FLEXIBLE THERMOPLASTIC COMPOSITIONS COMPRISING NYLON

Abstract: The invention provides novel blends and processes for producing such blends which include a polyamide, an olefinic acid copolymer or salt thereof, and a maleated ethylene/propylene rubber, wherein such novel blends may be processed by conventional extrusion and molding techniques, do not require a separate curing step or procedure in the overall production process, and which produces articles which have some physical characteristics similar to those exhibited by thermoplastic elastomers. The inventive compositions exhibit feature excellent resistance to zinc chloride solutions and are formable in a single melt blending step.

Description: FLEXIBLE THERMOPLASTIC COMPOSITIONS COMPRISING NYLON The invention is directed to polymeric compositions, particularly to thermoplastic compositions which comprise nylons, and more particularly to flexible thermoplastic compositions comprising nylon. Certain thermoplastic materials which comprise nylon 6 and which are flexible and are partially elastomeric in character are known. Such materials include polyamide/nitrile rubbers, and further include polγamides, with further constituents such as ethγiene/acrγlic acid, ethγlene/vinyl acetate copolymers and epichlorohydrin and polyureathane as well. In the production of such composition, the elastomeric or "rubber-phase" are cured through the addition of a curing agent which is added to the compositions during melt blending of the polymer composition prior to subsequent processing. Elastomeric thermoplastic polymeric materials described in European Patent Application 341 ,731 comprise a thermoplastic resin which may be a polyester, polyamide, copolyetherester, or copolyetheramide which forms less than 30 weight percent of the total composition, 50-89 weight percent of an acid containing ethylene copolymer, and 1-22 weight percent of a glycidyl containing copolymer. The compositions described therein are formable in a two- step process, wherein the thermoplastic resin is first reacted with the glycidyl containing copolymer, and the reaction product is then reacted with the acid containing ethylene copolymer. The present invention is directed to novel thermoplastic molding compositions comprising: up to 50 weight percent of a polyamide; between 1 and 49 weight percent of at least one modified ethylene copolymer comprising units of an C 3 -C 8 σ-olefin other than ethylene; between 1 and 49 weight percent of an ionomer of at least one olefinic acid copolymers having units derived from an σ-olefin of the formula RCH = CH 2 wherein R is hydrogen or an alkyl radical of 1-8 carbon atoms, and a second unit derived from an σ, ?-ethylenically unsaturated carboxylic acid and where the copolymer is between 10%-100% neutralized by a metal ion. Such novel blends may be processed by conventional extrusion and molding techniques, {particularly by a single melt blending operation, namely extrusion) do not require a separate curing step or procedure in the overall production process, and which produces articles which share certain physical characteristics similar to those exhibited by flexible thermoplastic materials. A further beneficial feature of the inventive compositions include excellent resistance to zinc chloride (ZnCI 2 ) solutions. The present invention further includes a process for producing a thermoplastic molding composition which is resistant to zinc chloride comprising solutions which is formable in a single melt blending step. Polyamides suitable for use include the long chain polymeric amides having recurring amide groups as part of the polymer backbone and preferably, have a number average molecular weight as measured by end group titration of about 10,000 to 50,000. The polyamides suitable for use herein can be produced by any conventional means known to the art. Polγamides which find use in accordance with the present invention include those which may be obtained by the polymerization of equimolar proportions of a diamine having two or more carbon atoms between the amine terminal groups including those according to the structure H 2 N(CH 2 ) n NH 2 wherein n has an integer value of 1 - 16 with a dicarboxylic acid including those having the structure HOOC-Z-COOH wherein Z is representative of a divalent aliphatic radical containing at least 2 carbon atoms, such as adipic acid, sebacic acid, octadecanedioic acid, pimelic acid, subecic acid, azelaic acid, undecanedioic acid, and glutaric acid or may be one or more aliphatic acids, or aromatic acids, such as isophtalic acid and terephthalic acid. Alternately, suitable polyamides may be those obtained by the polymerization of a monoamino carboxylic acid or an internal lactam thereof with an equimolar proportion of a diamine