Core-shell impact modifier for amorphous aromatic polyester

Abstract: Impact modifiers which produce transparent, high notched Izod impact strength blends with amorphous, aromatic polyesters are described. The impact modifiers are core-shell polymers with cores comprised mainly of rubbery polymers of diolefins and vinyl aromatic monomers and shells comprised mainly of styrene copolymers (e.g. styrene and hydroxyalkyl (meth)acrylate).

Description: The invention is concerned with impact modifiers which may be used to improve the notched impact resistance, while maintaining clarity of, amorphous aromatic polyester resin (hereafter referred to as polyester). The impact modifiers contain rubbery polymer and polymer containing a hydroxyl group. Polyesters (e.g., polyethylene terephthalate and polybutylene terephthalate) exhibit various excellent properties such as resistance to temperature, chemicals, weathering, radiation and burning and also exhibit excellent clarity (in amorphous form), reasonable cost, as well as moldability. Accordingly, polyesters are used for various purposes (e.g., fibers, films, molded and extruded products.) The notched impact resistance of the polyester, however, is less than satisfactory. Plastics such as poly (butylene terephthalate) (PBT) and poly(ethylene terephthalate) (PET) have insufficient notched impact strength, and many attempts have been made to improve the impact strength by the use of agents which are added to resins and subjected to melt-blending. In particular, when a cut (notch) is created in a molded or extruded part, the impact resistance of polyester is poor, and consequently notched impact strength must be further improved for polyester articles. Various attempts have been made using conventional fibrous inorganic fillers (e.g., glass fiber and asbestos fiber) to improve the impact resistance of polyester. Even when these methods are implemented, however, the impact resistance improvement is less than satisfactory and clarity in amorphous polyesters is adversely affected. Various techniques wherein rubbery polymers or rubber- containing polymers are mixed with polyesters have been developed to improve the impact resistance of polyesters and thermoplastic materials. Specifically, certain core-shell polymers comprising a core made of rubbery polymer and a shell, around the core, made of a glassy polymer are excellent agents for improvement of notched impact strength of polyesters where clarity is not an object. When these prior art methods are used, the polyester resin generally exhibits poor compatibility with the shell of the rubber-containing polymer, and therefore impact resistance (especially notched Izod impact resistance) is not fully optimized. Even when these prior art core-shell modifiers are added to amorphous polyesters and found to produce ductile, notched breaks, the clarity of amorphous polyester resins is destroyed. An amorphous polyester may contain a small amount of crystallinity, but the level must be low enough so that clarity is not adversely affected. Further, although the polyester may be crystallized under certain conditions, in the present invention the molding and cooling conditions are such that crystallization (and loss of clarity) is avoided. Lane, U.S. Patent 4,034,013 teaches core/shell polymers functionalized with an epoxy group, such as a shell of methyl methacrylate/glycidyl methacrylate, to improve the melt strength of polyesters. Although Lane broadly teaches butadiene-based elastomers with optional minor amounts of styrene in the core and teaches styrene as a major component of the outer stage, she does not teach or suggest a solution to preparing an efficient impact modifier which will retain clarity in the amorphous polyester. Kishimoto et al., Japanese Kokai 54-48850, disclose butadiene-based core/shell polymers with hydroxyalkyl groups in the shell portion as modifiers for crystalline polyesters, such as poly(butylene terephthalate), but do not teach the means to modify such core/shell polymers to make them useful as impact modifiers in clear, amorphous polyesters. The object of the present invention is to provide a composition for improving the impact strength of polyesters, such as PET or PET copolyesters, when they are processed into clear, tough objects while retaining their amorphous nature. The composition will provide tough, ductile notched Izod breaks (> 540 J/m (10 ft. lbs./in.), at room temperature) at loadings of 25% or less in amorphous polyesters and copolyesters. It is another objective that said composition provide tough ductile notched Izod breaks without reducing the transparency of amorphous polyesters. Another object is to provide a composition which will also overcome the embrittlement caused by physical aging which commonly occurs in amorphous aromatic polyesters when conditioned at temperatures approaching glass transition temperature (Tg). A further object is to provide clear amorphous extrusion/melt shaped or injection molded PET or PET copolyester articles. In the instant invention, impact strength of amorphous aromatic polyesters is increased substantially by the addition of small amounts of certain core-shell modifiers which disperse very readily in aromatic polyesters and do not detract from clarity. These and other objects as will become apparent from the following disclosure are achieved by the present invention which comprises in one aspect a composition for improving the impact strength characteristics of aromatic polyesters, such as PET in amorphous form. The impact modifier composition of this invention is a core-shell polymer with a core comprised mainly of a rubbery core polymer such as a copolymer containing a 1,3-diene, and a shell polymer comprised mainly of a vinyl aromatic monomer such as styrene, and hydroxyalkyl (meth)acrylate. There are two general types of impact modifiers meeting this description. In the preferred case, for lowest raw material cost, is a core-shell impact modifier composition comprising: (A) from 40 to 65 parts by weight of a core polymer comprising: from 40 to 60 percent by weight of units derived from at least one vinyl aromatic monomer, from 60 to 40 percent by weight of units derived from at least one 1,3-diene monomer, such as isoprene, 3-chlorobutadiene or butadiene, optionally, up to 5 percent by weight of at least one cross-linking or graft-linking monomer, and optionally up to 10% by weight of units derived from at least one copolymerizable vinyl or