CA2002695A1 - Polymer compositions compatibilized with styrene block copolymers and articles produced therefrom - Google Patents

Abstract

FERO-971(CIP) Title: POLYMER COMPOSITIONS COMPATIBILIZED WITH STY-RENE BLOCK COPOLYMERS AND ARTICLES PRODUCED
THEREFROM

Abstract of the Disclosure Blended polymer compositions are described which comprise (A) an olefin polymer, (B) at least one second polymer having a glass transition temperature greater than the glass transition temperature of olefin polymer (A) such as: copolymers and terpolymers of styrene and maleic anhydride or a maleimide; polystyrene blended with a polyarylene ether, and optionally an elastomer; blends or reaction products of styrene-maleic anhydride or maleimide copolymers or terpolymers with elastomers; polycarbonates, etc., and (C) at least one compatibilizing agent selected from the group consisting of various block copolymers of vinyl aromatic compounds and conjugated dienes, and their partially hydrogenated derivatives.
The blended polymer compositions of the present invention can be extruded, coextruded, thermoformed, blow-molded, injection-molded, compression-molded, calen-dered, laminated, foamed, stamped, pultruded, or extru-sion die coated onto a continuous fiber to form shaped articles useful in a variety of applications. The com-patibilized and blended polymer compositions of the present invention exhibit excellent heat distortion properties as well as excellent strength, toughness, stiffness, gloss, ease of processing and forming, improv-ed filler interaction, hardness, adherability and shrink-age characteristics and they are retortable and micro-waveable.

Description

POLYMER COMPOSITIONS COMPATIBILIZED WITH STYRENE
BLOCK COPOLYMERS AND ARTICLES PRODUCED THEREFROM

Back~round of the Invention Field of the Invention This invention relates generally to compatibil-izing two or more incompatible polymer systems. The invention also relates to compounded, compatibilized polyolefin-styrene copolymer or polymeric blend composi-tions and articles of manufacture produced therefrom.
State of the Art Polymeric blends have been known for years.
Typically, blends of polymers result in a material which combines the poorest properties of the constituents.
This is a result of the incompatibility of the constitu-ent polymers resulting in little, if any, adhesion at the interface between the different constituent poly-mers. Furthermore, this incompatibility stems in part from the structure of the individual polymers. Thermo-dynamically, one polymeric phase has more of an affinity for itself than for the other polymeric phase so that `~ !, t~ r'~

intermolecular forces between the two polymers are weak.
For example, a b]end of a polar polymer ar.d a non-polar polymer would result in an incompatible system demon-strating poor physical properties for lack of wetting and adhesion at the interface. Even in cases when the polarity of the polymers in a blend is similar, compat-ibility is generally not achieved because the entropy change upon mixing of high polymers is not favorable.
Such incompatibility problems may be overcome through the use of a compatibilizing agent. A compat-ibilizing agent is a materi~l which, on a molecular scale, has particular regions which are compatible with each of the incompatible constituent polymers. Such compatibilizing agents typically surround one polymeric phase providing a chemical and/or physical bridge to the other polymeric phase. Insomuch as portions of the compatibilizing aqent are compatible with each of the constituent polymers, the bonding between the two incom-patible polymeric phases is effectively enhanced through this intermediate compatibilizing phase. Such a system of incompatible polymers coupled by a compatibilizing agent results in a material which advantageously com-bines the more desirable properties of the constituent polymers. Lindsey et al, J. Appl. Polymer Sci., Vol.
26, 1-8 (1981) describe a method of reclaiming mixed immiscible polymers by employing a compatibilizing agent. The system studied was a high density polyethyl-ene (HDPE) and polystyrene (PS) and a styrene-ethylene-butene-1-styrene (SEBS3 copolymer (a linear triblock copolymer) as the compatibilizing agent. These ternary blends exhibited a considerable improvement in the balance of mechanical properties over a binary blend of high density polyethylene and polystyrene.

200~695 sartlett et al, Modern Plastics, Dec. 1981, 60-62 describes a system comprising polypropylene, poly-styrene and styrene-ethylene-butene-1-styrene as a com-patibilizer. This work focused on those parameters that affected the extent of the polypropylene crystallinity.
Polystyrene homopolymers and copolymers compat-ibilized with polyolefins have been available for sever-al years. Furthermore, molded articles have been pro-duced from such compatibilized polymer compositions.
For example, U.S. Patent Nos. 4,386,187 and 4,386,188 disclose a thermoformable polymer blend of a polyolefin, a styrene polymer and styrenic diblock and triblock copolymer rubbers. While a number of styrene polymers and copolymers are disclosed, a copolymer of styrene and maleic anhydride is not.
U.S. Patent 4,647,509 discloses a multilayer thermoformable packaging material comprising a first layer of (a) a vinylidene chloride polymer, (b) an incompatible polymer, e.g., polyesters and nylons, and (c) a compatibilizing agent, and a second layer of (a) a blend of an olefin polymer, a styrenic polymer, and a compatibilizing polymer, and (b) scrap material produced from the first and second layers. The compatibilizing polymers for the second layer are preferably block copolymers of olefins and styrene such as copolymers of styrene-butadiene, styrene-butadiene-styrene, styrene-isoprene, etc.
U.S. Patent 4,107,130 discloses a multicompon-ent polymer blend comprised of a polyolefin, a selective-ly hydrogenated monoalkenyl arene-diene block copolymer, and at least one dissimilar engineering thermoplastic resin.

Summary of the Invention Blended polymer compositions are described which comprise (A) an olefin polymer, (B) at least one second polymer having a glass transition temperature greater than the glass transition temperature of olefin polymer (A) such as: copolymers and terpolymers of styrene and maleic anhydride or a maleimide;
polystyrene blended with a polyarylene ether, and optionally an elastomer; blends or reaction products of styrene-maleic anhydride or maleimide copolymers or terpolymers with elastomers;
polycarbonates, etc., and (C) at least one compatibilizing agent selected from the group consisting of various block copolymers of vinyl aromatic compounds and conjugated dienes and/or their partially hydrogenated derivatives.
The blended polymer compositions of the present invention can be extruded, coextruded, thermoformed, compression molded, blow-molded, injection-molded, calendered, laminated, stamped, pultruded, foamed, or extrusion die coated onto continuous fibres, to form shaped articles useful in a variety of applications. The compatibilized and blended polymer compositions of the present invention exhibit excellent heat distortion properties as well as excellent strength, toughness, stiffness, gloss, ease of processing, improved filler interaction, hardness, adherability and shrinkage character-istics, and they are retortable and microwaveable.
In a broad aspect, the present invention relates to a polymer composition comprising: (a) from 1% by weight to 99% by weight polypropylene; (b) from 1% by weight to 99% by weight of a copolymer of styrene and maleic anhydride; and (c) from 1% by weight to 15% by weight of a compatibilizing agent comprising a multiblock styrene-butadiene copolymer.
Description of the Preferred Embodiments The novel blended polymer compositions of the present invention comprises a mixture of two or more polymers and a compatibilizing agent as described in more detail herein. An essential component of the blended polymer compositions of the present invention is at least one olefin polymer.

2(:~02695 (A) The Olefin PolYmers.
The olefin polymers employed in the blends of the present invention generally are semi-crystalline or crystallizable olefin polymers including homopolymers, copolymers, terpolymers, or mixtures thereof, etc., containing one or more monomeric units. Polymers of alpha-olefins or 1-olefins are preferred in the present invention, and these alpha-olefins may contain from 2 to about 20 carbon atoms. Alpha-olefins containing 2 to about 6 carbon atoms are preferred. Thus, the olefin polymers may be derived from olefins such as ethylene, propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-octene, 1-decene, 4-ethyl-1-hexene, etc. Examples of particularly useful olefin polymers include low-density polyethylene, high-density polyethylene, linear low density polyethylene, ultra low density polyethylene, polypropylene, (high and low density) poly(1-butene), ultra low molecular weight polyethylene, ethylene-based ionomers, poly(4-methyl-1-pentene), ethylene-propylene copolymers, ethylene-propylene-diene copolymers (EPDM) copolymers of ethylene and/or propylene with other copolymerizable monomers such as ethylene-1-butylene copolymer, ethylene-vinyl acrylate copolymer, ethylene-ethyl acetate copolymer, propylene-4-methyl-1-pentene copolymer, ethylene-vinyl acetate, ethylene vinyl alco-hol, ethylene-methyl acrylate-acrylic acid terpolymers, etc. Halogenated olefins, polymers and copolymers may also be used in this invention.
Olefin polymers having a semi-crystalline or crystallizable structure are particularly useful in the present invention since such polymers are capable of forming a continuous structure with the other polymers in the polymer blend of the present invention. The Z0026~3Si number average molecular weight of the polyolefins is preferably above about 10,000 and more preferably above about 50,000. In addition, it is preferred in one embodiment that the apparent crystalline melting point be above about 75C and preferably between about 75C
and about 250C. Most commercial polyethylenes have a number average molecular weight of from about 50,000 to about 500,000. The olefin polymers useful in preparing the polymer blends of the present invention are well-known to those skilled in the art and many are available commercially. The olefin polymers may be homopolymers, impact copolymers, block copolymers, random copolymers, thermoplastic olefinic elastomers (TPO), etc., or mixtures thereof. Polyethylene and polypropylene are preferred olefin polymers, and polypropylelles such as Himont's Profax 6523 (homopolymer) and Shell's 7C06 or Exxon's PD7132 or Aristich's 4040F (polypropylene-ethyl-ene copolymers) are particularly preferred.
(B) Hiqher Glass Transition TemPerature Second PolYmer.
The second polymer in the blended polymer compo-sitions of the present invention is at least one polymer having a glass transition temperature which is greater than the glass transition temperature of the olefin poly-mer (A). Generally, the glass transition temperature of the second polymer will be above about 75C.
(B-1) CopolYmers of VinYl Aromatic ComPounds and Unsat-urated DicarboxYlic Acid Anhydrides Imides. Metal Salts or Partial Esters of the DicarboxYlic Acids.
A particularly preferred second polymer in the blended polymer compositions of the present invention is at least one copolymer of a vinyl aromatic compound and unsaturated dicarboxylic acid anhydrides, imides, metal salts and partial esters. Copolymers of a vinyl aroma-tic compound and maleic anhydride, N-substituted male-imide, metal salts or partial esters of maleic acid derivatives are particular examples.
The vinyl aromatic compounds include styrene and the various substituted styrenes which is represent-ed by the following formula R&=C~2 ~Z)p wherein R is hydrogen, an alkyl group containing from 1 to about 6 carbon atoms, or halogen; Z is a member sel-ected from the group consisting of vinyl, halogen and alkyl groups containing from 1 to about 6 carbon atoms;
and p is a whole number from 0 up to the number of replaceable hydrogen atoms on the phenyl nucleus. Speci-fic examples of vinyl aromatic compounds such as repre-sented by the above formula include, for example, in addition to styrene, alpha-methyl styrene, beta-methyl styrene, vinyl toluene, 3-methyl styrene, 4-methyl sty-rene, 4-isopropyl styrene, 2,4-dimethyl styrene, o-chloro styrene' p-chloro styrene, o-bromo styrene, 2-chloro-4-methyl styrene, etc. Styrene is the prefer-red vinyl aromatic compound.
The maleic anhydride and maleimide derivative compounds utilized in the formation of the copolymers with vinyl aromatic compounds may generally be represented by the formula R-C--C
Il \X
R-C--C. ~

