PROCESS FOR PREPARATION OF CHLORINATED POLY(VINYL CHLORIDE) THERMOPLASTIC ALLOYS

Abstract: A process and a composition for preparing chlorinated poly(vinyl chloride) alloys containing aromatic polycarbonates, ethylene-based functional polymers, and impact modifiers is described. The alloys have good thermo-mechanical properties such as good dimensional stability under heat, good impact resistance, good ductility, and the like. Although the percent of chlorine of the chlorinated poly(vinyl chloride) is 57% or greater by weight, the alloys can be melt-processed at relatively low temperatures, that is approximately at 230°C or less.

Description: TECHNICAL FIELD The present invention relates to a process for preparing thermoplastic alloys containing chlorinated poly(vinyl chloride) having a chlorine content of at least 57% by weight. More specifically, the present invention relates to a process for preparing chlorinated PVC containing alloys which have low temperature processing properties. BACKGROUND OF THE INVENTION It is well known that a chlorinated vinyl polymer referred to as chlorinated polyvinyl chloride, hereinafter CPVC, has excellent high temperature performance characteristics, among other desirable physical properties. Typically, commercial CPVC has in excess of about 57 percent by weight (% by weight) bound chlorine, and is most conveniently prepared by the chlorination of polyvinyl chloride as described in U.S. Patent Nos. 2,996,489; 3,100,762; 3,334,077; 3,334,078; 3,506,637; 3,534,013; 3,591,571; 4,049,517; 4,350,798; 4,377,459; 4,412,898; and 4,459,387 inter alia. The term CPVC is used herein to define a chlorinated vinyl chloride polymer having in excess of about 57% by weight bound chlorine. Chlorinated PVC (CPVC) has become an important specialty polymer due to its relatively low cost, high glass transition temperature, high heat distortion temperature, outstanding flame and smoke properties, chemical inertness and low sensitivity to hydrocarbon feed stock costs. The glass transition temperature of CPVC generally increases as the percentage of chlorine increases. However, a well known undesirable characteristic of CPVC resin is that it inherently has low impact properties, a characteristic which is also common to vinyl chloride homopolymers. Also, as the chlorine content increases, the CPVC resin becomes more difficult to melt process, and also becomes more brittle. The poor melt processability of CPVC resins is exemplified by milling CPVC on a roll mill which results in high torque and high temperatures as well as decomposition of the CPVC. Softening additives or plasticizers have been added to CPVC in order to improve its processability. Although its processability is somewhat improved, these additives produce undesirable effects. Some of the more significant detrimental effects produced by inclusion of these softening or plasticizer additives are lower heat distortion temperatures, softness and weakness in terms of lower tensile strength, and less desirable chemical properties than that exhibited by CPVC alone. These negative attributes of the additives on CPVC limit usefulness of the modified CPVC in the manufacture of rigid plastic articles. The burgeoning demand for CPVC pipes, vessels, valve bodies and fittings, and the fact that an impact-deficient CPVC matrix can be improved by compounding and alloying it with other polymers, has instigated concerted efforts to develop better impact modified CPVC compositions having increased heat distortion temperatures, and increased ease of melt-processing. Most of these efforts have been channeled toward rigid CPVC applications where acceptable impact strength and dimensional stability under heat are critical. Such applications include the manufacture of exterior structural products, rigid panels, pipe and conduit, injection-molded and thermoformed industrial parts, appliance housing, and various types of containers both large and small. U.S. Patent No. 3,882,192 to Elghani, et al relates to molding compositions consisting of from 5 to 95 parts by weight of a polycarbonate, from 5 to 95 parts by weight of a vinyl chloride polymer, and from 5 to 95 parts by weight of an ABS graft polymer, a styrene/maleic anhydride copolymer or an ethylene/vinyl acetate copolymer. Molding compositions are made by solution casting, that is by seperately dissolving each component in a suitable inert organic solvent. The three components can then be mixed together and the molding composition isolated from the solutions by precipitation with non-solvents or by removal of the solvents by distillation. Processing of the molding compositions is carried out at a temperature of about 250°C. In addition