and a dicarboxylic acid as well as those derived by the condensation of a monoaminocarboxylic acid or an internal lactam thereof having at least two carbon atoms between the amino and the carboxylic acid groups, as well as other means. General procedures useful for the preparation of polyamides are well known to the art. Of these polyamides, preferred polyamides include polycaprolactam, which is also commonly referred to as nylon 6, and polyhexamethγiene adipamide, which is also commonly referred to as nylon 6,6, as well as mixtures of the same. Of these, polycaprolactam is most preferred. Polyamides suitable for use in the instant invention may comprise a variety of terminal functionalities, which include the terminal functionalities of: a carboxyl group as both terminal groups in the polyamide chain, a carboxyl group attached to one end of the polyamide chain, and an amide group attached to the other end of the polyamide chain, an amino group attached to both ends of the polyamide chain, and a carboxyl group attached to one end and one amino group attached to the other end of the polyamide chain. Monocarboxylic acids or dicarboxylic acids, including acetic acid, azelaic acid, or sebacic acid can be used to terminate the polyamide chain. Preferred polyamides feature an equal number of amine groups to acid groups, (also referred to as "balanced" end groups) as well as those which feature a preponderance of amine groups to acid groups. In preferred embodiments the polyamide exhibits a number average molecular weight of between about 10,000 and about 50,000; preferably between about 20,000 and 30,000. The basis for this particular order of preferences is based on observations that the mechanical properties improve rapidly with increasing numerical average molecular weight to about 20,000 and processing becomes more difficult when the number average molecular weight approaches and/or exceeds about 30,000. A further constituent used in the inventive compositions are modified elastomeric polymers, also interchangeably referred to herein and in the art as "elastomers" or "rubbery" polymers. Such useful elastomeric polymers which may be subsequently modifed include a copolymer of ethylene and an σ-olefin other than ethylene. The σ-olefin preferably is an σ-olefin selected from at least one C 3 -C 8 , and preferably is an σ-olefin selected from at least one C 3 -C β σ-olefin. Propylene is a preferred monomer selected as the C 3 -C 8 σ-olefin copolymer. Other C 3 -C β σ-olefins which find use in conjunction with the composition include 1-butene, 1-peπtene, and 1-hexene can be used in place of or in addition to propylene in the copolymers. The copolymer has an average of 2 to 10, most preferably 2 to 4 reactive moieties per copolymer molecule which is preferably grafted to the copolymer. It is believed that the greater than one reactive moiety groups on the reactive copolymer enhances the networking between the amine end groups of the polyamide and the reactive copolymer. The reactive moiety may be a carboxyl or carboxylate functionality, which can be supplied by reacting the ethylene/C 3 -C β σ- olefin copolymer with an unsaturated reactive moiety taken from the class consisting of σ,£-ethylenically saturated dicarboxylic acids having from 4 to 8 carbon atoms, or derivatives thereof; such derivatives include anhydrides of the dicarboxylic acids, or the metal salts of the acids, or the monoester of the dicarboxylic acid having from 0 to 100 percent of the carboxylic acid groups ionized by neutralization with metal basic salt and the like. Illustrative of such acids and derivatives are: maleic acid, maleic anhydride, maleic acid monoethyl ester, metal salts of maleic acid monoethyl ester, fumaric acid, fumaric acid monoethyl ester, itaconic acid, vinyl phthalic acid metal salts of fumaric acid monoethyl ester, monoesters of maleic or fumaric acid or itaconic acids wherein the alcohol is methyl, propyl, isopropyl, butyl, isobutyl, hexyl, cyclohexyl, octyl, 2-ethyl hexyl, decyl, stearyl, methoxy ethyl, ethoxy ethyl, hydroxy or ethyl. The reactive moiety can be grafted to the ethylene copolymer by any well-known grafting process. Alternatively, the reactive moiety can be copolymerized into the backbone of the ethylene co-polymer; the reactive copolymer can include or more types of reactive moieties. The preferred modifiers are the anhydrides of cyclic alipahtic acids and the most preferred modifier is maleic anhydride. The use of this modifier in conjunction with the most preferred elastomer provides a maleated ethylene/propylene copolymer which may be further characterizeds as including from 30-60 percent, more preferably 40- 45 percent by weight of the σ-olefin based on the ethylene. This copolymer also contains from 0.1 