Polyarylate-polyethylene composite laminated structures

Abstract: Composite laminated structures comprising a poly­ arylate film bound to a polyethylene film via an inter­ mediate tie layer are described. The structures are fabricated by coextrusion of three layer blown tubular films with the center layer being present to bond the polyethylene to the polyarylate.

Description: Field of the Invention Composite laminated structures comprising a polyarylate film bound to a polyethylene film via an intermediate tie layer are described. The structures are fabricated by coextrusion of three layer blown tubular films with the center layer being present to bond the polyethylene to the polyarylate. The composition of the center material is critical if good adhesion and clarity are desired. The instant composite films display good mechanical properties and excellent UV resistance. They are useful in a variety of outdoor applications such as, for example, covering for greenhouses. Background of the Invention Polyarylates are aromatic polyesters derived from dihydric phenols and aromatic dicarboxylic acids. The material based on 2,2-bis(4-hydroxyphenyl)propane (bis-phenol-A) and a 50:50 mixture of terephthalic and isophthalic acids (l) is offered commercially by Amoco Performance Products, Inc. under the tradename of ARDEL® D-100. Polyarylates are high temperature, high performance thermoplastic polymers with a good combination of thermal and mechanical properties. They display excellent UV resistance and have good processibility which allows them to be molded into a variety of articles. It is known that upon exposure to ultraviolet light polyarylates undergo the Photo-Fries rearrangement. Korshak et al., in Synthesis and Properties of Self-Protecting Polyarylates, Journal of Polymer Science, Part A-1, Vol.7, pages 157 to 172 (1969) describe a mechanism to explain what happens when polyarylates are exposed to UV light. The authors propose that polyarylates undergo the Photo-Fries rearrangement resulting in carbonyl and hydroxyl groups ortho to one another, structurally similar to o -hydroxybenzophenones which are known light absorbers. Thus, the polyarylates have increased photo-stability in the bulk of the material. Cohen et al., in Transparent Ultraviolet-Barrier Coatings, Journal of Polymer Science, Part A-1, Vol. 9, pages 3263 to 3299 (1971) describe a number of phenyl polyesters, including polyarylates, which were synthesized to furnish molecules whose backbones rearrange under UV light to an o -hydroxybenzophenone structure. This Photo-Fries rearrangement produced ultraviolet opacity in an irradiated film while maintaining visual transparency. Thin coatings of these polyesters completely protected substrates ordinarily sensitive to ultraviolet light. The authors state that spectroscopic analysis of various rearranged films and coatings showed that the o-hydroxybenzophenone polymer formed was concentrated at the irradiated surface of the original polyester coating as a "skin". Such a skin, formed in situ during the irradiation, functioned to protect both the original polyester coating as well as the coated substrate from degradation by ultraviolet irradiation. Furthermore, a significant "healing" mechanism appeared inherent in the coatings, for as the exposed skin ultimately degraded under extended ultraviolet irradiation, more of the underlying polyester layer apparently rearranged to compensate for the loss. Thus, the clear coating functioned both as a protective skin and a rearrangeable reservoir. US-A- 3,492,261 describes film forming solutions of rearrangeable aromatic polyesters which are the polymeric reaction product of an aromatic dihydric compound and an aromatic dicarboxylic compound. It is stated in this patent that the preferred dihydric compounds are the ester derivatives of 4,4-bis(4'-hydroxyphenyl)pentanoic acid. The solutions of aromatic polyesters can be coated onto a substrate and dried to transparent films; they are capable of absorbing ultraviolet light and undergo rearrangement in the presence of the substrate to form a transparent compound which is stable to and will act as a barrier to ultraviolet light. US-A-3,503,779 discloses substrates which are coated with rearrangeable aromatic polyesters which are the polymeric reaction product of an aromatic dihydric compound and an aromatic dicarboxyl compound. The outer exposed surface of the aromatic polyester coatings rearrange under the influence of ultraviolet light to form a new transparent compound which is stable to and will act as a barrier to ultraviolet light. US-A- 3,444,129 discloses rearrangeable aromatic polyesters which are the polymeric reaction product of an aromatic dihydric compound, and an aromatic dicarboxylic compound. The preferred dihydric compound is stated to be the ester derivatives of 4,4-bis(4'-hydroxyphenyl) pentanoic acid. The rearrangeable aromatic polyesters are useful as ultraviolet light barriers. US-A- 3,460,961 describes substrates which are protected with a transparent aromatic polyester coating of two contiguous superposed layers. The aromatic polyester compounds are the reaction product of an aromatic dihydric compound and an aromatic dicarboxylic compound. The aromatic polyester coating undergoes rearrangement in the presence of ultraviolet light to form a transparent compound which is stable to and acts as a barrier to ultraviolet light. However, in all of these references coatings are being