THERMAL OXIDATION STABILIZER COMPOSED OF PHOSPHITE DERIVATIVES OF AN ALCOHOL AND PPE MONOMER STILL BOTTOMS, AND PPE COMPOSITIONS CONTAINING SAID PHOSPHITES

Abstract: Novel compositions comprising a mixture of two or more phosphites derived from monomer still bottoms from the orthoalkylation of phenols are made by reacting a phos­ phorous halide with the still bottom. The monomer still bottom phosphites are effective as thermal oxidative stabilizers for engineering themoplastics, such as polyphenylene ether resins.

Description: THERMAL OXIDATION STABILIZER COIPOSED OF PHOSPHITE DERIVATIVES OF AN ALCOHOL AND PPE MONOMER STILL BOTTOMS; AIND PPE COINPOSITIONS CONTAINING SAID PHOSPHITES Methods for methylating the ortho position of a phenol by the vapor phase reaction of a phenol with methanol in the presence of a catalyst are well known in the art. Procedures are described in the patent literature, for instance, U.S. Patent Nos. 3,446,856, and 3,479,410 to Hamilton, and U.S. Patent Nos. 3,873,628; 3,972,828 and 3,974,229 to Van Sorge. In general, the procedures involve heating phenolic compounds, methanol and catalyst in a reactor, condensing the vapors issuing from the reactor and separating the desired end product, e.g., 2,6-xylenol, from the other components by distillation. The reaction provides a means for converting phenol to ortho-cresol, a useful disinfectant and wood preservative, and for converting both phenol and orthocresol to 2,6-xylenol, a monomer which can be polymerized to a polyphenylene oxide, a high performance engineering thermoplastic. Methods for producing polyphenylene oxide resins from 2,6-xylenol or other substituted phenols are described in many publications, including Hay, U.S. Patent Nos. 3,306,874 and 3,306,875 and Stamatoff, U.S. Patent Nos. 3,257,357 and 3,257,358. The polyphenylene oxides (also sometimes referred to as polyphenylene ethers) are normally subjected to elevated temperatures during processing, as during extruding or injection molding, which can cause degradation, oxidation or other deterioration of the polymer. It is, therefore, not uncommon to incorporate a thermal oxidative stabilizing compound or compounds into the polymer to prevent or at least retard the tendency toward deterioration. One such stabilizer is diphenyldecylphosphite (DPDP), used alone or together with zinc compounds. Other phosphites are also knawn to stabilize. Their effectiveness is demonstrated by the decreased yellowness index of molded samples. Thus stabilizers impart color stability. The discovery has now been made that certain phosphite derivatives of monomer still bottoms from the preparation of polyphenylene ether resins (also referred to throughout this disclosure as "monomer still bottom phosphites," and also "MSBP" for the sake of brevity), are satisfactory substitutes for conventional phosphite thermal stabilizers such as DPDP. This discovery not only provides a less costly stabilizer, but also enables productive use of the monomer still bottoms generated during manufacture of polyphenylene ether resin. The invention thus includes, in addition to the novel stabilizer, polyphenylene ether resins and blends into which the stabilizer has been incorporated in effective amount. In greater detail, the phosphite deritÅatives which constitute the basis of this invention are derived from monomer still bottoms resulting from the ortho-alkylation of phenolic compounds represented by the formula: EMI4.1 where each R is a monovalent substituent selected from the group consisting of hydrogen, alkyl, e.g., Cl-Cl2 alkyl, phenyl and alkyl-substituted phenyl, e.g., C1-C12 alkyl-substituted phenyl. More specifically, ortho-alkylated products of the above compounds are formed by a process which comprises the vapor phase reaction of the compound with an alkyl alcohol, for example, a saturated aliphatic alcohol such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, tert-butyl, aryl, isoamyl, hexyl, heptyl, octyl, nonyl, decyl, lauryl, cetyl, cyclohexyl, and the like, at a temperature at least 3000C., and preferably between 400 and 5000C. In general, the process conditions are similar to those described in the aforementioned patents, but may differ chiefly in the selection of the catalyst. Particular mention is made of ortho-alkylating