to 10 percent, most preferably 0.3 to 2.0 percent by weight of the reactive moiety. The reactive copolymer has a number average molecular weight of from 21 ,000 to 100,000, preferably 2,000 to 65,000, more preferaiby 5,000 to 35,000, and most preferably 5,000 to 20,000. Typical values of reduced solution viscosity (RSV) are from 0.5 to 3.5. A RSV of 2.8 corresponds to a number of average molecular weight of about 80,000; an RSV of 2.0 corresponds to a number average molecular weight of about 35,000; an RSV of 1.0 corresponds to a number average molecular weight of 12,000 where the measurements of the RSV is as in a 0.1 % solution in decalin at a temperature of 135 deg.C. Exemplary modified elastomers which are commercially available are included in the subsequent examples. The inventive compositions include olefinic acid copolymers having units derived from an σ-olefin of the formula RCH = CH 2 wherein R is hydrogen or a C,-C 8 alkyl radical and which further comprises a second unit which may be derived from an a,β- ethylenically unsaturated carboxylic acid. The C*,-C 8 alkyl radical is an σ-olefin which may be ethylene, propylene, butene-1, pentene-1 , hexene-1 , heptene-1 , 3-methylbutene-1 , 4-methylpentene-1 , as well as others σ-olefins. The copolymer herein described is also interchangeably referred to as the "base" copolymer as it forms the base unit of the olefinic acid copolymer and of the ionic copolymer according to the invention. The second unit of the base copolymer may include an a,β- ethylenically unsaturated carboxylic acid group preferably of between 3 to 8 carbon atoms inclusive; examples of such useful monomers include acrylic acid, methacrylic acid, ethacrylic acid, itaconic acid, maleic acid, fumaric acid, monoesters of dicarboxylic acid which by way of example includes methyl hydrogen maleate, methyl hydrogen fumarate, ethyl hydrogen fumarate and although it is not a carboxylic acid as it lacks a hydrogen attached to carboxyl groups, maleic anhydride exhibits chemical reactivity similar to that of an acid and is to be considered suitable for use. Further, the base copolymer being described need not be limited to solely a two-component copolymer but is meant to further include other copolymerizable monoethylenically unsaturated monomers which my be used in combination with the σ-olefin and the σ, ?-ethylenically unsaturated carboxylic acid group containing monomer. Particularly, terpolymers featuring these characteristics are also contemplated to be useful as the so called base copolymers and in forming both the olefinic acid copolymers as well as the ionic copolymer constituents which form part of the instant invention. The use of such a further copolymerizable monoethylenically unsaturated monomer augments the possible range of base copolymers which may be used in producing the ionic copolymer resin. By way of example, these include: ethylene/acrylic acid copolymers, ethylene/methacrylic acid copolymers, ethylene/itaconic acid copolymers, ethylene/methyl hydrogen maleate copolymers, ethylene/maleic acid copolymers, ethylene/acrylic acid/methyl methacrylate copolymers, ethylene/methacrylic acid/ethyl acrylate copolymers, ethylene/itaconic acid/methyl methacrylate copolymers, ethylene/methyl hydrogen maleate/ethyl acrylate copolymers, ethylene/methacrylic acid/vinyl acetate copolymer, ethylene/acrylic acid/vinyl alcohol copolymers, ethylene/propylene/acrylic acid copolymers, ethylene/styrene/acrylic acid copolymers, ethylene/methacrylic acid/acrylonitrile copolymers, ethylene/fumaric acid/vinyl methyl ether copolymers, ethylene/vinyl chloride/acrylic acid copolymers, ethylene/vinylidene chloride/acrylic acid copolymers/ ethylene/vinyl fluoride/methacrylic acid copolymers, and ethylene chlorotrifluoroethylene/methacrylic acid copolymers. The concentration of the second unit of the base copolymer is preferably 50 percent or less of the total of the base copolymer, and most preferably 20 percent or less. The base copolymer resins may be random copolymers or terpolymers, or copolymers or terpolymers having regularly repeating units. The preparation of the copolymers or terpolymers which comprise the base copolymers may be in accordance with any of a plurality of methods known to those skilled in the art, including the copolymerization of a mixture of the first and second components, and in the alternative, the copolymerization of a mixture of first, second and third components wherein the three components may be simultaneously combined or non-simultaneously combined. lonomers which find use in compositions according to the present invention include the metal salts of the olefinic acid copolymers described above which may be prepared by neutralizing a percentage of the acid groups of the base copolymer described previously with metal ions. As discussed before with reference to the olefinic acid copolymer, ionomers useful in the present invention need not be limited to being a two-component copolymer but is meant to further include other copolymerizable monoethylenically unsaturated monomers which my be used in combination with the σ-olefin and the σ, ?