METHOD FOR MODIFYING UNSATURATED RUBBERS AND PRODUCT OBTAINED THEREBY

Abstract: By synthesizing a polyphenylene oxide using a catalyst comprising a primary or secondary amine and/or a man­ ganese compound, the same can be grafted to an unsatu­ rated compound such as an unsaturated rubber at high yield. A process for so modifying an unsaturated compound such as an unsaturated rubber and the product obtained thereby are disclosed.

Description: METHOD FOR MODIFYING UNSATURATED RUBBERS AND PRODUCT OBTAINED THEREBY ABSTRACT By synthesizing a polyphenylene oxide using a catalyst comprising a primary or secondary amine and/or a manganese compound, the same can be grafted to an unsaturated compound such as an unsaturated rubber at high yield. A process for so modifying an unsaturated compound such as an unsaturated rubber and the product obtained thereby are disclosed. BACKGROUND OF THE INVENTION The present invention relates to a process for modify. ing unsaturated compounds such as unsaturated rubbers by grafting a polypbenylene oxide thereon, the polyphenylene oxide having been synthesized using a catalyst comprising a primary or secondary amine and/or a manganese compound, and products obtained by saie process. DESCRIPTION or THE PRIOR ART .- Self-condensation reactions of certain phenols employ- ing oxygen in combination with an effective oxidative coupling catalyst system to form monofunctional polyphenylene oxides are well known in the prior art, such polyphenylene oxides typically having an average hydroxyl group per molecule of 1.0 or less. See, e.g., D.S. Patents 3,306,875; 3,914,266; and 4,028,341 Hay and U.S. Patents 3,956,442; 3,965,069;-3,972,851 and 4,054,553 Olander. In more detail, U.S. Patent 3,306,874 Ray discloses the preparation of self-condensation products of aromatic compounds containing a hydroxy group directly bonded to an aromatic nucleus which comprises reacting such compounds with oxygen in the presence of a dissolved oxygen-carry mg intermediate comprising an aliphatic amine-basic cupric salt complex where the amine has at least one hydrogen on the amine nitrogen and products formed thereby. Per the teaching of this patent, however, "the amine does not become an integral part of the reaction product", though recent analyses have shown secondary amines in the catalyst are chemically bound to the polyphenylene oxide, approximately one amino group per polyphenylene oxide molecule. U.S. Patents 3,929,930 and 3,929,931 Izawa et al disclose grafting polystyrene onto an oligophenylene ether using a radical initiator such as an organic peroxide. Since the grafting disclosed in these two patents results from a chemical treatment of a polyphenylene oxide with a peroxide, presumably the peroxide reacts with the polyphenylene oxide to form a reactive site to which styrene can be grafted. Per the present invention, of course, a different functional group in the polyphenylene oxide is used which is present from the time the polyphenylene oxide is mags, whereupon grafting to rubber (not styrene monomer) at high temperature can be effected. U.S. Patent 4,054,553 Olander discloses forming selfcondensation products of a phenol under polymer forming reaction conditions to yield a polyphenylene oxide using a mixed manganese chelate complex in the presence of a secondary amine. U.S. Patent 4,129,555 white discloses a process of forming self-condensation products of an aminophenol and another phenol under polymer forming reaction conditions which comprises contacting an aminophenol and another phenol with oxygen in the presence of an effective oxidative coupling catalyst system. SUMMARY OF THE INVENTION It has been discovered that certain polyphenylene oxides can be grafted to unsaturated compounds such as unsaturated rubbers when heated in the molten state if the polyphenylene oxides have been synthesized with a catalyst comprising a primary or secondary amine and/or manganese. DESCRIPTION OF TRE PREPERRED EMBODIMENTS According to the present invention there is disclosed a graft copolymer of polyphenylene oxide and an unsaturated compound produced by a process which comprises heating said polyphenylene oxide and said unsaturated compound under a pressure and at a temperature for a time sufficient to graft the same, wherein said polyphenylene oxide initially contains a primary or secondary amine and/or other functional group imparted by a manganese compound bonded thereto, said amine and/or manganese compound being a component of the catalyst used to form said polyphenylene oxide. Also disclosed is a process for producing a polyphenylene oxide unsaturated compound graft copolymer which comprises heating said polyphenylene oxide and said unsaturated compound at a temperature and pressure for a tine sufficient to form said graft copolymer, said polyphenylene oxide initially containing a primary or secondary amine and/ or other functional group imparted by a manganese compound and chemically bound thereto, said amine and/or manganese compound being a component of the catalyst used to form said polyphenylene oxide. In general, it is to be noted that the interaction of polyphenylene oxide with an unsaturated compound as per the present invention differs in several respects from the prior art. Firstly, chemically bound amine (up to one per molecule) or an equivalently reactive