wherein each R group is hydrogen or an aliphatic or aromatic hydrocarbyl group or the two R groups are joined together to form a fused ring derivative, X is -O- or >NR2 where R2 is a hydrocarbyl group which may be an aliphatic or an aromatic hydrocarbyl group such as phenyl, methyl, ethyl, propyl, butyl, etc.
Preferably both R groups are hydrogen.
Examples of maleic derivatives which are cyclic or bicyclic compounds include ~C~' obtained by a Diels-Alder reaction of butadiene with maleic anhydride or a maleimide ~ C~

obtained by a Diels-Alder reaction of cyclopentadiene with maleic anhydride or maleimide, and CH3 /~
¢L~/X

~0 g obtained by a Diels-Alder reaction of isoprene with maleic anhydride or an N-substituted maleimide male-imide. These cyclic or bicyclic derivatives have high glass transition temperatures.
Copolymers comprising a vinyl aromatic compound and metal salts of maleic acid also are useful as the second polymer in the blended polymer compositions of the present invention. The metals present in the metal salt of maleic acid may be Group I metals, Group II
metals or transition metals. Alkali metals and transi-tion metals are preferred. Partial esters of the unsat-urated anhydrides also can be used. These can be obtain-ed, for example, by reacting or esterifying, maleic acid or maleic anhydride with less than one equivalent of an alcohol such as methanol, ethanol, propanol, etc.
The copolymers of the vinyl aromatic compounds with maleic anhydride, N-substituted maleimides or metal salts of maleic acid are obtained, in one embodiment, by polymerizing equimolar amounts of styrene and the core-actant, with or without one or more interpolymerizablecomonomers. In another embodiment, substantially homo-geneous copolymers of styrene with maleic anhydride or maleimide or metal salts of maleic acid can be obtained by (1) heating a vinyl aromatic compound to a tempera-ture at which the vinyl aromatic compound with polymer-ize, (2) stirring the polymerizing vinyl aromatic com-pound while (3) adding maleic anhydride, maleimide, or the metal salt of maleic acid, or mixtures thereof at a continuous and uniform rate. Generally, the addition of the maleic anhydride, maleimide, or metal salts or esters of maleic acid is made at a rate in moles per unit time that is slower than the rate, in moles per unit time at which the vinyl aromatic compound is poly-- 1 o -merizing. Procedures for preparing such copolymers are known in the art and have been described in, for exam-ple, U.S. Patent 2,971,939.
In one embodiment, the styrene-maleic anhydride copolymers are preferred second polymers in the blended polymer compositions of the present invention. The styrene-maleic anhydride copolymers (SMA) are available commercially from, for example, ARCO under the general trade desi~nation Dylark. Examples include: Dylark DsK-290 reported to comprise about 18% by weight of maleic anhydride and about ~2% by weight of styrene;
Dylark 332 reported to comprise about 14% by weight of maleic anhydride and 8~% by weight of styrene; and Dylark 134 reported to comprise about 17% by weight of maleic anhydride, the balance being styrene.
Other Dylark materials available include trans-parent grades: Dylark* 132 (Vicat 109C), Dylark*232 (Vicat 123C), and Dylark* 332 (Vicat 130C). Impact grades include Dylarks* 150, 250, 350 and 700 which are believed to be blends and/or grafts of SMA with SBR.
Other examples of impact modified styrenic and alpha-methyl styrene copolymers with maleic anhydride and acrylonitrile include Arvyl*300 MR and 300 C~.
Low molecular wei~ht styrene-maleic anhydride copolymers (Mw as low as 1500) also are useful and these are available commercially such as from Monsanto under the designation "Scripset"* and from Atochem under the designation "SMA Resins". Sulfonated styrene-maleic anhydride copolymers (and their metal salts) also are available and useful in this invention. Two such pro-ducts are available from Atochem:SSMA-1000 which is a sulfonated copolymer of about 50% styrene and 50% maleic anhydride; and SSMA 3000, a sulfonated SMA comprising about 75% styrene and 25% maleic anhydride.
* Denotes Trade Mark ;

(B-2) TerpolYmers of Vinyl Aromatic ComPounds, ~nsatur-ated DicarboxYlic Acid Anhvdrides, Imides Metal Salts or Partial Esters of the Dicarboxvlic Acids, and CoPolY-merizable Unsaturated Monomers.
The terpolymers useful in the present invention comprise (1) a vinyl aromatic compound as described above, (2) unsaturated dicarboxylic acid anhydrides, imides, metal salts or partial esters as described above; and (3) copolymerizable monomers. Examples of copolymerizable monomers used to form the above-describ-ed terpolymers include acrylic acid alkyl-substituted acrylic acids, acrylic esters and alkyl-substituted acrylic esters containing from 1 to 4 carbon atoms in the ester moiety, acrylonitriles, and mixtures thereof.
Acrylates and methacrylates are preferred comonomers.
Examples of such comonomers include methy' acrylate, ethyl acrylate, butyl acrylate, methyl methacrylate.
Other vinyl monomers can be utilized as the comonomers, and these include vinyl acetate, vinyl methyl ether, vinyl ethyl ether, vinyl chloride, isobutene, etc.
In one embodiment, the terpolymers comprise about 45 to 83% (preferably 50 or 60 to 75%) by weight of the vinyl aromatic monomer, from 15 to 35% (prefer-ably 20-30%) by weight of an unsaturated dicarboxylic acid anhydride and from 2 to about 20% (preferably 4-10%) by weight of a C1_3 alkyl methacrylate ester.
Terpolymers of this type are available commercially from Monsanto.
(B-3) Blends or Reaction Products of Elastomers and the Co~olymer of (B-1) or Terpolymer of (B-2).
The second polymer utilized in the blended compositions of the present invention may comprise a blend or reaction product of an elastomer and the copolymer of (s-1~ or the terpolymer of ~B-2) described '~
above. The elastomers utilized in this embodiment may be polybutadienes, isobutylene-isoprene copolymers, styrene butadiene copolymers, butadiene-acrylonitrile copolymers, ethylene-propylene copolymers, polyiso-prenes, ethylene-propylene diene monomer terpolymers (EPDM), etc. Particularly preferred elastomers are the so-called "high-cis" diene rubbers which contain at least 90% by weight of cis-1,4-polybutadiene units. The preferred rubbers generally have a Tg of less than -20C.
The polymer component (B-3) may comprise blends of the elastomers and the copolymers or terpolymers or the elastomer may be grafted into the copolymer or terpolymer. Alternatively, the polymer component (B-3) may comprise a polymer wherein the elastomer is both blended and grafted into the copolymer or terpolymer. A
typical method of preparinq the elastomer modified graft copolymers is found in U.S. Patent 3,9l9,354. Elastomer-modified styrenic terpolymers such as the terpolymers (B-2) are described in U.S. Patent 4,341,695.

The amount of elastomer incorporated into the blends or grafts of this embodiment may be up to about 50% by weight of elastomer in the total blend or graft.
Elastomer-modified graft vinyl aromatic maleic anhydride copolymers are available commercially from ARCO Polymers Inc. (ARCO) under the general designations Dylark and Arvyl. Examples of such elastomer-modified copolymers include Dylark DKB-218 which is reported to comprise about 10~ by weight of elastomer in the total graft copolymer, 17~ by weight of maleic anhydride and 83% by weight of styrene in the resin phase; Dylark 338S
reported to comprise 4% by weight of elastomer in the total graft copolymer, and 14~ by weight of maleic anhydride and 86% by weight of styrene in the resin phase; Dylark 350 reported to comprise 15% by weight of rubber in the total graft polymer and 13% by weight of maleic anhydride and 87~ by weight of styrene in the resin phase.
Blends or reaction products of SMA copolymers and polybutylene terephthalate (PBT) (50:50) are useful, and these are available from Arco under the general designation Dylark DPN-500 series. Blends of SMA with polycarbonates are available under the designation Arloy.*~
Blends or reaction products of elastomers with terpolymers (B-2) also are available from the Monsanto Chemical Company under the general trade designation "Cadon".* Cadon*is reported to be a blend of a reaction product of polybutadiene with a styrene:maleic anhy-dride:methyl methacrylate terpolymer.
(B-4) Blends Com~risinq a Polvmer of a VinYl Aromatic ComPound and a PolYarvlene Ether and, OPtionallY an Elastomer.
Blends comprising a polymer of a vinyl aromatic compound and a polyarylene ether are also useful as the second polymer in the blended polymer compositions of the present invention. Among the preferred polyarylene ethers are polyphenylene ethers which may be represented by the following formula R~ R1 n * Denotes Trade Mark wherein the oxygen ether atom of one unit is connected to the phenyl nucleus of the next adjoining unit; each R1 is independently a monovalent substituent selected from the group consisting of hydrogen, halogen, hydro-carbon groups free of a tertiary alpha-carbon atom, halohydrocarbon groups having at least 2 carbon atoms between the halogen atom and the phenyl nucleus and also being free of a tertiary alpha-carbon ator.l, hydrocarbon-oxy groups free of aliphatic, tertiary alpha-carbon atoms and halohydrocarbonoxy groups containing at least 2 carbon atoms between the halogen atom and the phenyl nucleus and being free of an aliphatic, tertiary alpha-carbon atom; n is an integer of at least about 50 such as from about 50 to about 800 and preferably from about 100 to about 300. Such polyarylene ethers may have mole-cular weights in the range of between 1000 and 100,000 and more preferably between about 6000 and 100,000. A
preferred example of a polyarylene ether is poly(2,6-di-methyl-1,4-phenylene)ether. Examples of polyphenylene ethers useful in the blended polymer compositions of the present invention and methods for their preparation are described in, for example, U.S. Patents 3,306,874;