-ethylenically unsaturated carboxylic acid group containing monomer. Particularly, terpolymers featuring these characteristics are also contemplated to be useful as so called base copolymers and in forming the ionic copolymer resin useful in the instant invention and includes those which have already been described in conjunction with the olefinic acid containing copolymers. The preparation of the copolymers or terpolymers used in forming ionomers of the olefinic acid copolymer may be in accordance with any of a plurality of methods known to those skilled in the art, including the copolymerization of a mixture of the first and second components, as well as the copolymerization of a mixture of first, second and third components. The base copolymers may be subsequently neutralized to form the ionomer thereof, by contacting the base copolymer with a basic compound which contains a particular metal ion in order to obtain the desired degree of neutralization. What is to be understood by the term "neutralization" is that the acid groups of the base copolymer are reacted with the particular metal ion in order to obtain the ionomer. Useful metal ions may include those which have a valence of 1 to 3 inclusive, and particularly include those of Groups IA, IB, IIA, IIB, III A, IVA, VA, VIB, VIIB, and VIIIB of the Periodic Table of Elements. Preferred metals include: lithium, sodium, potassium, calcium, beryllium, magnesium, zinc, cadmium, strontium, aluminum, lead, chromium, molybdenum, manganese, iron, cobalt, germanium, nickel, copper, silver, mercury, tin, platinum, boron, antimony, copper manganese, zinc, lithium, calcium and lead. Most preferred is zinc. The degree of neutralization of the carboxylic acid groups of the base copolymer by the metal cations should is between 10% - 100% but is preferably at least 50%. A feature of such ionomers in the inventive compositions is that in its non-molten state the ionomer acts as if it were cross-linked, due to the ionic attraction forces, but in its molten state, and subject to the shear forces commonly encountered in fabrication devices which disrupts the ionic attraction, acts much like a linear base copolymer and feature good melt processability as a behavioral characteristic. Subsequent to a fabrication or forming step, the ionic nature of the ionomer reforms cross-links and the solidified ionomer where the composition would be allowed to solidify, the ionomer again displays cross-linked type properties. The compositions of the present inventions comprise a polyamide, an olefinic acid copolymer or ionomer thereof, and a modified elastomeric polymer wherein the relative weight percentage of the polyamide to these other constituents is a minor percentage, that is to say, less than 50% by weight of the total weight of these constituents. It has been observed that when the relative weight percentage of the polyamide is limited to less than 50% by weight, that it does not form the dominant phase in the thermoplastic composition and is believed to be simply dispersed and grafted to the other elastomeric components of the thermoplastic composition. While not being bound to any theory, it is believed that the limitation of the polyamide so to form a minor percentage of composition allows for the composition to exhibit a more flexible behavior than in compositions wherein nylon forms the dominant phase of such a composition. The composition of the invention may optionally also include one or more conventional additives which do not materially affect the physical properties of the inventive composition. Examples of such include: stabilizers, lubricants, mold release agents, flame-retarding agents, oxidation inhibitors, dyes, pigments and other coloring agents, ultraviolet light degradation inhibitors, fillers including paniculate and fibrous fillers, reinforcing agents, nucleators, plasticizers, as well as others. Typically such conventional additives are included in the mixing step and included in an extrudate. By way of example suitable fillers include inorganic fillers, including those of fibrous and granular nature, such as glass fibers, ravings, tows, spheres or other particles, as wells as mixtures thereof. Preferred inorganic fillers include glass fibers, carbon fibers, metal fibers, potassium titanate whisker, glass beads, glass flakes, wollastonite, mica, talc, clay, titanium oxide, aluminum oxide, calcium carbonate