moiety, possibly an aryloxy, methoxy or hydroxy group is required for the reaction (possibly generation of a quinone sethide intermediate) Secondly, unsaturated groups in the unsaturated compound, or, to a lesser extent, aryl groups, are required. Thirdly, low concentrations of polyphenylene oxide in the unsaturated compound give more grafting of polyphenylene oxide to unsaturated compound than high concentrations. Polyphenylene oxides useful in the present invention include those of the type disclosed in U.S. Patent 3,306,874 Bay, U,S. Patent 4,054,553 Olander and U.S. Patent 4,129,555 White, all hereby incorporated by reference. It will be appreciated by one skilled in the art, of course, that per the present invention a catalyst comprising a primary or secondary amine and/or manganese is utilized to form such polyphenylene oxide and said amine and/or manganese is present as an integral part of the resulting polyphenylene oxide Accordingly, the immediate following discussion of exemplary polyphenylene oxides useful in the grafting procedure of the present invention is merely in the context of the polyphenylene oxide structure which is formed, with later discussion being directed to incorporation of the primary or secondary amine and/or manganese. Thus, using starting materials as described in U.S. Patent 3,306,874 Hay, polyphenylene oxides having a molecular structure represented by the formula: EMI5.1 can be used with success herein wherein Q is a monovalent substitutent selected from the group consisting of hydrocarbon radicals free of a tertiary a-carbon, hydrocarbonoxy radicals free of a tertiary carbon atom, haloaryl radicals wherein all halogens are substituted on aromatic carbon atoms, and haloaryloxy radicals wherein all halogens are substituted on aromatic carbon atoms, Q' is the sane as Q and in addition halogen, and 0. is the same as O and in addition hydrogen and halogen, with the proviso that X lust be halogen when 9 and Q' are each a member of the group consisting of aryl radicals, haloaryl radicals, hydrocarbonoxy radicals and haloaryloxy radicals, both 0 and 0' cannot be aryl at the same time, and n is an integer of indeterminate value since the resinous products are mixtures of different chain links and the ordinary means of determining molecular weights give an average value. For those materials of low molecular weight, n is an average of 10 to 15 while for the high molecular weight resins having film and fiber forming properties it is 100 to 1,500 or greater. In a similar fashion, following the teaching of U.S. Patent 4,054,553 Olander, by the reaction of oxygen with a phenol having the structural formula: EMI6.1 where X is a substituent selected from the group consisting of hydrogen, chlorine, bromine, and iodine; R' is a monovalent substituent selected from the group consisting of hydrocarbon radicals, halohydrocaibon radicals having at least two carbon atoms between the halogen atoms and -a phenol nucleus, hydrocarbonoxy radicals, and halohydrocarbonoxy radicals having at least two carbon atoms between the halogen atoms and a phenol nucleus, R" and R''' being the same as R' and, in addition. halogen, one obtains the corresponding polyphenylene oxides. Finally, with reference to U.S. Patent 4,129,555 White, involving the reaction of an alinophenol and another phenol, aminophenols of the formula below can be reacted with an Wanother phenol" of the formula below to prepare the corresponding polyphenylene oxides. Aminophenol reactants include those of the following formula EMI7.1 wherein X is hydrogen, chlorine, bromine, or iodine, R' is hydrogen, a hydrocarbon radical, a halohydrocarbon radical having at least 2 carbon atoms between the halogen atoms and a phenol nucleus, a hydrocarbonoxy radical1 or a halohydrocarbonoxy radical having at least two carbon atoms between the halogen atoms and a phenol nucleus, R" being the same as R' and, in addition, halogen, R being ethylene or a substituted methylene hydrocarbon group, including saturated and unsaturated, branched and unbrtnched. ' acyclic and cyclic, aromatic and aliphatic hydrocarbon groups, Rb and Rc being acyclic or cyclic -- including combinations of Rb and Rc to form a cyclic ring structure(s) -- saturated or unsaturated hydrocarbon groups, subject to the proviso that Rb and Rc either alone or in combination do not constitute an aromatic ring structure having an aromatic ring carbon atom directly bonded to the nitrogen atoi of the amino group and further subject to the proviso that at least one of Rb and. Rc is a hydrocarbon group. Preferably Ra is a divalent alkylene radical. Rb is hydrogen or a primary or secondary alkyl radical. and Rc is a primary or secondary alkyl radical. In a presently preferred embodiient Ra is methylene and Rb and Rc are C15 primary or secondary alkyl radicals. Generally illustratively, the Ra group can be methylene, ethylidene, isopropylidene. cyclopentylidene, beazylidene. 