Polyketone polymer compositions

Abstract: Improved compositions comprise polymer blends of (1) a linear alternating polymer of carbon monoxide and at least one ethylenically unsaturated hydrocarbon with (2) a high rubber graft copolymer, and, optionally, (3) an acidic polymer containing moieties of an α-olefin and an α,β-ethylenically unsaturated carboxylic acid. The blends demonstrate improved toughness and impact strength at both ambient and low temperatures.

Description: This invention relates to an improved polyketone polymer composition, i.e. a blend comprising a linear alternating polymer of carbon monoxide and at least one ethylenically unsaturated hydrocarbon. The class of polymers of carbon monoxide and olefins has been known for some time. More recently, the class of linear alternating polymers of carbon monoxide and at least one ethylenically unsaturated hydrocarbon, now becoming known as polyketones or polyketone polymers, has become of greater interest. U.S. patent specification 4,880,903 discloses a linear alternating polyketone terpolymer of carbon monoxide, ethylene, and other olefinically unsaturated hydrocarbons, such as propylene. Processes for production of the polyketone polymers typically involve the use of a catalyst composition formed from a compound of a Group VIII metal selected from palladium, cobalt or nickel, the anion of a strong non-hydrohalogenic acid and a bidentate ligand of phosphorus, arsenic or antimony. U.S. patent specification 4,843,144 discloses a process for preparing polymers of carbon monoxide and at least one ethylenically unsaturated hydrocarbon using the preferred catalyst comprising a compound of palladium, the anion of a non-hydrohalogenic acid having a pKa of below about 6 and a bidentate ligand of phosphorus. The resulting polymers are relatively high molecular weight materials having established utility as premium thermoplastics in the production of shaped articles such as containers for food and drink and parts for the automotive industry which are produced by processing the polyketone polymer according to well known methods. For some particular applications however, it has been found to be desirable to have properties which are somewhat different from those of the polyketone polymer. It would be of advantage to retain the more desirable properties of the polyketone polymer and yet improve other properties. It is the object of the present invention to provide a composition which has improved impact resistance, in particular when measured according to the Gardner test, rather than the Izod test, as hereinafter explained. This has been found to be possible by blending in a certain amount of a high rubber graft copolymer. The present invention provides blends of a linear alternating polymer of carbon monoxide and at least one ethylenically unsaturated hydrocarbon with certain other polymeric materials. More particularly, the invention provides blends of (1) the linear alternating polymer with (2) a high rubber graft copolymer, and, optionally, (3) an acidic polymer containing moieties of an α-olefin and an α,β-ethylenically unsaturated carboxylic acid, optionally containing a non-acidic, low molecular weight, third polymerizable monomer wherein, optionally, a portion of the carboxylic acid groups of the acidic polymer are neutralized with non-alkali metal wherein the high rubber graft copolymer is obtainable by graft polymerizing less than 50 %wt of a monomer selected from the group of vinyl nitrile monomers, vinyl nitrile monomers combined with vinyl monomers and mixtures thereof, in the presence of at least 50 %wt of the preformed rubbery substrate. The blends of the invention exhibit improved toughness and impact strength at both ambient and low temperatures. The polyketone polymers of the blends of the invention are of a linear alternating structure and contain substantially one molecule of carbon monoxide for each molecule of unsaturated hydrocarbon. Suitable ethylenically unsaturated hydrocarbons for use as precursors of the polyketone polymers have up to 20 carbon atoms inclusive, preferably up to 10 carbon atoms, and are aliphatic such as ethene and other α-olefins including propene, 1-butene, isobutene, 1-hexene, 1-octene and 1-dodecene, or are arylaliphatic containing an aryl substituent on an otherwise aliphatic molecule, particularly an aryl substituent on a carbon atom of