3,306,875; 3,257,357; and 3,257,358, Typical styrene polymers which can be blended or reacted with the polyphenylene ethers include, for example, homopolymers such as polystyrene and polychloro-styrene, modified polystyrenes such as rubber-modified polystyrenes (high impact styrenes) and the styrene-containing copolymers such as the styrene-acrylonitrile copolymers (SAN), styrene-butadiene copolymers, styrene-acrylonitrile-alpha-alkyl styrene copolymers, styrene-c~r; . I

acrylonitrile-butadiene copolymers (ABS), poly-alpha-methyl styrene, copolymers of ethyl vinyl benzene and divinyl benzene, etc.
Blends of styrene resins with these polyarylene ethers such as polyphenylene ethers are particularly useful in this invention and are available commercially.
Eor example, blends comprising polystyrene and poly-phenylene ether typically containing from about 25 to about 50~ by weight of polystyrene units are commercial-ly available from the General Electric Company under thetradename NORYL~ thermoplastic resin. The molecular weight of such blends may range from about 10,000 to about 50,000 and more often will be about 30,000.
The elastomers which may be included in the blends of or reacted with the polymer of a vinyl aroma-tic compound and a polyarylene oxide include the elastomers described above with respect to polymer type (B-3)-(B-5) Co~olYmers and TerpolYmers of a Vinvl Aromatic Com~ound With an AcrYlic Ester and/or AlkYl-Substituted Acrylic Ester.
The second polymer utilized in the blended polymer compositions of the present invention may com-prise terpolymers of a vinyl aromatic compound with an acrylic ester and/or an alkyl-substituted acrylic ester.
Vinyl aromatic compounds such as those described above and including styrene and substituted styrenes may be utilized in the preparation of these particular copoly-mers. The acrylic ester and alkyl-substituted acrylic esters useful in preparing these polymers include esters characterized by the following formula CH2=C(Rl)COOR2 wherein R1 is hydrogen, a lower alkyl group containing from 1 to 4 carbon atoms, or a halogen; and R2 is a lower alkyl group containing from 1 to about 4 carbon atoms. Specific e~amples of esters characterized by the above Formula I include methyl acrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, ethyl methacrylate, ethyl ethacrylate, etc.
The polymers of a vinyl aromatic compound such as styrene with an acrylic ester and/or an alkyl-substi-tuted acrylic ester can be prepared by procedures well-known to those skilled in the art. The mole ratio of vinyl aromatic compound to acrylic ester and/or alkyl-substituted ester may vary over a wide range such as from about 10:90 to about 90:10. Such terpolymers are available commercially from CYRO under the designations "XT* Polymer Series" and "Cyrolite G-Series". These terpolymers are referred to as acrylic-based multipoly-mer products. They are believed to be terpolymers of styrene, methyl methacrylate and ethyl acrylate. Some of the products may be impact modified with polybuta-diene during copolymerization.
Other acrylic based multipolymer products are available from Polysar under the designation "Zylar*
90". This product is believed to comprise styrene, butadiene and methyl methacrylate.
(B-6) Product of the Reaction of an Alpha~Beta-Olefinic-allY _Unsaturated Carboxvl c Reaaent and a Hvdroqenated Block CoPolvmer.
Also useful in the blended polymer compositions of the present invention are polymeric products of the reaction of an alpha,beta-olefinically unsaturated car-boxylic reagent in a hydrogenated block copolymer of a vinyl aromatic compound and an aliphatic conjugated * Denotes Trade Mark Bl-diene. The hydrogenated block copolymers of a vinyl aromatic compound and an aliphatic conjugated diene may be either normal block copolymers (true block copoly-mers) or random block copolymers, although the normal block copolymers are preferred. The vinyl-substituted aromatic compounds generally contain from about 8 to about 12 carbon atoms and preferably about 8 or 9 carbon atoms. Examples of such vinyl aromatic compounds include styrene and the various substituted styrenes described above. The conjugated dienes used to form the block copolymers generally contain from about 4 to about carbon atoms, and preferably from 4 to about ~ carbon atoms. Examples of such conjugated dienes include a 2,3-dimethyl-1,3-butadiene, chloroprene, isoprene, and 1,3-butadiene. Isoprene and 1,3-butadiene are particu-larly preferred, and mixtures of such conjugated dienes may be used.
The normal block copolymers have a total of from 2 to about 5, and preferably 2 or 3 polymer blocks of the vinyl-substituted aromatic and the conjugated diene, with at least one polymer block of said vinyl-sub-stituted aromatic and at least one polymer block of said conjugated diene being present. The vinyl substituted aromatic content of these copolymers is in the range of from about 20% to about 70% by weight and preferably from about 40~ to about 60% by weight. The block copoly-mers can be prepared by conventional methods well-known to those in the art, and these copolymers usually are prepared by anionic polymerization using, for example, an alkali metal hydrocarbon such as sec-butylithium as a polymerization catalyst.
The block copolymers of the vinyl aromatic compound and a conjugated diene are hydrogenated prior 2002~95 to reaction with the olefinically unsaturated carboxylic acid to remove virtually all of the olefinic double bonds. Techniques for accomplishing this hydrogenation are well-known to those skilled in the art. Generally, hydrogenation is accomplished by contacting the copoly-mers with hydrogen at superatmospheric pressure in the presence of a metal catalyst such as colloidal nickel, palladium supported on charcoal, etc. These block copolymers typically have number average molecular weights in the range of about 10,000 to about 500,000, and preferably from about 30,000 to about 200,000.
The alpha,beta-olefinically unsaturated carbox-ylic reagent includes the carboxylic acids per se and functional derivatives thereof such as anhydrides, esters, amides, imides, salts, acyl halides, etc. The carboxylic acid reagents may be either monobasic or polybasic in nature, and when polybasic, they are prefer-ably dicarboxylic acids. The monobasic alpha,beta-ole-finic unsaturated carboxylic acid reagents are carbox-ylic acids corresponding to the formula RCH=C ( R~ ) COOH

wherein R iS hydrogen or a saturated aliphatic or ali-cyclic, aryl, alkaryl or heterocyclic group. Preferably, R iS hydrogen or an alkyl group containing from 1 to about 10 carbon atoms; R1 is hydrogen or an alkyl group containing from about 1 to about 10 carbon atoms.
The total number of carbon atoms in R and R1 should not exceed 18 carbon atoms. Specific examples of useful monobasic alpha,beta-olefinic unsaturated carboxylic acids include acrylic acid, methacrylic acid, cinnamic acid, crotonic acid, etc.

As noted above, the olefinic unsaturated carbox-ylic acid reagent may be a dibasic acid. Examples of useful dibasic acids include maleic acid, fumaric acid, mesaconic acid, itaconic acid and citraconic acid. A
preferred alpha,beta-olefinically unsaturated carboxylic acid reagent is maleic anhydride.
The amount of alpha,beta-olefinically unsatur-ated carboxylic reagent reacted with the block copoly-mers is an amount which is effective to modify the pro-perties of the block copolymers in a desired manner.
Generally, the amount of reagent will be from about 0.2 to about 20% by weight and preferably from about 0.5 to about 5% by weight based on the total weight of the block copolymer and the reagent.
In order to promote the reaction to generate reaction cites, free radical initiators are utilized, and these initiators usually are either peroxides or various organic azo compounds. The amount of initiator utilized generally is from about 0.01% to about 5% by weight based on the combined weight of the block copoly-mer in the carboxylic reagent. The amount of carboxylic reagent incorporated into the block copolymers can be measured by determining the total acid number of the product.
(B-7) PolYcarbonates.
The polycarbonates utilized in the preparation of the blends of this invention may be characterized by the formulae ( Ar-A-Ar-O-C(O)O ) n and ~ Ar-O-C(O)O ~ n wherein Ar is selected from the group consisting of phenylene and alkyl, alkoxyl, halogen and nitro-substi-tuted phenylene; A is selected from the group consisting of carbon-to-carbon bonds, alkylidene, cycloalkylidene, alkylene, cycloalkylene, azo, imino, sulfur, oxygen, sulfoxide and sulfone, and n is at least 2.
The preparation of the polycarbonates is well-known and the details thereof need not be delineated herein. There are a variety of preparative procedures set forth in ChemistrY and PhYsics of Polvcarbonates by Herman Schnell, Interscience Division of John Wiley &
Company, New York, (1964), first edition, as well as in U.S. Patent 3,028,365. In general, a preferred reaction is carried out by dissolving a dihydroxy component in a base such as pyridine and bubbling phosgene into the stirred solution at the desired rate. Tertiary amines may be used to catalyze the reaction as well as to act as acid acceptors throughout the reaction. Since the reaction is normally exothermic, the rate of phosgene addition can be used to control the reaction tempera-ture. The reactions generally utilize equimolar amounts of phosgene and dihydroxy reactants, however, the molar ratios can be varied dependent upon the reaction condi-tions.
A preferred polycarbonate utilized in this invention is obtained when Ar is p-phenylene and A is isopropylidene. This polycarbonate is prepared by reacting para, para'-isopropyldienediphenol with phos-gene and is sold by General Electric Company under thetrademark LEXAN~ and by Mobay under the trademark MERLON~. This commercial polycarbonate typically has a 20026~ ~

