Thermoplastic elastomer blends of a polyvinyl chloride-acrylate copolymer and a cured acrylate elastomer
FIELD OF THE INVENTION 
     The present invention relates to thermoplastic elastomer blends of a polyvinyl chloride-acrylate copolymer and a cured acrylate elastomer. The acrylate elastomer can be precrosslinked before blending, or can be crosslinked in situ when blended with the copolymer, or can be crosslinked after blending. The blends have exceptional softness, very low compression set, good high temperature deformation resistance, improved oil resistance, and low temperature flexibility. 
     BACKGROUND 
     U.S. Pat. No. 4,380,606 to Coran and Patel relates to a thermoplastic composition containing a blend of neutralized acrylic-olefin copolymer, and a polyvinyl chloride. 
     SUMMARY OF THE INVENTION 
     The blends of the present invention containing polyvinyl chloride therein have several favorable properties including good oil resistance, high temperature heat deformation resistance, good low temperature flexibility, and very low compression set. The blend, which is a thermoplastic elastomer, is also very soft and thus exhibits plasticized properties and has no bleeding out of any material. The blend contains a copolymer made by the polymerization of vinyl chloride monomers with optional vinyl chloride component comonomers and one or more acrylate monomers. The blend also contains an acrylate elastomer which generally has a very high weight average molecular weight, as for example at least 100,000, and can be a homopolymer or a copolymer. The acrylate elastomer generally contains reactive or functional groups therein such as halogen and/or carboxyl groups which permit the acrylate elastomer to be crosslinked. Cure can occur after blending with the acrylate elastomer or in situ as when the acrylate elastomer is blended with the polyvinyl chloride-acrylate copolymer or it can be precured and subsequently blended with the polyvinyl chloride-acrylate copolymer. 
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     The thermoplastic elastomer blends of the present invention contain polyvinyl chloride generally in the form of a copolymer. The copolymer is a polyvinyl chloride-acrylate copolymer made from (a) a vinyl chloride constituent, that is, a vinyl chloride monomer and an optional vinyl component comonomer and (b) one or more acrylate monomers. The amount of vinyl chloride monomer and optional vinyl component comonomer utilized to make the polyvinyl chloride-acrylate copolymer is a sufficient amount so that the polyvinyl chloride-acrylate copolymer generally contains from about 10 parts to about 90 parts by weight, desirably from about 25 parts to about 80 parts by weight and preferably from about 40 parts to about 60 parts by weight of vinyl chloride and/or optional vinyl component units therein for every 100 parts by weight of the copolymer. Thus, the amount of the acrylate units in the copolymer is generally from about 90 parts to about 10 parts by weight, desirably from about 75 to about 20 parts by weight, and preferably from about 60 to about 40 parts by weight. The amount of the optional vinyl component units in the copolymer is from about 0 to about 45 parts by weight with from about 0 to about 20 parts by weight being preferred. In other words, the vinyl chloride constituent can contain up to 50 percent thereof and preferably up to 22 percent thereof by weight of the vinyl component unit. By the term &#34;vinyl component&#34;, it is meant a vinyl unit other than vinyl chloride. Such units are well known to the art and to the literature and are derived from vinyl esters wherein the ester portion contains from 1 to 18 carbon atoms such as vinyl acetate; vinylidene chloride; 1,2-dichloroethylene; styrene and styrene derivatives having a total of from 8 to 15 carbon atoms such as alphamethylstyrene, vinyl toluene, chlorostyrene, chloromethylstyrene; vinyl naphthalene; diolefins having a total of from 4 to 18 carbon atoms such as butadiene, isoprene, including halogenated diolefins such as chloroprene; monoolefins having a total of from 2 to 18 carbon atoms and preferably 2 to 4 carbon atoms; and the like. Vinyl acetate is a preferred vinyl component comonomer which, upon polymerization, becomes a vinyl component unit. 