the ethylenic unsaturation. Illustrative of this latter class of ethylenically unsaturated hydrocarbons are styrene, p-methylstyrene, p-ethylstyrene and m-isopropylstyrene. The preferred polyketone polymers are copolymers of carbon monoxide and ethene or terpolymers of carbon monoxide, ethene and a second ethylenically unsaturated hydrocarbon of at least 3 carbon atoms, particularly an α-olefin such as propene. When the preferred polyketone terpolymers are employed as the major polymeric component of the blends of the invention, there will be within the terpolymer at least 2 units incorporating a moiety of ethylene for each unit incorporating a moiety of the second hydrocarbon. Preferably, there will be from 10 units to 100 units incorporating a moiety of the second hydrocarbon. The polymer chain of the preferred polyketone polymers is therefore represented by the formula wherein G is the moiety derived from ethylenically unsaturated hydrocarbon of at least 3 carbon atoms polymerized through the ethylenic unsaturation and the ratio of y:x is no more than 0.5. When copolymers of carbon monoxide and ethene are employed in the blends of the invention, there will be no second hydrocarbon present and the copolymers are represented by the above formula wherein y is zero. When y is other than zero, i.e., terpolymers are employed, the -CO(CH 2 CH 2 ) units and the -CO(G) units are found randomly throughout the polymer chain, and preferred ratios of y:x are from 0.01 to 0.1. The end groups or "caps" of the polymer chain will depend upon what materials were present during the production of the polymer and whether or how the polymer was purified. The precise nature of the end groups does not appear to influence the properties of the polymer to any considerable extent so that the polymers are fairly represented by the formula for the polymer chain as depicted above. Of particular interest are the polyketone polymers of number average molecular weight from 1000 to 200,000, particularly those of number average molecular weight from 20,000 to 90,000 as determined by gel permeation chromatography. The physical properties of the polymer will depend in part upon the molecular weight, whether the polymer is a copolymer or a terpolymer and, in the case of terpolymers, the nature of the proportion of the second hydrocarbon present. Typical melting points for the polymers are from 175 °C to 300 °C, more typically from 210 °C to 270 °C. The polymers have a limiting viscosity number (LVN), measured in m-cresol at 60 °C in a standard capillary viscosity measuring device, from 0.5 dl/g to 10 dl/g, more frequently from 0.8 dl/g to 4 dl/g. A preferred method for the production of the polyketone polymers is illustrated by U.S. patent specification 4,843,144. The carbon monoxide and hydrocarbon monomer(s) are contacted under polymerization conditions in the presence of a catalyst composition, suitably formed from a compound of palladium, the anion of a non-hydrohalogenic acid having a pKa (measured in water at 18 °C) of below 6, preferably below 2, and a bidentate ligand of phosphorus. The second component of the compositions of the invention is a high rubber graft copolymer, that is, a (rigid) graft copolymer on a rubbery substrate. These high rubber graft copolymers are conventional graft copolymers obtainable by graft-polymerizing (less than 50 wt% of) a rigid (when polymerized) monomer selected from the group consisting of vinyl nitrile monomers, vinyl nitrile monomers combined with vinyl monomers, and, optionally, acrylic monomers, and mixtures thereof, in the presence of (at least 50 wt% of) a (pre-formed) rubbery substrate selected from 1,3-diene polymers and (rubbery) copolymers thereof. The rigid graft copolymer, more particularly, is a vinyl nitrile monomer such as acrylonitrile, or a vinyl nitrile monomer combined with a vinyl aromatic monomer such as styrene, and, optionally, an acrylic monomer such as methyl methacrylate, or mixtures thereof. Especially preferred copolymers are copolymers of styrene and acrylonitrile, and optionally, methyl methacrylate. The rigid graft copolymer suitably comprises from 10 wt% to less than 50 wt% of the high rubber graft copolymer. The rubbery substrate, more particularly, is a 1,3-diene polymer such as polybutadiene or polyisoprene, or a copolymer of a 1,3-diene with less than 50 wt% of a rigid copolymerizable monomer