utilized which, as discussed above, require expensive solvent coating equipment and require evaporation of a solvent. US-A-4,503,121 describes laminate compositions comprising a polyarylate, or blends thereof, derived from a dihydric phenol and an aromatic dicarboxylic acid which is laminated upon the surface of a poly(aryl ether), particularly polysulfone. It is stated therein that excellent protection is afforded the polysulfone against degradation resulting from prolonged UV exposure by laminating the polyarylate upon its surface. Similarly, laminates formed from a layer of a polyarylate sheet and a layer of an aromatic polycarbonate, a polyester, or mixtures of these resin sheets, useful in glazing applications, are described in U.S. 4,643,937. Blends containing polyarylates and polyolefins are known and have been discussed in US-A-4,281,079. Polyolefin/polyester blends have also been melt-extruded into shaped articles such as filaments, or films - see US-A-3,534,120. EP-A-0,113,117 describes a process for producing a moulded thermoplastic resin in a die in which a removable skin layer thermoplastic resin having a thickness of l/10th or less of the thickness of a core layer thermoplastic resin to be moulded is interposed between the inner surface of the die and the core layer resin, the two resins being co-moulded together under pressure and at a temperature above the glass transition temperatures of the core layer resin, and the skin layer resin being thereafter removed from the core layer to yield the desired moulded article. Any of the thermoplastic resins generally used for extrusion or compression moulding may be used to make the moulded article (core resin), e.g., polystyrene, styrene-acrylonitrile copolymer, ABS resin, polyvinyl chloride, polymethyl methacrylate, polycarbonate, polyester, nylon, polyphenylenether, polyoxymethylene, polyolefins such as polyethylene or polypropylene or blends, and copolymers of these resins. The core resin used may also be an ultra-high molecular weight thermoplastic resin having a viscosity average molecular weight of 800,000 or more, preferably 800,000 to 8,000,000, more preferably l,000,000 to 5,000,000, such as polyethylene or polymethyl methacrylate, a readily heat-decomposable thermoplastic resin, such as polyvinylidene chloride or a thermoplastic resin containing a blowing agent. The core resin used may be a multi-layer structure consisting of two or more kinds of thermoplastic resins, if desired. It is known that low density (≦0.94g/cm³) polyethylenes and EVA-modified polyethylene films are widely used as covering for greenhouses. Although UV absorbers are incorporated into the resins, the useful life of such films is usually one to two years in Florida-California outdoor exposure. Hence, laminate structures of polyarylates, which display outstanding weatherability characteristics, with polyethylenes, in which the latter would be protected against UV irradiation by a thin layer of the aromatic polyester, were deemed of utmost importance and practical interest. Such multilayer films are the subject of the instant invention. The Invention In the instant invention it has been found that a sheet made from low density polyethylene (d≦0.94g/cm³) or from a polyethylene copolymer can be protected from ultraviolet light by laminating thereon a sheet made from a polymer which undergoes a Photo-Fries rearrangement such as a polyarylate, onto one or both of its surfaces. As compared with the prior art methods which utilize a coating to protect a substrate against UV light, the present invention does not have the disadvantage of solvent removal. Also, this invention provides permanent protection to the underlying surface as compared to a coating which can wear off. It was found that an appropriate tie layer is required to ensure proper adhesion between the polyethylene and the polyarylate. The nature of the tie layer is important both with respect to adhesion and to the clarity of the laminated film. The instant composite films display good mechanical properties and excellent UV resistance. They are useful in a variety of outdoor applications such as, for example, covering for greenhouses. According to the present invention, there is provided a laminated structure comprising a layer of a low density ethylene polymer or copolymer, a tie layer, and a layer of a polyarylate, a polyarylate blend, or a polyarylate copolymer, wherein the composition of said tie layer is composed of at least one member selected from: (a) maleic acid modified waxy ethylene polymers prepared by (i) polymerizing ethylene in the presence of hydrogen using as a catalyst an halogen compound of titanium or vanadium supported on a carrier composed of an hydrocarbon-insoluble magnesium-containing compound and an organoaluminum compound, the amount of hydrogen being 3 to 90 molar percent of the vapor phase in the polymerization vessel, excluding the vapor portion of the solvent, and (ii) oxidizing and modifying the waxy ethylene polymer by reaction with a maleic acid compound, wherein the degree of oxidation in the waxy ethylene polymer is such that the amount of oxygen in the oxidized material is in the range of from 0.1 to 1 percent by weight; and (b) maleic anhydride functionalized ethylene-vinyl acetate copolymers having melt index values in the range of 0.8 to 2.5g/10 minutes and displaying Vicat softening points of 60 to 83°C. Specifically, the instant invention comprises a laminate