vinylidene monomer; (B) from 35 to 60 parts by weight of a shell polymer comprising: from 2 to 40 percent by weight of units derived from at least one hydroxyalkyl (meth)acrylate, and from 60 to 98 percent by weight of units derived from at least one vinyl aromatic monomer; and up to 25 percent by weight of units derived from one or more copolymerizable vinyl or vinylidene monomers, the core shell impact modifier having a refractive index of from 1.55 to 1.58 measured according to ASTM-D-524. Intermediate shells may also be present. The second type utilizes a vinyl aromatic monomer of high refractive index chosen from the class of polybromoaromatic monomers and polycyclic aromatic monomers. Such monomers include e.g. dibromostyrene, tribromostyrene, tetrabromostyrene, monomethyldibromostyrene, vinyl naphthalene and isopropenyl naphthalene. Because these monomers are more effective in raising refractive index, they may be used in lesser amounts, allowing more 1,3-diene to be present in the core polymer or a higher amount of core in the core/shell polymer. In this instance, the invention encompasses a core-shell impact modifier composition comprising: (A) from 40 to 90 parts by weight of a core polymer comprising: from 20 to 60 percent by weight of units derived from at least one vinyl aromatic monomer of high refractive index selected from polybromo vinyl aromatic monomers and polycyclic vinyl aromatic monomers, from 40 to 80 percent by weight of units derived from at least one 1,3-diene monomer, such as isoprene, 3-chlorobutadiene or butadiene, optionally up to 5 percent by weight of at least one graft-linking or cross-linking monomer; and optionally up to 10% by weight of units derived from at least one copolymerizable vinyl or vinylidene monomer; (B) from 10 to 60 parts by weight of a shell polymer comprising: from 2 to 40 parts by weight of units derived from at least one hydroxyalkyl (meth)acrylate, and from 60 to 98 percent by weight of units derived from at least one vinyl aromatic monomer; and up to 25 percent by weight of units derived from one or more copolymerizable vinyl or vinylidene monomers, the core shell impact modifier having a refractive index of from 1.55 to 1.58 measured according to ASTM-D-524. A further variation of the impact modifier structure is to form a three-stage polymer comprising: (A) from 10 to 50 parts of a core polymer comprising: at least 80 percent by weight of units derived from at least one vinyl aromatic monomer, up to 20 percent by weight of units derived from at least one other copolymerizable vinyl or vinylidene monomer, up to 20 percent by weight of units derived from at least one 1,3-diene, and up to 5 percent by weight of units derived from at least one graft-linking or cross-linking monomer; (B) from 40 to 80 parts by weight of a second-stage polymer comprising: from 20 to 60 percent by weight of units derived from a vinyl aromatic monomer, from 30 to 70 percent by weight of units derived from at least one 1,3-diene, up to 10 percent by weight of units derived from at least one copolymerizable vinyl or vinylidene monomer, and up to 5 percent by weight of units derived from at least one graft-linking or cross-linking monomer; (C) from 10 to 40 parts by weight of a shell polymer comprising: from 2 to 40 percent by weight of units derived from at least one hydroxyalkyl (meth)acrylate, from 60 to 98 percent by weight of units derived from at least one vinyl aromatic monomer; and up to 25 percent by weight in the shell of units derived from one or more copolymerizable vinyl or vinylidene monomers, the core-shell impact modifier having a refractive index of from 1.55 to 1.58 measured according to ASTM-D-524. The hard-core technology, based on U.S. Patents 3,793,402 and 3,971,835, offers a means to add a vinyl aromatic monomer to adjust the refractive index upwards without requiring that monomer to be copolymerized with the diene monomer and thus adversely affect the rubbery characteristics of the copolymer. Another aspect of the invention is the blending of the impact modifier composition with at least one amorphous, aromatic polyester or copolyester having a refractive index of from 1.55 to 1.58 measured according to ASTM-D-524, at a weight ratio of polyester: impact modifier of 99/1 to 70/30. A still further aspect of the invention comprises molded, or extrusion blow molded, injection molded, extruded parts, bottles, sheets, films, pipes, foams, containers, profiles, and hollow parts prepared with the above-mentioned blends. The core-shell impact modifiers produce clear, and unexpectedly tough blends with amorphous aromatic polyesters. These modifiers produce a large increase in impact strength, while maintaining excellent optical clarity of the polyesters. These modifiers have cores composed principally of rubbery polymers, such as copolymers of 1,3-diene with vinyl aromatic monomers, such as copolymers of butadiene with styrene, and shells composed principally of vinyl aromatic copolymers (e.g. styrene/hydroxyalkyl (meth)acrylate copolymers). For example, the vinyl aromatic core-shell impact modifiers (i.e. "modifiers") which give this unexpected result contain shells derived from copolymers of vinyl aromatic monomers with certain hydroxyalkyl (meth)acrylates, for example, hydroxyethyl methacrylate (HEMA), hydroxypropyl methacrylate (HPMA), 4-hydroxybutyl acrylate, ethyl alphahydroxymethylacrylate, or hydroxyethyl acrylate (HEA), and at least one copolymerizable vinyl or vinylidene monomer. The monomer concentrations in the cores and shells of the modifier composition are adjusted to provide a refractive index (RI) to match that of the polyesters with which they are blended (i.e. 1.55 to 1.58). This produces a clear blend under processing conditions which will maintain the polyester in its amorphous form. Almost all rubbery polymers (e.g. core polymers) have RI's well below this range. Therefore it is necessary that the rubber phase concentration of the impact modifier composition be kept relatively low and the other components of the modifier be used to bring the RI into the desired range. However, the impact strength obtainable with a given concentration of any core-shell impact modifier tends to vary directly with the amount of rubber polymer in the modifier. This means that high RI modifiers having low rubber contents have to be exceptionally efficient to produce good toughening. From a practical standpoint the most desirable monomer to produce rubbery polymer