to high processing temperatures, which is too high for processing of high chlorine CPVC, no mention is made of the utilization of an ethylene-based functional polymer. U.S. Patent Nos. 4,105,711; 4,239,361; and 4,515,925 while relating to polymer mixtures containing polycarbonate, do not utilize any ethylene-based functional polymer. At present, no entirely satisfactory means is available for improving properties such as impact strength, heat distortion temperatures, improved ease of melt processing of chlorinated PVC resins, or any combination thereof. Since PVC processes easily and CPVC does not, since CPVC has heat resistance but PVC does not, and furthermore, since CPVC has a high melt viscosity but PVC does not, it should be apparent that CPVC and PVC are different materials and that PVC prior art is not analogous to patentability issues relating to CPVC. SUMMARY OF THE INVENTION In accordance with the present invention there is provided a process for making a low temperature melt processable CPVC polymer alloy composition comprising the steps of: forming a polycarbonate premixture, said polycarbonate premixture containing from 10 % to 80 % by weight of said polymer alloy of an aromatic polycarbonate, wherein the weight average molecular weight of said polycarbonate is from 10,000 to 200,000 and 1 % to 15 % by weight of said polymer alloy of an ethylene-based functional polymer being a copolymer of ethylene and at least one other monomer containing functional groups thereon to provide said polycarbonate premixture with a melt processing temperature or 230 °C or less; forming a CPVC premixture, said CPVC premixture comprising from 20 % to 70 % by weight of said polymer alloy of a chlorinated poly(vinyl chloride) containing from 57 % to 75 % by weight of chlorine therein and optionally 1 % to 25 % by weight of said polymer alloy of an impact modifier having a Tg of 0°C or less, and optionally 0.1 % to 20 % by weight of said polymer alloy of a viscosity improver polymer, forming the low temperature melt processable CPVC polymer alloy by mixing said CPVC premixture with said polycarbonate premixture at a temperature of 230 °C or less. DETAILED DESCRIPTION OF THE INVENTION The thermoplastic polymer alloy generally contains a chlorinated poly(vinyl chlorine), a polycarbonate, an ethylene-based functional polymer, an optional impact modifier and an optional viscosity improver. The chlorinated poly(vinyl chloride), i.e. CPVC, resins include any post-chlorinated poly(vinyl chloride), hereinafter CPVC, containing at least 57% by weight of chlorine. The CPVC resins contain from 57% to 75% of chlorine by weight and preferrably from 63% to 72% of chlorine by weight. Generally, any poly(vinyl chloride) (PVC) can be utilized for chlorination having an intrinsic viscosity, obtained utilizing a 99% by weight tetrahydrofuran solution with the PVC being the remaining 1% by weight, of from about 0.46 to about 1.4 and desirably from about 0.54 to about 1.0. The PVC can be prepared in any conventional manner such as by suspension, emulsion, or mass polymerization. Such methods of preparation are well known to the art as well as to the literature. The chlorination process can be carried out according to any method such as by a solution process, a fluidized bed process, a water slurry process, a thermal process, or a liquid chlorine process. Inasmuch as CPVC resins are known to the art as well as to the literature, they will not be discussed in great detail herein. Rather, reference is hereby made to the several CPVC patents set forth in the background, e.g. U.S. Patent Nos. 2,996,489; 3,100,762. The CPVC resins utilized in the present invention generally have a density of from about 1.45 to about 1.67 gm/cc at 25°C and a glass transition temperature (Tg) of from about 95°C to about 200°C. Such Tgs are at least 20°C higher than the glass transition temperature of unchlorinated PVC resins. The glass transition temperature was measured by a differential scanning calorimeter. The preferred CPVC resins have densities in the range of from about 1.55 to about 1.60 gm/cc at 25°C and a glass transition temperature of at least 100°C. Based upon the total amount of the above polymers forming the thermoplastic alloy blend, the amount of the CPVC resins therein is from 20% to 70% and desirably from 30% to 65% by weight. Inasmuch as the thermoplastic alloy can be either polycarbonate rich or CPVC rich, the preferred amount of CPVC will vary accordingly. In the polycarbonate rich embodiment, the preferred amount of the CPVC will be from about 20% to about 50% by weight. In the CPVC rich embodiment, the preferred amount of CPVC will be from about 50% to about 70% by