of low density polyethylene polymer or copolymer, a tie layer as defined above, and a polyarylate, a polyarylate blend or a polyarylate copolymer. A preferred laminate comprises a layer where the polyarylate is derived from bisphenol-A and isophthalic and terephthalic acids. The components of the laminated films have the following thicknesses: the low density polyethylene polymer or copolymer from 0.051 to 2.54 mm (2 to 100 mils), preferably from 0.10 to 0.25 mm (4 to 10 mils); the polyarylate, the polyarylate blend, or the polyarylate copolymer - from 2.54 to 102 µm (0.1 to 4.0 mils), preferably from 12.7 to 50.8 µm (0.5 to 2.0 mils); the tie layer - from 7.62 to 25.4 µm (0.3 to 1.0 mils), preferably from 7.62 to 20.32 µm (0.3 to 0.8 mils). The polyarylates useful in the instant invention are based on: (a) at least one dihydric phenol of the formula: where Y is independently selected from alkyl groups of l to 4 carbon atoms, chlorine or bromine; Z independently has a value of from O to 4, inclusive; R is independently selected from a divalent C₆ to C₂₀ aromatic or saturated aliphatic or cycloaliphatic hydrocarbon radical, particularly an alkylene or alkylidene radical having from 1 to 8 carbon atoms, especially C(CH₃)₂, a cycloalkylene or cycloalkylidene radical having up to and including 9 carbon atoms, 0, S, SO, S0₂, CO or a covalent chemical bond; and x is O or l; and (b) at least one aromatic dicarboxylic acid. The dihydric phenols that may be used in this invention include the following: 2,2-bis(4-hydroxyphenyl)propane, bis-(2-hydroxyphenyl)methane, bis-(4-hydroxyphenyl)methane, bis-(4-hydroxy-2,6-dimethyl-3-methoxyphenyl)methane, 1,1-bis(4-hydroxyphenyl)ethane, 1,2-bis(4-hydroxyphenyl)ethane, 1,1-bis-(4-hydroxy-2-chlorophenyl)ethane, 1,1-bis-(3-methyl-4-hydroxyphenyl)ethane, 1,1-bis-(3-methyl-4-hydroxyphenyl)propane, 2,2-bis-(3-phenyl-4-hydroxyphenyl)propane, 2,2-bis-(3-isopropyl-4-hydroxyphenyl)propane, 2,2-bis-(2-isopropyl-4-hydroxyphenyl)propane, 2,2-bis-(4-hydroxyphenyl)pentane, 3,3-bis-(4-hydroxyphenyl)pentane, 2,2-bis-(4-hydroxyphenyl)heptane, 1,2-bis-(4-hydroxyphenyl)-1,2-bis-(phenyl)-propane, 4,4'-(dihydroxyphenyl)ether, 4,4'-(dihydroxyphenyl)sulfide, 2,2-bis-(4-hydroxy-3,5-dichlorophenyl)propane, 4,4'-(dihydroxyphenyl)sulfone, 4,4'-(dihydroxyphenyl)sulfoxide, 4,4'-(dihydroxybenzophenone), and 4,4'-biphenol. In addition, diphenols such as hydroquinone, and the naphthalene diols are also useful. These dihydric phenols may be used individually or in any combination which when reacted with an aromatic dicarboxylic acid or mixtures thereof produces polyarylate polymers and copolymers that are soluble in inert organic solvents as hereinbelow defined. The preferred dihydric phenol is 2,2-bis(4-hydroxyphenyl)propane. The aromatic dicarboxylic acids that may be used in this invention include terephthalic acid, isophthalic acid, any of the naphthalene dicarboxylic acids and mixtures thereof, as well as alkyl substituted homologs of these carboxylic acids, wherein the alkyl groups contain from 1 to 4 carbon atoms, and acids containing other inert substituents such as halides or alkyl or aryl ethers. Preferably, mixtures of isophthalic and terephthalic acids are used. The isophthalic acid to terephthalic acid ratio in the mixture is from 20:80 to 100:0 while the most preferred acid ratio is from 25:75 to 50:50. Also, from 0.5 to 20 mole percent of aliphatic diacids containing from 2 to 10 carbon atoms, such as adipic acid or sebacic acid, may be additionally used in the polymerization reaction. The polyarylates may be prepared using any of the methods known in the art. These include: (a) The acid chloride route. In this route the polyarylate is obtained via the reaction of an aromatic diacid chloride with dihydric phenol. Two procedures are useful. One is carried out at low temperature and the other at high temperature. In the low temperature technique, polycondensation of the aromatic acid chloride with the dihydric phenol is effected at ambient temperatures in an inert solvent, such as methylene chloride, in the presence of a basic catalyst and an acid acceptor. This type of process is described in, for example, US-A- 3,234,168. The condensation may also be performed in the presence of an inorganic acid acceptor, such as Ca(OH)₂ suspended in an inert organic solvent, as described in US-A-3,939,117. A second immiscible solvent, e.g., water, may be present in these low-temperature reactions. This process variant is referred to as the interfacial or phase boundary polymerization. In the interfacial reaction the phenolic components are dissolved in an aqueous alkaline phase. Small quantities, e.g., 0.1 to 1.0 percent by weight (based on the phenolic materials used) of reducing alkaline substances, such as sodium bisulfite for example, may be added to the aqueous phase. Quarternary ammonium or phosphonium compounds, in amounts ranging from 0.5 to 5.0 mole percent based on the phenolic components, may be used as the polymerization catalysts. The acid chlorides are dissolved in the organic solvent and the solution is brought into contact with the aqueous alkaline solution which contains the phenolates. The two phases are vigorously stirred and polymer formation occurs at the interface. Preferred solvents for the low-temperature polymerization include methylene chloride, chloroform, tri- and tetrachloroethylene, tetrachloroethane, chlorobenzene, dichlorobenzene, tetrahydorfuran, and mixtures