and barium sulfate. One additive which has been found to improve the compatibility between the polyamide, particularly the polyamide, with a polyolefin is the inclusion of amounts of magnesium oxide (MgO) to the inventive compositions. Small amounts of MgO to comprise 5% by weight, preferably 2% and less by weight relative to the total weight of a composition, is noted enhance the compatibiity between the a polyamide and a polyolefin within the inventive compositions. It has been further found that the inclusion of such minor amounts of magensium oxide does not significantly detract or diminish the physical properties of the composition within which it is used as compared to a like composition without the inclusion of magnesium oxide. A further advantageous constituent which acts as a useful viscosity reducing agent is elastomeric polymer of the type which is described above but which is non-modified. The use of the non- modified elastomeric polymer provides for a useful viscosity reduction to the overall composition, improving the processability of the composition particularly in conjunction with standard process machinery, especially screw type extruders, while retaining good impact and flexural properties. Such a non-modified elastomeric polymer may be included in quantities to comprise up to 50 weight percent of the overall composition. Blending or mixing of the constituents which comprise the composition may be by any effective means which will effect their uniform dispersion. All of the constituents are mixed simultaneously by a mixer, blender, kneader, roll, single screw or multiple screw extruder, or the like in order to assure a uniform blend of the constituents. The resulting molding composition may be subsequentiγ provided to a molding apparatus used for forming articles, or alternately, the molding composition may be stored for later use.. In contrast to the suggestions of the prior art, it has surprisingly been found that the inventive compositions may be successfully produced by conventional melt blending methods by combining all the constituents making up a composition and blending them in a single blending or mixing operation, as contrasted to operations wherein less than all of the constituents are first preblended in a first melt blending operation, after which the product from this first operation is subsequently combined with the remaining constituents and then melt blended in a second operation to form the final mixture. A further advantageous feature of the present invention is that compositions in accordance with the present teachings eliminate the need for curatives or curing agents in the compositions which are usually required to cross-link an elastomeric constituent which might be used in compositions forming the prior art. Typically these are combined and blended in a separate mixing or blending operation prior to subsequent processing. Further, the lack of a curing agent further removes the requirement of a curing reaction or curing step, also known to the art as a "vulcanization step" in a process for forming articles from such compositions, which might otherwise be necessary. Surprisingly, it has also been found that compositions according to the inventive teachings do not require additives or a melt blending step prior to processing; by coextruding the nylon with the maleated rubber in conjunction with the ionomer or olefinic acid copolymer that there is realized a cross-linked rubber network which is chemically bound to the nylon matrix. In such a system, the ethyiene/propylene copolymer having more than one maleic anhydride per chain is used, and as the olefinic acid or salt of the ionomer has a high carboxylate content, the cross-linking reaction may occur. Nonetheless, the extent of cross-linking is limited so that the composition can be processed like a thermoplastic elastomer using conventional techniques. EXAMPLES In the following examples of inventive compositions and comparative compositions, it is to be understood that all quantities are parts by weight; any exceptions to this convention will be particularly denoted as being otherwise. EXAMPLES 1 - 5 Compositions denoted on Table 1 were produced using the following recited constituents and generally in accordance with the production protocol outlined below. TABLE 1 Example: Nylon 6 Nylon-X Exxon #5 Surlyn 9721 G-203 EAA '+" indicates that constituents were first pre-extruded together and then reextruded with the remaining constutuents of a blend composition The "Nylon-6" used was a nylon-6 having a preponderance of amine terminal groups and which is further described as having approximately 80% to 85% amine end groups, and a formic acid viscosity (FAV) of 55-57 and a number-average molecular weight of approximately 