     The one or more acrylate units contained in the polyvinyl chloride-acrylate copolymer has the formula, before polymerization, ##STR3## wherein R 1  is an aromatic, an aliphatic (especially an alkyl), or combinations thereof, having from 1 to 18 carbon atoms, or a halogen derivative thereof, desirably is methyl, and preferably is hydrogen. R 2  is an aliphatic group, especially an alkyl, an aromatic, an alkyl hydroxyl, or combinations thereof, having from 1 to 18 carbon atoms, desirably from 2 to 10 carbon atoms, and preferably from 2 to 8 carbon atoms, or a halogen derivative thereof; or R 2  is a hydrocarbyl ether such as alkoxyalkyl, a phenoxyaryl, or a phenoxyalkyl, or combinations thereof having from 2 to 1,000 carbon atoms, desirably from 2 to 18 carbon atoms, and preferably from 2 to 8 carbon atoms, or a substituted halogen, oxygen, nitrogen, or sulfur derivative thereof. Examples of specific acrylate monomers include ethyl acrylate, propyl acrylate, butyl acrylate, hexyl acrylate, octyl acrylate, 2-ethyl hexyl acrylate, nonyl acrylate, decyl acrylate, phenyl acrylate, nonylphenyl acrylate, ethyl methacrylate, butyl methacrylate, hexyl methacrylate, 2-ethyl hexyl methacrylate, methoxymethyl acrylate, methoxyethyl acrylate, ethoxyethyl acrylate, butoxyethyl acrylate, ethoxypropyl acrylate, 2(2-ethoxyethoxy)ethyl acrylate, and the like. Especially preferred acrylate monomers include butyl acrylate, 2-ethyl hexyl acrylate, ethyl acrylate, and the like. As noted hereinabove, the R 2  group can be a hydrocarbyl ether group. That is, it can be an ether, a diether, or a multiple ether of an alkyl, an aryl, or combinations thereof, such as an alkoxyalkyl, a phenoxyaryl, a phenoxyalkyl, and the like, generally having from 2 to 1,000 carbon atoms, desirably from 2 to 18 carbon atoms, and preferably from 2 to 8 carbon atoms, or combinations thereof. Examples of specific alkoxyalkyl acrylates include methoxymethyl acrylate, butoxyethyl acrylate; ethoxypropyl acrylate, methoxyethyl acrylate, ethoxyethyl acrylate, 2(2-ethoxyethoxy)ethylacrylate, and the like. Examples of specific phenoxyalkyl acrylates include 2-phenoxylethyacrylate and 2-phenoxyethylmethacrylate. In addition to the above R 2  ether groups, halogen, oxygen, nitrogen, or sulfur derivatives of such hydrocarbyl ether groups can also be utilized. For examples R 2  can be an alkoxyalkyl containing at least one halogen therein in lieu of a hydrogen atom. 
     The molecular weight of the polyvinyl chlorideacrylate copolymer is measured in terms of inherent viscosity and is from about 0.3 to about 4.0, desirably from about 0.8 to about 2.0, and preferably from about 1.0 to about 1.5. The inherent viscosity is measured utilized cyclohexanone as the solvent. The copolymer is dissolved in the solvent at 90° C. for 90 minutes and then measured with a viscometer in a water bath at 30° C. 
     The polyvinyl chloride-acrylate copolymer can be polymerized from the above-noted monomers in any conventional manner such as emulsion, mass, solution, and the like with suspension being preferred. Generally, polymerization is initiated with a free radical initiator such an alkanoyl, aroyl, alkaroyl, or an aralkanoyl diperoxide, a monohydroperoxide, or an azo compound, a peroxy ester, a percarbonate or any other suitable free radical-type initiator. Examples of specific initiators include benzoyl peroxide, laurayl peroxide, diacetyl peroxide, cumene hydroperoxides, methyl ethyl ketone peroxide, diisopropylbenzene hydroperoxide, 2,4-dichlorobenzoyl peroxide, naphthoyl peroxide, t-butyl perbenzoate, di-t-butyl perphthalate, isopropyl percarbonate, acetyl cyclohexane sulfonyl peroxide, disecondary butyl peroxydicarbonate, t-butyl peroxyneodecanoate, dinormal propyl peroxydicarbonate, azo-bisisobutyronitrile, alpha, alpha&#39;-azodiisobutyrate, 2,2&#39;-azo-bis-(2,4-dimethyl valeronitrile), and the like; Polymerization can be carried out at suitable temperatures with temperatures of from about 10° to 85° C. being desired and from about 40° to about 65° C. being preferred. The amount of the initiator utilized is generally quite small as from about 0.005 parts by weight to about 1.0 parts by weight and preferably from about 0.01 to about 0.1 parts by weight for every 100 parts by weight of the total monomers being copolymerized. 