molecular weight of around 18,Q00, and a melt tempera-ture of over 230C. Other polycarbonates may be pre-pared by reacting other dihydroxy compounds, or mixtures of dihydroxy compounds, with phosgene. The dihydroxy compounds may include aliphatic dihydroxy compounds although for best high temperature properties aromatic rings are essential. The dihydroxy compounds may include within the structure diurethane linkages. Also, part of the structure may be replaced by siloxane linkage. These and other variations of polycarbonate structure are des-cribed in the Schnell reference cited above. The same reference presents a long list of monomers (particularly dihydroxy compounds) that may be used in polycarbonate synthesis.
(8-8) Graft CopolYmer of a MonoethYlenicallY Unsatur-ated Resin Forminq Monomer and EPDM TYpe Elastomers.
The blended polymer compositions of the present invention may contain a graft copolymer of a monoethylen-ically unsaturated resin forming monomer on an EPDM type of rubber. The monoethylenically unsaturated resin-form-ing monomers include monomers such as styrene, halo sty-rene, alpha-methyl styrene, para-methyl styrene, acrylo-nitrile, methacrylonitrile, acrylic acid, methacrylic acid, maleic anhydride, the lower (1-8 carbon atoms), alkyl esters of acrylic acid and methacrylic acid, etc.
Monomers of particular interest are styrene, methyl methacrylate, mixtures of styrene and acrylonitrile, mixtures of styrene and methyl methacrylate, etc.
The terpolymers or rubbery polymers comprise two different linear alpha-monoolefins and a non-conju-gated diene. One of the alpha-olefins is ethylene and the other is a higher alpha-monoolefin containing 3 to 16 carbon atoms such as propylene, 1-butene, 1-octene, etc. Examples of useful non-conjugated dienes include the 5-methylene-2-norbornene, 5-ethylidene-2-norbornene, 5-isopropylidene-2-norbornene, etc. The weight ratio of the ethylene to the higher alpha-monoolefin in the terpolymer is ordinarily within the range of from 20:80 to 80:20. The amount of diene should be such that the iodine number of the terpolymer is in the range of from about 15 to about 40, preferably from about 20 to about which corresponds generally to about 7 to 20 weight percent and preferably from 9 to 17 weight percent of the diene monomer units in the terpolymer.
The weight ratio of the monoethylenically unsaturated resin-forming monomer to the terpolymer is from about 95:5 to 30:7. In one embodiment, the resin forming monomer is polymerized in situ in the presence of the terpolymer. The specific example of a graft copolymer is a graft copolymer of styrene and acrylo-nitrile on ethylene-propylene-5-ethylidene-2-norbornene terpolymer wherein the terpolymer comprises 60 weight percent ethylene, 30 weight percent propylene and 10% of the norbornene monomer. Graft copolymers of the type useful in the present invention, and methods of prepar-ing such graft copolymers are described in, for example, U.S. Patent 4,202,948 and 4,l66,08l. Graft copolymers are commercially available such as from Dow Chemical Company under the trade designation "Rovel"*.
(B-9) Acryllc Polymers.
The blended polymer compositions of the present lnvention may contain acrylic polymers including acrylic polymers derived from acrylic esters and methacrylic esters. Generally acrylic polymers are based on methyl methacrylate monomer (MMA). The acrylic monomers may be * Denotes Trade Mark ~'' polymerized by free radical processes using peroxides.
MMA may be homopolymerized or copolymerized with other acrylates such as methyl or ethyl acrylate. Acrylic polymers which have been modified with various ingredi-ents also can be utilized, and these various ingredients include butadiene, styrene, vinyl and butyl acrylate which increase impact strength of the acrylics.
(B-10) Nitrile Resins.
Nitrile resins also may be used as the second polymer in the blended compositions of the present inven-tion. Nitrile resins or polymers based upon acryloni-trile, and the polymers have moderately high tensile properties, good impact properties when modified with rubber or oriented, good gas barrier properties, good chemical resistance and good taste and odor-retention properties.
The nitrile resins (B-10) are preferably those thermoplastic materials having an alpha,beta-olefinical-ly unsaturated mononitrile content of 50% by weight or greater. These nitrile barrier resins may be copoly-mers, grafts of copolymers onto a rubbery substrate, or blends of homopolymers and/or copolymers.
The alpha,beta-olefinically unsaturated mono-nitriles encompassed herein have the structure CH2=C(R)CN

where R is hydrogen, an alkyl group having from 1 to 4 carbon atoms, or a halogen. Such compounds include acrylonitrile, alpha-bromoacrylonitrite, alpha-fluoro-acrylonitrile, alpha-methacrylonitrile, alpha-ethacrylo-nitrile, and the like. The most preferred olefinically unsaturated nitriles in the present invention are acrylo-nitrile, methacrylonitrile and mixtures thereof.

~002695 These nitrile resins may be divided into sever-al classes on the basis of complexity. The simplest molecular structure is a random copolymer, predominantly acrylonitrile or methacrylonitrile. The most common example is a styrene-acrylonitrile copolymer. Block copolymers of acrylonitrile, in which long segments of polyacrylonitrile alternate with segments of polysty-rene, or of polymethyl methacrylate, are also known.
Simultaneous polymerization of more than two comonomers produces an interpolymer, or in the case of three components, a terpolymer. A large number of comonomers for the acrylonitrile are possible. These include lower alpha olefins of from 2 to 8 carbon atoms, e.g., ethylene, propylene, isobutylene, butene-1, pen-tene-1, and their halogen and aliphatic-substituted derivatives as represented by vinyl chloride, vinylidene chloride, etc.; monovinylidene aromatic hydrocarbon monomers of the general formula Ar-c(R1)=cH2 wherein R1 is hydrogen, chlorine or methyl and Ar is an aromatic group of 6 to 10 carbon atoms which may also contain substituents such as halogen and alkyl groups attached to the aromatic nucleus, e.g., styrene, alpha methyl styrene, vinyl toluene, alpha chlorostyrene, ortho chlorostyrene, para chlorostyrene, meta chlorosty-rene, ortho methyl styrene, para methyl styrene, ethyl styrene, isopropyl styrene, dichloro styrene, vinylnaph-thalene, etc. Especially preferred comonomers are iso-butylene and styrene.
Another group of comonomers are vinyl ester monomers of the general formula Z002~9S

R3C(H)=C(H)-OC(O)R3 wherein each R3 is independently selected from the group comprising hydrogen, alkyl groups of from 1 to 10 carbon atoms, aryl groups of from 6 to 10 carbon atoms including the carbon atoms in ring-substituted alkyl substituents; e.g., vinyl formate, vinyl acetate, vinyl propionate, vinyl benzoate and the like.
Similar to the foregoing and also useful are the vinyl ether monomers of the general formula H2C=C(H)-OR4 wherein R4 is an alkyl group of from 1 to 8 carbon atoms, an aryl group of from 6 to 10 carbon atoms, or a monovalent aliphatic radical of from 2 to 10 carbon atoms, which aliphatic radical may be hydrocarbon or oxygen-containing, e.g., an aliphatic radical with ether linkages, and may also contain other substituents such as halogen, carbonyl, etc. Examples of these monomeric vinyl ethers include vinyl methyl ether, vinyl ether ether, vinyl n-butyl ether, vinyl 2-chloroethyl ether, vinyl phenyl ether, vinyl isobutyl ether, vinyl cyclo-hexyl ether, 4-butyl cyclohexyl vinyl ether or p-chloro-phenyl glycol, etc.
Other comonomers are those comonomers which contain a mono- or dinitrile function. Examples of these include methylene glutaronitrile, (2,4-dicyano-butene-1), vinylidene cyanide, crotonitrile, fumarodi-nitrile, maleodinitrile.
Other comonomers include the esters of olefin-ically unsaturated carboxylic acids, preferably the lower alkyl esters of alpha,beta-olefinically unsatur-ated carboxylic acids and more preferred the esters having the structure C~2=C ( R1 ) COOR2 wherein R1 is hydrogen, a halogen, or an alkyl group having 1 or 2 carbon atoms and R2 is hydrogen or an alkyl group having from 1 to 8 carbon atoms. Compounds of this type include methyl acrylate, ethyl acrylate, methyl methacrylate, ethyl methacrylate, methyl alpha-chloroacrylate, and the like. Most preferred are methyl acrylate, ethyl acrylate, methyl methacrylate, ethyl methacrylate, butyl acrylate and butyl methacrylate.
Another class of nitrile resins are the graft copolymers which have a polymeric backbone on which branches of another polymer chain are attached or graft-ed. Generally the backbone is preformed in a separate reaction. Polyacrylonitrile may be grafted with chains of styrene, vinyl acetate, or methyl methacrylate, for example. The backbone may consist of one, two, three, or more components, and the grafted branches may be composed of one, two, three or more comonomers.
The methods of forming these various nitrile resins and examples of these resins can be found in the following U.S. Patents 3,325,458; 3,336,276; 3,426,102;
3,451,538; 3,540,577; 3,580,974; 3,586,737; 3,634,547;
3,652,731; and 3,671,607.
The chemical composition of the nitrile resins in general useful as resin (B-10) may be varied consi-derably, but in general, useful nitrile resins will include about 70% by weight of acrylonitrile monomer, 20 to 30% methyl acrylate or styrene as a comonomer and from 0 to about 10% butadiene as the impact-modifying termpolymer. Nitrile polymers of these types are offered commercially under the trade designation Barex* ;
resins supplied by BP Chemicals International.
(B-11) Acr~lic-Styrene-AcrYlonitrile PolYmers.
The blended polymer compositions of the present invention may contain one or more acrylic-styrene-acrylo-nitrile polymers. These terpolymers are often referred to as "ASA". The ASA polymers are generally similar to ABS resins with regard to properties. The type and amount of the monomers used to prepare these terpolymers may be varied, and the choice will be dependent in part on the properties desired. Various acrylic monomers, styrene monomers and acrylonitrile monomers can be used in various combinations. For example, alpha-methylsty-rene or methacrylonitrile also can be used. An example of a commercially available acrylic-styrene-acryloni-trile terpolymer is the polvmer available from General Electric Company under the designation Geloy. Other examples include an acrylic:styrene:methacrylonitrile terpolymer.
(s-12) AcrYlonitrile-Haloqenated PolYolefin-Stvrene Ter-polymers.
The blended polymer compositions of the inven-tion also may include at least one acrylonitrile-halogen-ated polyolefin-styrene terpolymer. These terpolymers often are referred to as ACS polymers when the halogen is chlorine. A commercially available example of such terpolymers is an acrylonitrile-chlorinated polyethyl-ene-styrene terpolymer which is available in three grades: flame retardant, weather resistant, and optical reflector. These terpolymers are manufactured by the Specialty Plastics Division of Showa Denko K.K.
* Denotes Trade Mark 2(~02695 (C) Compatibilizinq Aqent.
The polymer blends of the present invention also contain at least one compatibilizing agent which may be block copolymers selected from the group consist-ing of diblock, triblock, multiblock, starblock, poly-block or graftblock copolymers of a vinyl aromatic compound and a conjugated diene, or their partially hydrogenated derivatives and mixtures thereof. The choice of compatibilizing agent included in the blended lOpolymer compositions of the in~ention may depend upon the type of polymers (A) and (s) included in the blend.
In one preferred embodiment, the compatibiliz-ing agent is at least one multiblock, starblock, poly-block or graftblock copolymer with multiblock copolymers being particularly preferred. In another preferred embodiment, the compatibilizing agent is a multiblock copolymer as described above comprising at least about 40% by weight of styrene, and more often, from about 40 to about 75% by weight of styrene. Many of the charac-20teristics of the block copolymers can be varied and controlled by balancing between the hard (polystyrene) and rubber (polydiene) components, and utilizing linear or branched structures with different molecular weights.
Throughout this specification and claims, the terms diblock, t.riblock, multiblock, polyblock, and graft or grafted-block with respect to the structural features of block copolymers are to be given their normal meaning as defined in the literature such as in the Encyclopedia of Polymer Science and Engineering, 30Vol. 2, (1985) John Wiley & Sons, Inc., New York, pp.
325-326, and by J.E. McGrath in Block CopolYmers, Sci-ence TechnoloqY, Dale J. Meier, Ed., Harwood Academic Publishers, 1979, at pages 1-5. In particular, the ~0026~5 structure of the various block copolymers may be illustrated as follows:

Block Co~olymers diblock copolymer A-B or triblock copolymer A-B-A A ~
B-A-B ~,v,_----~4~~~-multiblock copolymer (A-B)n ~ ~ ~ n A
starblock copolymer3 B-A-X-A-B ~ ~-A ~
B ~3 graft- or grafted-block copolymer 8 2 hard -~ soft.
Sometimes designated segmented or poly block copoly-mers, n is >1.
3 X is a junction unit, also called radial block.

It will be understood that blocks A and B and C
may be either homopolymer or random copolymer blocks as long as each block predominates in at least one class of the monomers characterizing the blocks and as long as the A block is predominantly a vinyl aromatic compound and the B block is predominantly a diene or its hydrog-enated derivatives. The vinyl aromatic compounds which may be present in the block copolymers utilized in the present invention may be any of the vinyl aromtic compounds described above with respect to polymer component (B-1) and (B-2). Preferred vinyl aromatic compounds are styrene and alpha-methyl styrene with styrene being particularly preferred. The conjugated dienes may contain from 4 to 10 carbon atoms and more generally contain from about 4 to about 6 carbon atoms.
Butadiene and isoprene are particularly preferred conju-gated dienes useful in preparing the block copolymer compatibilizers useful in the present invention.
Partially hydrogenated block copolymer deriva-tives also are useful as compatibilizers in the polymer compositions of the present invention. The conjugated diene portion of the block copolymer is at least 90%
saturated and more often at least 95% saturated while the vinyl aromatic portion is not significantly hydrog-enated. More particularly useful hydrogenated block copolymer is the block copolymer of polystyrene-polyiso-prene-polystyrene which has been hydrogenated to a polystyrene-poly(ethylene/propylene)-polystyrene block polymer. When a polystyrene-polybutadiene-polystyrene block copolymer is hydrogenated, it is desirable that the 1,2-polybutadiene to 1,4-polybutadiene ratio in the polymer is from about 30:70 to about 70:30. When such a block copolymer is hydrogenated, the resulting product resembles a regular copolymer block of ethylene and butene-1 (EB). As noted above, when the conjugated diene employed as isoprene, the resulting hydrogenated product resembles a regular copolymer block of ethylene and propylene (EP).
Hydrogenation of the precursor block copolymers can be effected by known techniques such as by the use of a catalyst comprising the reaction product of an aluminum alkyl compound with nickel or cobalt carboxyl-ates or alkoxides under conditions which result in substantial complete hydrogenation of at least 80% of the aliphatic double bonds while hydrogenating 25% of the vinyl aromatic double bonds remaining in the poly-mer. Preferred hydrogenated copolymers of those wherein at least 99% of the aliphatic double bonds are hydrogen-ated while less than 5% of the aromatic double bonds are hydrogenated.
The average molecular weights of the individual blocks within the copolymers may vary within certain limits. In most instances, the vinyl aromatic block will have a number average molecular weight in the order of about 5000 to about 125,000, and preferably between about 7000 and 60,000. The conjugated diene blocks either before or after hydrogenation will have number average molecular weights in the order of about 10,000 to about 3C0,000 and more preferably from about 30,000 to 150,000. The total number average molecular weight of the block copolymers is typically in the order of about 25,000 to about 250,000.
Specific examples of diblock copolymers include styrene-butadiene, styrene-isoprene, and the hydrogen-ated derivatives thereof. Examples of triblock polymers include styrene-butadiene-styrene, styrene-isoprene-sty-rene alpha-methylstyrene-butadiene-alpha-methylstyrene, alpha-methylstyrene-isoprene-alpha-methylstyrene, and their partially hydrogenated derivatives. The diblock and triblock polymers are commercially available from a variety of sources under various tradenames. Examples of commercially available diblock resins include Sol-prene* 314D (Phillips) and K Resin 04 (Phillips). A
number of styrene-butadiene-styrene triblock copolymers are sold by the Shell Chemical Company under the trade-marks "Kraton* 2103", "Kraton* 2104", and "Kraton*2113".
Such thermoplastic rubbery block copolymers are made by * Denotes l'rade Mark B~

anionic polymerization, and the above three identified Shell Kratons differ in molecular weight and viscosity, and also in the ratio of butadiene to styrene. For example, "Kraton 2103" and "Kraton 2113" have a styrene to butadiene ratio of 28:72 while "Kraton 2104" as a styrene to butadiene ratio of 30:70. Blends of diblock and triblock copolymers are also available. Kraton 1118 (Shell) is a blend of SB diblock and SBS triblock copoly-mers. A Kraton G-1652 is a hydrogenated SBS triblock comprising 30% styrene end blocks and a midblock equiva-lent to a random copolymer of ethylene and 1-butene (EB). This copolymer is sometimes designated as SEBS.
Functionalized block copolymers such as those obtained by reacting a block copolymer with maleic anhydride also are useful in this invention. Kraton FG
1901X is a maleated SEBS block copolymer available from Shell.
Multiblock copolymers of styrene and either isoprene or butadiene also are commercially available.
Commercially available and preferred styrene-butadiene multiblock copolymers include Stereon*840A, Stereon*841A
and Stereon* 845A which are available from The Firestone Tire & Rubber Company.
Starblock copolymers of styrene and isoprene or styrene and butadiene are commercially available from Phillips Petroleum Company under such designations as "K-Resin". Generally, the K-Resins have a high polysty-rene content such as about 75%, and these resins are transparent and rigid. One particularly preferred star-block copolymer is K-Resin KR03 from Phillips. A
similar material (75% styrene:25% butadiene) is avail-able from Fina under the designation "Finaprene*520".
Radial or starblock copolymers also are available from * Denotes Trade Mark Fina under the general designation "Finaprene SBS
Polymer1'. Various grades are available containing from 20% to 40% of styrene.
The relative amounts of the two or more poly-mers and compatlbilizers utilized in the blended polymer compositions of the present invention may vary over a relatively wide range depending on the specific mater-ials used, the desired properties, and particular end use for the blended polymer compositions of the inven-tion. Thus, the blended polymer compositions of the present invention may comprise (A) from 1 to about 99% by weight of at least one olefin polymer;
(s) from 1 to about 99% by weight of at least one styrenic polymer or any of the polymers and polymer blends identified herein as components (s-1) through (B-12); and (C) from 1 to about 40% by weight and more generally from 1 to about 15% of the compatibilizer.
In one embodiment of the invention, the compositions of the present invention comprise from about 49 to about 90% by weight of polyolefin (A), 10 to about 30~ of the polymer or polymer blend (B-1) through (B-12), and from about 2 to about 10% by weight of the compatibilizing agent.
Generally, the order of mixing of the polymers (A) and (B) and the compatibilizers (C) is not critical.
Accordingly, it is possible to mix the compatibilizer with the polyolefin and other polymers by mixing all of the components at the same time. Alternatively, the order of mixing can be varied in order to match the relative viscosities of the various components. The blended polymer compositions of the present invention 20~269S