catalysts comprising the calcination residue of a magnesium compound,e.g., basic magnesium carbonate, and a manganese compound, e.g., manganese hydroxide. Such catalysts are made by known procedures, such as by precipitation of manganous hydroxide from aqueous media in the presence of suspended particles of the magnesium compound, followed by drying, shaping and calcining the resultant material at elevated temperatures. The catalyst can be used alone but is frequently employed together with a sllapinn aid such as methyl- cellulose or acrylic polymers or binders such as powdered graphite, as is well known to those skilled in the art. Although, as explained, the process is broadly applicable two a variety of phenolic compounds and alcohols as the starting materials, of chief interest is the ortho-methylation of phenol and ortho-cresol to form 2,6-xylenol because of the extensive use of this material as a monomer for the synthesis of the corresponding polyphenylene ethers, i.e., poly(2,6 dimethyl-l,4-phenylene ether) resin. The vapors is suing from the reactor are condensed to yield a condensate containing the desired ortho-alkylated end product which can be in major or minor proportion, one or more alkylation by-products and unreacted phenolics and/or alcohol. The condensate is then distilled to separate and take off the desired ortho-alkylated product, leaving behind a residue (monomer still bottom). With particular reference to the ortho-methylation of phenol/o-cresol,this residue can comprise any one of the following: (1) MSB from the production run less non-volatiles, i.e., the volatile fraction of MSB. A typical composition is about 85-908 of 2,4,6-trimethylphenol, about 5-10% of 2,4-xylenol and minor amounts-of other components such as 2,3,6-trimethylphenol; (2)A Further fractionation product of (1) formed by distilling off 2,4-xylenol. A typical composition is 95-98% of 2,4,6-trimethyl phenol, less than about 2% of 2,4-xylenol and a small amount of 2,3,6-mesitoll or (3) Substantially pure mesitol. This residue, or monomer still bottom, is taken and formed into the phosphite derivative stabilizer of the invention by reacting it with a phosphorous halide, e.g., phosphorus dichloride, phosphorus trichloride, phosphorous pentachloride, phosphorous bromide, etc.,and an alcohol at an elevated temperature in the range between about 180 to 2350C. The phosphite derivative which results, that is,MSBP, can be of a waxy or liquid nature, depending on the composition of the monomer still bottom from which it is derived. By way of illustration, MSB and alcohol in an approximate molar ratio of 2:1 are mixed in a suitable vessel The alcohol can be aromatic, e.g., phenol, or aliphatic, straight or branched chain, preferably having 1 to 10 carbon atoms, e.g., methanol, ethanol, propanol, butanol, pentanol, hexanol, heptanol, octanol, nonanol, decanol, isodocanol, etc. If the MSB is a solid, the mixture is heated to a sufficient temperature to melt the solid,for example, 60-700C. The phosphorous halide, e.g., liquid PC13, is then added at the same mole level as the alcohol. This should be done gradually, as, for instance, by means of a funnel. The entire addition will normally take 1-2 hours. The reaction mixture is then heated, with stirring, to a temperature of from 1800C. to 2350C. for about 3-5 hours Gaseous HCL is evolved during the course of the reaction. The phosphitization can be facilitated by carrying out the reaction in the presence of a catalyst, for example, diphenylphosphite or potassium carbonate, which is added in minor amount, preferably 0.5-5t by weight based on the weight of the phenolics content of the MSB. Preferably, the reaction is conducted under a nitrogen blanket with the pressure controlled to prevent back suction. After the reaction is completed, the mixture is allowed to cool to room temperature, e.g., 250C. Any catalyst residue is separated, as by filtration, and the remainder of the reaction mixture is stripped of hydrogen chloride and unreacted phenolics by heating gently under vacuum, preferably at 65-1500C. Care should be taken that the MSBP mixture is not also distilled off. Gas chromatographic analysis of the resultant MSBP shows the presence of a statistical mixture of phosphites, with trimesitylphosphite