19,500. As an alternate polyamide, "Nylon-X", a nylon-6 having a balance of terminal end groups, wherein the number of amine terminal end groups was approximately equal to the acid terminal end groups, and which is further described as having a formic acid viscosity of 70 and having a "balance" of end groups, specifically as having 50 mole percent amine end groups and 50 mole percent amine end groups is used. "EAA" is an ethylene/acrylic acid copolymer described as being 93.5% by weight of polyethylene, and 6.5% by weight of acrylic acid and commercially available under the tradename Primacor ® 3330 from the Dow Chemical Co. "Exxon #5" is an ethylene/propylene elastomer described as having a molecular weight of 56,000 and includes 0.56% grafted maleic anhydride. The constituent "Surlyn ® 9721 " is a zinc ionomer resin described as a modified ethylene copolymer having a melt flow index of 1.0 as measured in accordance with ASTM D-1238 and which is commercially available from DuPont. The constituent "G-203" is an ethylene/propylene rubber which is described as having a molecular weight of 58,000, and which further includes 0.70% grafted maleic anhydride. The compositions were formed by providing the mixed constituents, which were premixed by tumble blending, and then melt blending in a NRM single screw extruder with a length to diameter ratio (L/D) of 24/1 and equipped with a general purpose extruder screw. The NRM single screw extruder was operated under the following conditions: four melt zones 1-4 were maintained at 270 deg.C, and the die was maintained at 260 deg.C; screw rotational speed was 80-82 rpm. The extruded composition was quenched in water and pelietized. Test specimens having a standard ASTM "dumbbell" configuration were prepared on a Van Dorn molding machine set at a temperature approximately 30 deg.C above the melting point of the polyamide contained in each of the compositions. The mold temperature was maintained at 48.8 deg.C (120 deg.F). The molding cycle was 10 to 25 seconds forward ram, and 20 to 30 seconds on hold. The test specimens formed were subsequently subjected to physical testing in accordance with ASTM D-638 to evaluate tensile and elongation characteristics, ASTM D-790 to determine the flexural modulus, ASTM D-1484 testing procedures to test the Shore D hardness. The results of the physical tests associated with each of the compositions are denoted on Table 2. EXAMPLES 6-13 The following examples illustrative of certain embodiments of the invention are compositions which do include magnesium oxide. A composition was formulated to illustrate the physical properties of a composition within the scope of the invention and wherein the ratio of nylon to the polyolefin was varied within the range of approximately 55:45 to approximately 45:55; a control sample of nylon 12 was also produced. The samples of Examples 6-9 were tested for their resistance to zinc chloride solutions. The compositions included; Surlyn 9721, and Exxon #5 both of which have been previously described. Further constituents include: "Nylon 1539" a random copolymer consisting of 85 weight percent caprolactam, and 15 weight percent of hexamethylene adipamide, which is characterized as having balanced terminal end groups, and having a formic acid viscosity (FAV) of approximately 85, "Nylon 12", a homopoiymer of polylaurolactam which is characterized as having a medium viscosity extrusion grade material commonly used for extrusion of tubing and pipes. A heat stabilizer for polymeric compositions, "HSMB", comprises a nylon master batch which includes nylon 6, and further including cuprous iodide and potassium bromide in weight percents of 2.1 % and 22.5% respectively. A further constituent is magnesium oxide, MgO. To form the compositions of Examples 6-9, the constituents were first combined by dry mixing, and extruded in accordance with the procedure outlined with reference to Examples 1-5. These compositions are outlined on Table 3. TABLE 3 Example: 6 7 8 9 10 11 12 13 Test specimens in the shape of test bars having a length of 5 inches, a width of 112 inch and a thickness of were prepared on a Van Dorn molding machine set at a temperature approximately 30 deg.C above the melting point of the polyamide constituent. The Van Dorn molding machine was operated under the same conditions, and the test specimens produced were evaluated as described for Examples 1- 5 above. To evaluate the resistance of formed articles to zinc chloride solutions, and the physical properties after immersion to these solutions, the following testing protocol was used. For the tested compositions, molded test bars or extruded tubing comprising the compositions were tested. The molded bars tested were 5 inches in length, 1/2 inch in width and 1/8 inch in