2,4-cyclohexadien-lyidene. etc., and the Rb and Rc group(s) or combinations thereof are aethyl, ethyl, normal propyl, isopropyl, secondary butyl, tertiary butyl, normal hexyl. cyclohexyl, dodecyl, eicosyl, triacontyl, etc. The "another phenol N can be any of the phenols eseployed in any of the prior art process for the preparation of polyphenylene oxides. Among the phenols of the prior art defined herein as "another phenol" are those of the following structural formula: EMI8.1 wherein X, R' and R'' are the sane as defined bereinbefore vith respect to the azinophenol, R"' being the sane as R' and in addition, a halogen. The unsaturated cospound(s) onto which the polyphenyl- ene oxide(s) of the present invention is grafted is not particularly limited so long as the unsaturated compounds(s) contains double bonds, i.e., saturated compounds are not useful in the present invention The number of double bonds present per repeating unit in the unsaturated compound used herein is not particularly limited, but it is generally preferred that there be at least an average of about 0.1 unsaturated bond per repeating unit, and it is most preferred that there be an average of at least 0.3 unsaturated bonds per repeating unit. As one skilled in the art will appreciate, the maximum number of unsaturated bonds per repeating unit is not limited in any fashion, but typically most commercially available unsaturated compounds contain no more than about one unsaturated bond per repeating unit. Examples of useful unsaturated compounds include unsaturated rubbers such as natural rubber (which is of the polyisoprene type). polyisoprene rubbers. polybutadiene rubbers and styrene butadiene rubbers Other useful unsaturated compounds include those which are not unsaturated rubbers but which can be grafted to polyphenylene oxide because of their unsaturation, e.g., poly-trans -1. 4-butadiene, polyacetylenes such as polyphenyl acetylenes, and the like. Polystyrene with pendent vinyl groups may also be used. Polystyrene itself has aryl rings that could be considered unsaturated; however, since they are aromatic they are less reactive. Thus. while polystyrene may also be used instead of the above unsaturated compounds or in combination thereyith, with polystyrene the amount of grafting noted is generally less than with the recited unsaturated rubbers and such is not preferred in the present invention The unsaturated compounds used per the present invention are formed in a conventional fashion as will be apparent to one skilled in the art, i.e.. no special sodifi- cation of commercially available unsaturated compounds is needed for the same to be used with success in the present invention. The amount of polyphenylene oxide and unsaturated compounds can be relatively freely varied, noting that if polyphenylene oxide is present in relatively low amounts the proportion of polyphenylene oxide grafted onto the unsaturated compound will be greater than if the polyphenylene oxide is present in larger amounts. While not meant to be limitative, generally I prefer to use from about 5 to about 80 parts by weight of polyphenylene oxide and about 20 to about 95 parts by weight of unsaturated compound, more preferably from 10 to 50 parts of polyphenylene oxide to 50 to 90 parts of unsaturated compound. At present, it does not appear that there is any particular special limit on the molecular weight of the polyphenylene oxide used with success in the present invention The most important criterion that a polyphenylene oxide must exhibit is to have sufficient reaction during the polymeri- zation, i.c., exhibit a sufficiently high molecular weight to have incorporated one amine group per polyphenylene oxide molecule. However. generally I prefer to use polyphenylene oxides having a relatively high molecular weight, for examples1 on the order of about 5,000 to about 50,000 (number average molecular weight). more preferably from 10,000 to 30.000 (number average molecular weight). In a similar fashion, the molecular weight of the unsaturated compounds(s) onto which the polyphenylene oxide of the present invention is grafted is not overtly important. However, I believe that better results will be obtained using unsaturated compounds(s), especially rubbers, having number average molecular weights from 5,000 to 1,000,000. As will be apparent to one skilled in the art, it is possible to use one or more unsaturated compounds, most especially one or more unsaturated rubbers, in combination with one or more polyphenylene oxides. As indicated, the polyphenylene oxide used per the present invention can be prepared according to the disclosures of the above-indicated patents to Hay, Olander and White, and reference should be made to these patents for a detailed discussion of starting materials, catalysts used, reaction systems used, reaction conditions and the like. It is mandatory, per the present invention, that the polyphenylene oxide used herein be prepared using a catalyst prising a primary or secondary amine and/or a manganese compound. Said amine and/or functional groups imparted by said manganese compound must be retained as an integral portion of the resulting polyphenylene oxide prior to grafting onto the unsaturated compound. A polyphenylene oxide prepared in a similar fashion without using said amine and/or said manganese compound will not undergo extensive grafting as per the present invention . In this regard, the presence of said amine provides improved grafting as compared to the situation where said amine is omitted, i.e., where only the manganese compound is present. Por example, if a polyphenylene oxide is prepared using a copper catalyst, the catalyst should comprise a primary or secondary anine as in this instance the copper catalyst alone