predominating in the case of waxy MSBP and with dimesityl phenyl phosphite predominant in the case of liquid MSBP. The exact composition of the MSBP will vary, however, depending on the composition of the monomer still bottom from which it is derived and which itself can vary widely in composition. The monomer still bottom phosphites (MBSP) are effective thermal oxidative and color stabilizers for thermoplastic resins in general and polyphenylene ether resins in particular, preferably those having the formula: The preferred polypaenylene ethers are homoand copolymers of the formula: EMI8.1 wherein Q, Q', Q" and Q"' are independently selected from the group consisting of hydrogen, hydrocarbon radicals, halohydrocarbon radicals having at least two carbon atoms between the halogen atom and the phenol nucleus, hydrocarbonoxy radicals and halohydrocarbonoxy radicals having at least two carbon atoms between the halogen atoms and the phenol nucleus, and Q', Q" and O"' in addition may be halogen with the proviso that Q and Q' are preferably free of a tertiary carbon atom; and n represents the total number of monomer residues and is an integer of at least 50. These can be prepared by any number of well known procedures, including those described in Hay, U.S. Patent Nos. 3,306,874 and 3,306,875 and Stamatoff, U.S. Patent Nos. 3,257,357 and 3,257,358. As is well known, the polyphenylene ether resins can be employed with a variety of modifying resins. This invention thus also contemplates blends of the described MSBP and polyphenylene ether resins in admixture with supplementary polymeric modifiers such as those described in Cizek, U.S. Patent No. 3,383,435 and elsewhere in the patent literature. Modifying resins include polyalkenyl aromatics such as polyphenylene homopolymers alone or combined as by admixture or copolymerization with elastomeric materials such as polybutadiene rubber or elastomeric styrene copolymers. The MSBP stabilizers can be incorporated in the blends in any desired manner, and typically by mechanical admixing with the other ingredients. In the case of waxy or semi-solid MSBP, however, it can be somewhat difficult to distribute evenly in the resin blend by dry mixing, extrusion or other compounding techniques. Preferably, therefore, the waxy or semisolid MSBP is first dissolved in a liquid additive for the blend,for example, liquid flame retardant agent, then the resultant solution is added to the blend. The stabilized blends can and often do also contain supplementary non-resinous agents customarily employed with polyphenylene ether resins to improve certain other chemical and/or physical properties. The agents include flame retardants, plasticizers, strengthening fibers, mineral fillers, pigments, dyes, abrasion resistant components, and so forth. The following examples are set forth only as an illustration of the invention, and are not intended as a limitation on the scope of the invention. Unless stated otherwise, all proportions are stated on a parts by weight basis. EXAMPLE 1 This example illustrates the preparation of a phosphite stabilizer derived from a monomer still bottom. A reaction mixture from the manufacture of 2,6-xylenol by ortho-methylation of a mixture of phenol and o-cresol before removal of 2,6-xylenol is found to have the following composition: 10% by weight of 2,6-xylenol, 15% by weight of 2,4-xylenol, 73% by weight of 2,4,6-mesitol, the balance comprising o-cresol, 2,3,6-mesitol, anisole and monomer catalyst residue. The mixture is distilled to remove the 2,6xylenol. The resultant monomer still bottom is introduced into a three-neck round bottom flask, to which is also added phenol in an amount sufficient to provide a molar ratio to the monomer still bottom of 2.1 to 1, and about 0.5% of potassium carbonate. The mixture is heated, with stirring, to 60-70 C. until the waxy solid is dissolved and a uniform liquid blend of MSB and the phenol is achieved. An amount of liquid PC13 stoichiometrically equivalent to the amount of alcohol is added gradually over a period of 1-2 hours. The mixture is then heated, with stirring, to a temperature of 2000C. for about 4 hours. The mixture is allowed to cool, then is run through a filter to separate the potassium carbonate catalyst residue. The filtrate, which constitutes