     The utilization of a cured acrylate elastomer blended with the above copolymer has been found to impart unexpected good physical properties such as low compression set, high temperature heat deformation resistance, good oil resistance, and yield a soft plastic. In effect, the acrylate elastomer acts as a plasticizer in that it softens the system and yet does not bleed out and hence does not result in shrinkage of the polymer following immersion in hot oil. Rather, the polymer will actually swell. One or more acrylate monomers can be utilized in forming the acrylate elastomer. Such monomers have the formula ##STR4## wherein R 3  is an aromatic, an aliphatic (especially an alkyl), or combinations thereof, having from 1 to 18 carbon atoms, or a halogen derivative thereof, desirably is methyl, and preferably is hydrogen. The R 4  group is an aliphatic, especially an alkyl group, an aromatic, an alkyl hydroxyl, or combinations thereof, having from 1 to 18 carbon atoms, desirably from 2 to 10 carbon atoms, and preferably from 2 to 8 carbon atoms, or a halogen derivative thereof; or R 4  is a hydrocarbyl ether such as alkoxyalkyl, a phenoxyaryl, or a phenoxyalkyl, or combinations thereof, having from 2 to 1,000 carbon atoms, desirably from 2 to 18 carbon atoms, and preferably from 2 to 8 carbon atoms, or a substituted halogen, oxygen, nitrogen, or sulfur derivative thereof. Examples of specific acrylate monomers include ethyl acrylate, propyl acrylate, butyl acrylate, hexyl acrylate, octyl acrylate, 2-ethyl hexyl acrylate, ethyl methacrylate, butyl methacrylate, hexyl acrylate, and the like. Often, as noted, two or more acrylate monomers are utilized such as ethyl acrylate and butyl acrylate, butyl acrylate and 2-ethyl hexyl acrylate, ethyl acrylate and 2-ethyl hexyl acrylate, and the like. Generally the amount of any one acrylate monomer to the remaining acrylate monomers forming the acrylate elastomer can range from about 0.1 percent to about 99.9 percent by weight. Examples of specific alkoxyalkyl acrylates include methoxymethyl acrylate, butoxyethyl acrylate; ethoxypropyl acrylate; methoxyethyl acrylate, ethoxyethyl acrylate, 2(2-ethoxyethoxy)ethylacrylate, and the like. Examples of specific phenoxyalkyl compounds include 2-phenoxylethyacrylate and 2-phenoxyethylmethacrylate. In addition to the above R 4  ether groups, halogen, oxygen, nitrogen, or sulfur derivatives of such hydrocarbyl ether groups can also be utilized. The amount of the hydrocarbyl ether acrylate monomer utilized in forming the acrylate elastomer is generally from about 0.1 to about 60 percent by weight and preferably from about 10 to about 50 percent by weight based upon the total weight of the acrylate elastomer Formula II type monomers. A preferred acrylate elastomer is made from about 20 to about 60 percent by weight of methoxy ethyl acrylate, from about 20 to about 40 percent by weight of ethyl acrylate, and from about 20 to about 40 percent by weight of butyl acrylate. Another preferred acrylate elastomer is made from about 40 percent to about 60 percent by weight of methoxyethyl acrylate and from about 40 to about 60 percent by weight of butyl acrylate. Still another preferred acrylate elastomer is made from about 70 to about 90 percent by weight of butyl acrylate monomers and from about 10 percent to about 30 percent by weight of ethyl acrylate monomers. Yet another preferred system contains from about 80 to about 100 percent by weight of ethyl acrylate monomers and from about 0 to about 20 percent by weight of butyl acrylate monomers. 
     During the polymerization of the acrylate elastomer, a small amount of reactive or functional groups are added to the polymer so that it can be cross-linked. Such functional groups are well known to the art and to the literature and include various halogens such as chloro groups and/or carboxyl groups that are derived from various monomers. Examples of halogen-containing monomers include vinyl chloroacetate, allyl chloroacetate, 2-chloroethyl acrylate, 2-chloroethyl vinyl ether, vinyl benzyl chloride, 5-chloromethyl-2-norbornene, 5-chloroacetoxymethyl-2-norbornene, and the like. Examples of suitable carboxyl-containing monomers are the various monocarboxylic or polycarboxylic monomers containing from 3 to 8 carbon atoms such as acrylic acid, methacrylic acid, itaconic acid, and the like. The amount of such functional containing monomers is from about 0.1 to about 10 parts by weight and preferably from about 0.5 to about 5 parts by weight for every 100 parts by weight of the acrylate elastomer forming monomers. 