will not produce the active site to provide the preferred grafting degree desired herein, On the other hand, polyphenylene oxides prepared with a manganese chloride-benzoin oxime catalyst will graft to some extent even if said amine is omitted, but will also show improved grafting if said amine is present during the formation of the polyphenylene oxide. It appears that a certain amount of reactive sites similar to those formed with said amine are also formed using a manganese chloride-benzoin oxime catalyst. Given the improved grafting results obtained using said amine as a catalyst component, it is thus most preferred to use a primary or secondary amine/manganese containing catalyst, since in this instance both the amine and manganese will contribute to the grafting effect. Since primary or secondary amines as a catalyst component are preferred, hereafter the following discussion will largely be with reference to such amine containing catalyst systems. Generally, the catalysts of the present invention will comprise a primary catalyst component and an amine component. The primary catalyst component utilized is not especially limited and includes those disclosed in U.S. Patent 3,306,874 Hay, U.S. Patent 4,054,553 Olander, U.S. Patent 4.129,555 White and U.S. Patent 3,639,656 Bennett et LI. Thus, exemplary of such primary catalysts are the copper salt based catalysts disclosed in the above Bay patent and the manganese (II) oxide chelate catalyst disclosed in the above Olander patent. both incorporated herein by reference. The amounts of primary catalyst used herein are as defined in the above patents to Bay, Olander, White and Bennett et al. The amount of primary or secondary amine can be freely varied so long as sufficient amine is present in the polyphenylene oxide and bound chemically thereto to provide the desired nmher of reactive sites. Usually one or more amines is/are used in an amount of at least about 0.002 mole per mole of monomer present in the reaction system, more preferably in an amount of 0.005 mole to 0.02 mole per mole of monomer present in the reaction system. Lot is most preferred that the amine be present in the catalyst system used to form the polyphenylene oxide so as to provide at least one amine group bound chemically per one polyphenylene oxide molecule. There does not appear, at present to be any particular critical limitations on the identity of the amine utilized. However, it is mandatory, as earlier indicated, that the amine be present in the reaction mixture used to form the polyphenylene oxide per the present invention and the amine be chemically bound to the polyphenylene oxide prior to grafting per the present invention During the grafting procedure, of course, the amine is stripped from tho polyphenylene oxide to provide a reactive site which will react with the unsaturated compound and provide the desired graft copolymer. Certain background factors should be kept in mind in selecting the amine, however. Firstly, extremely bulky amines may be difficult to incorporate in the polyphenylene oxide due to steric hinderance. For example, N,N-di(t-butyl) amine is difficult to incorporate in large quantities into the polyphenylene oxid Additionally, aromatic amines are quite often easily oxidized during formation of the polyphenylene oxide, and generally these will not be preferred for use in the present invention unless critical control of reaction parameters can be exercised. Balancing all of the above factors, a highly preferred class of amines for use in the present invention are those represented by the formula: R-NH-R' wherein R is linear alkyl, branched alkyl, aralkyl or heteroalkyl; R' is the same as R or hydrogen; and wherein R and R' can combine to yield cycloalkyl, cycloaralkyl or cycloheteroalkyl. Of the above amines, most preferred amines include dibenzylamine, ethylamine, dmmethylamine, methy lethylamine, butylamine, diethylamine, methyipropy lamine, propylamine, dipropylamine, ethoxylethylmethylaiine, dibutylanine. di-isopropyl amine, diqyclohexylamine, morpholine, piperazine, piperidine, etc., and a currently most preferred amine for use in the present invention is dibutylamine. Baving thus described the essential components reacted per the present invention, the following discussion deals with process conditions. Since it is most preferred to use one or more unsaturated rubbers as the unsaturated compounds per the present invention, hereafter the discussion will be in terms of such unsaturated rubbers. I believe the following discussion regarding process conditions applies with equal force tQ other unsaturated compounds and the following discussion should be so read. Process Conditions The first essential process step per the present invention is to bring the polyphenylene oxide containing the amine and the unsaturated rubber into intimate contact.. While this can be accomplished in a number of ways. typically the polyphenylene oxide and unsaturated rubber are dissolved in an appropriate solvent for both materials, for example. chloroform and benzene, followed by solvent removal. Alternatively, dry blending can be used. while the exact solvent selected will depend upon the exact polyphenylene oxide and unsaturated rubber being used, such can easily be determined by one skilled in the art. Useful solvents include, for example, aromatic solvents