for this application is butadiene whose homopolymer has a RI=1.52. It has the best combination of RI, cost, stability, and processability. For the same reasons, styrene is the most desirable component for the rest of the modifier. However, even if butadiene and styrene were the only components of the modifier, a butadiene/styrene ratio ranging from 50/50 to 20/80 would be required for the modifier RI to be in the 1.55 to 1.58 range needed for matching the RI's of amorphous, aromatic polyesters. One skilled in the art of impact modification would expect a 50% concentration of butadiene to be very low for good core-shell impact modifier efficiency. The results found herein for modification of polyesters with such functionalized "rubber-poor" modifiers are surprisingly good. In response to the need to match RI's of amorphous aromatic polyesters and simultaneously have excellent impact modifier efficiency, it was unexpectedly discovered that when low concentrations of certain hydroxyalkyl (meth)acrylates are copolymerized with aromatic vinyl monomers to form the shell polymer of core-shell impact modifiers having RI's in the 1.55 to 1.58 range, very high notched Izod impact strengths are obtained with amorphous polyesters at 30% or lower modifier loadings, and preferably at from 5 to 20% loadings. Substitution of the hydroxyalkyl methacrylate with other functional monomers promoting compatibility of the shell with the polyester will give similar results in impact improvement and maintenance of clarity. The requirement for a "rubber-poor" modifier can be relaxed somewhat if the vinyl aromatic monomer is changed from e.g. styrene, vinyl toluene, para methylstyrene and monochlorostyrene to one of high refractive index, viz., the polybrominated vinyl aromatics or the polycyclic vinyl aromatics. The core polymer in the impact modifier composition is a rubbery polymer and generally comprises a copolymer of butadiene and a vinyl aromatic monomer. The rubbery polymer may include diene rubber copolymers (e.g., butadiene-styrene copolymer, butadiene-styrene-(meth)acrylate terpolymers, butadiene-styrene-acrylonitrile terpolymers and isoprene-styrene copolymers). Of the afore-mentioned rubbery polymers, those which can be produced as a latex are especially desirable. In particular, a butadiene-vinyl aromatic copolymer latex obtained as a result of emulsion polymerization is preferred. In the core polymer, a partially crosslinked polymer can also be employed if crosslinking is moderate. Further, at least one of a cross- or graft- linking monomer, otherwise described as a multi-functional unsaturated monomer, can also be employed. Such monomers include e.g. divinylbenzene, diallyl maleate, butylene glycol diacrylate and allyl methacrylate. The ratio of comonomers in the core depends on the desired core-shell ratio and hardness of the rubber phase. The ratio range of butadiene to the vinyl aromatic in the core polymer is 70/30 to 40/60 (parts by weight). If the quantity added is below 40 parts by weight butadiene, it is difficult to improve the impact resistance. If the quantity added exceeds 70 parts by weight butadiene on the other hand, it is difficult to obtain a high enough RI modifier to match that of the polyester, unless the vinyl aromatic monomer is of high refractive index and selected from the polybrominated or polycyclic monomers described above. Optionally, a small concentration, up to 5, preferably from 0.01 up to 5, and further preferably from 0.1 up to 2 percent, by weight of a crosslinking monomer, such as divinyl benzene or butylene glycol dimethacrylate is included, and optionally up to 5 preferably 0.01 to 5 percent by weight of a graftlinking monomer for tying the core and shell together, such as allyl maleate may be included in the rubbery core polymer. Further examples of crosslinking monomers include alkanepolyol polyacrylates or polymethacrylates such as ethylene glycol diacrylate, ethylene glycol dimethacrylate, butylene glycol diacrylate, oligoethylene glycol diacrylate, oligoethylene glycol dimethacrylate, trimethylolpropane diacrylate, trimethylolpropane dimethacrylate, trimethylolpropane triacrylate or trimethylolpropane trimethacrylate, and unsaturated carboxylic acid allyl esters such as allyl acrylate, allyl methacrylate or diallyl maleate. In the shell polymer of the impact modifier composition, a hydroxyalkyl (meth)acrylate is employed. A hydroxyalkyl (meth)acrylate is copolymerized with at least one copolymerizable vinyl aromatic monomer. Examples of the aforementioned hydroxyalkyl (meth)acrylates include hydroxyethyl (meth)acrylate and hydroxypropyl (meth)acrylate. Vinyl aromatic monomers to be copolymerized with the aforementioned hydroxyalkyl (meth)acrylates include vinyl aromatic monomers such as styrene, alpha-methyl styrene, para-methyl styrene, chlorostyrene, vinyl toluene, bromostyrene, dibromostyrene, tribromostyrene, vinyl naphthalene and isopropenyl naphthalene. The hydroxyalkyl (meth)acrylates and vinyl aromatic monomers may be used either singly or in combination of two or more. In the shell polymer, the ratio between the hydroxyalkyl (meth)acrylate (e.g. HEMA, HPMA) and the other copolymerizable vinyl aromatic monomers (e.g. styrene, tribromostyrene) ranges from 2/98 to 40/60 parts by weight, and preferably 3/97 to 30/70 parts by weight. Below 2 parts, the performance is not improved over the vinyl aromatic homopolymer shell, and above that level, side reactions, such as crosslinking, may occur, with adverse effects on dispersion. Optionally, one or more additional monomers may be added to the shell to adjust the RI. This additional monomer is preferably an alkyl (meth)acrylate (such as C 1 -C 4 alkyl (meth) acrylate), but it can be any monomer which copolymerizes with the other two monomers used in the shell polymer and produces a terpolymer which permits the RI of the modifier to match that of the polyesters with which it is blended. The additional monomer may include one or more of any of the following monomers: acrylonitrile, methacrylonitrile, methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, decyl acrylate, methyl methacrylate and ethyl methacrylate. In the impact modifier composition, the ratio of the core polymer to the shell polymer ranges from 90/10 to 40/60, and preferably especially when styrene is the vinyl aromatic monomer from 65/35 to 40/60 (parts by weight). The resultant composition preferably has a particle size range of 75 to 300 nm., more