selected from the group consisting of vinyl or vinylidene monomers (such as styrene), vinyl nitrile monomers (such as acrylonitrile), and acrylate ester monomers (such as n-butyl acrylate). The rubbery substrate suitably comprises 50 wt% to 90 wt% of the high rubber graft copolymer. As is conventional in the preparation of high rubber graft copolymers, either or both the rubbery substrate and the graft copolymer phase may further include minor amounts, usually less than 10 wt%, of a copolymerizable difunctional or trifunctional monomer to cross-link either or both polymeric components. The use of the term rigid is somewhat inappropriate when applied to a monomer or monomer mixture. The term rigid monomer for the purposes of this invention means a polymerizable monomer which when polymerized provides a homopolymer having rigid, plastic or non-rubbery character, including a glass transition temperature greater than 20 °C. The term rubbery substrate or rubbery copolymer means, as is conventionally recognized, a polymer having a rubbery or elastomeric character including a glass transition temperature below 20 °C, and preferably below 0 °C. Although often referred to as rubbery modifiers, the high rubber graft copolymers for the most part are not truly elastomeric and do not exhibit useful elastomeric properties without further modification and vulcanization. These materials therefore are not considered to be thermoplastic elastomers. The high rubber graft copolymers may be prepared by any of the variety of conventional graft polymerization processes including emulsion, suspension, sequential, bulk and solution polymerization processes. These methods are well-known in the polymerization art. Typical of the high rubber graft copolymers useful in the practice of this invention are those generally referred to as high rubber acrylonitrile butadiene styrene (ABS) resins, which may generally be described as graft copolymers of styrene and acrylonitrile on polybutadiene or styrene-butadiene rubbers containing more than 50 wt% of rubbery substrate, which includes the similar high rubber graft copolymers such as methyl methacrylate-styrene-acrylonitrile grafts on polybutadiene or on styrene-butadiene rubbers (MABS resins), and the like. These resins are widely known and commercially available. The precise percentage of the high rubber graft copolymer to be employed in the blends of the invention is not critical. Compositions containing from 0.5 wt% up to 45 wt%, based on total blend, of the toughened blend component are satisfactory, with 15% to 30 wt% being preferred, and 20 wt% to 25 wt% being most preferred. High rubber graft copolymers of the type described in U.S. patent specification No. 4,659,766, incorporated herein by reference, are particularly useful in the subject invention. Graft copolymers of styrene and acrylonitrile, and optionally methyl methacrylate, on a diene rubber substrate containing a high rubber content, are commercially available, and are useful in the subject invention. The optional, third polymeric component of the blends of the invention, present as a minor component if present at all, is an acidic polymer containing moieties of an α-olefin and an α,β-ethylenically unsaturated carboxylic acid, optionally polymerized with a third monomer and optionally having a portion of the carboxylic acid groups neutralized with non-alkali metal. The α-olefin monomer of this optional blend component is an α-olefin of up to 10 carbon atoms inclusive such as ethene, propene, 1-butene, isobutene, 1-octene and 1-decene. Preferred α-olefins are straight chain α-olefins of up to 4 carbon atoms inclusive and most preferred is ethene. The α-olefin monomer of this optional blend component is present in at least 65 mol% based on total component and is preferably present in at least 80 mol% on the same basis. The ethylenically unsaturated carboxylic acid monomer is an α,β-ethylenically unsaturated carboxylic acid of up to 10 carbon atoms inclusive and is illustrated by acrylic acid, 2-hexenoic acid and 2-octenoic acid. The preferred α,β-ethylenically unsaturated carboxylic acids have up to 4 carbon atoms inclusive. These acids are acrylic acid, methacrylic acid and crotonic acid, of which acrylic acid and methacrylic acid are particularly preferred. The unsaturated acid monomer of the optional third polymeric blend component is present in an