weight. It is to be understood that such weight percentages is based upon only the polymer alloy and not upon any additives, stabilizers, etc. The polycarbonate utilized in the polymer alloy composition is an aromatic polycarbonate. The thermoplastic polymer alloy of CPVC and polycarbonate is generally a two-phase system. That is, a single overall glass transition temperature Tg, is not obtained. Depending upon whether the thermoplastic polymer alloy is CPVC rich or polycarbonate rich, the rich component will often exist in a continuous phase. The non-rich phase will often exist as a discontinuous phase within the continuous phase. Should generally equal amounts of these two polymers be utilized, portions of a continuous phase as well as a discontinuous phase of each material within the overall polymer alloy will often exist. Inasmuch as the CPVC and the polycarbonate polymers are partially compatible, small homogeneous phases will also exist. It is thus to be understood that various continuous, discontinuous, and even small homogeneous phases can exist within the polymer alloy but that the overall polymer alloy system will generally contain two separate and distinct phases. The aromatic polycarbonates have a low molecular weight, that is a weight average molecular weight of from 10,000 to 200,000 and preferrably from 10,000 to 30,000. Aromatic polycarbonates include various homopolycarbonates, various copolycarbonates and/or mixtures of various homo- and copolycarbonates. The amount of such aromatic polycarbonates is from 10% to 80% by weight and desirably from 30% to 70% by weight based upon the total weight of the various polymers forming the thermoplastic polymer alloy. When a CPVC rich composition is desired, the amount of the polycarbonate is from about 20% to about 50% by weight based upon the total weight of the alloy forming polymers. When a polycarbonate rich alloy is desired the amount of the aromatic polycarbonate is from about 60% to about 80% by weight. The specific types of aromatic polycarbonate utilized are generally not critical to the present invention provided that they are utilized in an amount and have a molecular weight as set forth herein above. Accordingly, various conventional types of aromatic polycarbonates can be utilized as well as other polycarbonates known to the art and to the literature. As part of the literature, numerous polycarbonate patents exist and the specific types of aromatic polycarbonate set forth therein can be utilized. Suitable aromatic polycarbonates which can be utilized are set forth in U.S. Patent No. 4,515,925. Generally, such aromatic polycarbonates are made from diphenols corresponding to the formula HO-Z-OH wherein Z represents a divalent mono- or polynuclear aromatic radical having from 6 to 30 carbon atoms, and is constructed such that each of the two OH groups is directly bound to a carbon atom of an aromatic system. Examples of other types of polycarbonates are set forth in U.S. Patent Nos. 3,544,514; 4,005,037; 4,105,711; 4,239,861; and 4,513,119. A description of other suitable polycarbonates is set forth in the Kirk-Othmer Encyclopedia of Chemical Technology, third edition, Volume 18, pages 479 - 494, Wiley 1982, New York. In polycarbonates, groups of dihydric or polyhydric phenols are linked through carbonate groups. Typically, polycarbonates are derived from bisphenol A and diphenyl carbonate through an ester exchange. Polycarbonates can also be made utilizing small amounts of other polyhydric phenols. The polycarbonates of the present invention are usually melt processable at temperatures of from about 260°C to about 300°C. Such temperatures are generally too high for melt mixing or blending with CPVC resins. Aromatic polycarbonates are commercially available with specific examples including General Electric Lexan polycarbonates, desirably Lexan® High Flow; Dow Chemical's Calibre® polycarbonates, and preferably such high melt flow polycarbonates; and Mobay Chemical's Merlon® polycarbonate resins, preferably Merlon FCR series. Ethylene-based functional polymers are utilized to reduce the processing temperature, to reduce the melt viscosity of the polycarbonate and also to impart high impact properties to the polymer alloy. An effective amount is utilized such that the Izod notch impact strength of the polymer alloy is at least 53.38 J/m (1.0 ft-lbs/inch) and desirably at least 106.76 J/m (2.0 ft-lbs/inch) or greater and the processing temperature is 230°C or less, desirably 220°C or less and preferably 215°C or less. Generally, the ethylene-based functional polymer is premixed with the polycarbonate at a temperature of about or below 220°C. Usually, an effective amount is