     The various acrylate elastomers can generally be prepared in any conventional manner such as suspension, emulsion, solution, bulk, and the like, with free radical emulsion polymerization being preferred. Various conventional soaps, emulsifiers, and surfactants, known to the art and to the literature can be utilized in forming the acrylate elastomer. Specific examples of free radical initiators include organic peroxides and hydroperoxides such as benzoyl peroxide, dicumyl peroxide, cumene hydroperoxide, and the like, used alone or with redox systems; diazo compounds such as azobisisobutyronitrile, and the like; persulfate salts such as sodium, potassium, and ammonium persulfate, used alone or with redox systems. Polymerization temperature is generally from about -10° to about 100° C. with from about 5° about 80° C. being preferred. Once the polymer has been formed, it can be recovered by any conventional method such as coagulation and the like. The weight average molecular weight of the acrylate elastomer is generally quite high, that is generally in excess of 100,000. 
     The polyvinyl chloride-acrylate copolymer desirably is not crosslinked so that it has good processing properties. However, it is to be understood that it is within the ambit of the present invention to either partially crosslink or crosslink the polyvinyl chlorideacrylate copolymer to provide improved physical properties. Should the polyvinyl chloride-acrylate copolymer be crosslinked or cured, any conventional crosslinking agent can be utilized such as diallyl phthalate, various diacrylates such as butanediol diacrylate, diethylene glycol diacrylate, and the like. The acrylate elastomer is generally cured, that is an amount of crosslinking agent is utilized such that an increase and preferably a significant increase in the modulus of the acrylate elastomer will occur. According to the concepts of the present invention, the acrylate elastomer can either be precured, that is cured before blending with the polyvinyl chloride-acrylate copolymer, or cured either when blending therewith or after blending. Desirably the product is cured before blending or cured while blending. However, it is to be understood that it is within the ambit of the present invention that the acrylate elastomer can be cured after blending of the acrylate elastomer with the polyvinyl chloride-acrylate copolymer. However, precure, or in situ cure while blending in the acrylate elastomer, is preferred. 
     Suitable crosslinking agents are well known to the art and to the literature and include various quaternary ammonium salts, various phosphonium compounds, and the like, either in a one-part system or in a two-part system, such as those set forth in U. S. Pat. No. 3,875,092, to Morris, which is hereby fully incorporated by reference. The total amount of the crosslinking agent generally utilized is from about 0.1 to about 30 parts by weight and preferably from about 1 to about 10 parts by weight for every 100 parts by weight of the acrylate elastomer forming monomers. 
     When the acrylate elastomer is crosslinked prior to blending with the polyvinyl chloride-acrylate copolymer, crosslinking is carried out by adding the above-noted amount of crosslinking agent to the acrylate elastomer and curing the same as at a temperature of from about 85° to about 230° C. and preferably from about 150° to about 204° C. Once the acrylate elastomer has been crosslinked, it is subsequently blended with the polyvinyl chloride-acrylate copolymer. The amount of the precrosslinked acrylate elastomer utilized is from about 1 to about 400 parts by weight, desirably from about 50 to about 300 parts by weight, and preferably from about 75 to about 200 parts by weight for every 100 parts by weight of the polyvinyl chloride-acrylate copolymer. In order that the crosslinked or cured acrylate elastomer can be readily blended in the copolymer in order to provide improved properties, it is usually ground to a suitable size as from about 1 micron to about 20,000 microns, desirably from about 1 micron to about 10,000 microns, and preferably from about 1 micron to about 1,000 microns. Any suitable or conventional grinding or cyrogenic grinding apparatus can be utilized. Blending can occur utilizing any conventional mixing device in which some shear or mechanical mixing occurs as for example, an extruder, a two-roll mill, a banbury, and the like. The blending operation occurs at a temperature of from about ambient, that is from about 20° C. to about 230° C., desirably from about 35° C. to about 205° C., and preferably from about 120° C. to about 175° C. Mixing generally continues until a relatively thoroughly dispersed blend is obtained. A true physical thermoplastic elastomer blend is achieved since the crosslinked acrylate elastomer is dispersed throughout the polyvinyl chloride-acrylate copolymer. 
