FUNCTIONALIZED POLYPHENYLENE ETHERS, METHOD OF PREPARATION, AND POLYPHENYLENE ETHER-POLYAMIDE COMPOSITIONS PREPARED THEREFROM

Abstract: Functionalized polyphenylene ethers are prepared by reacting a polyphenylene ether with a polymerizable olefinic compound containing a phosphorus or silicon atom or an epoxy or lactam group, preferably in the presence of a free radical initiator. They may be used in the preparation of compatible polyphenylene ether blends with such polymers as polyesters and polyamides.

Description: The present invention relates to functionalized polyphenylene ether compositions which are capable of compatibilizing blends of polyphenylene ethers with such polymers as polyamides and linear polyesters. It includes novel polyphenylene ether-polyamide compositions with desirable properties. Specifically, the present invention concerns a resinous composition comprising at least one polyphenylene ether, at least one polyamide, characterized in that 10 to 90 weight % of said polyphenylene ether comprises a functionalized polyphenylene ether prepared by reacting a polyphenylene ether with at least one of glycidyl methacrylate, glycidyl acrylate, glycidyl ethyl maleate, glycidyl ethyl fumarate and allyl glycidyl ether. Preferably 10-50 weight % of the polyphenylene ether is functionalized. The polyphenylene ethers (also known as polyphenylene oxides) used in 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 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, amino-alkyl, 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 us 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 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 others 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 amino. 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 dialkylaminos, alkanolamines, alkylenediamines, o-hydroxyaromatic aldehydes, o-hydroxyazo compounds and ω-hydroxyoximes. Among the polyphenylene others 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 R² is independently, hydrogen or alkyl, with the proviso that the total number of carbon atoms in both R² radicals is 6 or less; and each R³ is independently hydrogen or a C₁₋₆ primary alkyl radical. Preferably, each R² is hydrogen and each R³ 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 dimethylamine, frequently become chemically bound to the polyphenylene ether, most often by replacing one of 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 disclosure of U.S- A - 4,477,649 is again pertinent as are those of US-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 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. According to the present invention, the polyphenylene ether is reacted with at least one of glycidyl methacrylate, glycidyl acrylate, glycidyl ethyl maleate, glycidyl ethyl fumarate and allyl glycigyl ether. The reaction between the polyphenylene ether and the glycidyl compound is typically conducted at temperatures in the range of 100-350°C. The proportions of reagents are subject to wide variation, depending on the degree of functionalization desired; the weight ratio of glycidyl compound to polyphenylene ether is typically in the range of 0.1-1.5:1. It is frequently advantageous to employ a free radical initiator in the reaction. Typical initiators are known in the art and include such compounds as benzoyl peroxide, dicumyl peroxide, di-t-butyl peroxide, t-butyl hydroperoxide and azobisisobutyronitrile. The proportion of free radical initiator is typically in the range of 1-10% by weight, based on polyphenylene ether. The reaction may be conducted in solution in a substantially inert diluent such as toluene, xylene, chlorobenzene, o-dichlorobenzene or 1,2,4-trichlorobenzene, followed by isolation of the functionalized polyphenylene ether by conventional operations such as precipitation by a non-solvent therefor. It is also possible to conduct the reaction in the melt. Melt reactions are often conveniently carried out in an extruder or similar equipment. It is frequently found that some homopolymerization of the glycidyl compound occurs simultaneously with functionalization of the polyphenylene ether. Since the presence of homopolymer is not beneficial for the purposes of the invention, removal thereof is often advisable. It may be achieved by conventional means, typically involving precipitation of a methylene chloride complex of the polyphenylene ether as described by Factor et al. in J. Polymer Sci., Polymer Letters Ed. , 7 , 205-209 (1969). The precise chemical nature of the functionalization which takes place upon practice of this method is not known with certainty. The principal reaction may be a thermally initiated free radical interaction of the carbon-carbon double bond with the aromatic rings or the substituents thereon, especially the latter, to produce a product which may include single moieties and/or grafted side chains derived from vinyl compound. The preparation of the functionalized polyphenylene ethers used in this invention is illustrated by the following examples. The polyphenylene ether used in each example herein 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. Examples 1-3 Various glycidyl compounds, in combination with dicumyl peroxide as a free radical initiator, were added to solutions of polyphenylene ether in chlorobenzene. The solutions were heated