METHOD FOR THE PREPARATION OF POLYPHENYLENE ETHER-POLYESTER COPOLYMERS

Abstract: Polyphenylene ether-polyester copolymers, useful for com­ patibilizing blends of polyphenylene ethers with polyesters such as poly (alkylene terephthalates), are prepared by heating a polyphenylene ether with a polyester containing olefinic structural units, such as those derived from maleic or fumaric acid.

Description: This invention relates to a novel process for preparing polyphenylene ether-polyester copolymers useful in the preparation of resinous compositions with high impact resistance and solvent resistance. The polyphenylene ethers are a widely used class of thermoplastic engineering resins characterized by excellent hydrolytic stability, dimensional stability and dielectric properties. They are also resistant to high temperature conditions under many circumstances. Because of the brittleness of many compositions containing polyphenylene ethers, they are frequently blended with impact modifiers such as elastomers to form molding compositions. A disadvantage of the polyphenylene ethers which militates against their use for molding such items as automotive parts is their low resistance to non-polar solvents such as gasoline. For increased solvent resistance, it would be desirable to blend the polyphenylene ethers with resins which have a high degree of crystallinity and therefore are highly resistant to solvents. Illustrative of such resins are the poly(alkylene dicarboxylates), especially the poly(alkylene terephthalates). However, such blends frequently undergo phase separation and delamination. They typically contain large, incompletely dispersed polyphenylene ether particles and no phase interaction between the two resin phases. Molded parts made from such blends are typically characterized by extremely low impact strength. In EP -A- 0248263, there are disclosed a large number of polyphenylene ether-polyester copolymers useful for the compatibilization of blends of polyphenylene ethers and polyesters. These copolymers are, for the most part, prepared by the reaction of functionalized polyphenylene ethers with polyesters or by the reaction of amine- or isocyanate-functionalized polyesters with polyphenylene ethers. Interest continues in the development of copolymers of this type which may be used for the compatibilization of such blends. US -A- 3 703 564 describes copolymerizing polyester and polyphenylene ether by reacting a polyester having acyl halide groups on both ends with a polyphenylene ether. US -A- 3 637 578 describes a process for obtaining a thermoset resin comprising thermosetting by application of heat a mixture of (i) a polyphenylene ether; (ii) monomers or prepolymers having carbon-to-carbon double bond unsaturation; (iii) liquid reactive polyester and (iv) free radical catalyst. A principal object of the present invention, therefore, is to provide a method for the preparation of copolymers suitable for the compatibilization of polyphenylene ether-polyester blends. In one of its aspects, the present invention is directed to a method for preparing polyphenylene ether-polyester copolymers, which comprises heating, in solution or in the melt, at a temperature in the range of 180-350°C in the absence of both a free radical catalyst and a polymerizable unsaturated monomer containing carbon-to-carbon double bond, at least one polyphenylene ether with at least one polyester containing olefinic structural units and being free from terminal acyl halide groups, the weight ratio of polyester to polyphenylene ether being 0.5-3.0:1. The polyphenylene ethers (also known as polyphenylene oxides) used in the method of this invention are a well known class of polymers. They are widely used in industry, especially as engineering plastics in applications requiring toughness and heat resistance. Since their discovery, they have given rise to numerous variations and modifications all of which are applicable to the present invention, including but not limited to those described hereinafter. The polyphenylene ethers comprise a plurality of structural units having the formula In each of said units independently, each Q¹ is independently halogen, primary or secondary lower alkyl (i.e., alkyl containing up to 7 carbon atoms), phenyl, haloalkyl, aminoalkyl, hydrocarbonoxy, or halohydrocarbonoxy wherein at least two carbon atoms separate the halogen and oxygen atoms; and each Q² is independently hydrogen, halogen, primary or secondary lower alkyl, phenyl, haloalkyl, hydrocarbonoxy or halohydrocarbonoxy as defined for Q¹. Examples of suitable primary lower alkyl groups are methyl, ethyl, n-propyl, n-butyl, isobutyl, n-amyl, isoamyl, 2-methylbutyl, n-hexyl, 2,3-dimethylbutyl, 2-, 3- or 4-methylpentyl and the corresponding heptyl groups. Examples of secondary lower alkyl groups are isopropyl, sec-butyl and 