amount from 1 wt% to 35 wt% based on total blend component, but amounts from 5 mol% to 20 mol% on the same basis are preferred. The acidic polymeric optional blend component is suitably a copolymer of the α-olefin and the unsaturated carboxylic acid and in general such copolymers are preferred. On occasion, however, it is useful to incorporate as an optional third monomer a non-acidic, low molecular weight polymerizable monomer of up to 8 carbon atoms inclusive. Such optional monomer may be another α-olefin such as propene or styrene when the major α-olefin monomer is ethene, an unsaturated ester such as vinyl acetate, methyl acrylate or ethyl methacrylate, an unsaturated halohydrocarbon such as vinyl fluoride or vinyl chloride, or an unsaturated nitrile such as acrylonitrile. Amounts of the third monomer up to about 5 mol%, based on total optional blend component polymer are satisfactory with amounts up to about 3 mol% on the same basis being preferred. Independent of whether the polymer of the optional third blend component is a copolymer or a terpolymer, in an optional embodiment of the third polymeric blend component a portion of the carboxylic acid groups is neutralized with non-alkali metal. When partially neutralized, this optional blend component is polymeric in form while exhibiting ionic character and is conventionally referred to as a metal ionomer. In the partially neutralized embodiment of the optional polymeric blend component the α-olefin/unsaturated carboxylic acid polymer, with or without the optional third monomer, is reacted with a source of ionizable zinc, aluminium or magnesium compound sufficient to neutralize from 10% to 90%, preferably from 20% to 80%, of the carboxylic acid groups present in the polymer. Such neutralization, particularly with zinc, the preferred metal, results in a uniform distribution of metal throughout the polymer. The ionizable metal compound utilized in the neutralization is a source of complexed or uncomplexed non-alkali metal ions including zinc, aluminium or magnesium ions which are provided in compounds of the type known as metal salts, e.g., uncomplexed metal ion salts such as zinc acetate, zinc chloride or zinc formate, or complexed metal ion salts in which the metal is bonded to two types of groups, at least one of which is readily ionizable and the other is not. Illustrative of such complexed metal ion salts are mixed zinc salts with one weak acid such as oleic acid or stearic acid and one more ionizable acid such as acetic acid or formic acid. In general, neutralization with a complexed non-alkali metal ion is preferred. The optionally partially neutralized polymers employed as the optional polymeric blend component are broadly conventional and many are commercial. Copolymers of ethene and methacrylic acid and copolymers of ethene and acrylic acid are marketed. Partially neutralized polymers are also marketed. The amount of the optional third component will suitably be up to 10 wt% based on the total polymer blend. Amounts of the optional blend component up to 5 wt% on the same basis are preferred. The blends of the invention may also include conventional additives such as antioxidants and stabilizers, fillers and fire resistant materials, mould release agents, colorants and other materials designed to improve the processability of the polymers or the properties of the resulting blend. Such additives are added by conventional methods prior to, together with or subsequent to the blending of the polyketone and the modifier. The method of producing the blends of the invention is not material so long as a uniform blend is produced without undue degradation of the blend or its components. In one modification the polymer components of the blend are extruded in a corotating twin screw extruder to produce the blend. In an other modification, the polymer components are blended in a mixing device which exhibits high shear. The blends are processed by conventional methods such as extrusion and injection moulding into sheets, films, plates and shaped parts. Illustrative of such applications are the production of internal and external parts for automotive use. The blends of the invention are categorized as compatible due to their desirable mechanical properties, and due to the strong interaction between the high rubber graft copolymer and the polyketone polymer matrix. While not wishing to be