of these solvents. Temperatures are generally in the range of from 0 to 40°C, preferably in the range of from 15 to 30°C. The high-temperature acid chloride process involves the condensation reaction at elevated temperatures (>100°C) in high boiling solvents. The reactions may be performed in the absence of catalysts, in which case temperatures in excess of 200°C are preferred. The polycondensations may also be catalyzed, for example with magnesium, as described in US-A- 3,733,306 and by Matzner and Barclay, Journal of Appl. Polymer Science, Vol. 9, pp 3321-3336 (1965). Another class of catalysts are, for example, the titanate esters described in DE-A- 1,933,657. Lower temperatures are satisfactory for the catalyzed reactions and are generally in the range of from 110°C to 220°C, although higher temperatures may be necessary in some instances. Inert, high boiling solvents which can be used in the high temperature process are those that do not react with the starting materials or with the final polyester. Also, the solvents should dissolve the polyarylate formed. Representative solvents include the chlorinated aromatic hydrocarbons such as chlorobenzene, dichloro-, trichloro-, and tetrachlorobenzenes, chlorinated biphenyls or diphenyl ethers, chlorinated naphthalenes; as well as non-chlorinated aromatics such as anisole, nitrobenzene, ditolymethane, terphenyl, benzophenone and the dibenzylbenzenes. (b) The diacetate process. The diacetate process consists in the reaction of aromatic diacids with diesters of the dihydric phenols, i.e., derivatives of the formula R₁-COO Ar OCOR₁ where R₁ is, for example, a C₁ to C₁₀ aliphatic group, and Ar is the residuum of the dihydric phenol. Thus, the polymerizations using the diacetate process require first the preparation of a diester of the dihydric phenol with a monocarboxylic acid. In principle, any monocarboxylic acid can be used; aliphatic acids containing from two to eleven carbon atoms are preferred; most preferred are C₂ to C₄ aliphatic acids. The esters (3) are then reacted under acidolysis conditions with the dicarboxylic acid or mixtures of dicarboxylic acids; the reaction yields the polyarylate and the monocarboxylic acid, which can be recycled. The two steps, i.e., the preparation of the monocarboxylic acid esters (3), and their polymerization, can be performed separately, or in an one-pot procedure. It is preferred that the intermediate diesters contain ≦ than 1,500 parts per million of residual acid anhydride prior to polymerization. This procedure, as described in US-A- 4,321,355, yields polyarylates having good color and melt-stability. The acidolysis reaction can be performed in bulk or in the presence of a processing aid. The preferred processing aids are a diphenyl ether compound as described in US-A-4,294,956 and US-A- 4,296,232; a cycloaliphatic substituted aromatic or heteroaromatic compound as described in US-A- 4,294,957; and an halogenated and/or etherated substituted aromatic or heteroaromatic compound as described in US-A- 4,374,239. The polymerization reaction may also be conducted using a slurry process as described in US-A-4,083,829. The acidolysis reactions are carried out in the temperature range of from 200°C to 350°C; preferably in the temperature range of from 250° to 325°C. However, lower and higher temperatures may also be used. The reactions can be carried out at atmospheric or subatmospheric pressures; they can also be performed under pressures higher than atmospheric. The acidolysis reaction generally does not require a catalyst. In some instances, however, the use of an appropriate catalyst may prove advantageous. Typical catalysts include dialkyl tin oxide (e.g., dibutyl tin oxide), diaryl tin oxide, titanium dioxide, antimony trioxide, alkoxy titanium silicates, titanium alkoxides, alkali and alkaline earth metal salts of carboxylic acids (e.g., zinc acetate), the gaseous acid catalysts, such as Lewis acids (e.g., BF₃) and hydrogen halides (e.g., HCl). The quantity of catalyst utilized typically is from 0.001 to 1 percent by weight based upon the total monomer weight, and most commonly from 0.01 to 0.2 percent by weight. (c) The diphenate process The third basic polyarylate process, referred to as the diphenate route, consists in reacting a diaryl ester of an aromatic diacid, for example, (4), with a dihydric phenol. In formula (4) Ar₁ is a monovalent radical. The reaction yields the polyarylate and the phenol Ar₁OH, which can be recycled. The group Ar₁ can be derived from any phenol; phenyl or tolyl groups are preferred. The polymerization is essentially an ester-interchange reaction; the two steps, i.e., the preparation of (4) and their polymerization, may be performed separately or in an one-pot procedure. The ester-exchange reaction can be performed in bulk or in the presence of a processing aid. The preferred processing aids are a diphenyl ether compound, a cycloaliphatic substituted aromatic or heteroaromatic compound, or an halogenated and/or etherated substituted aromatic or heteroaromatic compound as described for example, in US-A- 4,459,384. It is most preferred to use the diphenyl iso- and terephthalates. The ester-exchange reaction is generally carried out in the temperature range of from 200° to 350°C. However, lower or higher temperatures may be used. The reaction can be performed at atmospheric, reduced, or higher than atmospheric pressures. Catalysts, generally compounds containing metals such as