     An alternative blending technique or system involves adding the uncrosslinked or uncured acrylate elastomer to the polyvinyl chloride-acrylate copolymer and blending it therewith and at the same time, i.e., simultaneously (in situ), cure the acrylate elastomer. The amount and type of crosslinking agents utilized are the same as set forth hereinabove with regard to the precrosslinked technique and accordingly are hereby incorporated. Any suitable mixing device can be utilized such as a two-roll mill, a banbury, an extruder, and the like. The blending as well as curing temperature of the in situ technique is ambient, that is from about 20° C. to about 230° C. Inasmuch as cure occurs generally in excess of 85° C., desirable in situ mixing and curing temperatures are from about 85° C. to about 230° C. and preferably from about 150° C. to about 204° C. Generally, high shear mixers are preferred because they better reduce the size of the elastomer domains and yield better surface appearance of the final thermoplastic elastomer blend. The amount of acrylate elastomer blended with the polyvinyl chlorideacrylate copolymer according to the in situ cure method is generally from about 1 to about 300 parts by weight, desirably from about 50 to about 200 parts by weight, and preferably from about 60 to about 140 parts by weight for every 100 parts by weight of the polyvinyl chlorideacrylate copolymer. Blending is continued until the acrylate elastomer is generally cured and dispersed throughout the copolymer. 
     Still another alternative blending technique or system involves blending and mixing the uncrosslinked or uncured acrylate elastomer with the polyvinyl chlorideacrylate copolymer and blending the same and subsequently, that is later, curing the acrylate elastomer. The amount of the acrylate elastomer utilized in this post cure system is the same as the in-situ system. The mixing temperature of the blending can occur from about ambient to below the curing temperature of the acrylate elastomer such as to about 85° C. Cure occurs at a temperature of from about 85° to about 230° C., with from about 150° to about 204° C. being preferred. Generally, high shear mixers are utilized and the amount of the acrylate elastomer is the same as set forth hereinabove with regard to the in-situ cure system. 
     Various conventional additives in conventional amounts can be utilized in the blends of the present invention. Thus, various heat stabilizers such as barium/cadmium compounds, lead compounds, and organotin compounds, various conventional lubricants generally utilized with polyvinyl chloride polymers such as paraffin, polyethylene, stearic acid, various processing aids such as polyacrylates, various antioxidants such as BHT, that is butylated hydroxy toluene, BHA, that is butylated hydroxy anisole, and various hindered phenols, various UV inhibitors such as substituted benzophenones, and the like, can be utilized. Moreover, plasticizers, such as those typically used to plasticize polyvinyl chloride and known to one skilled in the art, for example dioctyl phthalate, dioctyl adipate, etc., can also be utilized. Generally, if a plasticizer is utilized, it is utilized in a small amount since the acrylate elastomer as well as the acrylate portion of the polyvinyl chloride/acrylate copolymer act as plasticizing agents. 
     Various fillers and pigments can also be utilized in conventional amounts such as up to about 200 or 300 parts by weight for every 100 parts by weight of the polyvinyl chloride-acrylate copolymer. Examples of fillers include calcium carbonate, clay, silica, the various silicates, talc, carbon black, and the like. Such fillers are generally added in high amounts as from about 10 to about 200 parts by weight for every 100 parts by weight of the polyvinyl chloride-acrylate copolymer. Examples of various pigments include titanium dioxide, carbon black, and the like. Generally, the amount of such pigments is not as large as the amounts of the fillers. 
     The various additives, fillers, pigments, and the like in the precured acrylate elastomer system are generally added to the mixer with the acrylate elastomer. In the in situ blending operation, such additives are generally added with the acrylate elastomer and dispersed within the thermoplastic elastomer system during cure and blending of the acrylate elastomer. 
     Regardless of the particular blending technique or operation utilized, an important processing advantage of the present invention is that the various components can be processed on conventional elastomer equipment as well as conventional thermoplastic equipment. Examples of conventional elastomer equipment include mills, mixers, and extruders designed for the processing of elastomers. Such equipment is generally heated and/or cooled. The extruders generally have a length/diameter ratio of 20 or less. 
     The thermoplastic elastomer blends of the present invention in comparison with monomerically plasticized polyvinyl chloride of the same hardness have several improved properties such as improved oil resistance which tends to increase as larger amounts of the acrylate elastomer are utilized. Another property is high temperature heat deformation resistance. That is, the blends of the present invention can withstand higher temperatures without being deformed as much as conventional polyvinyl chloride. Low temperature flexibility is also improved. A notable and significant unexpected result achieved by blends of the present invention is low compression set, that is good recovery. The term &#34;compression set&#34; is defined as set forth in ASTM specification D-395, Method B. 