the remainder of the reaction mixture, is returned to the flask and distilled under a vacuum equivalent to about 0.2 mm of mercury to remove chlorides and unreacted phenolics (head temperature 67-1500C.). The residue is a waxy solid. GC analysis shows the presence of a mixture of trimesitylphosphite, dimesityl phenyl phosphite, diphenyl mesityl phosphite and triphenyl phosphite. EXAMPLE 2 The stabilizing effect of the waxy solid produced in Example 1 is evaluated in a composition comprising 45 parts of poly(2,6-dimethyl-l,4-phenylene ether) resin (PPO, General Electric Co.), 55 parts of rubber modified high impact polystyrene (Foster;Grant's FG 834), 1.5 part of polyethylene, 0.15 part of zinc sulfide, and 0.15 part of zinc oxide. The compositions are dry blended, extruded and injection molded. For purposes of comparison, the corresponding composition is prepared in which none of the stabilizer is present. The results for the injection molded compositions are shown in the Table below. Table 1. Properties of Polyphenylene Ether Composition Containing MSBP or No Phosphite Sample No. 1 2 3 MSBP 0 0.5 1.0 Yellowness Index (Y.T.)(units) 63.3 61.1 61.5 % Change in Y.I.* 0 -3.5 -2.8 Notched Izod Impact Strength at room temp. (J/m) 218.9 224.2 226.3 % Change in Impact Strength 0 +2.4 +4.3 HDT at 3.75 Kg/cm2 (OC) 124 121 120.5 Tensile Strength (Kg/cm2) 587.8 620.1 624.3 Tensile Elongation (%) 60.5 55.7 58.6 * (% Change)=[(value with phosphite - value without phosphite) /value without phosphite ] X 1005 The phosphite stabilizer of Example 1 is evaluated in a base molding composition comprising 45 parts of PPO, 55 parts of FG 834, 1.5 parts of polyethylene, 0.15 part of zinc sulfide, 0.15 part of zinc oxide and 13 parts of isopropylated triphenyl phosphate liquid flame retardant (FMC's Kronitex-50). The composition is prepared by dissolving the MSBP in the amounts noted below in the liquid flame retardant agent (except as noted below), then blending all of the ingredients on a Henschel mixer, extruding the blend through a 28 mm twin screw Werner-Pfleiderer extruder at 260 C (vacuum vented to an equivalent of 22.86 cm. of mercury), cooling and chopping the extrudate and molding at an injection temperature of 232"C (820C mold temperature). The molded test bars have the following properties: TABLE 2 Sample No. 1 2 3 4* MSBP 0 0.5 1.0 1.0 Yellowness Index (units) 66.6 56.9 56.3 59.1 % Change in Y.I. 0 -14.6 -15.5 -11.3 Notched Izod Imp. Str. at room temp. (Jim) 213.5 256.2 266.9 240.2 % Change in Imp. Str. 0 +20 +25 +12.5 HDT at 3.75 Kg/cm2 (OC) 90.5 90 80.5 98.0 Tensile Strength (Kg/cm2 ) 539.3 555.4 531.5 558.2 Tensile Elongation (%) 46.2 63.6 46.0 49.4 * Prepared without "dissolution" treatment. EXANSLE 4 The MSBP prepared in Example 1 is compAred with diphenyl decyl phosphite in a base molding composition comprising 40 parts of PPO, 60 parts of FG 834, 8 parts of Kronitex 50 flame retardant and polyethylene, zinc oxide and zinc sulfide in the same amounts as for the previous examples. Processing conditions are as stated in Example 3. The test results are noted below in Table 3. TABLE 3. Properties of Polyphenylene Ether Resin Blends Containing MSBP or DPDP Sample 1 2 Phosphite, (0.5 phr) MSBP-1 DPDP Tensile Yield, (Kg/cm2 ) 576.5 576.5 Tensile Strength, (Kg/cm2) 548.4 548.4 Tensile Elongation, (%) 47 54 Notched Izod Impact Strength, at 230C (J/m) 245.5 245.5 Gardner Impact Strength (m.-K) 1.73 1.56 HDT at 18.56 Kg/cm2 (OC) 101.1 97.7 Channel Flow at 62.78 Kg/cm2 48.25 '47.0 Melt Viscosity (cm) 1500 sect1 , poise 1300 1400 UL-94 Flame Resistance V-1(7.8 sec) V-1(10.3 sec) 45% Gloss 62 62 Yellowness Index 52.7 48.8 Whiteness Index -33.0 -31.2 EXAMPLE 5 The MSBP of Example 1 is evaluated versus DPDP in a base molding blend having the composition described in Example 3. The results are set forth in Table 4. TABLE 4 Sample No. 1 2 3 4 5 Composition DPDP 0 0.5 0 1 0 MSBP-1 0 0 0.5 0 1 Tensile Str. (Kg/cm2) 539.3 554.0 555.4 523.1 531.5 Tensile Elong. (%) 46.2 49.7 63.6 50.9 46.0 Tensile Yield (Kg/cm2) 618.7 653.9 644.0 621.5 630.0 Izod Impact Strenqth at 230C (J/m) 213.5 234.9 256.? 