alkali and alkaline earth metals, cerium, manganese, cobalt, zinc, germanium, tin, antimony and bismuth, may be used to accelerate the polymerization. Examples of typical catalysts are the alkali metal phenoxides, hydroxides, and alkoxides. Useful polyarylates have a reduced viscosity of from 0.4 to greater than 1.0, preferably from 0.5 to 0.8 dl/g as measured in chloroform (0.5g/100 ml. chloroform) or other suitable solvent at a suitable temperature. Note, that in addition to polyarylates per se, one may also use their blends with other polyesters, such as poly(ethylene terephthalate) and other poly(alkylene phthalates). Heating of said blends results in ester-interchange of the components and formation of polyarylate-poly(alkylene phthalate) copolymers. Such copolymers are also useful for the purposes of the instant invention. Another class of polyarylate copolymers that may be employed are the poly (arylate-carbonates). These are described in, for example, US-A- 3,169,121, herein incorporated by reference. Such copolyesters comprise recurring carbonate groups carboxylate groups and aromatic carbocyclic groups in the linear polymer chain, in which at least some of the carboxylate groups and at least some of the carbonate groups are bonded directly to ring carbon atoms of the aromatic carbocyclic groups. The copolyesters are prepared by reacting, as essential ingredients, a difunctional carboxylic acid, a difunctional phenol, and a carbonate precursor, methods for preparing the copolyesters being well known, and disclosed in US-A-3,030,331 and US-A-3,169,121, among others. These copolyesters comprise at least two of the following four recurring units in their linear chain: wherein A and R₃ are independently aromatic groups such as phenylene, biphenylene, naphthylene or anthracenylene; F may be an alkylene, cycloalkylene, alkylidene or cycloalkylidene group such as methylene, ethylene, propylene, propylidene, isopropylidene, butylene, butylidene, amylene, isoamylene, amylidene, isoamylidene, cyclohexylene or cyclohexylidene; R₂ is hydrogen, alkyl, cycloalkyl or aryl; T is an inorganic atom such as chlorine, bromine, or fluorine, an inorganic group such as nitro, an organic group such as R₂ above, or any alkoxy group such as OR₂, it being only necessary that T be inert to, and unaffected by, the reactants and reaction conditions; m is any whole number from and including zero through the number of positions available on A for substitution; p is any whole number from and including zero through the number of available positions on F; q is a whole number equal to at least one. s is either zero or one; t is a whole number equal to at least one; and u is any whole number including zero. Examples of dihydric phenols useful in making polyester carbonates include all of those mentioned in connection with making polyarylates, supra. The carboxylic acids useful in making polyester carbonates include: saturated, aliphatic dibasic acids derived from straight chain paraffin hydrocarbons such as oxalic, malonic, dimethyl malonic, succinic, glutaric, adipic, pimelic, suberic, azelaic, and cebacic acid, and halogen-substituted derivatives thereof; aliphatic carboxylic acids containing hetero atoms in their aliphatic chain, such as thio-diglycolic or diglycolic acid; unsaturated acids such as maleic or fumaric; aromatic and aliphatic-aromatic dicarboxylic acids such as phthalic, isophthalic, terephthalic, homo-phthalic, o -, m -, and p -phenylene diacetic acid, and polynuclear aromatic diacids (e.g. naphthalene dicarboxylic); hydroxy acids including aliphatic hydroxy acids such as hydroxybutyric, glycolic, and lactic acid, aliphatic-aromatic hydroxy acids such as mandelic and o -, m -, and p -hydroxybenzoic acid; and long chain fatty acids such as 12-hydroxystearic acid; cycloaliphatic acids including tetrahydrophthalic, tetrahydroterephthalic or tetrahydroisophthalic. A preferred polyester carbonate results from the condensation of phosgene, terephthaloyl chloride or isophthaloyl chloride with bisphenol-A and a small amount of p -tert-butylphenol as the chain terminator. The polyester carbonates should contain at least 50 mole percent of polyarylate groups. Their reduced viscosities are generally in the range that was found to be useful for polyarylates. By the term polyolefin are meant homo- and copolyethylenes having a density of ≦0.94g/cm³. The materials include: conventional low density polyethylene (LDPE) made under high pressure; LDPE copolymers incorporating other α-olefins; polyethylene/vinyl acetate copolymers; linear low density polyethylenes (LLDPE) which include copolymers of ethylene with one or more of propylene, butene, hexene, 4-methyl pentene-l, octene-l and other unsaturated aliphatic hydrocarbons. The materials have a density range of 0.91-0.94 g/cm³ and a melting peak range of 100-135°C. These LLDPE resins are generally prepared using transition metal catalysts such as compounds of titanium, aluminum or chromium. [Note that these LLDPE resins are different from conventional LDPE materials. Thus, because of the methods by which low density polyethylenes (LDPE) are prepared, they are highly branched materials which have a tendency to coil on themselves. The linear low density materials, on the other hand, as their name indicates, have very little of this long-chain branching and have on the backbone just short chain-branches introduced by the use of a comonomer]; and very low density ethylene