from 1% to 15%, and preferably from 3% to 10% by weight of the ethylene-based functional polymers based upon the total weight of compounds forming the polymer alloy, that is the CPVC, the aromatic polycarbonate, the optional impact modifier, the optional viscosity improver, and the ethylene-based functional polymer. Large improvements in impact strength and/or decreases in processing temperatures are unexpectedly obtained when the ethylene-based functional polymer is premixed with the aromatic polycarbonate. Although the viscosity improver can also be mixed therewith, it is generally mixed with the CPVC. While not being intended to be bound to theory, it is thought that the ethylene type functional polymer reduces the viscosity of the polycarbonate and thus can lower the processing temperature. Mixing of the polycarbonate premixture can occur by utilizing any conventional melt method. For example, the various premixture components can be mixed on a two-roll mill, in a compounding screw extruder, in a twin screw extruder. Regardless of mixing method, the temperature is such to generally produce a melt mixture of from about 210°to about 230°C, desirably from about 210°to about 220°C, and preferably from about 215°to about 220°C. A stabilized CPVC premixture can also be made and contains the CPVC, a heat stabilizer, the optional impact modifiers, and the optional viscosity improvers. The CPVC premixture can also contain small amounts of the ethylene-based functional polymers although such is desirably utilized in the polycarbonate premixture. Mixing of the CPVC premixture can occur in any conventional melt mixing method such as by extrusion mixing, roll mill mixing. The temperatures are maintained generally below 230°C and preferably below 220°C. Otherwise, the CPVC tends to degrade or to decompose. If this occurs, the overall polymer alloy will have poor physical properties. The CPVC premixture is then mixed with the polycarbonate premixture in any conventional melt mix manner, for example extrusion mixing and roll mill mixing, at comparatively low temperatures, that is generally at temperatures of 230°C or less and preferably at 220°C or less. The polymer alloy is made utilizing the polycarbonate premixture, since as noted above, surprisingly good high impact properties and relatively low processing temperatures are achieved. In contrast thereto, should all the various components be simultaneously mixed together, high mixing temperatures, that is generally in excess of 220°C and usually in excess of 230°C are required with resulting deleterious effects upon the CPVC compound. Simultaneous mixing, furthermore, does not result in producing a polymer alloy having good impact strength. In addition to having good impact resistant properties, the properties of the the polymer alloy of the present invention include good ductility, good flame retardancy, good high heat distortion temperatures, and also good thermal and color stability. The polymer alloys can thus be utilized wherever such properties are desired, for example in structural plastics, calendering sheet and injection molding for equipment housings. The ethylene-based functional polymer is generally a copolymer of ethylene and at least one other monomer containing functional groups thereon. Generally, the remaining comonomer can be a vinyl ester having a total of from 1 to 10 carbon atoms with acetate being preferred. The amount of the vinyl ester component of the ethylene-based functional copolymer is from 5 to 50% by weight and desirably from 10 to 35% by weight. The ethylene-vinyl ester copolymers are often utilized as a blend with a small amount of another ethylene copolymer. The additional monomers of the second copolymer which contains functional groups are usually vinyl organic acids or organic anhydrides. For example, the additional comonomer can be acrylic acid, methacrylic acid, and various hydrocarbon derivatives thereof as well as maleic anhydride, or various derivatives thereof, wherein said acids and said anhydrides have a total of from 3 to 12 carbon atoms. Methacrylic acid is a preferred comonomer. The additional monomer of the second copolymer generally exists in a small amount as from 1% to 25% by weight based upon the total weight of the second or additional copolymer. When utilized, the amount of the second copolymer is generally small, as from 0 or 1% to 50% by weight and desirably from 5% to 40% by weight. Thus, the amount of the ethylene-viny ester copolymer exists in amount of from 50% to 100% by weight and preferably from 60% to 95% by weight. Other types of ethylene-based functional polymers or copolymers are set forth in U.S. Patent No. 4,230,830. This patent