such as bexizene, toluene, xylene, chlorobenzene and the like, haloalkanes such as chloroform, trichlorocthane, trichloro methylene and the like, cyclic ethers such as tetrahydrofuran, dioxane and the like, compounds such as carbon disulfide, etc. The amount of polyphenylene oxide and unsaturated rubber dissolved in the solvent is not overly important, but for ease of processing usually the total amount of polyphenylene oxide and unsaturated rubber is from about 5 to about 15 parts based on 100 parts by weight of the solvent. After the dissolution is effected, the resulting intimate mixture of polyphenylene oxide and unsaturated rubber is typically co-precipitated into an appropriate solvent, such as methanol, and then washed and dried. The co-precipitation solvent is not limited to methanol, of course, and other co-precipitation solvents such as lower hydrocarbons, e.g.. pentane, hexane, heptane and the like, lower ketones such as acetone, methylcthyl- ketone and the like. alcohols such as ethanol and propanol and the like, nitroalkanes such as nitromethane, nitroethane and the like, nitriles such as acetonitrile, propionitrile and the like, water, and dilute acids can be used with success, if the solvent is miscible with water (e.g. tetrtydrOfuan One skilled in the art will easily be able to determine appropriate solvents and co-precipitation solvents for any particular polyphenylene oxide/unsaturated rubber system. It is important, in the above procedure, that the polyphenylene oxide not be heated to a temperature near its glass transition temperature or higher prior to grafting per the present invention I have discovered that if the polyphenylene oxide has been heated to a temperature close to its glass transition temperature. for example, to a temperature about l0'C lower than the glass transition temperature or higher, grafting is substantially reduced. For reasons which are not entirely clear, preheating the polyphenylene oxide prior to the grafting procedure of the present invention drastically decreases the reactivity of the polyphenylene oxide; however, I believe that this is due to activating reactive sites in the polyphenylene oxide, causing the same to graft to polyphenylene oxide. It is lost preferred per the present invention to effect grafting in a mold at elevated pressure using a temperature close to or in excess of the glass transition temperature of the polyphenylene oxide. The exact pressure selected is not overly important so long as proper plastic flow results during the molding. For commercial grade products. of course, the pressure should be sufficient to ensure that bubbles and streaks are removed from the system. For example, pressures on the order of about 1,000 pcig to about 20,000 psig can be used with success, more preferably from 2,000 to 10,000 psig. In a similar fashion, temperature can be relatively freely selected so long as the secondary amine is liberated from the polyphenylene oxide to provide the desired reactive intermediate which will react with the unsaturated ruhber. Generally, temperatures along the line of about 250 C to about 350-C, more preferably 270 to 330'C, are used. Finally, the time of molding (curing) is relatively unimportant since the grafting reaction proceeds very rapidly. Usually times on the order of about 0.5 minute to about five minutes can be used with success, more preferably 1 to 2 minutes. In order that those skilled in the art may better understand my invention, the following Examples are given which are illustrative of the currently preferred best modes of practicing the invention. All parts are by weight unless otherwise stated. GENERAL PROCEDURE The polyphenylene oxide materials used were prepared following the procedure of Example 7 of U.S. Patent 4,092,294 Bennett (coppar/diamine), Example 1 of U.S. Patent 3,661,848 Cooper (coppar/dibutylamine) when hydrolytically stable catalysts were used and by Procedure A of U.S. Patent 4,129,555 White when manganese/benzoin oxime catalysts were used. In the Run using a catalyst per procedure A of U.S. 4,129,555 White, in addition to the 2,6-dimethylphcnol in the reaction mixture 1 mole percent of 3,5-dimethyl-4-(N,N-diethyl- aminomethyl)phenol was used as a cononoier. The polyphenylene oxides obtained had the number average molecular weights and contained amine unit(s) per polyphenylene oxide molecule as indicated in the following Table where DBA means dibutylamine and the diamine was a mixture of N,N'-di-tbutyl-1,1,2-ethylene diamine and dimetnylbutylanine. Table I No. Avg. No. of Polyphenylene mole. Amine Units Catalyst Oxide Wt. Per Molecule Cu/DBA U.S. Pat. 3,661,848 20,000 ca. 2.0 Cu/diXmine DBA U.S. Pat. 4,092,294 15,000 ca. 0.9 Mn/DBA U.S. Pat. 4,129,555 15,000 ca. 0.7 The unsaturated rubbers were commercially obtained. The styrene butadiene (SBR) was a random copolymer composed of 5% styrene and 95t butadiene obtained from Cellomer Associates, had a number average molecular weight of 6',000 (PS calibration) and contained one double bond per repeating butadiene unit and the syndiotactic-1,2-polybutadiene (PBD) was obtained from JSR America, was 92@ syndiotactic and had a number average molecular weight of 121,000 (PS calibration) Polystyrene (PS) was also used and was obtained from Dow Chemical Company under the tradename PS-3 StyrontHW 33000. The polystyrene