copolymers. These materials, having a density of between 0.855 and O.910g/cm³ are described in EP-A-120,503 published on October 3, 1984. The olefins which can be polymerized with ethylene to produce the low density, low modulus copolymers may contain from 3 to 8 carbon atoms. These α-olefins should not contain any branching on any of their carbon atoms closer than two carbon atoms removed from the double bond. Suitable α-olefins include propylene, butene-l, pentene-l, hexene-l, 4-methylpentene-1, heptene-l, and octene-l. The preferred α-olefins are propylene, butene-l, hexene-l, 4-methylpentene-1 and octene-l. These ethylene polymers and copolymers may be produced by the process described in the said EP-A-120,503, which process comprises continuously contacting, in a fluidized bed, at a temperature of from 30°C up to 80°C, a gaseous mixture containing (a) ethylene or ethylene and at least one higher α-olefin in a molar ratio of such higher α-olefin to ethylene of from 0.35:1 to 1, and (b) at least 25 mole percent of a diluent gas, with a catalyst composition prepared by forming a precursor composition from a magnesium compound, titanium compound, and-electron donor compound; diluting said precursor composition with an inert carrier; and activating the diluted precursor composition with an organoaluminum compound. The low density polyethylene homo- and copolymers generally have melt-indices in the range of 0.5 to 5.0g/10 minutes, as measured using ASTM test D-1238, at 190°C under 303 kPa (44 psi) pressure. Melt index values in the range of from 1 to 2g/10 minutes are preferred. The most critical component of the laminated film structure is the tie layer. The latter, when properly chosen, ensures both a good adhesion of the polyolefin to the polyarylate and good clarity. Several known tie polymers were investigated. It was found that only two resins gave the desired performance. The first, marketed by Mitsui Chemical Company under the tradename of ADMER AT 469® is a material based on maleic acid modified waxy ethylene polymers as described in US-A-3,892,717. According to the latter patent, the resins are prepared by polymerizing ethylene in the presence of hydrogen, using as a catalyst an halogen compound of titanium and/or vanadium supported on a carrier composed of an hydrocarbon-insoluble magnesium-containing compound and an organoaluminum compound, the amount of hydrogen being 3 to 90 molar percent of the vapor phase in the polymerization vessel, except the vapor portion of the solvent, and oxidizing and modifying the waxy ethylene polymer by reaction with a maleic acid compound. The term "waxy" is defined in the subject patent as a waxy substance that has a softening point (determined by the ring and ball test in accordance with JIS K-2531) of from 80°C to 135°C, a melt viscosity at l40°C of 0.001 to 100 Pas (1 to 10⁵ centipoises), a hardness of O to 5O, (determined by penetration in accordance with JIS K-2530), a density of 0.85 to 0.98g/cm³, and a viscosity average molecular weight [the viscosity of the polymer being measured at 135°C using decalin as a solvent, and the viscosity average molecular weight being then calculated by the formula: M v =2.51xlO⁴ [η]1.235] of 400 to 2,000. Furthermore, the degree of oxidation of the wax required for satisfactory reactivity with the maleic acid compound must be such that the oxygen content of the oxidized material be in the range of 0.1 to 1 percent by weight. Most of the bound oxygen is in the form of peroxide. Oxidation temperatures range from above the melting point of the polyethylene to 140°C. To promote the oxidation, 0.1 to 1 percent by weight of an organic peroxide may be added. The term "maleic acid compound" comprises maleic acid, maleic anhydride and the C₁ to C₈ dialkyl esters of maleic acid. The degree of grafting is such that the oxygen content of the final material is in the range of from 0.1 to 5.0 percent by weight, preferably in the range of from 0.5 to 2.0 percent by weight. The excellent performance obtained with ADMER® was surprising. Thus, two resins, very similar to ADMER®, namely, those available from the Chemplex Company of Rolling Meadows, IL, under the tradenames of PLEXAR 3026® and PLEXAR PX-3® gave either a good bond, but a hazy laminate; or good clarity with fair adhesion only. PLEXAR® resins are based on blends disclosed in US-A-4,087,587 and US-A-4,087,588. These blends comprise a polyolefin component and an high density polyethylene (HDPE) grafted with an unsaturated fused ring carboxylic acid anhydride. The polyolefin component of the blend may include a number of resins such as high, low and medium density polyethylene and polyolefin copolymers such as ethylene/vinyl acetate copolymers and ethylene/acrylic acid copolymers. The second tie layer material which gave good results was BYNEL CXA 3101® sold by the Dupont Company. The BYNEL CXA® series (coextruded adhesive) are maleic anhydride functionalized ethylene-vinyl acetate copolymers. The CXA 3000 series generally have melt index values in the range of 0.8 to 2.5g/10 minutes and display Vicat Softening Points of 60 to 83°C - see, Digest of Polymer Developments, Polyolefins, Series 1, No.42, January 1987, pp 70-71, published by Springborn Laboratories, Inc., Enfield, CT. In view of the poor performance of the PLEXAR® materials, the good adhesion and transparency achieved with the BYNEL® resin were again quite surprising and unexpected. The laminate may be prepared