preferably from 140 nm. to 230 nm., and a RI range of 1.55 to 1.58 measured according to ASTM-D-524. When the impact modifier composition containing 40-90 parts by weight of the aforementioned rubbery core polymer and 60-10 parts by weight of the shell hydroxyl-group-containing polymer (total: 100 parts by weight) is manufactured, conventional methods for manufacturing ordinary rubber-modified polymers (e.g., ABS resin and impact resistant polystyrene) may be effectively employed. These impact modifiers may be prepared by emulsion polymerization. The preferred procedure is emulsion polymerization using soaps, initiators and processing conditions normally used for making MBS polymers, that is, impact modifiers based on butadiene-styrene rubbers with one or more stages of styrene or methyl methacrylate polymers. Isolation from the emulsion can be achieved by standard procedures such as spray drying or coagulation. For example, a polymer latex characterized by an appropriate particle size and degree of conversion is produced by means of emulsion polymerization (e.g. copolymerizing a hydroxyalkyl (meth)acrylate with another copolymerizable vinyl aromatic monomer in the presence of a polymerized rubber latex). Further, the polymer can be prepared by a method wherein a core polymer is uniformly graft-polymerized with a hydroxyalkyl (meth)acrylate and another copolymerizable vinyl aromatic monomer constituting the shell polymer, but also by a method wherein the core polymer is partially graft-polymerized with the vinyl aromatic monomer and/or hydroxyalkyl (meth)acrylate, wherein a copolymer, such as that described in U.S. Patent Application Serial No. 755,701, filed September 6, 1991 (US-A-5 268 438) for which two of the present inventors are inventors and which also is assigned to the same assignee as the present application, is produced by copolymerizing the remainder of the vinyl aromatic monomer and/or hydroxyalkyl (meth)acrylate and the two are finally mixed. In such a case, an impact modifier composition which provides an extremely high impact resistance can be obtained if the following composition is employed. For example: 50-80 parts by weight (solid content) of the rubbery polymer latex are emulsion graft-polymerized with 50-20 parts by weight of hydroxyl-group-free vinyl aromatic monomer. Next, a hydroxyalkyl (meth)acrylate is separately emulsion-polymerized with a vinyl aromatic monomer identical to that used for the aforementioned emulsion graft polymerization or a different vinyl aromatic monomer which yields a copolymer with a high affinity with said graft polymer. The resulting core polymer latex and the side-chain hydroxyl-group-containing shell polymer latex are then mixed in latex form prior to isolation. The advantage to this method is that higher molecular weight polymer can be produced in the absence of the butadiene-containing rubber, and the higher molecular weight component may be more effective in improving rheological properties, such as blow molding. Further, such allows for intimate mixing prior to blending with the polyester. Thus, when the impact modifier composition is manufactured, general free radical polymerization techniques (e.g., emulsion polymerization, solution polymerization, and suspension polymerization) may be employed so long as the resulting impact modifier composition is characterized by a core-shell structure wherein hydroxyl groups are preserved. The impact modifier composition may be isolated from the reaction medium by any of several known processes. For example, when prepared in emulsion, the composition may be isolated by coagulation, including coagulation in an extruder from which the water is removed as a liquid, or by spray-drying. Additives such as thermal stabilizers and anti-oxidants may be added to the composition prior to, during or after, isolation. It is important that no crystallization promoter is present in the composition since this invention is directed to compositions suitable for producing amorphous, non-crystalline articles. If substantial crystallization occurs in the process, the resultant articles become opaque and brittle. In some cases, such as with pipe, foam and profile extrusion, a small degree of crystallinity may be acceptable and can be achieved by control of the cooling cycle. However, in most cases it is preferred to prepare amorphous articles on standard injection molding and extrusion equipment. The type of articles to be produced, whether it be molded parts, bottles, films, foams, pipes, tubing, sheets or profiles, will govern the auxiliary equipment to be employed. For instance, to produce bottles, extrusion blow molding equipment is necessary. To produce films, blown film equipment is necessary. The amorphous, aromatic polyesters, such as PET, and copolyesters, such as Eastman PETG (i.e., (poly)ethylene-co-1,4- cyclohexanedimethylene terephthalate), of this invention include poly (C 1 to C 6 alkylene terephthalates), poly(alkylene naphthalene dicarboxylates), such as poly(ethylene naphthalene-2,6-dicarboxylate), and aromatic amorphous polyester which contains units derived from at least one aliphatic diol or cycloaliphatic diol or combinations of aliphatic diols and cycloaliphatic diols and one or more aromatic dibasic acids. Examples include e.g. polyethylene terephthalate (PET) and polypentylene terephthalate, or an aromatic copolyester which contains units derived from two glycols (e.g., ethylene glycol and cyclohexanedimethanol) and from two dibasic acids (e.g. terephthalic acid and isophthalic acid). Such polyesters may be obtained by polycondensing polyol components (e.g., ethylene glycol) with dicarboxylic acid components (e.g., terephthalic acid, isophthalic acid and naphthalenedicarboxylic acid), as well as mixtures consisting of two or more polyesters. The modifiers and polyesters may be combined by melt blending in an extruder. The polyesters should be dried to 0.03% moisture content. A mix of the two components can be directly extruded or molded or the components can be combined in an initial blending step and the pellets from this blend can then be molded after drying to a 0.03% moisture content. The concentration of modifier in these polyester blends can range from 1 to 30% by weight and preferably from 5 to 20% by weight. The blends can be extruded or molded into clear parts which have very high notched impact strength, and exhibit ductile type failures and physical aging resistance. The required modifier concentration