was atactic and had a number average molecular weight of 45,000. Polyphenylene Oxide/Rubber Grafting The procedure used to graft the polyphenylene oxide on SBR and PBD was identical, and accordingly both are referred to merely as "rubber". Standard solutions of rubber and polyphenylene oxide were formed by dissolving 5 g of rubber in 50 ml of chloroform and 5 g of poly(2,6-dimethyl-l.4-phenylene oxide) in 50 ml of chloroform. The rubber solution was filtered to remove any rubber that was insoluble in chloroform. Desired portions of the rubber solution and the polyphenylene oxide solution were then combined to give a composition ar indicated in the Table below (for PPO and SBR) and then 10 ml of the desired composition was added to 100 ml of vigorously stirred methanol to form chopped strands of the blend. For brevity. hereafter polyphenylene oxide is often abbreviated PPO. The resulting blends were then dried at 500C to constant weight, and portions of the blends were analyzed by NMR to confirm the composition thereof. Table II t41 of Ml of Composition of Precipitated PPO Solution SBR Solution Blend (wit.%) PPO SBR 1.0 92.9 7.2 7.5 2.5 81.1 18.9 2.5 7.5 32.3 67.7 1.0 9.0 13.7 86.3 The blends were then pressed (in an amount slightly less than 1 g per sample) in a Carver press between Teflon coated aluminum sheets which were between two ferrotype plates. The blend samples were placed between preheated platens aDd allowed to come to temperature over a 30 second period. Thereafter, pressure (5,000 psig) was applied and after 2 minutes at the desired temperature (270 or 2S0'C) the sample was removed and cooled rapidly to 25 C. It is to be noted in this regard that the cooling rate is not critical as once the temperature drops below 200 C the sample rapidly cools below 2000C simply by removing the same from the press and the plates. The resulting flexible films of a thickness of 5-10 mils were then weighed and then extracted in a stirred chloroform vat at 25'C. The chloroform was replaced with fresh chloroform at intervals of 3 hours. After overnight extraction, the extracted films were dried and weighed. Control samples of re-precipitated rubber, i.e., the rubber was dissolved in chloroform and precipitated with methanol before pressing without polyphenylene oxide addition, and blends of the SBR and PBD with polyphenylene oxide were also pressed into films under identical conditions to determine the percentage of gelation in the rubber. The S@R control ss$e had been processed at 270'C for 2 minutes ar 5,000 psig contained 85@ insoluble gel and the PBD control sample which had been processed at 270 C for 2 minutes at 5,000 psig contained 81% insoluble gel. EXAMPLE I Polyphcnylene Oxide/Rubber Grafting A blend of PPO from U.S. 3,661,848 - Cooper, )Example 1; contains 2000 ppm bound nitrogen, [@] 0.51 dl/g) and SBR was prepared by adding a solution of 5.0 g PPO in 50 ml chloroform and 5.0 g SBR in chloroform (filtered to remove insoluble SBR) to a liter of methanol in a mechanical blender. The precipitate was dried in a vacuum cven at 80 C NMR analysis showed 58 + 2t PPO and 42 + 28 SBR, by weight. A portion was compression molded at 270 C (0.5 min preheat. 2 min. at 5000 psig) to produce a translucent film 0.006' thick. The film was extracted Cx- haustivelywith chloroform and then dried. From the weight of the extracted film and correcting for 15t of the SBR being soluble after heating at 270 , the galled film still contained 41t of the total PPO. The presence of PPO in the gel was confirmed by measurement of the IR spectrum and by proton NnR spectroscopy of a deuterochloroform swelled sample. Polyphenylene oxides do not form a gel when heated at 270C whereas unsaturated rubbers do. Since there was too much gel to be due to the rubber alone, some polyphenylene oxide was thus also present in the gel. For polyphenylene oxide to be in the gel, it had to be chemically bound to the rubber, i.e.. grafted. Any ungrafted polyphenylene oxide was dissolved from the gel. Thus, for example, if an unsaturated rubber is heated alone atr270C, a crosslinked gel results. On the other hand, when heating a polyphenylene oxide alone at the same temperature, while molecular weight increases, there is no gelation. Finally, when heating a polyphenylene oxide and a rubber in combination at the same temperature, a cross linked gel results having a greater weight than if rubber alone is present. The gel will contain polyphenylene oxide if the polyphenylene oxide has reactive sites. If the polyphenylene oxide does not have reactive sites, there will be no polyphenylene oxide in the gel. The quantity of polyphenylene oxide in the extracted films was determined by the weight difference of the films before and after extraction (after correcting for the soluble rubber fraction), and the presence of polyphenylene oxide in the films was also confirmed qualitatively by ZR and semiquantitatively by broadline NMR studies on deuterochloroform swollen gels. Polyphenylene Oxlde-Polsstvrtne Grafting Polyphenylene oxide (obtained per Example 1 of U.S. Patent 3,661,848 and as used above in Example 1) in an amount of 1.5 g and polystyrene in an amount of 3.5 g were dissolved in 60 ml of benzene and then precipitated by addition to 400 ;1 of vigorously stirred methanol. The resulting sample weighed 4.9 g and contained 32t (w/w) polyphenylene oxide by NMR analysis. 