by the procedure and using the apparatus described in US-A-3,557,265. In the method of the latter patent, film or sheet having a plurality of layers is formed by deforming a flowing stream having layers of diverse thermoplastic material wherein the cross-sectional configuration of the plurality of flowing streams is altered by reducing the dimension of the stream in a direction generally perpendicular to the interfaces between the individual streams and by increasing the dimension of the stream in a direction generally parallel with the interface to provide a sheet having a laminar structure. In another method previously extruded sheets are brought together under pressure and temperature conditions or in the presence of adhesives in order to obtain adherence of the sheets to one another. Coextrusion offers the least expensive means of preparing the laminate. Within coextrusion, three different techniques are most often employed. In one of these techniques, the sheets are extruded from separate extruders through separate sheet dies into contact with one another while still hot, and are then passed through a single set of rollers or another extrusion die and down a single sheet line. Another coextrusion technique employs an adaptor or other means of bringing different plastic materials from corresponding extruders into contact with one another prior to their passage through an extrusion die. A further coextrusion technique is where polymer melts meet in an extrusion die to form a laminate. Coextrusion is the preferred technique for forming the laminates of this invention. The laminate may be formed into a shaped article such as a lens or a globe. If the laminate is to be used as a window, the laminate may be coated with a mar-resistant coating. EXAMPLES The following examples serve to give specific illustrations of the practice of this invention with the exception of Reference Example l, which is included for reference purposes only. The following designations used in the examples have the following meanings: Polyarylate: a blend of 60 parts by weight of the polyarylate of formula (l) wherein (l) has a reduced viscosity in the range of from 0.5 to 0.65dl/g, as measured in p -chloro phenol, at a concentration of 0.2g/100 ml. of solvent, and at 49°C, and wherein the ratio of terephthalic acid to isophthalic acid units in (l) is 1:1, with 40 parts by weight of poly(ethylene terephthalate). Natural Polyethylene: LDPE having a melt index of from 1 to 2g/10 minutes, as measured at l90°C, under 303 kPa (44 psi) pressure using the method of ASTM test D-1238. Polyethylene USI NA 235-75: - low density polyethylene containing 4 percent of vinyl acetate. Tie polymers used were: ADMER AT 469® - based on waxy polyethylene, grafted with a maleic acid compound as described in US-A-3,892,717 and sold by the Mitsui Chemical Company. PLEXAR 3026® and PLEXAR PX-3®: - based on blends described in US-A-4,087,587 and US-A-4,087,588 and as sold by the Chemplex Company. BYNEL CXA 3101® - maleic anhydride functionalized ethylene-vinyl acetate copolymers sold by the Dupont Company. Reference Example 1. UV weatherability studies. Test samples were prepared by clamping a layer of polyarylate over a layer of natural polyethylene, the "laminated" structures were exposed to Atlas XW™ accelerated weathering. Three thicknesses of polyarylate were used. The results, shown in Table I, indicate that the polyarylate provides the polyethylene with excellent UV protection. XW Weathering of Polyarylate Protected Polyethylene Film Exposure Time (hours) Tensile Break Elongation. % Unproteted Polyarylate Protected Thickness of Polyarylate Layer 7.62-12.7µm (0.3-0.5 mil) 25.4 µm (l mil) 51 µm (2 mils) Original 680 600 680 680 600 310 725 700 700 1000 5.5 675 720 685 2000 Brittle 650 740 720 Example 2 Coextrusion Experiments. Using three extruders (one for each component of the laminated structure) three-layer blown films were prepared. For both the polyethylene and the polyarylate, continuous taper, 2:1 compression ratio screws were used. Since polyethylene processes satisfactorily on this screw and the low 2:1 compression is needed for the polyarylate, this allowed interchangeability of resins between the two machines feeding the inner and the outer layers of the laminate. A conventional 3:1 feed-transition-metering screw was used for the tie layer. Typical extrusion temperatures were: 107-177°C (225-350°F) for the polyethylene; 260-288°C (500-550°F) for the polyarylate; and 149-177°C (300-350°F) for the tie layer. The polyethylene used was USI NA 235-75. Because of the short distance [∼2-2.5 m (∼7-8 ft.)] between extrusion and bubble collapse, the polyarylate layer was on the inside; when the inner layer was polyethylene, bonding occurred upon bubble collapse, except at very low output rates. The following was observed with respect to the tie materials: PLEXAR 3026® produced a good bond, but the laminate was hazy; PLEXAR PX-3® gave a transparent laminate, but the adhesion was only fair; ADMER AT 469® and BYNEL CXA 3101® extruded very well through a die set at polyarylate temperatures 260-288°C (-500-550°F); bonds between the polyethylene and the polyarylate were excellent as was also the transparency. Weatherability studies on the coextruded structures using the XW-Weatherometer are summarized in Table II below. The data show that the laminates display vastly improved weatherability characteristics as compared with the polyethylene.