     Blends of the present invention containing at least 40 parts, desirably at least 50 parts by weight, and preferably at least 60 parts by weight of acrylate elastomer therein based upon 100 parts by weight of the polyvinyl chloride-acrylate copolymer have a compression set of 40 percent or less, and preferably 30 percent or less when measured after heating at 100° C. for 22 hours. Another notable improved property of the present invention is the achievement of a very soft plastic. That is, thermoplastic elastomer blends containing acrylate elastomer in an amount of at least 50 parts and preferably at least 100 parts by weight based upon 100 parts by weight of the polyvinyl chloride-acrylate copolymer wherein the acrylate portion is greater than 40 percent by weight, generally have a Shore A hardness of 50 or less, and preferably 40 or less. 
     The thermoplastic elastomer blends of the present invention can be utilized wherever such properties are desired such as for example in injection molding, extrusion, thermoforming, compression molding, calendering, and the like, with specific applications including gaskets, seals, weatherstripping, sporting equipment, hoses, tubing, automobile bumpers, and the like. 
     The invention will be better understood by reference to the following examples. 
     EXAMPLE 1 
     Procedure of Vinyl Chloride Monomers/2-ethylhexyl Acrylate Polymerization 
     The polymerization vessel was charged with the following ingredients: 
     
         ______________________________________                                    
Water                   2223   kg.                                        
Vinylchloride monomer   889    kg.                                        
2-ethylhexyl acrylate   593    kg.                                        
Polyvinyl alcohol dispersants                                             
                        28.2   kg.                                        
Substituted cellulose dispersant                                          
                        22.7   kg.                                        
Initiator               0.445  kg.                                        
______________________________________                                    
 
    
     The vessel was charged with water and the dispersants first. After evacuation, the mixture of monomers was added and after the mixing of the contents, the temperature was adjusted to 55° C. Lastly, the initiator was added and the reaction started. The polymerization was carried out for 420 minutes after which time the reactor was cooled to room temperature. The polymer was transferred to a stripping vessel to remove unreacted monomers. After the stripping, the polymer was recovered by filtration and dried. 
     EXAMPLE 2 
     A crosslinked acrylate elastomer was prepared by blending a commercial acrylate elastomer (Polymer A) with a curative system consisting of sodium stearate (4 parts by weight per 100 parts of elastomer) and cetyl trimethyl ammonium bromide (1 part by weight per 100 parts of elastomer) in a laboratory size Banbury mixer. The mixture was mixed in the Banbury for eight minutes and dropped. The stock temperature was 254° F. and the material had a crumb-like consistency coming out of the Banbury. This product was cryogenically ground through a 3/8 inch screen and coated with 6 percent magnesium silicate. 
     The ground crosslinked acrylate elastomer was blended with a copolymer of vinyl chloride and 2-ethylhexyl acrylate which had been prepared in a manner similar to Example 1. The polyvinyl chloride/2-ethylhexyl acrylate copolymer thus formed contained approximately 56 percent polyvinyl chloride and 44 percent 2-ethylhexyl acrylate based on chlorine analysis of a similarly prepared resin. 
     The ground crosslinked acrylate elastomer and the polyvinyl chloride/2-ethylhexyl acrylate copolymer plus other compound ingredients were blended in a laboratory (BR size) Banbury and then milled on a 6&#34;×16&#34; unheated mill for two minutes after banding and removed as a sheet from the mill. The milled sheet was cut both into approximately 1&#34; wide strips and 6&#34;×6&#34; plaques. The 6&#34;×6&#34; plaques were compression molded using a two minute preheat and a three minute press time at 320° F. These molded sheets were then used to determine the physical properties as given in Table I. The 1&#34; wide strips were extruded on an extruder designed to process elastomeric materials. The extruder has an approximate 7:1 length/diameter ratio (deep-flighted screw) and is heated by circulating hot water. The samples were extruded using a Garvey die and surface appearance was measured and is reported in Table I. 
     This example illustrates that blends of a ground crosslinked acrylate elastomer with a polyvinyl chloride/2-ethylhexyl acrylate copolymer will produce a product with improved compression set resistance, oil resistance, high temperature deformation properties, low temperature flexibility and lower hardness. These blends are also extrudable on equipment designed for processing elastomers. 