to reflux under nitrogen, with stirring, and the crude functionalized polymers were cooled and precipitated with methanol. The products of Examples 1-3 were purified by dissolving at a level of about 5% by weight in methylene chloride, allowing the solution to stand until the methylene chloride complex had precipitated, filtering, washing with methylene chloride and drying in an oven. The relevant parameters are given in Table I. Example 4 To a solution of 12.5 grams of polyphenylene ether in 125 ml. of toluene was added under nitrogen, with stirring, 7 ml. of glycidyl methacrylate and 0.48 gram of benzoyl peroxide. The mixture was heated under reflux for 3 hours and the epoxide-functionalized polyphenylene ether was isolated as in Examples 1-3. Example 5 A mixture of 970 grams of polyphenylene ether and 30 grams of mixed glycidyl ethyl maleate and glycidyl ethyl fumarate was extruded on a twin-screw extruder at 290°C. The resulting epoxy-functionalized polyphenylene ether was purified by reprecipitation from toluene with methanol, formation of the methylene chloride complex and thermal decomposition thereof as in Examples 1-3. Example 6 A mixture of 2.2 grams of polyphenylene ether, 0.5 ml. of glycidyl methacrylate and 0.1 gram of benzoyl peroxide was heated at 320-330°C under nitrogen for 5 minutes, with gentle stirring. Upon dissolution in toluene, reprecipitation with methanol, formation and thermal decomposition of the methylene chloride complex as previously described, there was obtained the desired epoxide-functionalized polyphenylene ether. The functionalized polyphenylene ethers used in this invention are used in the preparation of the compatibilized blends of polyphenylene ethers with polyamides of this invention. In particular, said functionalized polyphenylene ethers form copolymers with the polyamides, which are be used for compatibilization of such blends. Polyamides suitable for use in said compositions may be made by any known method, including the polymerization of a monoamino-monocarboxylic acid or a lactam thereof having at least 2 carbon atoms between the amino and carboxylic acid group, of substantially equimolar proportions of a diamine which contains at least 2 carbon atoms between the amino groups and a dicarboxylic acid, or of a monoaminocarboxylic acid or a lactam thereof as defined above together with substantially equimolar proportions of a diamine and a dicarboxylic acid. (The term "substantially equimolar" proportions includes both strictly equimolar proportions and slight departures therefrom which are involved in conventional techniques for stabilizing the viscosity of the resultant polyamides.) The dicarboxylic acid may be used in the form of a functional derivative thereof, for example, an ester or acid chloride. Examples of the aforementioned monoamino-monocarboxylic acids or lactams thereof which are useful in preparing the polyamides include those compounds containing from 2 to 16 carbon atoms between the amino and carboxylic acid groups, said carbon atoms forming a ring with the -CO-NH-group in the case of a lactam. As particular examples of aminocarboxylic acids and lactams there may be mentioned ε-aminocaproic acid, butyrolactam, pivalolactam, ε-caprolactam, capryllactam, enantholactam, undecanolactam, dodecanolactam and 3- and 4-aminobenzoic acids. Diamines suitable for use in the preparation of the polyamides include the straight chain and branched chain alkyl, aryl and alkaryl diamines. Such diamines include, for example, those represented by the general formula H₂N(CH₂) n NH₂ wherein n is an integer of from 2 to 16. Illustrative diamines are trimethylenediamine, tetramethylenediamine, pentamethylenediamine, octamethylenediamine, hexamethylenediamine (which is often preferred), trimethylhexamethylenediamine, m-phenylenediamine and m-xylylenediamine. The dicarboxylic acids may be represented by the formula HOOC-Y-COOH wherein Y is a divalent aliphatic or aromatic group containing at least 2 carbon atoms. Examples of aliphatic acids are sebacic acid, octadecanedioic acid, suberic acid, glutaric acid, pimelic acid and adipic acid. Aromatic acids, such as isophthalic and terephthalic acids, are preferred. Typical examples of the polyamides or nylons, as these are often called, include, for example, polyamide-6, 66, 11, 12, 63, 64, 6/10 and 6/12 as well as polyamides from terephthalic acid and/or isophthalic acid and trimethylhexamethylenediamine; from adipic acid and m-xylylenediamines; from adipic acid, azelaic acid and 2,2-bis-(p-aminocyclohexyl)propane and from terephthalic acid and 4,4'-diaminodicyclohexylmethane. Mixtures and/or copolymers of two or more of the foregoing polyamides or prepolymers thereof, respectively, are also within the scope of the present invention. Preferred polyamides are polyamide-6, 66, 11 and 12, most preferably polyamide-66. To prepare the copolymer compositions of this invention the functionalized polyphenylene ether and polyamide are heated together in solution or in the melt. The reaction temperature is typically within the range of 100-350°C, preferably 150-290°C. The proportions of functionalized polyphenylene ether and polyamide are not critical and may be adjusted over a wide range to yield copolymer compositions having the desired properties. The polyphenylene ether-polyamide compositions, however, generally