relates to a polymer blend consisting essentially of a. about from 80-99% by weight of a first olefinic polymer selected from (i) non-polar ethylene polymers and copolymers having a density of about from 0.930 to 0.965 g/cc and (ii) copolymers of ethylene having up to about 30 weight percent of at least one ethylenically unsaturated ester having from 4 to 12 carbon atoms; and b. about from 1-19% of a second olefinic polymer selected from the group consisting of (i) non polar ethylene polymers and copolymers having a density of about from 0.945 to 0.965 g/cc and (ii) terpolymers of ethylene, at least one a-olefin having from 3-6 carbon atoms, and at least one nonconjugated diene; the second olefinic polymer being thermally grafted with an unsaturated acid or anhydride to give a copolymer having about from 0.002 to 4.0 weight percent of grafted succinic groups, provided, however, that when the second olefinic polymer is (ii), then the first olefinic polymer is (ii). Regardless of whether or not a second or a terpolymer ethylene-based functional copolymer is utilized, as described in the preceding paragraph the melt index of the overall ethylene-based functional polymer, that is an ethylene-vinyl ester copolymer or blends thereof, is from about 2 to 40g/10 min and desirably from about 6 to about 25g/10 min. The density is from about 0.92 to about 1.1 g/cc and desirably from about 0.92 to about 0.96 g/cc. The ethylene-based functional polymer or blends thereof useful in the present invention are available from DuPont under the name Bynel® CXA resins such as CXA resin 1123 and/or resin 1124. A specific example of a suitable ethylene-based functional polymer is a blend of 92.5% by weight of an ethylene-vinyl acetate copolymer containing 28% by weight of vinyl acetate therein and 7.5% by weight of an ethylene-methacrylic acid copolymer containing 15% by weight of methacrylic acid therein. The impact modifiers which can be optionally utilized in the CPVC premixture are generally added in an effective amount which helps improve the impact strength, for example, the Izod notch strength of the polymer alloy. Such amounts when utilized generally range from 1 to 25%, desirably from about 2 to 15% and preferably 3 to 5% by weight based upon the total weight of the polymer alloy forming compounds. Suitable impact modifiers which can be utilized in the present invention have a Tg of generally 0°C or less and very often a much lower Tg is desirable. As known to the art as well as to the literature, many polymeric compounds which could impart good impact strength for rigid PVC can be utilized. Accordingly, various impact modifiers which impart improved impact resistance to the polymer alloy can be utilized including those known to the literature, such as for example those set forth in The Encyclopedia of PVC, Volume 2, Chapter 12, Marcel Dekker, Inc., New York, 1977. Examples of specific impact modifiers include the various acrylonitrile-butadiene-sytrene (ABS) polymers, the various chlorinated polyethylenes, the various acrylic rubbers, the various poly(ethylene-co-vinyl acetates, styrene-butadiene-styrene block copolymers, poly(methyacrylate-co-butadiene-co-styrene) (MBS), and the like. Impact modifiers of these types are commercially available. Preferred impact modifiers include ABS, MBS, and chlorinated polyethylene. Various viscosity improvers can optionally be utilized in the present invention. Generally, effective amounts are utilized to reduce the viscosity of the polymer alloy and more specifically to reduce the viscosity of the CPVC compound as in the CPVC premixture. Such compounds also tend to prevent the CPVC from degrading and hence also stabilize the same. Effective amounts, when utilized, are from 0.1 to 20% by weight, desirably from 0.5 to 10% by weight and preferably from 3 to 10% by weight based upon the total weight of the polymer alloy forming compounds as defined hereinabove. Such viscosity improvers are known to the art as well as to the literature. Examples of such various types include conventional compounds such as the various styrene-acrylonitrile copolymers, for example those described in the Encyclopedia of Polymer Science and Engineering, Volume I, pages 452-470, 1985, John Wiley & Sons, Inc., New York; a polymer of alpha methylstyrene, styrene, methyl methacrylate, or an acrylonitrile as described in U.S. Patent No. 4,304,884 to Okamoto. Other viscosity improvers include various lubricants such as low molecular weight oxidized polyethylenes, stearic acid, low molecular weight polyethylene. Although these types of viscosity improvers can be utilized, it is to be understood that various other types can be utilized and that such