     EXAMPLE 3 
     The polyvinyl chloride/2-ethylhexyl acrylate copolymer of Example 1 plus other compounding ingredients were blended with a series of uncured acrylate elastomers (Polymer A, Polymer B, Polymer C) and a curative system in a laboratory Banbury (BR size) mixer. The mixture was dropped from the Banbury mixer at approximately 300°-350° F. and then placed on a 6&#34;×16&#34; unheated mill and formed into a sheet. The milled sheet was cut into both 1&#34; wide strips and 6&#34;×6&#34; plaques. The 1&#34; wide strips were extruded on an extruder designed for processing elastomer materials. The extruder contained an approximately 7:1 length/diameter deep-flighted screw and was heated using circulating hot water. The samples were extruded using a Garvey die and extrusion rates and surface appearance are give in Table II. The 6&#34;×6&#34; plaques were pressed using a 2 minute preheat and 3 minute press at 350° F. and then submitted for physical testing. The results of this testing are given in Table II. The results in Table II illustrate that blends of an uncured acrylate elastomer, a curative for the elastomer, and a polyvinyl chloride/2-ethylhexyl acrylate copolymer which are cured while mixing will produce products with improved compression set resistance, oil resistance, lower hardness, reduced high temperature deformation and, depending on the acrylate elastomer chosen, improved low temperature flexibility. 
     EXAMPLE 4 
     Blends of the polyvinyl chloride/2-ethylhexyl acrylate copolymer described in Example 1 with an uncured acrylate elastomer (Polymer A) were prepared in the presence of a curing system for the elastomer using a laboratory Banbury (BR size) mixer. Filler levels and types were varied in order to determine the effect on extrudate smoothness. The mixtures were compounded in the Banbury in the presence of stabilizers and an antioxidant and then dropped from the Banbury at stock temperatures of 299° to 352° F. The mixture was then placed on a 6&#34;×16&#34; unheated mill and formed into a sheet. The milled sheet was cut into both 1&#34; wide strips and 6&#34;×6&#34; plaques. The 1&#34; wide strips were extruded on an extruder designed for processing elastomeric materials as described in Example 2. The extrudates were rated for surface appearance and the extrusion rate was recorded. The 6&#34;×6&#34; plaques were compression molded using a 2 minute preheat and 3 minute press at 356° F. and then submitted for physical testing. The results of this testing are given in Table II. 
     This example illustrates that the proper choice of filler can significantly improve extruded part surface appearance while maintaining good compression set properties and oil resistance. The oil resistance was measured by ASTM D-471. 
     
         ______________________________________                                    
CODE                                                                      
______________________________________                                    
POLYMER A  ethyl, butyl and methoxyethyl acrylates                        
           1/3 each - plus chlorine and carboxyl                          
           containing reactive cure monomers                              
POLYMER B  ethyl acrylate - plus chlorine and                             
           carboxyl containing reactive cure monomers                     
POLYMER C  copolymer of butyl acrylate and ethyl                          
           acrylate (80/20) - plus chlorine and                           
           carboxyl containing reactive cure monomers                     
______________________________________                                    
 
    
     
                       TABLE I.sup.1                                               
______________________________________                                    
PVC/2-ethylhexyl                                                          
             100     100     100   100   100                              
acrylate copolymer                                                        
Ground Acrylate                                                           
             0       20      50    100   200                              
Elastomer                                                                 
(Polymer A)                                                               
Banbury Time (min.)                                                       
             5.5     4.2     3.2   3.9   3.2                              
Banbury Drop Temp.                                                        
             304     300     302   302   310                              
(°F.)                                                              
Extrusion Stock                                                           
             193     214     221   216   214                              
Temp. (°F.)                                                        
Extrusion Rate                                                            
             220     234     206   226   224                              
(g/min)                                                                   
Extrusion Surface                                                         
             small   smooth  smooth                                       
                                   smooth                                 
                                         smooth                           
Appearance   bumps/                                                       
             sticky                                                       
Compression Set                                                           
             67      50      44    28    18                               
(100° C./22 hrs)                                                   
ASTM D-395                                                                
Method B                                                                  
Oil Resistance                                                            
             205     152     136   96    66                               
(100° C./166 hrs)                                                  
ASTM #3 Oil -                                                             
% Volume Swell                                                            
Hardness - Shore A                                                        
             56      54      48    43    38                               
Deformation % -                                                           
             73      58      59    55    45                               
121° C./1 hour                                                     
2000 g. Load                                                              
Clash-Berg Stiffness,                                                     
             50,900  43,900  35,900                                       
                                   25,200                                 
                                         19,800                           
psi Modulus of                                                            
Rigidity at -35° C.                                                
______________________________________                                    
 .sup.1 Compound also contains stabilizer 5, costabilizer 3, filler 8 and 
 antioxidant 0.5                                                          
 
    
     