may be true blends of the polymers and compatibilizers, or some grafting of the compatibilizers to either or both of the polymers or another compatibilizer are possible.
The blended polymer compositions of the present invention may contain, in addition to the components identified above as components (A), (s) and (C) other components added to modify the properties of the blended polymer composition. The blended polymer compositions of the invention may be compounded further with other polymers (e.g., barrler resins), oils, fillers, coupling agents, reinforcements, antioxidants, stabilizers, fire-retardants, foaming agents, colorants, processing aids, etc. Such additives are selected to provide or modify desirable characteristics of the products prepared from the compositions.
(D) sarrier-Resins.
The blended polymer compositions of the present invention may contain at least one resin referred to in the art as a barrier resin. Barrier resins are charac-terized as having low gas and vapor transmission proper-ties. Any of the known barrier resins may be utilized as component (D) in the blended polymer compositions of the present invention. Particular examples of useful barrier resins (D) include resins selected from the group consisting of vinylidene chloride polymers, and copolymers of vinylidene chloride with one or more mono-ethylenically unsaturated monomers which are copoly-merizable with the vinylidene chloride; copolymers of ethylene and vinyl alcohol (EVOH), polyamides, and nitrile resins comprising alpha,beta-olefinically unsat-urated aliphatic mono-nitrile polymers and copolymers.
When utilized in the blended polymer compositions of the invention, the barrier resin (D) generally is present in amounts of from 0.1 to about 20% by weight based on the total weight of polymer and resin. It should be noted that polymer (s-10) has previously been described as a nitrile resin. Thus, when the blended polymer composi-tions include a nitrile resin (B-10) as the second poly-mer (B), it is generally not necessary to add additional nitrile resin as a barrier component, and it may not be necessary to add any additional barrier resin to the blended polymer composition.
Vinylidene chloride polymers and copolymers are useful barrier materials. Copolymers are particularly useful and these include copolymers having polymerized therein vinylidene chloride in an amount of from about 40 to about 98% by weight and at least one monoethylenic-ally unsaturated monomer which is copolymerizable with the vinylidene chloride in an amount of from about 60~
to about 2% by weight. The copolymerizable monomer may be a vinyl functional monomer such as vinyl chloride;
alkyl esters of acrylic and methacrylic acids such as alkyl acrylates and alkyl methacrylates; ethylenically unsaturated mono- and dicarboxylic acids such as acrylic acid, methacrylic acid, and itaconic acids; and cyano-functional monomers such as acrylonitrile and methacrylo-nitrile.
Ethylene vinyl alcohol copolymers (EVOH) that are useful as barrier resins in the compositions of the present invention generally will contain at least about 55% and as much as 80% by weight of vinyl alcohol, and the remainder of the molecule consists essentially of ethylene. These copolymers generally are prepared by hydrolysis of ethylene vinyl acetate copolymers, and, therefore, some vinyl acetate may remain in the resin.

The EVOH copolymers typically have molecular weights in the range of from about 20,000 to 30,000. The EVOH
copolymers useful as barrier resins in the compositions of the present invention are commercially available such as from the EVAL Company of America.
Polyamides may also be incorporated into the blended polymer compositions of the present invention to serve as barrier compositions. The polyamides are condensation products which contain recurring aromatic and/or aliphatic amide groups in integral parts of the main polymer chain. Such polyamide products are known generically as "nylons". These polyamides may be pre-pared by polymerizing a monoamino carboxylic acid or an internal lactam thereof having at least 2 carbon atoms between the amino and the carboxylic acid groups. Alter-natively, the polyamides may be obtained by a polymeriz-ing dicarboxylic acid with a diamine which contains at least 2 carbon atoms between the amino groups. Another procedure for preparing polyamides is to polymerize a monoamino carboxylic acid or an internal lactam thereof with a substantially equimolar portion of a diamine and a dicarboxylic acid. Examples of amino carboxylic acids and lactams include epsilon-amino caproic acid, butyro-lactam, pivalolactam, caprolactam, capryllactam, undec-anolactam and 3- and 4-aminobenzoic acids. Examples of diamines include diamines containing up to 16 carbon atoms such as trimethylenediamine, tetramethylenedia-mine, pentamethylenediamine, octamethylenediamine, decamethylenediamine, hexadecamethylenediamine and in particular, hexamethylenediamine. Aromatic amines such as p-phenylenediamine, 4,4'-diaminodiphenylsulfone, etc., may be utilized.

The dicarboxylic acids used to form the nylons may be aromatic, for example, isophthalic or terephthal-ic acids or aliphatic dicarboxylic acids represented by the formula HOOCYCOOH wherein Y represents a divalent aliphatic group containing at least 2 carbon atoms.
Examples of such aliphatic dicarboxylic acids include sebacic acid, octadecanoic acid, suberic acid, azelaic undecanedioic acid, glutaric acid, pimelic acid, and especially adipic acid. Specific examples of polyamides l~ useful as barrier compounds in the present invention include:
polyhexamethylene adipamide (nylon 6:6), polypyrrolidone (nylon 43, polycaprolactam (nylon 6), polyheptolactam (nylon 7), polycapryllactam (nylon 8), etc.
The number average molecular weights of the polyamides used in the polymer blends of the present invention are generally above about 10,000.
The nitrile barrier resins may be any of the resins identified earlier as polymer (s-10).
Commercial examples of nitrile barrier resins include BAREX~ 210 resin by BP Chemicals International, an acrylonitrile-based high nitrile resin containing over 65~ nitrile, and Monsanto's LOPAC0 resin containing over 70% nitrile, three-fourths of it derived from methacrylonitrile.
(E) Fillers and Fibers.
The blended polymer compositions of the present invention may contain one or more fillers of the type used in the polymer art. Examples of fillers employed in a typical compounded polymer blend according to the present invention include talc, calcium carbonate, mica, wollastonite, dolomite, glass fibers, boron fibers, carbon fibers, carbon blacks, pigments such as titanium dioxide, or mixtures thereof. Preferred fillers are a commercially available talc such as R.T. Vanderbilt's Select-O=~orb and glass fibers. The amount of filler and fibers included in the blended polymers may vary from about 1% to about 70% of the combined weight of polymer and resin. Generally amounts of 5% to 30% are included.
The fillers and fibers may be treated with coupling agents to improve the bond between the fillers and fibers to the resin. For example, the fillers can be treated with materials such as fatty acids (e.g., stearic acid), silanes, maleated polypropylene, etc.
The amount of coupling agent used is an amount effective to improve the bond between the fillers and fibers with the resin.
The blended polymer compositions of the present invention comprising the olefin polymer, the second poly-mers as described herein as components (B-1) through (B-12), the compatibilizer (C) and other resins such as barrier resins and additives can be prepared by tech-niques well known to those skilled in the art. For exam-ple, a particularly useful procedure is to intimately mix the polymers using conventional mixing equipment such as a mill, a Banbury, a Brabender, a single or twin screw extruder, continuous mixers, kneaders, etc. For example, the polymers may be intimately mixed in the form of granules and/or powder in a high shear mixer.
One preferred process for preparing the blended polymers utilizes the Farrell Continuous Mixer (FCM), CP-23.
Short residence times and high shear are readily obtained in a CP-23. "Intimate" mixing means that the mixture is prepared with sufficient mechanical shear and thermal energy to produce a dispersed phase which is finely divided and homogeneously dispersed in the continuous or principal phase.
Improved mixing is often obtained when the viscosities of the olefin polymer (A) and polymer (B~
are similar at the temperature and shear stress of the mixing process. The chance for formation of cocontin-uous interlocking networks on cooling is increased when approximately equal molar ratios of polymers (A) and (B) are utilized; for example a 50:50 molar ratio of styrene maleic anhydride copolymer and polyolefin.
The polymer blends of the present invention are characterized as having excellent heat distortion proper-ties as well as excellent strength, toughness, stiff-ness, gloss, ease of processing and fabrication, improv-ed filler interaction, and shrinkage characteristics, hardness, adherability, moldability, formability, and they are retortable and microwaveable. Another advant-age of the blended polymer compositions of the presentinvention is that they can be recycled in conventional procedures whereby the scrap is comminuted and dry-blended or extrusion-blended with fresh blended polymer, and the polymer blended with scrap does not lose its desirable properties. Accordingly, in one embodiment, the blend of fresh or virgin blended polymers of the invention and scrap polymer is extruded into a sheet which can be used in a multilayer structure, preferably as an inner layer, with sheets of virgin blended poly-mers of the invention, and/or other layers of, e.g.,barrier materials, polyolefins, aliphatic or aromatic polyolefins, etc. The blends of fresh and scrap polymer blends of the invention also can be coextruded into ~o--multilayer structures with any of the other polymer materials discussed above.
In some instances, the low temperature impact strength of materials prepared from the blended polymer compositions of the present invention is improved when compared to the typical performance of olefin polymers such as polyethylene and polypropylene, and, therefore, the blended polymer compositions of the present inven-tion possess the required low temperature impact perform-ance and other physical characteristics required for many applications for which polyolefins cannot be used.
The polymer blends of the present invention also exhibit excellent food, oil and fat-resistance and are therefore particularly suited for packaging food products. The polymer blends of the invention can be formed into pack-ages, containers, cups, and other products.
It also has been observed that the blended polymer compositions of the present invention can be processed into shaped articles by extrusion, coextru-sion, ther~oforming, blow molding, injection molding, compression molding, calendering, laminating, stamping, pultrusion, foaming or die coating of continuous fibers.
In particular, shaped articles can be prepared by thermo-forming sheets of the blended polymer compositions of the present invention. Sheets of the blended polymer compositions of the present invention can be prepared on an extruder such as a 3.5-inch HPM extruder with a two-stage screw of 30:1 L/D ratio and at a melt temperature of about 445F (230C). The extrudate is subsequently passed through polished rolls with a center roll heated to an elevated temperature to form a sheet which exhi-bits low sag since the polymers are appropriately compat-ibilized. The blended polymer compositions of the ;~00269S