1.1 g of the blend was then compression molded into a film 5 - 10 mils thick as earlier described (30 second preheat at 2700C; then 270'C for 2 minutes at 5,000 psig) between Teflon coated alinum plates to obtain Sample I A second portion of the blend was cast from the benzene solution onto a flat glass surface and the solvent was allowed to evaporate to form a film 5 -10 mile thick and yield Sample II. Each Sample was dissolved in methylene chloride (ca. 25 ml/g), and, when a polyphenylene oxide-methylene chloride complex began to form, the mixture was cooled to 0-C After 24 hours the crystals formed were filtered off, washed with methylene chloride and dried. NMR analysis shoved the presence of polystyrene in the fraction from Sample I but none in the fraction from Sample II. The results are summarized in the Table below where polystyrene is abbreviated PS. Table III Polystyrene-Polyphenylene oxide Interaction Determination by Methylene Chloride Fractionation Sample Pressed Film Cast rilm (graft) (blend) Yield of dried polyphenylene oxide complex 1071 9 et Composition of dried polyphenylene oxide complex 89t PPO 1008 PPO (mole t)b 11% PS 08 PS Composition of polystyrene 99+t PS 1008 PS (soluble) fraction ca. 0.4% PPO 0% PPO a) Based on initial polyphenylene oxide content; a mechanical loss of ca. 2@ was experienced in the isolation of the complexes. b) Measured by ZR spectroscopy (at 857 cm-l for PPO and 698 cm for PS) and by NMR spectroscopy. This separation demonstrates that the polyphenylene oxide fractionated from the heated blend contained 10t (w/w) polystyrene, whereas in the unheated blend more normal behavior was exhibited, that is, no polystyrene was in the polyphenylene oxide fraction. Grafting between polyphenvlene oxide and polystyrene accounts for the retention of the polystyrene in the complex. Any low molecular weight polyphenylene oxide that was grafted to high molecular weight polystyrene produced a graft copolymer too low in polyphenylene oxide content to form an insoluble complex with methylene chloride and resulted in small amount of PPO in the soluble fraction. EXAMPLE II Following the procedure of Example I and using polyphenylene oxide, SBR and PBD as described for Example 1, polyphenylene oxide was grafted onto SBR and PPO while varying the percentage of polyphenylene oxide in the blend. The results set forth in the Table below were obtained Table IV r of Total Polyphenylene Oxide. Grafted to Gelled Rubber Type of Rubber SBR PBD Reaction Temp. 270 270 280 Time 2 min. 2 min. 2 ilin. Wit 8 PPO in Blend 93 6 - -- 81 15 -- -- 50 47 29 33 40 -- 40 45 32 76 - -- 30 -- 54 77 20 -- 80 97 Not only is the amount of grafting found to vary with temperaturs and type of rubber, but also with the ratio of PPO to rubber. The results indicate that there is a competition between an activated PPO molecule to combine either with another PPO mole- cule or with a rubber molecule. At low PPO concentrations grafting to rubber is the major process. EXAMPLE III Following the procedure of Example I, polyphenylene oxides as described below and SBR as was used in Example I were grafted as described in Example I. The results are set forth in the Table below. Samples A to G were forced as follows: Samples A and B (before heating: bound N, 2000 ppm; Ins 0.51 dl/g) per Example 1 of U.S. Patent 3,661,B48: Samples C (bound N, 811 ppm; [#] 0.61 dl/g), D (bound N, 828 ppm; Inl 0.61 dl/g) and E per Example 7 of U. S. Patent 4,092,294; Sample F (bound N, 215 ppm; [#] 0.56 dl/g) was the same as the control for procedure A of U.S. Patent 4,129,555 and Sample G (bound N, 1110 ppn; In] 0.50 dl/g) was formed per procedure A of U.S. Patent 4,129,555. For Samples C and D, the quantity of DBA was 1% by weight of the weight of the monomer. For Sample G the the quantity of co-monomer was 1 mole 8 of the total monomer. Table V Polyphenylene oxide-SBR (1:1 wXw) Reaction at 270 (2 min.) EMI25.1 <SEP> ppO <SEP> t <SEP> of <SEP> Initial <SEP> PPO <tb> Sample <SEP> PPO <SEP> Grafted <SEP> to <SEP> Galled <SEP> SBR <tb> <SEP> A <SEP> Nade <SEP> with <SEP> Cu/DBA* <SEP> catalyst <SEP> 47 <tb> <SEP> B <SEP> Same <SEP> as <SEP> A <SEP> except <SEP> preheated <SEP> to <SEP> 9 <tb> <SEP> 270e <SEP> before <SEP> blending <tb> <SEP> C <SEP> Hade <SEP> with <SEP> Culdiamine <SEP> + <SEP> DBA <tb> <SEP> catalyst; <SEP> isolated <SEP> by <tb> <SEP> methanol <SEP> ppt'n. <SEP> 31 <tb> <SEP> D <SEP> ¯Same <SEP> as <SEP> C <SEP> except <SEP> isolated <SEP> by <tb> <SEP> steam <SEP> ppt'n. <SEP> 28 <tb> <SEP> E <SEP> Same <SEP> as <SEP> C <SEP> except <SEP> without <SEP> DBA <SEP> in <tb> <SEP> the <SEP> catalyst <SEP> o <tb> <SEP> r <SEP> Made <SEP> with <SEP> MW/ben2oinoxim. <SEP> catalyst <SEP> 34 <tb> <SEP> G <SEP> Same <SEP> as <SEP> E <SEP> but <SEP> with <tb> <SEP> Ela <SEP> 53 <tb> <SEP> as <SEP> a <SEP> co-monomer <tb> *DBA r dibutylamine These data indicate that polyphenylene oxide orly grafts well with an unsaturated rubber such U SBR if the polyphenylene oxide has not been previously heated to temperatures near 270'C. While the invention has been described in detail and with reference to specific embodiments thereof, it will be apparent to one skilled in the art that various changes and modifications can be made therein without departing from the spirit and scope of the invention.