are known to the literature as well as to the art. The important aspect is that they generally lower the viscosity and hence also improve the stability of the CPVC compounds. In addition to the above polymer alloy forming compounds, the CPVC premixture according to the present invention preferably comprises a CPVC resin which has been premixed with heat stabilizers. The stabilization of CPVC resins and compounds finds their roots in PVC stabilization technology. Consequently, the stabilizers being used for CPVC resins are based on, for example, lead, barium and/or cadmium, calcium and/or zinc and organotin stabilizers. Among these, organotin stabilizers are widely used. Other secondary stabilizers (or called a co-stabilizer) can also be utilized. For example, epoxy compounds; e.g. epoxidized soybean oil, epoxy esters, are strongly synergistic co-stabilizers for metal-based stabilizer system, as well as for organic stabilizers. A detailed description of stabilizers is available in PVC Technology, Fourth Edition, Chapters 9 and 10, W.V. Titow (Editor), Elsevier Applied Science Publishers, London and New York, 1984. In addition to the above stabilizers, various conventional antioxidants can be utilized in typical amounts with regard to the various polycarbonates and the various ethylene-based functional polymers. These compounds are well known to the art as well as to the literature. The invention will be better understood by reference to the following examples. The following recipes with ingredients as specified, are mechanically melt-mixed in a 6 inch electric mill at 215° C for about 2 minutes and compression molded at 215° C for one and a half minutes in a laboratory press. In Examples 1-2, TempRite® T-1310 CPVC, manufactured by The BFGoodrich Company, is masterbatch with stabilizer, antioxidants, with and without Bynel® CXA 1123, an ethylene-based functional polymer available from DuPont. The ethylene-based functional compound has a melt index of 6.6 and comprises a blend of 92.5% of ethylene/28% vinyl acetate copolymer and 7.5% of ethylene/15% methacrylic acid copolymer. TempRite® T-1310 CPVC contains 69.6% bound chlorine, and has an intrinsic viscosity of about 0.68 in tetrahydrofuran (THF). Each batch of 100 parts of CPVC contains 4 parts stabilizer, such as T-31 THERMOLITE® stabilizer, available from M&T which is dibutyl tin bisisooctylthioglycolate; also 1 part of Irganox® 1010 which is 2,2-bis[[3,5-bis(1,1-Dimethylenthyl)-4-hydroxyphenyl]-1-oxopr opoxy ]methyl]-1,3-propanediyl 3,5-bis(1,1-dimethyl-ethyl)-4-hydroxybenzenepropanoate available from Ciba Geigy, and 0.5 parts of BHT which is (2,6-di-tert-butyl-4-methylphenol) available from Alrich. Example 1 does not contain any ethylene-based polymers. Example 2 contains 10 parts by weight of the ethylene-based copolymer blend. In Examples 3-4, Lexan® HP 2110-111, which is a high flow polycarbonate resin available from General Electric Company, having a weight average molecular weight of about 25,000, is melt mixed with 1 part by weight of Irganox® 1010 and 0.5 parts BHT, with and without Bynel® CXA 1123. Example 3 does not contain Bynel® CXA resin. Example 4 contains 10 parts Bynel® CXA 1123. The thermomechanical properties of these examples are listed in Table I. The above data demonstrates that the Bynel® CXA resin reduces the shear viscosity of unmodified CPVC and also very drastically lowers the shear viscosity of polycarbonate. At 220°C, the magnitude of shear viscosity of polycarbonate premixture containing 10 parts Bynel® CXA resin (Example 4) is similar to that of unmodified CPVC resin (Example 1). This improves the processability of blending polycarbonate with CPVC resin as will be discussed below. The compositions tested in Table II hereinbelow are identified as follows: In Example 5-7, each batch is formulated with 50 parts CPVC TempRite® T-1310, with 2 parts T-31 THERMOLITE® stabilizer, and also 50 parts Lexan HP 2110-111 with 1 part Irganox® 1010 and 0.5 parts BHT antioxidant. Example 5 does not include Bynel® CXA resin, while Examples 6 and 7 both contain 10 parts Bynel® CXA 1123. Examples 5 and 6 are prepared by mixing all the ingredients simultaneously at 215°C for 2 mins. Example 7 was prepared by premixing the Bynel® CXA resin and polycarbonate and antioxidants at 215°C to form a polycarbonate premixture, and then adding this premixture to the CPVC (plus stabilizer) at 215°C. The Izod impact strength and heat distortion temperature are listed in Table II. The foregoing data demonstrate, that the blend, Example 7, prepared according to the present invention by mixing Bynel CXA resin with the polycarbonate at 215°C to form a premixture and then mixing the same with