3-pentyl. Preferably, any alkyl radicals are straight chain rather than branched. Most often, each Q¹ is alkyl or phenyl, especially C₁₋₄ alkyl, and each Q² is hydrogen. Suitable polyphenylene ethers are disclosed in a large number of patents. Both homopolymer and copolymer polyphenylene ethers are included. Suitable homopolymers are those containing, for example, 2,6-dimethyl-1,4-phenylene ether units. Suitable copolymers include random copolymers containing such units in combination with (for example) 2,3,6-trimethyl-1,4-phenylene ether units. Many suitable random copolymers, as well as homopolymers, are disclosed in the patent literature. Also included are polyphenylene ethers containing moieties which modify properties such as molecular weight, melt viscosity and/or impact strength. Such polymers are described in the patent literature and may be prepared by grafting onto the polyphenylene ether in known manner such vinyl monomers as acrylonitrile and vinylaromatic compounds (e.g., styrene), or such polymers as polystyrenes and elastomers. The product typically contains both grafted and ungrafted moieties. Other suitable polymers are the coupled polyphenylene ethers in which the coupling agent is reacted in known manner with the hydroxy groups of two polyphenylene ether chains to produce a higher molecular weight polymer containing the reaction product of the hydroxy groups and the coupling agent. Illustrative coupling agents are low molecular weight polycarbonates, quinones, heterocycles and formals. The polyphenylene ether generally has a number average molecular weight within the range of 3,000-40,000 and a weight average molecular weight within the range of 20,000-60,000, as determined by gel permeation chromatography. Its intrinsic viscosity is most often in the range of about 0.35-0.6 dl./g., as measured in chloroform at 25°C. The polyphenylene ethers are typically prepared by the oxidative coupling of at least one corresponding monohydroxyaromatic compound. Particularly useful and readily available monohydroxyaromatic compounds are 2,6-xylenol (wherein each Q¹ is methyl and each Q² is hydrogen), whereupon the polymer may be characterized as a poly(2,6-dimethyl-1,4-phenylene ether), and 2,3,6-trimethylphenol (wherein each Q¹ and one Q² is methyl and the other Q² is hydrogen). A variety of catalyst systems are known for the preparation of polyphenylene ethers by oxidative coupling. There is no particular limitation as to catalyst choice and any of the known catalysts can be used. For the most part, they contain at least one heavy metal compound such as a copper, manganese or cobalt compound, usually in combination with various other materials. A first class of preferred catalyst systems consists of those containing a copper compound. Such catalysts are disclosed, for example, in U.S. -A-3,306,874, 3,306,875, 3,914,266 and 4,028,341. They are usually combinations of cuprous or cupric ions, halide (i.e., chloride, bromide or iodide) ions and at least one amine. Catalyst systems containing manganese compounds constitute a second preferred class. They are generally alkaline systems in which divalent manganese is combined with such anions as halide, alkoxide or phenoxide. Most often, the manganese is present as a complex with one or more complexing and/or chelating agents such as dialkylamines, alkanolamines, alkylenediamines, o-hydroxyaromatic aldehydes, o-hydroxyazo compounds and ω-hydroxyoximes, Among the polyphenylene ethers which are useful for the purposes of this invention are those which comprise molecules having at least one of the end groups of the formulas wherein Q¹ and Q² are as previously defined; each R¹ is independently hydrogen or alkyl, with the proviso that the total number of carbon atoms in both R¹ radicals is 6 or less; and each R² is independently hydrogen or a C₁₋₆ primary alkyl radical. Preferably, each R¹ is hydrogen and each R² is alkyl, especially methyl or n-butyl. Polymers containing the aminoalkyl-substituted end groups of formula II may be obtained by incorporating an appropriate primary or secondary monoamine as one of the constituents of the oxidative coupling reaction mixture, especially when a copper- or manganese-containing catalyst is used. Such amines, especially the dialkylamines and preferably di-n-butylamine and dimethylamime, frequently become chemically bound to the polyphenylene ether, most often by replacing one or the α-hydrogen atoms on one or more Q¹ radicals. The principal site of reaction is the Q¹ radical adjacent to the hydroxy group on the terminal unit of the polymer chain. During further processing and/or blending, the aminoalkyl-substituted end groups may undergo various reactions, probably involving a quinone methide-type intermediate of the formula with numerous beneficial effects often including an increase in impact strength