Claims: What is claimed is: CLAIMS 1 A graft copolymer of polyphenylene oxide and an unsaturated compound produced by a process which comprises heating said polyphenylene oxide and said unsetursted compound under a pressure and at a temperature for a time sufficient to graft the same, wherein said polyphenylene oxide initially conthins a primary or secondary amine and/or other functiona; group imparted by a manganese compound bonded thereto, said anine and/ or manganese compound being a component of the catalyst used to form said polyphenylene oxide. 2. The graft copolymer of Claim 1, wherein said polyphenylene oxide initially contains said amine bonded thereto. 3. The graft copolymer of Claim 1, wherein said amine has the formula R-NE-R' wherein R is linear alkyl, branched alkyl. aralkyl or heteroalkyl. R' can be the same as R and in addition H and R and R' can combine to form a cycloalkyl, cycloaralkyl or cycloheteroalkyl group. 4. The graft copolymer of Claim 1, wherein said amine is selected from the group consisting of dimethylamine, dibenzylamihc, methylethylamine, butylatine, ethylamine. etnylpropylamine, propylamine, dipropylamine. ethoxyethylamine, dibutylamine, diisopropylamine, dicyclohexylamine, morpnoline, piperazine and piperidine. 5. The graft copolymer of Claim 1, wherein the polyphenylene oxide has not been heated to a temperature greater than about 100C lower than its glass transition tepperature prior te grafting. 6. The graft copolymer of Claim 1, wherein the pressure is from about 1,000 psig to about 20,000 psig. 7. The graft copolymer of Claim 1, wherein the t mperature is about 250-C to about 350'C. 8. The graft copolymer of Claim 1, wherein the time is from about 0.5 to about 5 minutes. 9. The graft copolymer of Claim 1, wherein the unsaturated compound has an average of at least about 0.1 unsaturated bond per repeating unit 10. The graft copolymer of Claim 1, wherein the unsaturated compound has an average of at least 0.3 unsaturated bonds per repeating unit. 11. The graft copolymer of Claim 9; wherein the unsaturated compound is an unsaturated rubber. 12. The graft copolymer of Claim 11, wherein the unsaturated rubber is selected from the group consisting of natural rubber, polyisoprene rubbers, polybutadiene rubbers and styrene butadiene rubbers. 13. The graft copolymer of Claim 1, wherein about 5 to about 80 parts by weight of polyphenylene oxide is present with about 20 to about 95 parts by weight of unsaturated rubber compound. 14. The graft copolymer of Claim 1, wherein the polyphenylene oxide has a number average molecular weight of from about 5,000 to about 50.000. 15. The graft copolymer of Claim 1, wherein the unsaturated compound has a number average molecular weight of from 5,000 td 1,000,000. 16. A process for producing a polyphenylene oxide unsaturated compound graft copolymer which comprises heating said polyphenylene oxide and said unsaturated compound at a temperature and pressure for a time sufficient to form said graft copolymer, said polyphenylene oxide initially containing a primary or secondary amine and/or other functional group imparted by a manganese compound and chemically bound thereto. said amine and/or manganese compound being a component of the catalyst used to form said polyphenylene oxide. 17. The process of Claim 16, wherein said polyphenylene oxide initially contains said amine bonded thereto. 15. The process of Claim 16, wherein said amine has the formula R-NE-R' wherein R is linear alkyl. branches aLkyl, aralkyl or heteroalkyl, R' can be the same as R and in addition B and R and R' can combine to form a cycloalkyl, cycloaralkyl or cycloheteroalkyl group. 19. The process of Claim 16, wherein said amine is selected from the group consisting of ethylamine, dieethylaDlne, dib.n:ylaaine, methylethy lamine, butylamine, ethyl propylamine. propylamine, dipropylamine. ethoxyethylamine, dibutylamine, diisopropylamine, dicyclohexylamine, morpholine. piperazine and piperidine. 20. The process of Claim 16., wherein the polyphenylei oxide has not been heated to a temperature greater than about 100C lower than its glass transition temperature prior to grafting. 21. The process of Claim 16, wherein the pressure is from about 1,000 psig to about 20.000 psig. 22. The process of Claim 16, wherein the temperature is about 2500C to about 350-C 23. The process of Claim 16, wherein the time is fra about 0.5 to about 5 minutes. 24. The process of Claim 16, wherein the unsaturated compound has an average of at least about 0.1 unsaturated bond - per repeating unit. 25. The process of Claim 16, wherein the unsaturated compound has an average of at least 0.3 unsaturated bonds per repeating unit. 26. The process of Claim 24, wherein the unsaturated compound is an unsaturated rubber. 27. The process of Claim 26, wherein the unsaturated rubber is selected fros the group consisting of natural rubber, polyisoprene rubbers, polybutadiene rubbers and styrene butadiene rubbers. 28. The process of Claim 16, wherein about 5 to about 80 parts by weight of polyphenylene oxide is present with about 20 to about 95 parts by weight of unsaturated rubber compound. 29. The process of Claim 16, wherein the polyphenylene oxide has a number average molecular weight of from about 5,000 to about 50,000. 30. The process of Claim 16, wherein the unsaturated compound has a number average molecular weight of from 5,000 to 1,000,000. 31. The process of Claim 16, wherein one or more amines is/are used in an amount of at least 0.002 mol per mol of monomer used to form the polyphenylene oxide. 32. The process of Claim 16, wherein one or more amines is/are used in amount of 0.005 mol to 0.02 mol per mol of monomers used to form the polyphenylene oxide.

Inventors: WHITE, DWAIN MONTGOMERY
Applicants: GENERAL ELECTRIC COMPANY
Application year: 1983
Main classification: C08G81
IPC codes: C08G65, C08G81