will depend on factors such as the molecular weight of the polyester, the impact strength desired, and the temperature at which the final object is utilized. Below 1% modifier concentration, no significant effect is seen. Blends should contain amorphous aromatic polyester or copolyester which has an intrinsic viscosity of greater than or equal to 0.7 dl/g. for best properties of molding and processing, but for some uses, lower molecular weight polyesters may be employed. ( PET or PETG may decrease in intrinsic viscosity after melt processing; the values in the specification refer to the polyester as supplied, prior to processing). Articles such as containers, bottles, foams, or hollow parts may be extrusion blow molded, extruded or injection molded from polyester blends described herein. Blending can be accomplished by melt extrusion in an extruder at temperatures of 193°C. to 288°C., preferably 204°C. to 265°C. For example, a high work, two stage screw which has a length/diameter ratio of 24/1, and a compression ratio of 3.0 to 3.5 gives a very adequate dispersion of the modifier in the polyester. A dwell time in the extruder of 1 to 5 minutes is adequate to insure complete mixing or dispersion under most conditions but of course lower and higher dwell times can certainly be used. Preferably the strands produced by extruder blending are pelletized and dried to a moisture content of less than 0.03 percent before molding. The ingredients used to make the composition of the invention are dispersed uniformly and it has been found that melt blending the ingredients, by using such equipment as a melt extruder (e.g., single screw extruders or twin screw extruders) in a separate step prior to molding is desirable. The blended product may be pelletized (i.e., the extruded strand is quenched and cut), dried and used for subsequent molding purposes. Other additives known in the art may be included in the composition at 0.1 to 30% by weight. These other additives may include antioxidants, flame retardants, reinforcing agents such as glass fiber, asbestos fiber and flake, mineral fillers, stabilizers, nucleating agents, ultraviolet light stabilizers, heat and light stabilizers, lubricants, dyes, pigments, toners, mold release agents and fillers, such as glass beads and talc. Minor amounts of other polymers (i.e. 1 to 10 percent by weight) can also be incorporated in the present composition, such as polyamides or polycarbonates. Most of these additives will adversely affect clarity. The additives listed above such as antioxidants, thermal stabilizers, fillers, pigments and flame retardant additives may be used in the composition of this invention provided they do not exert any adverse effect on the impact strength or clarity. It is preferred not to have glass fiber reinforcement in clear article applications or any additive which would decrease transparency. It is highly preferred that clear articles are produced. The polyesters must be thoroughly dried prior to melt processing to minimize the rapid hydrolytic degradation known to occur at processing temperatures and to reduce molecular weight. The modifiers of the present invention are much less sensitive to hydrolytic degradation than the polyesters. Higher than necessary melt temperatures should be avoided during processing to keep the impact strength as high as possible. Melt cooling should be carried out as rapidly as possible to prevent polyester crystallization and the loss of clarity. Aromatic amorphous polyesters are quite sensitive to embrittlement from physical aging, but this limitation is overcome by the modifiers herein (see Table 2). Therefore, polyester blends will now be able to compete successfully with, e.g. polycarbonate, cellulosics and impact modified polyvinyl chloride for a broad range of applications where high clarity and toughness are needed in the absence of exceptional heat resistance. The preferred poly(alkylene terephthalates) are polyethylene terephthalate (PET) and copolyesters of PET. Blends with other polyesters are also suitable. For example, blends of two or more polyesters may also be used, with polyester blends which have poly (ethylene terephthalate) being preferred. EXAMPLES The following examples and comparative examples are presented to illustrate the invention, but the invention should not be limited by these examples. All parts and percentages are by weight unless otherwise indicated, and the following abbreviations are employed in the examples and throughout the text: BA = butyl acrylate EA = ethyl acrylate ST = styrene HEMA = hydroxy ethyl methacrylate MMA = methyl methacrylate MAA = methacrylic acid HPMA = hydroxy propyl methacrylate GMA = glycidyl methacrylate PET = poly(ethylene terephthalate) PBT = poly(butylene terephthalate) BD = butadiene DVB = divinyl benzene BZMA = benzyl methacrylate AN= acrylonitrile MAN= methacrylonitrile APPARATUS and GENERAL PROCEDURE Standard ASTM test specimen molds are employed. Refractive indexes are determined according to ASTM-D-524, light transmission and haze according to ASTM-D-1003, and notched Izod impact strength according to ASTM-D-256. The modifiers are prepared by emulsion polymerization of butadiene with styrene and about 0.6% divinyl benzene. After this step was complete, styrene with HEMA or another comonomer is added to the emulsion and polymerized to form a shell stage on the butadiene rich core stage. The core-shell impact modifier polymer is then isolated from the emulsion by spray drying. The impact modifiers described herein have particle sizes in the 180-240 nm range. The modifier is combined with aromatic polyester resins by melt blending in an extruder. Strands of the blends are quenched in a water bath as they leave the extruder to prevent polyester crystallization. Blends in which the RI's of the modifier and polyester are equal form clear strands. Pellets cut from the strands are injection molded into test specimens under conditions which prevent polyester crystallization. The test specimens are then evaluated for physical properties. It should be noted that notched Izod impact strengths greater than about 10 ft.lbs/in. (ca. 540 J/m) usually exhibit ductile rather than brittle breaks. Also all the 1/8" (3.2 mm.) molded plaques prepared with modified PETG are transparent so that distant objects could be clearly seen through them even though the measured haze values ranged from about 7 to about 45%. These results in Table 1 clearly show the effectiveness of