bound by any particular theory, it is speculated that this attraction occurs due to a physical interaction between the nitrile groups of the rigid graft copolymer and the ketone groups of the polyketone polymer. The attraction is unexpected, and probably originates from the strongly dipolar nature of both blend components. The wettability and adhesion between the high rubber graft copolymer and the polyketone polymer are indicative of the physical interaction that occurs within the blends of the invention. The blends are particularly characterized by improved toughness and impact strength at both ambient and low temperatures without undue loss of strength, relative to the polyketone polymer alone. The invention is further illustrated by the following Examples which should not be regarded as limiting. Example 1 Linear alternating terpolymers of carbon monoxide, ethylene, and propene were produced in the presence of a catalyst composition formed from palladium acetate, trifluoroacetic acid and 1,3-bis[bis(2- methoxyphenyl)-phosphino]propane. Two polyketone polymers had melting points of 220 °C to 223 °C and limiting viscosity numbers of 1.7 to 1.8 dl/g when measured in m-cresol at 60 °C. One polyketone polymer had a melting point of 224 °C and an LVN of 1.37 dl/g when measured in m-cresol at 60 °C. The polyketone polymers all contained 1 %w of a commercially available copolymer of ethene and methacrylic acid. Example 2 Blends were prepared of a polyketone terpolymer of Example 1 and three different grades of a commercial high rubber graft copolymer modifier. The blends prepared are shown in Table 1. The blends were compounded on a 42 mm twin screw, counter-rotating, intermeshing extruder operating at 100 RPM. Subsequent to blending, specimens of the blends were injection moulded on a 25 ton moulding machine. Moulded specimens were stored over desiccant until tested. Mechanical testing was performed on "dry as moulded" specimens. Impact and tensile properties of the samples are shown in Table 1. The value of 4.61 m.kg for the Gardner test represents the upper energy limit of the testing apparatus. A falling weight type impact test, such as the Gardner impact test, is the most relevant for many engineering applications. Previous work has shown that, although a fair number of materials have been identified which can substantially improve the notched Izod impact resistance of polyketone polymers, almost all of them cause the Gardner impact values to decrease. Thus, the Gardner test may be considered more discriminating for the determination of impact modification, at least for polyketone-based materials. A secondary consideration in the Gardner test is the manner in which the specimens fail. The present modified compounds exhibited a desirable, highly ductile failure in this test. The modifier of the invention is primarily elastomeric, having an elastic modulus which is considerably less than that of the polyketone polymer. Therefore, blending to produce a toughened material invariably involves a compromise with regard to stiffness and strength. Tensile yield stress also tended to decrease upon rubber modification as demonstrated in Table 1. Ultimate tensile elongation, also shown in Table 1, was relatively undiminished upon blending. Three grades of modifier were investigated. The superior modifier with respect to impact modification was Code No. 338, which gave the maximum Izod and Gardner impact improvements. This is the softest and most rubber-rich of the modifiers. The general purpose grade, Code No. 310, was also effective; the "transparent" grade (in PVC formulations), Code No. 336, was the least effective in polyketone polymer blends. Example 3 Blends were prepared of a polyketone terpolymer of Example 1 and modifier 338. The blends prepared are shown in Table 2. The blends were compounded on a 42 mm counter-rotating, intermeshing twin screw extruder operating at 100 RPM. Subsequent to blending, specimens of the blends were injection moulded on a 25 ton moulding machine. Moulded specimens were stored over desiccant until tested. Mechanical testing was performed on "dry as moulded" specimens. Impact and tensile properties of the samples are shown in Table 2. The data indicate that modifier 338 is an effective toughener for the polyketone polymer. At ambient temperatures, Notched Izod values increased abruptly at 15% modifier, whereas