contain 5-75% by weight polyphenylene ether and 25-95% polyamide. In general, the copolymer compositions comprise only partially copolymer, with the balance being a polyphenylene ether-polyamide blend. The approximate proportion of copolymer in the composition may often be conveniently expressed as the percentage of copolymerized polyphenylene ether based on total polyamide. It may be determined by extracting unreacted polyphenylene ether with a suitable solvent, typically toluene or chloroform, and analyzing the insoluble residue (copolymer and residual polyamide) by proton nuclear magnetic resonance. The weight ratio of polyamide to total polyphenylene ether in the copolymer-containing blend is generally 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 10-80% by weight of total resinous components. The blends may also contain ingredients other than the copolymer, polyphenylene ether and polyamide. A particularly useful other ingredient in many instances is at least one elastomeric impact modifier which is compatible with the polyphenylene ether. It is generally present in the amount of 5-25% by weight of resinous components. Impact modifiers for polyphenylene ether-polyester or polyamide compositions are well known in the art. They are typically derived from one or more monomers selected from the group consisting of olefins, vinyl aromatic monomers, acrylic and alkylacrylic acids and their ester derivatives as well as conjugated dienes. Especially preferred impact modifiers are the rubbery high-molecular weight materials including natural and synthetic polymeric materials showing elasticity at room temperature. They include both homopolymers and copolymers, including random, block, radial block, graft and core-shell copolymers as well as combinations thereof. Polyolefins or olefin-based copolymers employable in the invention include for example poly(1-butene), poly(4-methyl-1-pentene), and propylene-ethylene copolymers. Additional olefin copolymers include copolymers of one or more α-olefins with copolymerizable monomers including, for example, acrylic acids and alkylacrylic acids as well as the ester derivatives thereof including, for example ethyleneacrylic acid, ethyl acrylate, methacrylic acid, and methyl methacrylate. Also suitable are the ionomer resins, which may be wholly or partially neutralized with metal ions. A particularly useful class of impact modifiers are those derived from the vinyl aromatic monomers. These include, for example, modified and unmodified polystyrenes, ABS type graft copolymers, AB and ABA type block and radial block copolymers and vinyl aromatic conjugated diene core-shell graft copolymers. Modified and unmodified polystyrenes include homopolystyrenes and rubber modified polystyrenes, such as butadiene rubber-modified polystyrene (otherwise referred to as high impact polystyrene or HIPS). Additional useful polystyrenes include copolymers of styrene and various monomers, including, for example, poly(styrene-acrylonitrile) (SAN), styrene-butadiene copolymers as, well as the modified alpha- and para-substituted styrene resins and any of the styrene resins disclosed in U.S - A -3,383,435. ABS types of graft copolymers are typified as comprising a rubbery polymeric backbone derived from a conjugated diene alone or in combination with a monomer copolymerizable therewith having grafted thereon at least one monomer, and preferably two, selected from the group consisting of monoalkenylarene monomers and substituted derivatives thereof as well as acrylic monomers such as acrylonitriles and acrylic and alkylacrylic acids and their esters. An especially preferred subclass of vinyl aromatic monomer-derived resins is the block copolymers comprising monoalkenyl arene (usually styrene) blocks and conjugated diene (e.g., butadiene or isoprene) blocks and represented as AB and ABA block copolymers. The conjugated diene blocks may be selectively hydrogenated. Suitable AB type block copolymers are disclosed in, for example, U.S - A - 3,078,254; 3,402,159; 3,297,793; 3,265,765 and 3,594,452 and GB-A-1,264,741. Exemplary of typical species of AB block copolymers there may be given: polystyrene-polybutadiene (SBR) polystyrene-polyisoprene and poly(alpha-methylstyrene)-polybutadiene. Such AB block copolymers are available commercially from a number of sources, including Phillips Petroleum under the trademark SOLPRENE. Additionally, ABA triblock copolymers and processes for their production as well as hydrogenation, if desired, are disclosed in U.S - A - 3,149,182; 3,231,635; 3,462,162; 3,287,333; 3,595,942; 3,694,523 and 3,842,029. Examples of triblock copolymers include: polystyrene-polybutadiene-polystyrene (SBS), polystyrene-polyisoprene-polystyrene (SIS), poly(α-methylstyrene)-polybutadiene-poly(α-methylstyrene) and poly(α-methylstyrene)-polyisoprene-poly(α-methylstyrene). Particularly preferred triblock copolymers are available commercially as CARIFLEX®, KRATON D® and KRATON G® from Shell. Another class of impact modifiers is derived from conjugated dienes. While many copolymers containing conjugated dienes have been discussed above, additional conjugated diene modifier resins include, for example, homopolymers and copolymers of one or more conjugated dienes including, for example, polybutadiene, butadiene-styrene copolymers, butadiene-glycidyl