modifiers with styrene/HEMA shells vs. shells with styrene, or styrene and other monomers. In 1/8" (3.2 mm.) thick samples, ductile failures (desirable) were observed at modifier loadings as low as 10% and in three cases at a temperature of 10°C (20% loading). Also some blends produced 1/4" (6.4 mm.) thick samples which gave ductile breaks. Unmodified polycarbonate, generally conceded to be the toughest clear polymer, exhibits only brittle breaks at 1/4" (6.4 mm.) thickness. The modifiers in the Tables are prepared by emulsion polymerization. The impact modifiers are blended with polyester in a 2.54 cm (1 inch), 24/1 length/diameter ratio, single screw extruder at the concentrations (i.e. modifier loading (%)) listed in Table 1. Impact strength is determined by ASTM-D- 256. Table 1 describes the effect of different impact modifiers ( butadiene/styrene//styrene/HEMA) on the impact strength of a commercial copolyester resin, Eastman's PETG 6763, with a 0.74 dl/g intrinsic viscosity (IV) (ASTM D- 4603), and another commercial copolyester, Eastman's Tenite 13339, with a 1.05 dl/g IV (ASTM D-4603). Many of the impact modifiers have RI's approximating those of the polyesters or copolyesters so that clear strands were extruded. Exact RI matches can be achieved by slightly adjusting the impact modifier.Compositions with HPMA or GMA replacing HEMA may be employed with similar results. Table 1 lists the compositions of a series of core-shell impact modifiers with RI's of about 1.565 except for Example 11 (lower) and Example 15 (higher). Modifiers are melt blended at the concentrations listed in the table with Eastman's PETG 6763, a non-crystallizable PET copolyester in which part of the ethylene glycol (EG) component is replaced with cyclohexane dimethanol (CHDM), having a RI = 1.565. These blends and unmodified PETG are molded into 1/8" and 1/4" (3.2 mm. and 6.4 mm.) thick notched Izod impact test (ASTM-D-256) specimens and into 2" x 3" x 1/8" (50.8 x 76.2 x 3.2 mm.) plaques. The impact test results are determined by ASTM D-256 on 1/8' and on 1/4" (3.2 mm. and 6.4 mm.) thick bars. Values for transparency and haze are determined on the 1/8" (3.2 mm.) thick plaques. Two blends with Modifiers 12 and 15 are prepared with Eastman's Tenite 13339 copolyester. This resin contains less CHDM than PETG and its composition is therefore much closer to that of PET than is PETG. It has an RI of 1.575. Since the modifier of Example 12 blended with it had an RI of only about 1.565, the RI mismatch caused the plaques to be translucent rather than transparent. The modifier of Example 15 with a RI of 1.575 gives a blend of low haze. Example 1 A 15g charge of a 10% aqueous solution of acetic acid was added to 5244.4g of deionized water in a stainless steel reactor capable of withstanding 200 psi (1.38 mPa) pressure. The solution was heated to 80°C while stirring and sparging with nitrogen for 30 minutes. The temperature was raised to 85°C and 360g of a 10% aqueous solution of sodium formaldehyde sulphoxylate were added along with a 50g rinse of deionized water. A mixture of 611.4g of styrene (ST) and 30g of divinyl benzene (DVB) were next added along with 2358.6g of butadiene (BD) and 240g of a 10% aqueous solution of sodium dodecyl benzene sulfonate over a 3 hour period. A 357.5 charge of a 1.4% aqueous solution of t-butyl hydroperoxide (tBHP) was added over a 6 hour period. At the end of this addition, the feed line was rinsed with a sufficient amount of deionized water to obtain an emulsion containing 33% solids. The emulsion was cooled to room temperature and stored for subsequent use as a seed for the following modifier examples. Example 2 A 18.2g charge of a 10% aqueous solution of acetic acid was added to 5800g of deionized water in a reactor. This was sparged with nitrogen while it was heated to 95°C. When the temperature reached 95°C, the nitrogen was turned off and 532.5g of the emulsion (solids basis) from Example 1 and 337.3g of a 5% aqueous solution sodium formaldehyde sulphoxylate were added to the reactor. About 350g of deionized water was used as a rinse. The reactor was then evacuated to 5" (0.17 Mdynes/ cm 2 ) of mercury. Next a mixture of 2020.8g of ST and 42.2g of DVB were added at a constant rate to the reactor over a 5 hour period. At the same time 590.2g of a 10% aqueous solution of Dowfax 2A-1 and 2241.3g of BD were added at a constant rate over the same 5 hour period. At the same time, 695.6g of a 1.4% aqueous solution of tBHP was added over a 7.25 hour period. At the end of the monomer feed, 227g of rinse water were added. At the end of the tBHP feed, the reaction was held for 30 minutes. After this the reactor was cooled to 62°C and vented to atmospheric pressure. This completed the preparation of the emulsified core of the modifier. The shell of the modifier was prepared by first adding 109.8g of a 5% aqueous solution of sodium formaldehyde sulphoxylate to the reactor containing the core emulsion. A nitrogen sweep of the reactor was started. A mixture of 2574g of ST and 390.2g of hydroxyethyl methacrylate (HEMA) was prepared and sparged with nitrogen for 20 min. This mixture was fed to the reactor, maintained at 60°C, for 90 minutes along with 288.9g of a 1.4% solution of tBHP. At the end of this feed the reaction was held for 15 minutes and then chased for 4 hours with 183.1g of a 1.4% aqueous solution of tBHP and 87.9g of a 5% aqueous solution of sodium formaldehyde sulphoxylate. At the end of this chase, a 50% solids emulsion containing 30.1g of trisnonyl phenyl phosphite, 30.1g of triethylene glycol bis(3-(3'-t-butyl-4'hydroxy- 5'methylphenyl) propionate) (Irganox 245, Ciba Geigy Co.) and 90.3g of dilauryl thiodipropionate was added. The emulsion was then spray dried. A fine powder having a refractive index (RI) of 1.565 was obtained. This powder was melt blended in a single screw extruder at an average melt temperature of 240°C with Kodar PETG 6763, a PET copolyester supplied by Eastman Chemical Co., which contains cyclohexanedimethanol substituted for part of the ethylene glycol. This copolyester has an RI of 1.565. Extruded strands of the blend were pelletized, dried for 8 hours at 60°C and injection molded into test specimens. Notched Izod impact tests were run according to ASTM Procedure D-256 and light transmission and haze tests were run on 32mm thick test specimens according to ASTM Procedure D-524. Results from these tests and tests run on the following examples are listed in Table 1. Some blends