thickness was molded and conditioned by placing the same in a hot air circulating oven at 70 deg.C for 12 hours. The bar was then cooled to room temperature (approximately 20 deg.C) and bent into a "U" or "horseshoe" shape and immediately immersed in a vessel containing aqueous ZnCI 2 solutions. Where extruded tubing was tested, an extruded tube having an external diameter of 3/8 inch was extruded, and then conditioned at 70 deg.C. The conditioned tube was then cooled, and a #6 jacketed Romex wire was fully inserted in the tube, after which the wire and tube were bent into a "U" or "horseshoe" shape and immersed in a vessel (which as immediately sealed thereafter) containing aqueous ZnCI 2 solutions. Two different solutions were used, 50% ZnCI 2 solutions at room temperature, or alternatively, 25% ZnCI 2 solutions at 60 deg.C, both for a period of 8 days. The bars were subsequently subjected to physical testing in accordance with procedures already described, and evaluated for cracking, appearance and delamination. With regard to appearance evaluation, little or no change in the surface appearance of a test bar subsequent to soaking was denoted as "excellent"; the appearance of white spots and/or dullness on the surface was denoted as "fair". With regard to delamination, tensile bar after elongation testing which showed no delamination were rated as "none", those exhibiting minor amounts of delamination were denoted as having "little", and those which exhibited appreciable amounts of delamination were denoted as having "appr." indicative of appreciable delamination. The results of these tests is outlined on Table 4. In light of the foregoing description and the accompanying examples, it can be seen that articles formed from the compositions taught hererin exhibit good physical properties, are highly resistant to degradation in zinc chloride solutions, and feature thermoplastic behaviour uncharacteristic to common compositions comprising polyamides. TABLE 4 Example: 10 11 12 13 Flexural Stress, psi. 5600 5100 3900 4100 Flex.Str., [kPa]: [2627] [2392] [1829] [1923] Flexural Modulus, psi. 125000 110000 89000 80000 138000 126000 89 95 Flex.Mod„ [kPa]: [5.8640] [51601] [41750] [37528] [64736] [59107] [41.7] [44.5] Tensile Strength, psi. 4200 3700 3300 4500 3900 4250 3400 3600 Tensile Str., [kPa]: [1970] [1730] [1548] [2110] [1830] [1993] [1595] [1688] Tensile Elongation, % 300 340 330 310 Shore D Hardness Mold Bar Appearance fair excellent excellent excellent Delamination none appr. little little

Claims: CLAIMS 1. A thermoplastic molding composition comprising: up to 50 weight percent of a polyamide having a number average molecular weight in the range of 10,000 to 50,000; characterized by further consisting of between 1 and 49 weight percent of at least one modified ethylene copolymer comprising at least 2 reactive moieties and comprising units of an C 3 -C 8 σ-olefin other than ethylene; between 1 and 49 weight percent of an ionomer of at least one olefinic acid copolymers having units derived from an σ-olefin of the formula RCH = CH 2 wherein R is hydrogen or an alkyl radical of 1-8 carbon atoms, and a second unit derived from an σ,yt?-ethylenically unsaturated carboxylic acid and where the copolymer is between 10%-100% neutralized by a metal ion selected from Group I - Group VIIIB metals. 2. The composition according to claim 1 wherein the modified ethylene copolymer is an ethylene/propylene copolymer. 3. The compositon according claim 8 wherein the modified ethylene copolymer comprises at least 2 reactive moities selected from carboxyl or carboxylate functionalities. 4. The composition according to claim 1 wherein the ionomer is a terpolymer comprising the σ-olefin and the σ, ?-ethyleπically unsaturated carboxylic acid and a monoethylenically unsaturated monomers. 5. The composition according to claim 1 further characterized by exhibiting resistance to stress cracking when immersed in a zinc chloride solutions. 6. The composition according to any preceeding claim further characterized as including up to 5 weight percent magnesium oxide. 7. A process for producing the thermoplastic molding composition according to any preceeding claim characterized in that : the thermoplastic molding composition is produced by a process wherein the thermoplastic molding composition is formed in a single process step wherein the polyamide, are melt blended with the modified ethylene copolymer and the ionomer in a single blending operation.

Inventors: KROLLICK THOMAS JOHN, MASON CHARLES DRISCOLL, TULLER HAROLD WILLIS, KROLLICK, THOMAS, JOHN, MASON, CHARLES, DRISCOLL, TULLER, HAROLD, WILLIS
Applicants: ALLIED SIGNAL INC, ALLIED-SIGNAL INC.
Application year: 1992
Main classification: C08L77
IPC codes: C08K3, C08L23, C08L51, C08L77