methacrylate copolymers, isoprene-isobutylene copolymers, chlorobutadiene polymers, butadiene-acrylonitrile copolymers, and polyisoprene. Ethylene-propylene-diene monomer rubbers may also be used. These EPDM's are typified as comprising predominantly ethylene units, a moderate amount of propylene units and up to about 20 mole percent of non-conjugated diene monomer units. Many such EPDM's and processes for the production thereof are disclosed in U.S - A - 2,933,480; 3,000,866; 3,407,158; 3,093,621 and 3,379,701. Other suitable impact modifiers are the core-shell type graft copolymers. In general, these have a predominantly conjugated diene rubbery core or a predominantly cross-linked acrylate rubbery core and one or more shells polymerized thereon and derived from monoalkenylarene and/or acrylic monomers alone or, preferably, in combination with other vinyl monomers. Such core-shell copolymers are widely available commercially, for example, from Rohm and Haas Company under the trade names KM-611, KM-653 and KM-330, and are described in U.S - A - 3,808,180; 4,034,013; 4,096,202; 4,180,494 and 4,292,233. Also useful are the core-shell copolymers wherein an interpenetrating network of the resins employed characterizes the interface between the core and shell. Especially preferred in this regard are the ASA type copolymers available from General Electric Company and sold as GELOY™ resin and described in U.S - A - 3,944,631. Especially for polyester blends, the core-shell elastomers containing, for example, a poly(alkyl acrylate) core attached to a polystyrene shell via an interpenetrating network are frequently useful. In addition, there may be employed the above-described polymers and copolymers having copolymerized therewith or grafted thereon monomers having functional groups and/or polar or active groups. Finally, other suitable impact modifiers include Thiokol rubber, polysulfide rubber, polyurethane rubber, polyether rubber (e.g., polypropylene oxide), epichlorohydrin rubber, ethylene-propylene rubber, thermoplastic polyester elastomers and thermoplastic etherester elastomers. 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 in the copolymer-containing blends include fillers, flame retardants, colorants, stabilizers, anti static agents, and mold release agents like, used in conventional amounts. The preparation of copolymer-containing blends is normally achieved under conditions adapted for the formation of an intimate resin blend. Such conditions often include extrusion, typically at temperatures in the range of 100-300°C and otherwise under the conditions previously described. Extrusion may be conveniently effected in a screw-type or similar extruder which applies a substantial shearing force to the composition, thereby decreasing the particle size thereof. It is sometimes found that the impact strength of the composition is increased if it is extruded more than once, thereby insuring effective blending. The preparation and properties of polyphenylene ether and polyamide blend compositions are illustrated by the following examples. Examples 7-9 Mixtures of 49 parts of polyphenylene ether including a functionalized polyphenylene ether of this invention, 41 parts of a commercially available polyamide-66 and 10 parts of an impact modifier were tumble mixed in a jar mill and extruded at temperatures in the range of 185-345°C and 200 rpm., using a twin-screw extruder. The impact modifier was a commercially available styrene-butadiene-styrene triblock copolymer with a selectively hydrogenated butadiene midblock, in which the weight average molecular weights of the end blocks and midblock are 29,000 and 116,000, respectively. The extrudates were quenched in water, pelletized and dried in a vacuum oven. They were then injection molded into notched Izod test specimens at 300°C and 77.3 kg./sq. cm. The results are listed in Table II. Functionalized PPE Example Identity % by wt. of total PPE Impact strength, joules/m. 7 Ex. 1 25 160 8 Ex. 3 12.5 85 9 Ex. 3 25 112

Claims: A resinous composition comprising at least one polyphenylene ether and at least one polyamide, characterized in that 10 to 90 weight % of said polyphenylene ether comprises a functionalized polyphenylene ether prepared by reacting a polyphenylene ether with at least one of glycidyl methacrylate, glycidyl acrylate, glycidyl ethyl maleate, glycidyl ethyl fumarate and allyl glycidyl ether. A composition according to claim 1 wherein the polyamide is nylon-6 or nylon-66 and 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 composition according to claim 2 wherein the polyphenylene ether is a poly(2,6-dimethyl-1,4-phenylene ether), and which also contains an impact modifier in the amount of 5-25% by weight of resinous components. A composition according to claim 3 wherein the impact modifying resin is a diblock copolymer of styrene and a conjugated diene or a triblock copolymer with styrene end blocks and a conjugated diene mid-block and is present in an amount up to 50 parts by weight per 100 parts of polyphenylene ether. A composition according to claim 4 wherein the diene block has been selectively hydrogenated.

Inventors: BROWN, STERLING BRUCE, MCFAY, DENNIS JOHN
Applicants: GENERAL ELECTRIC COMPANY
Application year: 1987
Main classification: C08G65
IPC codes: C08G65, C08L77, C08L71, C08L67, C08L81, C08F283, C08L75