were also prepared with Eastman Chemical Co.'s Tenite 13339, a PET resin containing less than 10% isophthalic acid substituted for terephthalic acid and having an intrinsic viscosity of 1.05 dl/g. Example 3 This modifier was prepared in the same way as Example 2 except that 2433.6g of ST and 530.5g of HEMA were used to prepare the modifier shell. Example 4 This modifier was prepared in the same way as Example 2 except that 2730g of ST and 234g of HEMA were used to prepare the modifier shell. Example 5 This modifier was the same as Example 2 except that the shell consisted of 2371.2g of ST, 296.4g of HEMA and 296.4g of ethyl acrylate. Example 6 This modifier was the same as Example 2 except that hydroxypropyl methacrylate was substituted for the HEMA. The following four examples compare results obtained with modifiers having the same cores as those in the examples above and RI's about equal to those of the above modifiers but with shells that do not fall within the claims of this application. Example 7 (Comparative) This modifier was the same as the one in Example 2 except that the ST charge used in making the core was 2122.2g and the BD charge for the core was 2373.9g. The shell consisted of 2552g of ST. No comonomer was used in preparing the shell. Example 8 (Comparative) This modifier was the same as Example 2 except that the shell was prepared with 2652g of ST, 156g of methyl methacrylate and 156g of ethyl acrylate. No HEMA was present. Example 9 (Comparative) This modifier was the same as Example 2 except that the shell consisted of 2652g ST, 156g of methyl methacrylate and 156g of methacrylic acid. No HEMA was present. Example 10 (Comparative) This modifier was the same as Example 2 except that the shell was composed of 1560g of ST and 1404g of benzyl methacrylate. Example 11 (Comparative) The modifier used in this example was Paraloid EXL3647, an MBS type commercial impact modifier supplied by Rohm and Haas Co. This modifier has a RI of 1.525 which is well below the RI's of aromatic polyesters and copolyesters. Although this modifier produced good notched impact strength, it also produced blends which were opaque. Example 12 This modifier was equivalent in composition to Example 2 but it was prepared by a different process. The difference was in the rate of addition of the ST/DVB mix and of the BD used in preparing the core. These two components were added according to the following schedule: First hour ST/DVB 12.7g/min. BD 1.2g/min. Second hour ST/DVB 9.1g/min. BD 4.9g/min. Third hour ST/DVB 7.0g/min. BD 7.1g/min. Fourth hour ST/DVB 4.2g/min. BD 9.8g/min. Fifth hour ST/DVB 1.4g/min. BD 12.7g/min. At the end of this monomer feed, the process and components used were the same as those in Example 2. Example 13 This modifier was the same as Example 12 except that the shell consisted of 2371.2g of ST, 296.4g of HEMA and 296.4g of ethyl acrylate. Example 14 This modifier had the same overall composition as Example 2 except that the seed polymer contained a high level of ST. This seed polymer was prepared in the same manner as Example 1. After the reactor was charged with 5244.4g of deionized water and 15g of a 10% aqueous solution of acetic acid, it was heated to 90°C while stirring and sparging with nitrogen for 30 minutes. When the temperature reached 90°C, 360g of a 10% aqueous solution of sodium dodecyl benzene sulfonate and 182g of a 5% aqueous solution of sodium formaldehyde sulphoxylate were added. Next a mixture of 2970g of ST and 30g of DVB, a 2358g charge of BD and a 240g charge of a 10% aqueous solution of sodium dodecyl benze sulfonate were added over 3 hours. A 367.5g charge a 1.4% aqueous solution of tBHP was added over 4 hours. At the end of the feed, the lines were rinsed with deionized water to produce a 33% solids emulsion. The procedure used for the rest of the preparation was the same as that used for Example 12 except that the above emulsion was substituted for the Example 1 emulsion used in Example 12 and the monomer charge for making the core was 182.4g of ST, 44.3g of DVB and 2425.5g of BD. All other components used in both the core and the shell and the procedure used were the same as for Example 12. Example 15 This modifier was the same as Example 12 except that the shell consisted of 2027.4g of ST, 296.4g of HEMA and 640.2g of vinyl naphthalene to give a modifier with a RI of 1.575. Example 16 This example shows blends of PETG and of PET and impact modifiers of the present invention, which blends show retained impact strength after a heat aging process which greatly lowers the impact strength of the unmodified polyester. Polymer A: a PET with less than 5% isophthalic acid, (h) = 0.90 dl/g; Polymer B = PETG (Eastman 6763), described in the previous table; Modifier C is the modifier of Example 12, viz., 34.1 Bd/27.3 St/0.6 DVB//33 St/5 HEMA. Samples are molded and tested as molded and after aging at condition D = 5 days at 60°C or condition E = 30 days at 65°C. Data are shown in Table 2. IMPACT STRENGTH AND OPTICAL PROPERTIES OF POLYESTER//IMPACT MODIFIER BLENDS Notched Izod Impact Strength of Blend (Joules/m) Blend Modifier Ex. No. Polyester Modifier Conc. (%) Modifier RI 3.2 mm Thick Specimen 6.4 mm Transparency Haze (%/%) 22°C 10°C 0°C 22°C No modifier PETG 6763 0 -- 101.4 69.4 58.7 69.4 86/2 2 " 20 1.565 1072.9 165.5 80.1 838.1 78/30 2 " 15 1.565 1142.3 170.8 37.4 784.7 79/29 2 " 10 1.565 1185.0 117.4 69.4 138.8 82/15 3 " 20 -- 1094.3 133.5 80.1 181.5 76/44 4 " 20 1.566 1131.7 1072.9 117.4 998.2 79/34 5 " 20 1.564 122.8 85.4 48.0 85.4 74/51 6 " 20 1.565 250.9 90.7 80.1 149.5 80/26 7 " 20 1.562 58.7 -- -- -- 72/25 8 " 20 1.564 133.5 -- -- -- 76/13 8 " 30 1.564 144.1 -- -- -- -- 9 " 20 1.565 69.4 -- -- -- 77/8 10 " 20 1.564 117.4 -- -- -- 79/10 11 " 20 1.525 763.3 -- -- -- opaque 12 " 20 1.565 1158.3 1147.7 1121.0 1056.9 78/31 13 " 20 1.564 1334.5 154.8 96.1 154.8 76/33 14 " 20 -- 1387.8 1121.0 1121.0 -- 65/18 No modifier Tenite 13339 0 -- 26.7 -- -- -- 80/4 12 " 20 1.565 976.9 160.1 138.8 224.2 translucent 15 " 20 1.575 1019.6 -- -- -- 76/56 Physical Aging Data Dart Impact, Joules Notched Izod, Joules/m Polymer As molded Condition D As molded Condition E A 45.2 2.9 A/C=85/15 48.1 45.0 B 68.0 43.9 48 42.7 B/C=85/15 60.1 60.7 1228 1142 Eastman PETG 6763, Eastman Tenite 13339 and Kodar PETG 6763 are trade marks of the Eastman Chemical Company and Paraloid is a trade mark of Rohm and Haas Company. These marks may or may not be registered in some or all of the designated states.

