹H-NMR pattern were similar to those of Example 1. (*) tritox = -OC(t-C₄H₉)₃. Example No. Conversion % Residue of MEK % M w (u.m a.) M.P. (°C) 1 (control) 59 93 660,000 275 2 35 95 630,000 273 3 38 95 680,000 273 4 38 99 720,000 274 5 49 99.6 750,000 273 6 32 91 580,000 269 7 15 93 480,000 267 8 10 50 177,000 271 Example 9 Into the apparatus described in Example 1 there were introduced: 150 mg of methylaluminoxane, 6 ml of toluene, 4 mg of TiAcCl₂. After 5 minutes, 16.3 g of styrene and 1.8 g of paramethylstyrene were added. The temperature was brought to 50°C in 30 minutes and polymerization was conducted for 3 hours. The polymer isolated according to the procedure of Example 1 amounted to 5 g and exhibited an inherent viscosity, measured in ODCB at 135°C, of 0.91 dl/g, a melting point of 227°C and a p-methylstyrene content of 22 % by weight. The X-ray diffractometric analysis revealed that the polymer was crystalline. Example 10 Into a glass reactor having an internal volume of 100 ml, equipped with a stirrer, there were placed, in an inert atmosphere and at 20°C: 200 mg of methylaluminoxane (A) 10 ml of toluene 2.8 mg of bisacetylacetonate titanium dichloride. After 5 minutes, 20 ml of para-methyl-styrene, passed through an alumina column and distilled over LiAlH₄, were added. Within 30 minutes the temperature was brought to 50°C and polymerization was conducted for 4 hours. After this period of time, the polymer was coagulated with methanol, acidified with hydrochloric acid and repeatedly washed with methanol. After drying there were obtained 12.5 g of polymer (corresponding to a conversion of 70 %) having a residue of MEK of 86 %, a melting point of 198°C and an intrinsic viscosity of 0.86 dl/g. On X-ray analysis, the residue of the extraction with MEK exhibited, after annealing at 180°C for 50 hours, reflexes of relatively high intensity corresponding to interplanar distances of 11.8 Å, 9.8 Å, 9.3 Å, 6.0 Å, 5.5 Å, 5.0 Å and 4.1 Å. The ¹³C-NMR pattern of the carbon atom of the aromatic ring linked to the CH group of the main chain is given in Fig. 2. The methylaluminoxane was prepared according to the process conditions of Example 1. Example 11 Example 10 was repeated, using: 160 mg of methylaluminoxane, 10 ml of toluene, 3.1 mg of [[(CH₃)₃C]₃-C-O]2TiCl₂ 5 g of polymer were obtained (conversion of 28 %) having a residue of MEK of 88 %, a melting point of 197°C and an intrinsic viscosity of 0.72 dl/g. The obtained polymer, according to X-ray diffractometric and ¹³C-NMR analysis, had a syndiotactic structure as described in Example 10. Specific examples of the various generic groups mentioned in the preceding description are: Alkyl and aliphatic radicals: methyl, ethyl, propyl, i-propyl, n-butyl, sec.-butyl, iso-butyl, tert.-butyl, pentyl, hexyl, heptyl, 2-ethylhexyl, n-octyl, nonyl, decyl, undecyl and dodecyl. Cycloaliphatic and cycloalkyl radicals: cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl. Arylalkyl: benzyl, (1- and 2-) phenylethyl, phenylpropyl, phenylbutyl. Halogen: F, Cl, Br and J. Carboxy: acetoxy, propoxy, butoxy. Alkoxy: methoxy, ethoxy, propoxy, butoxy.

Claims: A process for producing crystalline vinyl aromatic polymers having a predominantly syndiotactic structure, which comprises polymerizing the vinyl aromatic monomers, either alone or in admixture with up to 30 % of another copolymerizable ethylenically unsaturated monomer, in the presence of catalytic amounts of a catalyst system comprising the product of the reaction between: a) a titanium compound which contains at least one Ti-P or Ti-S bond or which is selected from: bis(methylcyclopentadienyl)titanium dichloride; Ti(OC₆H₅)₄; TiCl₃(OC₄H₉); TiCl₂(OC₄H₉)₂; Ti(OC₂H₅)₃; Ti(OC₃H₇)₃; Ti(O-t-C₄H₉)₄; Ti(OC₄H₉)₃; Ti(OCH₂-CH₂Cl)₄; TiCl₂[OSi(CH₃)₃]₂; (η⁵C₅H₅)₂Ti(C₆H₅)₂;[(η⁵C₅H₅)₂TiCl]₂O; acetylacetonate titanium dichloride; bisacetylacetonate titanium dichloride; titanium triacetylacetonate; titanium trichloro-p-dodecylbenzene sulphonate; {[(CH₃)₃C]₃C-O-}₂TiCl₂; MgCl₂·2Ti(OC₄H₉)₄; co-ground MgCl₂ + TiCl₄; MgTiCl₆·4CH₃COOC₂H₅; and b) an organoaluminium compound containing at least one oxygen atom, bound to one aluminium atom or located between two Al atoms. The process of claim 1, wherein the transition metal compound and the organoaluminium compound are supported on organic or inorganic carriers, such as SiO₂, Al₂O₃ or Mg halides. The process of claim 1 or 2, wherein the molar ratio of organoaluminium compound to transition metal compound is from 1 to 1000, preferably from 10 to 200. The process of any of the preceding claims, wherein the concentration of the organoaluminium compound ranges from 10⁻⁴ to 1 mole/liter, based on the reaction mixture. The process of any of the preceding claims, wherein the organoaluminium compound is selected from: wherein: n is 0 or an integer from 1 to 40, preferably from 10 to 30; R can be: an alkyl radical containing 1 to 20 carbon atoms, an aryl radical containing 6 to 20 carbon atoms, an arylalkyl radical containing 7 to 20 carbon atoms or a cycloalkyl radical containing 3 to 20 carbon atoms, a O-R' radical in which R' may be an alkyl radical containing 1 to 8 carbon atoms or an aryl radical containing 6 to 20 carbon atoms; or a halogen, provided that not all radicals R are halogen or O-R'. The process of claim 5, wherein the organoaluminium compound is the straight methylaluminoxane (A) with n = 20. The process of claim 5, wherein the organoaluminium compound is the cyclic methylaluminoxane (B) with n = 20. The process of any of the preceding claims, wherein polymerization is carried out in bulk at a temperature from -80°C to +200°C, preferably from -20°C to 100°C. The process according to any of the preceding claims, wherein the vinyl aromatic monomer is styrene or a styrene derivative, e.g. selected from alkylstyrene, halogenated styrene, vinylnaphthalene and vinyltetrahydronaphthalene, each containing from 9 to 12 carbon atoms in the molecule.

Inventors: ALBIZZATI, ENRICO, GIANNINI, UMBERTO, DR., GIUNCHI, GIOVANNI, DR., MAZZOCCHI, ROMANO, RESCONI, LUIGI, DR.
Applicants: MONTEDISON S.P.A.
Application year: 1987
Main classification: C08F12
IPC codes: C08F4, C08F12