invention also can be used to form an extrusion coating on lony fiber reinforcements such as used in long fiber reinforced thermoplastics.
Scrap material produced from processing of the blended polymer compositions of the present invention such as scrap material produced from thermoforming the multilayer structures of the present invention, may be recovered, reground and recycled for use as a component in the polyolefin-containing layer of the multilayer structures. Such scrap material may contain components from the various layers including the polyolefin-contain-ing layer and barrier layer when present. The amount of scrap utilized in the polyolefin-containing layer may vary widely, and may comprise from 1 to about 99% by weightj and more preferably from about 10 to about 60%
by weight of the polyolefin-containing layer.
In one embodiment of the present invention, thermoformable multilayer structures can be prepared which comprise (I) at least one layer of a blended polymer composition according to the present invention; and (II) at least one layer of an olefin polymer composition which may comprise any of the olefin poly-mers and olefin copolymers mentioned previously. In a preferred embodiment, the layer of olefin polymer compo-sition is a layer of filled or unfilled polyethylene or polypropylene.
In another embodiment, the multilayer structure may comprise (III) at least one layer of a barrier resin such as the high nitrile barrier resins described above.
Thus, in one embodiment, a thermoformable multilayer structure may comprise a layer of the polymer blend composition of this invention and a cap layer on one side of an olefin polymer such as polyethylene or polypropylene or a cap layer of a barrier material (D~
as described above, or a cap layer of an aliphatic or aromatic vinyl resin such as polystyrene or polymers and copolymers of acrylic esters and acrylonitrile. In another embodiment a multilayer structure comprises a central layer of the polymer blend composition of the present invention, a cap layer on one side comprising an olefin polymer such as polyethylene or polypropylene and a cap layer on the other side of a barrier material, or vinyl polymer.
The cap layers such as the layers of barrier resin, vinyl polymers, etc., can be applied by coextru-sion, laminating, etc., or the second layer can be applied from a solution or a dispersion of the barrier resin or vinyl polymer in water or an organic liquid such as acetone. On drying, a film or cap layer is left on the layer comprising the composition of the inven-tion.
Molded articles having desired shapes can be produced from each of the blended polymer compositions of the present invention by (A) Eeeding a sheet of the blended polymer composition of the invention to a heating station;
(B) heating the sheet to its softening point;
and (C) feeding the softened sheet to a forming station where it is molded înto articles of the desired shape.
In another embodiment, coextruded multilayered structures can be prepared wherein at least one layer comprises the blended polymer compositions of the pre-sent invention. In other embodiments, at least one additional layer comprises a polyolefin such as poly-ethylene or propylene.
Various features and aspects of the present invention are illustrated further in the examples that follow. While these examples are presented to show one skilled in the art ~how to operate within the scope of this invention, they are not to serve as a limitation on the scope of the invention where such scope is only defined in the claims. Moreover, in the following examples, preparation of blends, compounds, injection molded specimens, mono layer or laminated sheets are illustrated. These examples serve merely as illustra-tive embodiments of the present invention and are not to be considered limiting.
Unless otherwise indicated in the following examples and elsewhere in the specification and claims, all parts and percentages are by weight, temperatures are in degrees centigrade and pressures are at or near atmospheric. The physical properties described in the following examples are measured in accordance with ASTM
Standard Test Procedures as identified in the following Table 3.

20026~5 Property ASTM Method Melt Flow Rate D-1238*
Tensile Strength D-638 Elongation D-638 Flexural Strength D-790 Flexural Modulus (tangent) D-790 Izod Impact (notched) D-256**
Izod Impact (unnotched) D-256 Gardner Impact D-3209 Heat Deflection Temperature D-648 Instrumented Impact D-3763 * Condition 230C/2.16 kg.
** Method A.
Example 1 The compatible blend of polypropylene (PP), a styrene maleic anhydride copolymer (SMA) and a multi-block styrene-butadiene copolymer (SBR) is prepared on a laboratory Banbury mixer (Farrel) at about 155C, ground and injection-molded ('Van Dorn 110' at about 230C
stock temperature) into test specimens. The make-up of the composition and its properties are summarized in Table 4. A control is also summarized.

~002695 Composition* Control Example 1 Himont Profax 6523 (PP) 100 87.5 Arco Dylark 332 (SMA) --- 10.0 Phillips K-Resin KR03 (SBR) --- 2.5 Properties Melt Flow g/10 min. (Cond. L) 4.5 4.1 Tensile Strength, psi 4990 5070 Flexural Modulus, psi 230,000 274,000 Flexural Strength, psi 7360 8490 Notched Izod Impact, ft.lb./in~ 0.52 0.74 Gardner Impact, (RT) in.lb. 21 16 HDT at 66 psi, C 84 104 Linear Shrinkage, in./in. % 1.6 1.3 * % by weight.

In addition, the molded specimens of Example 1 have excellent surface characteristics with respect to appearance and hardness.
Example 2 A blended polymer composition in accordance with the present invention is prepared on a Farrel Continuous Mixer (FCM), CP-23 at a mixer speed of 1000 rpm and extruded at about 220C into strands which are passed through a water bath prior to pelletizing. The pellets are injection molded (220C stock temperature and 30C mold temperature) into test specimens. The makeup of the composition and its physical properties are summarized as follows:

2~)02695 TAsLE 5 Composition ~/wt.
Shell 7C06 (PP copolymer) 52.45 Arco Dylark 332 (SMA) 20.00 Firestone Stereon 840A (SBR) 5.00 RT Vanderbilt Select-O-Sorb (talc) 20.00 CR-834 (TiO2) 2.50 Ciba~Geigy Irganox 1010 (Stabilizer) 0.05 Properties Melt Flow, g/10 min. 2.0 Tensile Strength, psi 4036 Flexural Modulus, psi 373,000 Flexural Strength, psi 5967 Izod, Notched, ft.lb./in. 0.71 Izod, Unnotched, ft.lb./in. 8.40 Gardner Impact, in.lb. 27 HDT at 66 psi, C 118 Linear Shrinkage, in./in. % 0.7 In addition to the high-heat distortion tempera-ture and low shrinkage characteristics of the above com-pound, the molded specimens also exhibit high gloss and scratch resistant surface characteristics.
Example 3 A sheet is formed from the composition prepared in Example 2 on a 3.5-inch HPM extruder, with a two-stage screw of 30:1 L/D ratio and at a melt temperature of about 230C. The extrudate is passed through polish-ed rolls with a center roll temperature of about 94C to form a sheet which is 48 inches wide. The sheet is cut into about 12-inch squares and the squares are then fed to a CAM thermoformer. When the squares are heated to their softening point, they are advanced to a forming station where the squares are molded into the shape of a cup by a pressure-forming technique. The resulting cups are excellent in appearance and detail. The excellent thermoformability of the composition of Example 2 is similar to that obtained by commercial styrenics, and the talc-filled cups have superior gloss characteristics compared to a typically filled polypropylene compound.
Example 4 An extruded sheet prepared as in Example 3 with the composition of Example 2 is laminated on both sides with the polypropylene and/or a 20% talc-filled polypro-pylene sheet and subsequently thermoformed into cups in a single operation. The cups exhibit good adhesion between the layers of sheets, and the cups are of high quality.
Examples 5-9 Blends containing polypropylene, styrene maleic anhydride copolymer, talc and Phillips K-Resin KR03 (a multiblock copolymer) are prepared in a Banbury mixer (Farrel) at about 55C and extruded at about 220C into strands which are passed through a water bath prior to pelletizing. The pellets are injection-molded (220C
stock temperature) into test specimens. Table 6 identi-fies the various compositions of Examples 5-9 and a con--trol sample identified as Control-2. Properties of these reinforced compositions also are listed in the table.

o .. C~ ~ C~ V~
cn ¦ N O O N .J 1~1 r- ~ O
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a~ o N C
EI ~ N ~ I~ ~ d 1~1 ~~
v ~1 N
O Nl cn r~ I cno v . ~ ~ ~ O ~
¦ 1~`1N ~ID .-- ~ " ) ~ O
~D

~O N~ 1 c:n ~ o ~1 u~
L O + ¦ Il~
cC I CO C~ O ~ O
N

O O
c o .- cn O oo I I . o ~^V U~
C_~ CO N I I ~-- ~ N (~

O r C o C~
c V
C~ 0 N r E C Vl CD
0 C~ ; 0 N ~Y ~ 0 ~ ~ 0 U~ ~ O v~
O ~c~.~ L L r- C ~D . +' L
CL_ ~~ O ~ O C O ~I 0 ~ ~L~~O ~ c c ~ c _ X(D L_C L ~ 0 0 0 C O ~

As can be seen from the results summarized in Table 6, the blended compositions of the present inven-tion exhibit superior linear shrinkage, modulus and tensile strength compared to Control Example 2.
Examples 10-12 Blended polymer compositions in accordance with the present invention are prepared utilizing the general procedure of Example 2 and with the components identi-fied in the following Table 7. Examples 11 and 12 contain mixtures of two different compatibilizers and Example 12 also contains EVOH as a barrier polymer component. The properties of the blended polymer compo-s~tions of Examples 10-12 are summarized in Table 7.

Example 1~ 12 Shell 7C06 (PP copolymer) 75.45 65.45 43.95 Arco Dylark 332 (SMA) 9.60 9.60 14.50 Cain talc 4590 (talc) 10.00 10.00 15.00 White Pigment (TiO2) 2.50 2.50 2.50 Irganox*1010 (Stabilizer) 0.05 0.05 0.05 Firestone Stereon 840A (SBR) 2.50 2.40 3.70 Shell Kraton G 1652 (SEBS) --- 10.00 10.00 EVOH Copolymer --- --- 10.00 Pro~erties Melt Flow, g/10 min 1.5 1.5 1.0 Tensile Strength, psi 3840 3262 3265 Flexural Strength, psi 5334 4081 4477 Tangent Modulus, Kpsi 2.54 1.89 2.35 Izod, Notched, ft.lb./in. 1.07 2.4 0.75 Izod, Unnotched, ft.lb./in. 12.57 --- 7.99 HDT at 66 psi, C 93 89 92 Linear Shrinkage, in/in % 1.0 0.8 0.6 * Denotes Trade Mark l ~,, ~ i, zooz6gs Example 13 A two-layer laminate is prepared in the follow-ing manner. A 40 mil sheet of the composition of Exam-ple 2 is prepared by extrusion. To this sheet of Exam-ple 2 there is heat laminated a 12 mil polypropylene cap layer (Shell 7C06). The original sheet prepared from the product of Example 2 and the two layer laminate are evaluated for impact strength in an Instrumented Impact Tester, (Rhemetrics Model RDT-S000). This test provides information on the amount of force (in pounds) required to rupture the test specimen at a certain preset velo-city of a falling weight. The rating for the sheet - prepared with the product of Example 2 is 64.7 pounds, and the value for the laminate is 144.2 pounds, a signi~icant increase. Improved Gardner gloss also is observed. The Gardner gloss measured at a 60 angle.
For the laminate, the Gardner reading is 61 on the Example 2 sheet side and 76 for the polypropylene side. In addition, taste and odor characteristics of the two-layer laminate is better with respect to the monolayer sheet.
Examples 14-15 These examples illustrate the use of a poly-ethylene/polypropylene mixture as the polyolefin in the compositions of the invention. The blends are prepared in accordance with the general procedure of Example 2 utilizing the ingredients and the amounts identified in Table 8. The properties of the blended polymer composi-tions thus obtained are also summarized in Table 8.