and compatibilization with other blend components. Reference is made to U.S -A- 4,054,553, 4,092,294, 4,477,649, 4,477,651 and 4,517,341. Polymers with 4-hydroxybiphenyl end groups of formula III are typically obtained from reaction mixtures in which a by-product diphenoquinone of the formula is present, especially in a copper-halide-secondary or tertiary amine system. In this regard, the disclosures of U.S -A- 4,477,649 is again pertinent as are those of U.S A 4,234,706 and 4,482,697. In mixtures of this type, the diphenoquinone is ultimately incorporated into the polymer in substantial proportions, largely as an end group. In many polyphenylene ethers obtained under the above-described conditions, a substantial proportion of the polymer molecules, typically constituting as much as about 90% by weight of the polymer, contain end groups having one or frequently both of formulas II and III. It should be understood, however, that other end groups may be present and that the invention in its broadest sense may not be dependent on the molecular structures of the polyphenylene ether end groups. It will be apparent to those skilled in the art from the foregoing that the polyphenylene ethers contemplated for use in the present invention include all those presently known, irrespective of variations in structural units or ancillary chemical features. As previously indicated, the polyesters useful in the method of this invention have olefinic structural units. These are capable of undergoing reaction with the polyphenylene ether under the conditions of the invention. The preferred polyesters contain structural units of the formula and of at least one of the formulas and In these formulas, each of R³ and R⁴ is a divalent aliphatic, alicyclic or aromatic radical containing 2-10 carbon atoms and each R⁵ is independently hydrogen or a C₁₋₄ primary or secondary alkyl radical, at least one R⁵ being hydrogen. Illustrative R³ and R⁴ radicals are ethylene, propylene, trimethylene, tetramethylene, hexamethylene, decamethylene, 1,4-cyclohexane-bis-methylene, olefinic derivatives of the foregoing, p-phenylene, m-phenylene and bis(4-phenylene)propane. Also included are substituted radicals wherein the substituents do not substantially affect the relevant chemical properties of the radical; illustrative substituents are alkoxy, halo and nitrile. Most often, R³ is an alkylene radical, preferably ethylene or tetramethylene, and R⁴ is m- or p-phenylene. In formula VII, each R⁵ is hydrogen or a primary or secondary C₁₋₄ alkyl radical such as methyl, ethyl, 1-propyl, 2-propyl, 1-butyl or 2-butyl. At least one R⁵ value is hydrogen. Among the alkyl radicals, methyl is preferred. Thus, the radicals of formulas VII and VIII are derived from unsaturated dicarboxylic acids such as maleic, fumaric, citraconic or itaconic acid. Maleic and fumaric acids are preferred by reason of their availability and low cost. It is also contemplated to employ elastomeric polyesters. Such polyesters are known in the art; they are exemplified by compositions in which a portion of the R³ values are soft segment radicals such as polyoxyalkylene (typically polyoxyethylene or polyoxytetramethylene) and units derived from lactones such as ε-caprolactone. Numerous elastomeric polyesters of this type are commercially available; they include those sold by DuPont under the trademark HYTREL® and by General Electric under the trademark LOMOD®. Such polyesters may be prepared by the known reaction of dihydroxy compounds with mixtures of dicarboxylic acids or of functional derivatives thereof such as anhydrides, acid chlorides or lower alkyl (especially methyl) esters. The esters are often the preferred reactants. Polyester preparation is achieved under conventional conditions known in the art. Thus, a diol may be reacted with a mixture of dicarboxylic acid derivatives such as esters. Alternatively, a polyester oligomer may be prepared from the diol and one of the acid derivatives (typically corresponding to formula VI) and an ester of the other acid derivative (typically corresponding to formula VII and/or VIII) added at a later stage in the reaction. The latter ester is preferably a hydroxyalkyl ester of the same diol used in the earlier reaction. Said esterification reactions are typically conducted in the presence of conventional catalysts such as tetraalkyl titanates. The proportion of units of formula VII and/or VIII in the polyester is not critical and may be adjusted to provide the desired properties, chiefly the amount of copolymer formation with the polyphenylene ether. Most often, 5-20% of the total number of polyester structural units have formula VII and/or VIII, with the balance having formula VI. The preparation of suitable polyesters is illustrated by the following examples. Example 1 A mixture of 353.7 grams (1.82 moles) of dimethyl