213.5 266.9 HDTat 18.56 Kg/cm2 (OC) 90.7 90.4 90.2 89.2 89.2 Channel Flow at 7.31 Kg/cm2 (cm) 42.7 38.1 40.6 37.6 38.9 450 Gloss 29.2 26.0 20.9 27.1 28.1 Initial Color, Y.I. 66.6 58.1 56.9 50.5 56.3 Flame Resistance UL-94 (sec) V-0(3.7) V-0(3.0) V- 0-1 V-l V-1(10.7) (5.1) (5.9) It can be seen from the foregoing resultS that the blends containing MSBP in accordance with the invention exhibit higher impact strength, greater channel flow distance (indicating better flow), lower heat distortion temperature, comparable color improvement and tensile properties in comparison with DPDP. The patents and/or publications mentioned above are incorporated herein by reference. Other variations and modifications are possible in light of the above disclosure. For instance, copolymers such as poly (2,6-dimethyl-co- 2,3,6-trimethyl-l,4-phenylene ether) can be substituted for poly(2,6-dimethyll,4- phenylene ether) resin. Liquid MSBP can be used in place of,or in addition to,waxy or semi-solid MSBP, the specific nature of this material not being critical to successful practice of the invention. Other additive ingredients besides those exemplified can be included in the compositions,such as glass fibers or graphite whiskers for strength enhancement, dyes, pigments, plasticisers, solid flame retardants, and so forth. It should be understood, therefore, that changes may be made in the particular embodiments shown which are still within the full intended scope of the invention as defined in the appended claims.

Claims: iI.AiMS: 1. A thermal oxidative stabilizer composition which an aryl phosphite characterized in that the aryl phosphite is the phosphite derivative of a monomer still bottom from a process for selectively ortho-alkylating a phenol compound by reacting the phenolic compound with an alcohol in the presence of a catalyst. 2. A stabilizer composition according to Claim 1, characterized in that it comprises a mixture of triphenyl phosphite, dimesityl phenyl phosphite and trimesitylphosphite. 3. A stabilizer composition according to any preceding Claim, characterized in that the monomer still bottom comprises the distillation residue from the production of 2,6-xylenol by the catalyzed vapor phase reaction of phenol and ortho-cresol with methanol. 4. A stabilizer composition according to any preceding Claim, characterized in that it is prepared by reacting said monomer still bottom with a phosphorous halide in the presence of an alcohol. 5. A stabilizer composition according to Claim 4, characterized in that the monomer still bottom is reacted with the phosphorous halide in the presence of the alcohol at a temperature of 1800 to 235 C. 6. A stabilizer composition according to Claim 4 or 5 characterized in that the phosphorous halide is phosphorous trichloride. 7. A ,tabitizer csArrlposition according to any of Claims 4 to 6 characterized in that the alcohol is an aromatic alcohol or an aliphatic alcohol having from 1 to 10 carbon atoms. 8. A stabilizer composition according to any of Claims 4 to 7 characterized in that the monomer still bottoms are reacted with the phosphorous halide in the presence of a catalyst. 9. A stabilizer composition according to Claim 8, characterized in that the catalyst is potassium carbonate or diphenylphosphite. 10. A thermoplastic composition comprising a mixture of a polyphenylene ether resin and a stabilizer characterized in that the stabilizer is a composition according to any of Claims 1 to 9. 11. A composition according to Claim 10, characterized in that the polyphenylene ether resin is poly(2,6dimethyl-1,4-phenylene ether). 12. A composition according to Claim 10 or 11, characterized in that it includes a modifying resin. 13. A composition according to Claim 12, characterized in that the modifying resin is a polyalkenyl aromatic homopolymer or copolymer, alone or in admixture with rubber. 14. A composition according to Claim 13, characterized in that the polyalkenyl aromatic polymer is polystyrene or rubber modified high impact polystyrene. 15. A composition according to any of Claims 10 to 14, characterized in that it also includes a flame retardant agent. 6. A composition according to Claim 15, character- ized in that the flame retardant agent is isopropylated triphenyl phosphates.

Inventors: AXELROD, ROBERT JAY, SHU, PETER HUA-CHENG
Applicants: GENERAL ELECTRIC COMPANY
Application year: 1983
Main classification: C08K5
IPC codes: C08K5, C08L33, C08L21, C08L51, C08L71, C08L7, C07F9