the premix stabilized CPVC, exhibits better impact strength and also better heat distortion temperature, when compared with Example 6, an identical composition but wherein all of the ingredients were mixed simultaneously. Examples 8 - 11 relate to blend compounds comprising CPVC TempRite® T-1310 resin, polycarbonate, Bynel® CXA, impact modifiers, and processing improvers. The detailed compositions and processes are described hereinbelow. In Examples 12 and 13, however, a commercially available stabilized CPVC compound, TempRite® 3503, is used, a CPVC compound having a 67% Chlorine CPVC resin, and having an intrinsic viscosity of about 0.68 in THF. EXAMPLE 8 A CPVC mixture was prepared by mixing at 215°C in an electric two-roll mill, 70 parts by weight of CPVC TempRite® T-1310 (69.6% chlorine) with 10 parts by weight of styrene-acrylonitrile, 15 parts by weight of ABS modifier, 5 parts by weight of chlorinated polyethylene impact modifier, 2.8 parts of T-31 THERMOLITE® stabilizer and 0.5 parts of oxidized polyethylene lubricant. Various properties of this mixture are set forth in Table III. EXAMPLE 9 A polycarbonate mixture was prepared by mixing at 215°C in an electric mill, 30 parts by weight of polycarbonate with 5 parts by weight Bynel® CXA 1123 resin. The polycarbonate was Lexan® HP 2110-111 available from General Electric. The antioxidants used for polycarbonate premixture were 1 part by weight of Irganox® 1010 available from Ciba-Geigi and 1 part by weight of BHT available from Alrich. The melted polycarbonate premixture was then mixed at 215°C with 100 parts by weight of the stabilized CPVC-premixture as described in Example 8. Various properties are set forth in Table III. EXAMPLE 10 The composition was prepared as described in Example 9, using the same polymers with appropriate additives. The polycarbonate premixture, however, consisted of 100 parts by weight of polycarbonate and 5 parts by weight of Bynel® CXA 1123. Various properties are set forth in Table III. EXAMPLE 11 The composition was prepared as described in Example 9, using the same polymers with appropriate additives. The polycarbonate premixture consisted of 200 parts by weight of polycarbonate, and 10 parts by weight of Bynel® CXA 1123. Various properties are set forth in Table III. EXAMPLE 12 A 100 parts by weight of TempRite 3503 was melt-mixed at 215°C. The TempRite® 3503 was a CPVC compound based on 67% chlorine CPVC available from the BFGoodrich Company. Various properties are set forth in Table III. EXAMPLE 13 The polycarbonate premixture was prepared as described in Example 9, using 60 parts of Lexan® HP 2110-111, and 5 parts of Bynel® CXA 1123. A 100 parts of TempRite® 3503 as described in Example 12 was then mixed with the polycarbonate premixture at 215°C. Various properties are set forth in Table III. It is obvious from Table III that the polymer mixtures, Examples 9 - 11, according to the present invention, containing a high chlorine CPVC resin TempRite T-1310, polycarbonate, and also fully compounded with impact modifier and processing improvers, have much better impact strength and heat distortion temperatures than that without a premixture of polycarbonate-Bynel® CXA resin, i.e. Example 8. Example 13 containing a 67% chlorine CPVC compound TempRite® 3503 with polycarbonate and Bynel® CXA resin also had a much better impact strength and higher heat distortion temperature than that of TempRite 3503, Example 12.

Claims: A process for making a low temperature melt processable CPVC polymer alloy composition comprising the steps of: forming a polycarbonate premixture, said polycarbonate premixture containing from 10 % to 80 % by weight of said polymer alloy of an aromatic polycarbonate, wherein the weight average molecular weight of said polycarbonate is from 10,000 to 200,000 and 1 % to 15 % by weight of said polymer alloy of an ethylene-based functional polymer being a copolymer of ethylene and at least one other monomer containing functional groups thereon to provide said polycarbonate premixture with a melt processing temperature of 230 °C or less; forming a CPVC premixture, said CPVC premixture comprising from 20 % to 70 % by weight of said polymer alloy of a chlorinated poly(vinyl chloride) containing from 57 % to 75 % by weight of chlorine therein and optionally 1 % to 25 % by weight of said polymer alloy of an impact modifier having a Tg of 0°C or less, and optionally 0.1 % to 20 % by weight of said polymer alloy of a viscosity improver polymer, forming the low temperature melt processable CPVC polymer alloy by mixing said CPVC premixture with said polycarbonate premixture at a temperature of 230 °C or less. A process according to claim 1,wherein