Claims: A laminated structure comprising a layer of a low density ethylene polymer or copolymer, a tie layer, and a layer of a polyarylate, a polyarylate blend, or a polyarylate copolymer, wherein said tie layer is composed of at least one member selected from: (a) maleic acid modified waxy ethylene polymers prepared by (i) polymerizing ethylene in the presence of hydrogen using as a catalyst an halogen compound of titanium or vanadium supported on a carrier composed of an hydrocarbon-insoluble magnesium-containing compound and an organoaluminum compound, the amount of hydrogen being 3 to 90 molar percent of the vapor phase in the polymerization vessel, excluding the vapor portion of the solvent, and (ii) oxidizing and modifying the waxy ethylene polymer by reaction with a maleic acid compound, wherein the degree of oxidation in the waxy ethylene polymer is such that the amount of oxygen in the oxidized material is in the range of from 0.1 to 1 percent by weight; and (b) maleic anhydride functionalized ethylene-vinyl acetate copolymers having melt index values in the range of 0.8 to 2.5g/10 minutes and displaying Vicat softening points of 60 to 83°C. A laminated structure as claimed in claim l, wherein said tie layer is composed of a maleic acid modified waxy ethylene polymer, wherein said maleic acid compound is selected from maleic acid, maleic anhydride and the C₁-C₈ dialkyl esters of maleic acid. A laminated structure as claimed in claim 1 or claim 2, wherein the layer of the low density ethylene polymer or copolymer has a thickness of from 0.051 to 2.54 mm (2 to 100 mils); wherein the layer of the polyarylate, the polyarylate blend or the polyarylate copolymer has a thickness of from 2.54 to 102 µm (0.1 to 4.0 mils); and wherein the tie layer has a thickness of from 7.62 to 25.4 µm (0.3 to 1.0 mils). A laminated structure as claimed in any of claims 1 to 3, wherein said structure comprises a polyarylate which is a polyester of a dihydric phenol and an aromatic dicarboxylic acid. A laminated structure as claimed in claim 4, wherein said dihydric phenol is of the formula: where Y is independently an alkyl group of one to four carbon atoms, chlorine or bromine; Z independently has a value of from 0 to 4 inclusive; R is a divalent C₆ to C₂₀ aromatic or saturated aliphatic or cycloaliphatic radical, O, S, SO, SO₂, CO or a covalent chemical bond; and x is 0 or 1. A laminated structure as claimed in claim 4 or claim 5, wherein said dihydric phenol is a naphthalenediol. A laminated structure as claimed in any of claims 4-6, wherein said aromatic dicarboxylic acid is selected from one or more of terephthalic acid, isophthalic acid, and any of the naphthalene dicarboxylic acids, as well as the C₁ to C₄ alkyl, alkoxy and halo derivatives thereof. A laminated structure as defined in claim 4, wherein said polyarylate is a polyester derived from 2,2-bis(4-hydroxyphenyl)propane and an 1:1 molar mixture of isophthalic and terephthalic acids. A laminated structure as claimed in claims 1 to 3, wherein said structure comprises a polyarylate blend which is a blend of a polyarylate as defined in any of claims 4-8 with a poly (alkylene phthalate). A laminated structure as claimed in any of claims l to 3, wherein said structure comprises a polyarylate copolymer which is a copolymer of a polyarylate as defined in any of claims 4-8, with a poly(alkylene phthalate). A laminated structure as claimed in claim 9 or claim 10, wherein said poly(alkylene phthalate) is one or more of poly(ethylene terephthalate) and poly(butylene terephthalate). A laminated structure as defined in any of claims 1 to 3, wherein said structure comprises a polyarylate copolymer which is a poly(arylate-carbonate) copolymer comprising at least two of the following four recurring units [I]-[IV] in its linear chain: wherein A and R₃ are independently aromatic groups selected from phenylene, biphenylene, naphthylene and anthracenylene; F is an alkylene, cycloalkylene, alkylidene or cycloalkylidene; R₂ is hydrogen, alkyl, cycloalkyl or aryl; T is R₂, OR₂, chlorine, bromine, fluorine, or nitro; m is any whole number from and including zero through the number of positions available on A for substitution; p is any whole number from and including zero through the number of positions available for substitution on F; q and t are integers equal to at least one; s is zero or one; and u is any whole number including zero. A laminated structure as claimed in claim 12, wherein said poly(arylate-carbonate) is derived from a dihydric phenol as defined in claim 5 or claim 6, and a dicarboxylic acid, which is selected from saturated aliphatic dibasic acids and halogen-substituted derivatives thereof; aliphatic dicarboxylic acids containing hetero atoms in their chains; unsaturated diacids; aromatic, aliphatic-aromatic and polynuclear aromatic diacids; aliphatic and aromatic hydroxy acids; and cycloaliphatic dibasic acids. A laminated structure as claimed in any of claims l to 3, wherein said structure comprises a polyarylate copolymer which is a poly(arylate-carbonate) derived from 2,2-bis(4-hydroxyphenyl)propane and an acid selected from carbonic, terephthalic and isophthalic acids. A laminated structure as claimed in any of claims 1 to 4, wherein said ethylene polymer or copolymer has a density equal to or below 0.94 g/cm³, and a melt index of from 0.5 to 5.0 g/10 minutes as measured at 190°C under a pressure of 303 kPa (44 psi). A laminated structure as claimed in claim 15, wherein said ethylene polymer or copolymer is selected from conventional low density polyethylenes (LDPE) made under high pressure; LDPE copolymers incorporating other α-olefins; ethylene/vinyl acetate copolymers; linear low density polyethylenes (LLDPE); and the very low density copolymers of ethylene with other α-olefins.

Inventors: DICKINSON BARRY LEE, DICKINSON, BARRY LEE
Applicants: AMOCO CORP, AMOCO CORPORATION
Application year: 1989
Main classification: B32B27
IPC codes: C08G63, B32B27, B32B37