;~002695 Inqredients Example 14 ExamPle 15 Shell 7C06 52.5 47.4 Dylark 332 20.0 20.0 Stereon 840A 5.0 5.0 Cain (HDPE) 7030 --- 5.0 Select-A-Sorb 20.0 20.0 TiO2 (CR 834) 2.5 2.5 Properties Flexural Strength, psi 7310 7110 Flexural Modulus, Kpsi 391 357 HDT at 66 psi, C 117 115 Gardner Impact, in.lb. 14 21 Shrinkage, in./in. % 0.65 0.59 The properties show improved impact for Example 15 without loss of other desirable properties.
Examples 16-18 These examples illustrate the use of multi-block, linear triblock and hydrogenated triblock copoly-mers. In this example, the blends are processed on a Leistritz counter-rotating, twin-screw, and injection molded. The types and amounts of polymers blended in these examples are summarized in the following Table 9.
Some of the mechanical properties of the blended poly-mers also are summarized in the table.

Inqredients Example 16 Example 17 ExamPle 18 Profax 6523 76 76 76 Dylark 332 19 19 19 Stereon 840A 5 -- --Kraton D1102 -- S --Kraton G1652 -- -- 5 Properties Flexural Modulus, Kpsi 280 264 247 Gardner Impact, in.lb. 17.4 4.2 4.0 The results summarized in Table 9 demonstrated the multi-block styrene butadiene copolymers provide better impact/modulus balance than the triblock copolymers.
Examples 19-20 These examples illustrate the use of impact-modified styrene maleic anhydride copolymers in the blended polymer compositions of the present invention.
The blends were processed in accordance with the general procedure of Example 2 and molded. The composition of the formulations of these two examples and some of these properties are summarized in the following Table 10.

In~redients Example 19 Example 20 Aristich 4O40F1 52.4 52.4 Dylark 332 12.5 --Dylark 238 -- 12.5 Stereon 840A 12.5 12.5 Select-A-Sorb 20 20 TiO2 (CR 834) 2.5 2.5 B-2252 0.1 0.1 Properties Flexural Modulus, Kspi 223 228 Izod Impact, notched (ft.lb./in.) 1.8 2.2 Gardner Impact,in.lbs.
at RT 143 288 at -20C 112 125 Linear Shrinkage, in./in., % 0.7 0.7 2 A polypropylene copolymer from Aristich.
A stabilizer from Ciba-Geigy.
Examples 21-22 These examples illustrate the use of another impact-modified styrene maleic anhydride copolymer in a formulation containing talc. A control formulation also is prepared which does not contain a compatibilizer.
The blends are prepared on a Banbury mixer and injection molded (Van Dorn) by the general procedure of Example 1. The formulations and some of the properties obtained from the blended formulations are summarized in the following Table 11.

Inqredients Control-3 ExamPle 21 Example 22 Exxon PD 7132 (PP) 60 57 55 Arco Arvyl 300 MR 20 20 20 Stereon 840 -- 3 --Jet Fill 500 (talc) 20 20 20 Phillips KR03 -- -- 5 Properties Melt Flow, g/10 min (Cond. L) 1.4 1.0 1.3 Tensile Strength, psi 3460 3550 3810 Flexural Strength, psi 6300 6440 6870 Flexural Modulus, Kpsi 348 338 352 Notched Izod Impact ft.lb./in. 0.7 1.0 1.0 HDT at 66 psi, C 115 110 106 Gardner Impact (RT) in.lbs. 5 21 23 Linear Shrinkage in./in. % 0.69 0.65 0.59 The above results demonstrate the improved impact strength obtained when compatibilizers in accordance with the present invention are included in the formula-tions.
Example 23 This example illustrates the use of a high-den-sity polyethylene as the polyolefin. Control-4 does not contain the compatibilizer. The formulation of Example 23 and of Control-3, and some of the properties of the blended formulations are summarized in the following Table 12.

Inqredients Control-3 Exam~le 23 Cain 7820 59.9 56.2 Cain 7040 20.0 18.7 Dylark 332 20.0 20.0 Stereon 840 -- 5.0 B-225 Stabilizer 0.1 0.1 Properties Flexural Strength, psi 6764 6042 Flexural Modulus, Kpsi 214 203 HDT at 66 psi, C 97 97 &ardner Impact 1 RT ), in.lbs. 9 28 Linear Shrinkage in./in. % 1.34 1.27 The above results demonstrate the improved linear shrinkage and Gardner impact properties obtained when the compatibilizer is included in the blend.
Examples 24-25 These examples illustrate the use of functional-ized block copolymers such as maleated styrene-butadi-ene-styrene triblock copolymers. The blends are prepared in a twin screw extruder and molded. The formulations of Examples 24 and 25 and some of the properties of the blends are summarized in the following Table 13.

Inqredients Example 24 Examvle 25 Profax 6523 85.5 85.5 Dylark 332 9.5 9.5 Kraton G1652 5 --Kraton FG1901X -- 5 Properties Flexural Modulus, Kpsi 220 223 HDT at 66 psi,C 96 109 Gardner Impact (RT) in.lb. 14.7 29 The above results demonstrate that the maleated triblock copolymer FG1901X provides improvements with respect to Gardner impact and HDT when compared to non-functionalized SBS.
Examples 26-27 These examples illustrate the use of Barex, a barrier resin in the formulations of the present inven-tion. The polymer blend is prepared in a twin screw extruder and molded. The formulation and some of the properties of the blended formulation are summarized in the followin~ Table 14.

InqredientsControl-5 Example 26 Example 27 Profax 6523 76 76 76 Dylark 332 19 19 19 Stereon 840A -- 3 5 Barex 210 5 2 --Properties Flexural Modulus, Kpsi 282 251 235 Gardner Impact (RT) (in.lb.) <2 8.0 11 .6 Linear Shrinkage, in./in. % 1.07 1.10 1.11 Oxygen Permeation,***
cc/m2/day 539* 593* 703**
* 8 mil sheet ** 7 mil sheet *** at 0% relative humidity and 25C
The above results demonstrate that the addition of a small amount of Barex of the composition of this invention (Example 26) significantly improv~s the oxygen impermeability.
Foams of the blended polymer compositions of the present invention may be prepared by mixing low boiling foaming agents with the blended polymer composi-tions at a temperature above the softening point of the polymer temperature and under a pressure which prevents foaming of the mixture, followed by extrusion of the foamable mixture into a zone of lower pressure wherein the foamable mixture foams to provide the desired foamed body. Particularly suitable foaming agents include halo-hydrocarbons containing 1 or 2 carbon atoms such as methyl chloride, ethyl chloride, etc. Low boiling hydro-carbons also are suitable, and these include propane, butane, pentane, etc. Mixtures of the above described blowing agents also can be used. The amount of blowing agent included in the foamable compositions is from about 5 to about 30% by weight based on the total weight of the blended polymer composition of the invention.
The foamed articles prepared in this manner may be semi-rigid to rigid foams having densities of from 10 to about 200 g/l. By varying the temperature during extrusion of the foamable mixture, and by varying the expanding agent used, the foams produced have varying properties of open and closed cells. The foams are particularly useful in the building industry and as insulation.
Other uses for the blended polymer compositions of this invention include refrigeration parts such as inner liners, inner door panels, inner gaskets and trim, trays and shelves, etc. The blended polymers are useful in preparing parts for: the automotive industry;
communications such as telephones, ratio, TV, cassettes, etc.; power tools; appliances; business machines; toys;
furniture; etc. The properties of the blended polymer compositions of this invention can be varied to satisfy the requirements of these different applications.
While the invention has been described and illustrated with reference to certain preferred embodi-ments thereof, those skilled in the art will appreciate that various changes, modifications and substitutions can be made therein without departing from the spirit of the invention. For example, processing and molding tech-niques other than those preferred as set forth herein-above may be applicable due to variations in the desired end product and uses, etc. Moreover, the specific results observed with respect to the physical properties may vary depending on the specific polymers and formula-tions selected and whether same are used alone or in combination with each other, i.e., mixture, or other known agents. Accordingly, such expected changes and variations in results are contemplated in accordance with the objects and practices of the present invention.
It is intended therefore, that the invention be limited only by the scope of the claims which follow.

Claims (7)

1. A polymer composition comprising:
(a) from 1% by weight to 99% by weight polypropylene;
(b) from 1% by weight to 99% by weight of a copolymer of styrene and maleic anhydride; and (c) from 1% by weight to 15% by weight of a compatibilizing agent comprising a multiblock styrene-butadiene copolymer.

2. A polymer composition as set forth in Claim 1, wherein said polypropylene comprises a homopolymer of polypropylene.

3. A polymer composition s set forth in Claim 1, wherein said polypropylene comprises a copolymer of polypropylene.

4. A polymer composition as set forth in Claim 1, wherein said multiblock copolymer comprises from 40% to 75% by weight styrene.

5. A copolymer composition as set forth in Claim 1, wherein said composition further includes:
(a) at least one filler, fibre or mixture thereof.

6. A polymer composition as set forth in Claim 5, wherein said filler is talc or calcium carbonate and said fibre is a glass fibre.

7. A polymer composition as set forth in Claim 1, wherein said composition comprises from 49% by weight to 90% by eight of said polypropylene, from 10% by weight to 30% by weight of said copolymer of styrene and maleic anhydride, and from 2% by weight to 10% by weight of said multiblock styrene-butadiene copolymer.