at low temperatures, Izod values increased gradually with modifier content, from about 5 to 27 m.kg/m over the composition range studied. Izod values greater than 100 m.kg/m were obtained with modifier 338 levels of 15 wt% or more at room temperature. At low temperature (-30 °C), Gardner impact decreased slightly with low contents of the modifier and then increased considerably with additional modifier. The Gardner impact values greater than 4.61 m.kg at -30 °C are particularly significant. Compositions containing 15 wt% or more modifier 338 had higher impact energies than the neat polyketone. Tensile modulus and yield stress both decreased in the desired manner upon addition of the soft, elastomeric modifier. Tensile yield strains increased upon modification, but tensile elongation at break did not change significantly. Example 4 Blends were prepared of the low-LVN polyketone terpolymer of Example 1 and modifier 338. The blends prepared are shown in Table 3. The blends were compounded on a 42 mm counter-rotating, intermeshing twin screw extruder operating at 100 RPM. Subsequent to blending, specimens of the blends were injection moulded on a 25 ton moulding machine. Moulded specimens were stored over desiccant until tested. Mechanical testing was performed on "dry as moulded" specimens. Impact and tensile properties of the samples are shown in Table 3. The data indicate that modifier 338 is also an effective toughener for the low-LVN polyketone polymer. The modified blend exhibited greatly improved Notched Izod and Gardner impact strengths at ambient and at low temperatures. Notched Izod and Gardner values of the low-LVN polyketone polymer containing 20 wt% modifier are comparable to those for the regular polyketone polymer of Example 3 containing 10 wt% to 15 wt% modifier, and considerably better than those for the neat low-LVN polymer. Notably, the low temperature Gardner impact strength was improved by almost a factor of five by rubber toughening. Use of a modified low-LVN polyketone polymer may prove to be economically attractive in some applications.

Claims: Claims for the following Contracting States : AT, BE, CH, LI, DE, DK, FR, GB, GR, IT, LU, NL, SE Polyketone polymer composition comprising a blend of (1) a linear alternating polymer of carbon monoxide and at least one ethylenically unsaturated hydrocarbon, and (2) a rubber graft copolymer comprising a rigid graft copolymer on a rubbery substrate, and, optionally, (3) an acidic polymer incorporating moieties of an a-olefin and an α,β-ethylenically unsaturated carboxylic acid, optionally containing a non-acidic, low-molecular weight third polymerizable monomer, wherein optionally a portion of the carboxylic acid groups of the acidic polymer are neutralized with non-alkali metal, characterized in that the rubber graft copolymer is a high rubber graft copolymer wherein the rigid graft copolymer is obtainable by graft polymerizing less than 50 %wt of a monomer selected from the group consisting of vinyl nitrile monomers, vinyl nitrile monomers combined with vinyl monomers, and, optionally, acrylic monomers, and mixtures thereof, in the presence of at least 50 %wt of the preformed rubbery substrate. A composition as claimed in claim 1, characterized by comprising a blend of (1) a major proportion of a linear alternating polymer of carbon monoxide and at least one ethylenically unsaturated hydrocarbon, and (2) lesser proportions of (a) a high rubber graft copolymer, and, optionally, (b) an acidic polymer incorporating moieties of an α-olefin, an α,β-ethylenically unsaturated carboxylic acid and optionally a non-acidic, low molecular weight, third, polymerizable monomer, the acidic polymer optionally having a portion of the carboxylic acid groups neutralized with non-alkali metal. A composition as claimed in claim 2, wherein the linear alternating polymer is represented by the formula wherein G is a moiety derived from an ethylenically unsaturated hydrocarbon of at least 3 carbon atoms polymerized through the ethylenic unsaturation and the ratio of y:x is no more than 0.5. A composition as claimed in claim 1, 2 or 3, wherein the rubbery substrate is selected from the group consisting of 1,3-diene polymers and copolymers thereof. A composition as claimed in claim 4, wherein the rubbery substrate comprises at least one 1,3-diene polymer selected from the group consisting of