terephthalate, 14.61 grams (101 mmol.) of dimethyl maleate, 280 grams (2 moles) of 1,4-butanediol, 2.6 grams of a hindered phenol stabilizer and 0.44 ml. of tetra(2-ethylhexyl) titanate was heated at 175-225°C as methanol was removed by distillation. The mixture was then heated it 240-250°C at a pressure of about (0.1 torr) for about 1 hour. The product was the desired polyester. Example 2 A mixture of 282 grams (1.96 moles) of dimethyl maleate, 320 grams (3.55 moles) of 1,4-butanediol and a catalytic amount of tetraisopropyl titanate was heated at 165°C as methanol was removed by distillation. The product was bis(4-hydroxybutyl) maleate. A mixture of 360 grams (1.85 moles) of dimethyl terephthalate, 290 grams (3.22 moles) of 1,4-butanediol, 2.47 grams of a hindered phenol stabilizer and 0.44 ml. of tetra(2-ethylhexyl) titanate was heated at 180-230°C with stirring, as methanol was removed by distillation. When methanol evolution was complete, the temperature was increased to 245°C and reduced pressure was applied for 55 minutes. There was then added, under nitrogen, 50 grams (0.19 mole) of bis(4-hydroxybutyl) maleate. Stirring was continued for about 5 minutes, after which reduced pressure was applied and stirring was continued for an additional ½ hour. The product was the desired polyester. The compositions of this invention are prepared by heating the polyphenylene ether-polyester mixture, in solution or in the melt, at a temperature within the range of 180-350°C. The reaction conditions often include extrusion, which may be conveniently effected in a screw-type or similar extruder which supplies a substantial shearing force to the composition. The weight ratio of polyester to polyphenylene ether is generally in the range of 0.5-3.0:1, most often 0.9-2.5:1. The precise nature of the reaction which takes place upon practice of the method of this invention is not known with certainty. The principal reaction is most likely a thermally initiated free radical interaction of the olefinic bonds in the polyester with the aromatic rings of the polyphenylene ether or the substituents thereon, especially the latter, to produce a product which may include moieties derived from the polyester. However, the invention is in no way dependent on theory. In general, the compositions of this invention comprise only partially copolymer, with the balance being a polyphenylene ether-polyester blend. The approximate proportion of copolymer in the composition may often be conveniently expressed as the percentage of copolymerized polyphenylene ether based on total polyester. It may be determined by extracting unreacted polyphenylene ether with a suitable solvent, typically toluene, and analyzing the insoluble residue (copolymer and residual polyester) by proton nuclear magnetic resonance. The compositions of this invention may also contain ingredients other than the copolymer, polyphenylene ether and polyester. A particularly useful other ingredient in many instances is at least one elastomeric impact modifier which is compatible with the polyphenylene ether or polyester. It is generally present in the amount of 5-25% by weight of resinous components. Suitable impact modifiers include various elastomeric copolymers, of which examples are ethylene-propylenediene polymers (EPDM's), both unfunctionalized and functionalized with (for example) sulfonate or phosphonate groups; carboxylated ethylene-propylene rubbers; copolymers (usually block or graft) of alkenylaromatic compounds such as styrene and/or epoxy compounds such as glycidyl methacrylate with polymerizable olefins or dienes, including butadiene, isoprene, chloroprene, ethylene, propylene and butylene; and core-shell elastomers containing, for example, a poly(alkyl acrylate) core attached to a polystyrene shell via an interpenetrating network. The preferred impact modifiers are block (typically diblock, triblock or radial teleblock) copolymers of alkenylaromatic compounds and olefins or dienes. Most often, at least one block is derived from styrene and at least one other block from at least one of butadiene, isoprene, ethylene and butylene. Especially preferred are the triblock copolymers with polystyrene end blocks and olefin- or diene-derived midblocks. When one of the blocks is derived from one or more dienes, it is frequently advantageous to reduce the aliphatic unsaturation therein by selective hydrogenation. The weight average molecular weights of the impact modifiers are typically in the range of 50,000-300,000. Block copolymers of this type are commercially available from Shell Chemical Company under the trademark KRATON® and include KRATON® D1101, G1650, G1651, G1652, G1657 and G1702. Other conventional ingredients which may be present include fillers, flame retardants, colorants, stabilizers, antistatic agents, mold release agents, used in