the amount of said polycarbonate is from 10 % to 80 % by weight of said polymer alloy, wherein the weight average molecular weight of said polycarbonate is from 10,000 to 200,000 wherein the amount of said ethylene-based functional polymer is from 1 % to 15 % by weight of said polymer alloy, including melt processing said polycarbonate premixture at a temperature of 230 °C or less, wherein the amount of said CPVC is from 20 % to 70 % by weight of said polymer alloy, wherein said CPVC has a chlorine content of from 57 % to 75 % by weight, and including melt processing said CPVC premixture at a temperature of 230 °C or less. A process according to claim 2,wherein said ethylene-based functional polymer is a blend of an ethylene-vinyl ester and an ethylene-vinyl and functional containing copolymer, wherein said vinyl ester portion of said ethylene-vinyl ester copolymer has a total of from 1 to 10 carbon atoms, wherein the amount of said ethylene-vinyl ester copolymer is from 50 % to 100 % by weight based upon the total amount of said ethylene-vinyl ester copolymer and said ethylene-vinyl and functional containing copolymer, and wherein the amount of said ethylene-vinyl and functional containing copolymer is from 0 % or 1 % to 50 % by weight, and wherein said vinyl and functional portion of said ethylene-vinyl and functional copolymer is a vinyl organic acid or an organic anhydride having from 3 to 12 carbon atoms. A process according to claim 3, wherein the amount of said CPVC is from 30 % to 65 % by weight of said polymer alloy, including an impact modifier, wherein the amount of said impact modifier is from 2 % to 15 % by weight of said polymer alloy, wherein the amount of said polycarbonate is from 30 % to 70 % by weight of said polymer alloy, wherein said polycarbonate has a weight average molecular weight of from 10,000 to 30,000, wherein the amount of said chlorine in said CPVC is from 63 % to 72 % by weight, and wherein the total amount of said ethylene copolymers is from 3 % to 10 % by weight of said polymer alloy, and wherein the Izod notch impact strength of said polymer alloy is at least 53.38 J/m (1.0 ft-lb/in). A process according to claim 1, wherein said ethylene-based functional copolymer is a blend of an ethylene-vinyl ester copolymer and at least one ethylene-vinyl and functional containing copolymer, wherein the amount of said ethylene-vinyl ester copolymer is from 50 % to 100 % by weight based upon the total weight of said ethylene-vinyl ester copolymer and said ethylene-vinyl and functional containing copolymer, wherein the amount of said ethylene-vinyl and functional containing copolymer is from 0 % or 1 % to 50 % by weight, wherein said ester portion of said ethylene-vinyl ester copolymer contains a total of from 1 to 10 carbon atoms, wherein said vinyl and functional portion of said ethylene-vinyl and functional copolymer contains a vinyl organic acid or an organic anhydride having from 3 to 12 carbon atoms and wherein the weight of said vinyl ester portion of said ethylene-vinyl ester copolymer is from 5 % to 50 % by weight. A process according to claim 5, wherein the amount of said CPVC is from 30 % to 65 % by weight of said polymer alloy, wherein the amount of said polycarbonate is from 30 % to 70 % by weight of said polymer alloy, wherein said polycarbonate has a weight average molecular weight of from 10,000 to 30,000. A process according to claim 6, wherein the amount of said chlorine in said CPVC is from 63 % to 72 % by weight, wherein the total amount of said ethylene-based functional copolymers is from 3 % to 10 % by weight of said polymer alloy, and wherein said polymer alloy has a melt processing temperature of 220 °C or less. A process according to claim 7 wherein the amount of said ethylene-vinyl ester copolymer is from 60 % to 95 % by weight, wherein said vinyl ester is vinyl acetate, wherein the amount of said vinyl acetate in said ethylene-vinyl acetate copolymer is from 10 % to 35 % by weight, wherein the amount of said ethylene-vinyl and functional containing copolymer is from 5 % to 40 % by weight, wherein said vinyl and functional containing portion of said ethylene-vinyl and functional containing copolymer is a methacrylic acid, and wherein the amount of said methacrylic acid in said ethylene-methacrylic acid copolymer is from 1 % to 25 % by weight. A process according to claim 8, including from 2 % to 15 % by weight of an impact modifier, and including from 0.5 % to 10 % by weight of a viscosity improver.

Inventors: LEE, BIING-LIN
Applicants: THE B.F. GOODRICH COMPANY
Application year: 1987
Main classification: C08L27
IPC codes: C08L101, C08L27, C08L1, C08L7, C08L23, C08L69, C08L51, C08L77, C08L21