polybutadiene, polyisoprene, and copolymers of a 1,3-diene. A composition as claimed in claim 4 or 5, wherein the rigid graft copolymer is a copolymer of styrene and acrylonitrile, and optionally, methyl methacrylate. A composition as claimed in any one of claims 4-6, wherein the rubbery substrate comprises 50 wt% to 90 wt%, and the rigid graft phase comprises 10 wt% to 50 wt%, of the high rubber graft copolymer. A composition as claimed in any of claims 1-7, wherein the high rubber graft copolymer comprises from 15 wt% to 30 wt% of the total composition. A composition as claimed in any of claims 1-8, wherein the acidic polymer is a non-neutralized copolymer of ethene and acrylic acid or methacrylic acid, and is present in an amount of up to 10 wt% of the total blend. A composition as claimed in any of claims 1-8, wherein the acidic polymer has from 10% to 90% of the carboxylic acid groups neutralized with zinc, aluminium or magnesium, and is present in an amount of up to 10 wt% of the total blend. Claims for the following Contracting State : ES Process comprising blending (1) a linear alternating polymer of carbon monoxide and at least one ethylenically unsaturated hydrocarbon, and (2) a rubber graft copolymer comprising a rigid graft copolymer on a rubbery substrate, and, optionally, (3) an acidic polymer incorporating moieties of an α-olefin and an α,β-ethylenically unsaturated carboxylic acid, optionally containing a non-acidic, low-molecular weight third polymerizable monomer, wherein optionally a portion of the carboxylic acid groups of the acidic polymer are neutralized with non-alkali metal, characterized in that the rubber graft copolymer is a high rubber graft copolymer wherein the rigid graft copolymer is obtainable by graft polymerizing less than 50 %wt of a monomer selected from the group consisting of vinyl nitrile monomers, vinyl nitrile monomers combined with vinyl monomers, and, optionally, acrylic monomers, and mixtures thereof, in the presence of at least 50 %wt of the preformed rubbery substrate. Process as claimed in claim 1, characterized by blending (1) a major proportion of a linear alternating polymer of carbon monoxide and at least one ethylenically unsaturated hydrocarbon, and (2) lesser proportions of (a) a high rubber graft copolymer, and, optionally, (b) an acidic polymer incorporating moieties of an α-olefin, an α,β-ethylenically unsaturated carboxylic acid and optionally a non-acidic, low molecular weight, third, polymerizable monomer, the acidic polymer optionally having a portion of the carboxylic acid groups neutralized with non-alkali metal. Process as claimed in claim 2, wherein the linear alternating polymer is represented by the formula wherein G is a moiety derived from an ethylenically unsaturated hydrocarbon of at least 3 carbon atoms polymerized through the ethylenic unsaturation and the ratio of y:x is no more than 0.5. Process as claimed in claim 1, 2 or 3, wherein the rubbery substrate is selected from the group consisting of 1,3-diene polymers and copolymers thereof. Process as claimed in claim 4, wherein the rubbery substrate comprises at least one 1,3-diene polymer selected from the group consisting of polybutadiene, polyisoprene, and copolymers of a 1,3-diene. Process as claimed in claim 4 or 5, wherein the rigid graft copolymer is a copolymer of styrene and acrylonitrile, and optionally, methyl methacrylate. Process as claimed in any one of claims 4-6, wherein the rubbery substrate comprises 50 wt% to 90 wt%, and the rigid graft phase comprises 10 wt% to 50 wt%, of the high rubber graft copolymer. Process as claimed in any of claims 1-7, wherein the high rubber graft copolymer comprises from 15 wt% to 30 wt% of the total composition. Process as claimed in any of claims 1-8, wherein the acidic polymer is a non-neutralized copolymer of ethene and acrylic acid or methacrylic acid, and is present in an amount of up to 10 wt% of the total blend. Process as claimed in any of claims 1-8, wherein the acidic polymer has from 10% to 90% of the carboxylic acid groups neutralized with zinc, aluminium or magnesium, and is present in an amount of up to 10 wt% of the total blend.

Inventors: MACHADO JOSEPH MICHAEL, MACHADO, JOSEPH MICHAEL
Applicants: SHELL INT RESEARCH, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1991
Main classification: C08L73
IPC codes: C08L23, C08L73, C08L33, C08L51, C08L55, C08G67