Claims: A core-shell impact modifier composition comprising: (A) from 40 to 65 parts by weight of a core polymer comprising: from 40 to 60 percent by weight of units derived from at least one vinyl aromatic monomer, from 40 to 60 percent by weight of units derived from at least one 1,3-diene, optionally up to 10 percent by weight of units derived from at least one copolymerizable vinyl or vinylidene monomer, and optionally, up to 5 percent by weight of at least one graft-linking or cross-linking monomer; (B) from 35 to 60 parts by weight of a shell polymer comprising: from 2 to 40 percent by weight of units derived from at least one hydroxyalkyl (meth)acrylate, and from 60 to 98 percent by weight of units derived from at least one vinyl aromatic monomer; and up to 25 percent by weight of units derived from one or more copolymerizable vinyl or vinylidene monomers, the core-shell impact modifier having a refractive index of from 1.55 to 1.58 measured according to ASTM-D-524. A core-shell impact modifier composition comprising: (A) from 40 to 90 parts by weight of a core polymer comprising: from 20 to 60 percent by weight of units derived from at least one vinyl aromatic monomer of high refractive index selected from polybromo vinyl aromatic monomers and polycyclic vinyl aromatic monomers, from 40 to 80 percent by weight of units derived from at least one 1,3-diene, optionally up to 10 percent by weight of units derived from at least one copolymerizable vinyl or vinylidene monomer, and optionally up to 5 percent by weight of at least one graft-linking or cross-linking monomer; (B) from 10 to 60 parts by weight of a shell polymer comprising: from 2 to 40 percent by weight of units derived from at least one hydroxyalkyl (meth)acrylate, and from 60 to 98 percent by weight of units derived from at least one vinyl aromatic monomer; and up to 25 percent by weight of units derived from one or more copolymerizable vinyl or vinylidene monomers, the core-shell impact modifier having a refractive index of from 1.55 to 1.58 measured according to ASTM-D-524. A core-shell impact modifier composition comprising: (A) from 10 to 50 parts of a core polymer comprising: at least 80 percent by weight of units derived from at least one vinyl aromatic monomer, up to 20 percent by weight of units derived from at least one other copolymerizable vinyl or vinylidene monomer, up to 20 percent by weight of units derived from at least one 1,3-diene, and up to 5 percent by weight of units derived from at least one graft-linking or cross-linking monomer; (B) from 40 to 80 parts by weight of a second-stage polymer comprising: from 20 to 60 percent by weight of units derived from a vinyl aromatic monomer, from 30 to 70 percent by weight of units derived from at least one 1,3-diene, up to 10 percent by weight of units derived from at least one copolymerizable vinyl or vinylidene monomer, and up to 5 percent by weight of units derived from at least one graft-linking or cross-linking monomer; (C) from 10 to 40 parts by weight of a shell polymer comprising: from 2 to 40 percent by weight of units derived from at least one hydroxyalkyl (meth)acrylate, from 60 to 98 percent by weight of units derived from at least one vinyl aromatic monomer; and up to 25 percent by weight in the shell of units derived from one or more copolymerizable vinyl or vinylidene monomers, the core-shell impact modifier having a refractive index of from 1.55 to 1.58 measured according to ASTM-D-524. The composition of Claim 1, 2 or 3 wherein the vinyl aromatic monomer is styrene, para-methyl styrene, alpha-methylstyrene, chlorostyrene, vinyl toluene, bromostyrene, dibromostyrene, tribromostyrene, isopropenyl naphthalene, or vinyl naphthalene and wherein the 1,-3 diene is butadiene and/or wherein the hydroxyalkyl (meth)acrylate is hydroxyethyl (meth)acrylate or hydroxypropyl (meth)acrylate and/or wherein the one or more vinyl or vinvlidene monomers are acrylonitrile, methacrylonitrile, methyl methacrylate, ethyl methacrylate, butyl methacrylate, methyl acrylate, ethyl acrylate, or butyl acrylate. The composition of Claim I or 2 wherein the core polymer is butadiene-styrene copolymer, butadiene-styrene-acrylonitrile copolymer, or butadiene-butyl acrylate-styrene copolymer, and wherein the core polymer contains from 0.01 to 2 weight percent of units derived from at least one cross-linking or graft-linking monomer wherein styrene may be replaced by para-methyl styrene, alpha methylstyrene, chlorostyrene, vinyltoluene, bromostyrene, dibromostyrene, tribromostyrene, isopropenyl naphthalene or vinylnaphthalene. The composition of Claim 1, 2 or 3 wherein the shell polymer comprises vinyl aromatic monomer and hydroxyalkyl (meth)acrylate in the ratio 98:2 to 60:40. A clear, amorphous blend comprising: (A) at least one amorphous, aromatic polyester or copolyester having a refractive index of from 1.55 to 1.58 measured according to ASTM-D-524; and (B) a core-shell impact modifier composition of Claim 1, 2 or 3; at a weight ratio of 99/1 to 70/30 wherein, when the blend is formed by melt blending in an extruder the polyester has a 0.03% moisture content. The blend of claim 7 further containing 0.1 to 30% by weight, based on the weight of polyester and an impact modifier, of one or more other additives. The blend of claim 8 further containing 1 to 10% by weight based on the weight of polyester and an impact modifier, of one or more other polymers. The blend of claim 7 or 8 wherein the amorphous aromatic polyester is a poly(C 1 to C 6 polyalkylene terephalate), poly(alkylene naphthalene dicarboxylate) or an aromatic polyester which contains units derived from at least one aliphatic diol or cycloaliphatic diol, or a combination thereof, and at least one aromatic dibasic acid, preferably polyethylene terephalate or an aromatic copolyester which contains units derived from ethylene glycol, cyclohexanedimethanol, terephalic acid and isophthalic acid. Articles produced from the blend of any of the claims 7-10 under conditions which maintain the polyester in an amorphous condition. Articles of claim 11 which are molded, injection molded, extruded, or extrusion blow molded into parts, sheets, films, containers, bottles, pipes, foams, or hollow parts.

Inventors: CARSON WILLIAM GILMOUR, LAI CHOUNG-HOUNG, TROY EDWARD JOSEPH, CARSON, WILLIAM GILMOUR, LAI, CHOUNG-HOUNG, TROY, EDWARD JOSEPH
Applicants: ROHM & HAAS, ROHM AND HAAS COMPANY
Application year: 1993
Main classification: C08F257
IPC codes: C08F279, C08F285, C08F257, C08L67, C08L51