conventional amounts. The presence of other resinous components is also contemplated. Those include impact modifiers compatible with the polyester, such as various graft and core-shell copolymers of such monomers as butadiene, styrene, butyl acrylate and methyl methacrylate. The presence of such copolymers frequently improves the low-temperature ductility of the blends. The invention is illustrated by the following examples. The polyphenylene ether used in each example was a poly-(2,6-dimethyl-1,4-phenylene ether) having a number average molecular weight of about 20,000, an intrinsic viscosity (IV) in chloroform at 25°C of 0.48 dl./g. and 0.084% (by weight) hydroxy groups. Example 3-5 Solutions of 1.36 grams of each of polyphenylene ether and polyester and about 0.83 gram of a hindered phenol stabilizer in 27 ml. of 1,2,4-dichlorobenzene were stirred at 200°C under nitrogen for 6 hours. Toluene, 100 ml., was then added to the hot solution and the mixture was heated under reflux for ½ hour. The copolymer-containing products were removed by centrifugation, washed with toluene, centrifuged again and dried under reduced pressure. They were analyzed as described hereinabove for percentage of copolymerized polyphenylene ether. Examples 6-7 Blends of 45 parts polyphenylene ether, 45 parts polyester, 10 parts of an impact modifier and about 0.28 part of a hindered phenol stabilizer were prepared by dry blending on a jar mill followed by extrusion in a twin screw extruder at 260°C and 80 rpm. The extrudates were quenched in water, pelletized and analyzed for percent copolymerized polyphenylene ether. The impact modifier was a commercially available triblock copolymer in which the polystyrene end blocks have weight average molecular weights of 29,000 and the ethylene/butylene midblock has a weight average molecular weight of 116,000. The relevant parameters for Examples 3-7 are given in the following table. As previously mentioned, the compositions of this invention, and polyphenylene ether-poly(alkylene dicarboxylate) blends in which they are incorporated, have high impact strength, good solvent resistance and other advantageous properties. These properties make them useful for the preparation of molded and extruded articles. The weight ratio of polyester to polyphenylene ether in the blend, as in the copolymer composition, is in the range of 0.5-3.0:1, most often 0.9-2.5:1. The proportion of copolymerized polyphenylene ether therein is capable of wide variation, essentially any quantity thereof affording some improvement in properties. For the most part, said proportion is in the range of 5-80% by weight of total resinous components.

Claims: A method for preparing a polyphenylene ether-polyester copolymer which comprises heating in solution or in the melt, at a temperature in the range of 180-350°C in the absence of both a free radical catalyst and a polymerizable unsaturated monomer containing carbon-to-carbon double bond, at least one polyphenylene ether with at least one polyester containing olefinic structural units and being free from terminal acyl halide groups, the weight ratio of polyester to polyphenylene ether being 0.5 - 3.0:1. A method according to claim 1 wherein the polyphenylene ether comprises a plurality of structural units having the formula and in each of said units independently, each Q¹ is independently halogen, primary or secondary lower alkyl, phenyl, haloalkyl, aminoalkyl, hydrocarbonoxy, or halohydrocarbonoxy wherein at least two carbon atoms separate the halogen and oxygen atoms; and each Q² is independently hydrogen, halogen, primary or secondary lower alkyl, phenyl, haloalkyl, hydrocarbonoxy or halohydrocarbonoxy as defined for Q¹. A method according to claim 2 wherein the polyester contains structural units of the formula and of at least one of the formulas and wherein each of R³ and R⁴ is a divalent aliphatic, alicyclic or aromatic radical containing 2-10 carbon atoms and each R⁵ is independently hydrogen or a C₁₋₄ primary or secondary alkyl radical, at least one R⁵ being hydrogen. A method according to claim 3 wherein the polyphenylene ether is a poly(2,6-dimethyl-1,4-phenylene ether). A method according to claim 4 wherein R³ is ethylene or tetramethylene. A method according to claim 5 wherein R⁴ is m-phenylene or p-phenylene. A method according to claim 6 wherein 5-20% of the total number of polyester structural units have one or both of formulas VII and VIII. A method according to claim 7 wherein the polyester contains structural units of formulas VI and VII. A method according to claim 8 wherein each R⁵ is hydrogen. A method according to claim 9 wherein R³ is tetramethylene and R⁴ is p-phenylene.

Inventors: SYBERT, PAUL DEAN
Applicants: GENERAL ELECTRIC COMPANY
Application year: 1987
Main classification: C08G81
IPC codes: C08G63, C08L67, C08L71, C08G81, C08G65