                                           TABLE II.sup.1                          
__________________________________________________________________________
PVC/2-ethylhexyl                                                          
           100.sup.2                                                      
               100 100 100 100 100 100 100 100 100 100 100 100            
acrylate                                                                  
Polymer A  --  20  --  --  40  --  --  60  --  --  100 --  --             
Polymer B  --  --  20  --  --  40  --  --  60  --  --  100 --             
Polymer C  --  --  --  20  --  --  40  --  --  60  --  --  100            
Cetyl Trimethyl                                                           
           --  0.2 0.2 0.2 0.4 0.4 0.4 0.6 0.6 0.6 1.0 1.0 1.0            
Ammonium Bromide                                                          
Sodium Stearate                                                           
           --  0.8 0.8 0.8 1.6 1.6 1.6 2.4 2.4 2.4 4.0 4.0 4.0            
Banbury Time (min.)                                                       
           5.5 5.2 3.5 5   3.8 4.3 4   3.8 3.3 4.4 4   3.8 3.5            
Banbury Drop Temp.                                                        
           304 308 311 299 311 363 316 325 323 331 308 320 315            
(°F.)                                                              
Extrusion Stock                                                           
           193 220 218 218 220 220 218 218 221 221 220 221 220            
Temp. (°F.)                                                        
Extrusion Rate                                                            
           220 224 230 208 208 220 188 196 218 206 196 214 156            
(g/min.)                                                                  
Extrusion Appearance                                                      
           small                                                          
               nervy                                                      
                   slightly                                               
                       very                                               
                           Very                                           
                               Nervy                                      
                                   Ex- Very                               
                                           Nervy                          
                                               Very                       
                                                   Very                   
                                                       Nervy              
                                                           Ex-            
           bumps/  nervy                                                  
                       nervy                                              
                           Nervy   treme-                                 
                                       Nervy   Nervy                      
                                                   Nervy   treme-         
           sticky                  ly                      ly             
                                   Nervy                   Nervy          
Compression set                                                           
           67  48  44  53  34  48  32  29  19  29  23  18  17             
(100° C.22 hrs.)                                                   
ASTM D-395                                                                
Method B                                                                  
Oil Resistance                                                            
           205 142 140 161 111 119 127 99  91  116 83  73  101            
(100° C./166 hrs.)                                                 
ASTM #3 Oil -                                                             
% Volume Swell                                                            
Hardness - Shore A                                                        
           56  53  54  45  42  52  38  40  48  38  35  45  35             
Deformation % -                                                           
           73  64  55  66  53  55  56  57  46  54  49  37  39             
121° C.1 hr.                                                       
2000 g. Load                                                              
Clash-Berg Stiffness,                                                     
           50,900                                                         
               51,900                                                     
                   61,900                                                 
                       35,100                                             
                           33,700                                         
                               55,000                                     
                                   27,400                                 
                                       32,300                             
                                           64,600                         
                                               23,900                     
                                                    22,000                
                                                       68,500             
                                                           3200           
psi Modulus of                                                            
Rigidity at -35° C.                                                
__________________________________________________________________________
 .sup.1 Compound also contains stabilizer 5, costabilizer 3, filler 8 and 
 antioxidant 0.5                                                          
 .sup.2 Control from Example #2  pressed at 320° F.                
 
    
     
                                           TABLE III.sup.1                         
__________________________________________________________________________
PVC/2-ethylhexyl acrylate                                                 
                  100.sup.2                                               
                         100 100 100   100  100  100 100  100             
Polymer A         --     60  60  60    60   60   60  60   60              
Cetyl Trimethyl Ammonium Bromide                                          
                  --     0.6 0.6 0.6   0.6  0.6  0.6 0.6  0.6             
Sodium Stearate   --     2.4 2.4 2.4   2.4  2.4  2.4 2.4  2.4             
Calcium Carbonate -3.5 u uncoated                                         
                  8      8   50  100   8    8    8   8    8               
Carbon Black N-110                                                        
                  --     --  --  --    20   50   --  --   100             
Carbon Black N-990                                                        
                  --     --  --  --    --   --   50  100  --              
Banbury Time (min.)                                                       
                  5.5    3.8 4   4.5   3.8  4.3  4.3 4    3               
Banbury Drop Temp. (°F.)                                           
                  304    318 310 317   310  324  318 320  352             
Extrusion Stock Temp. (°F.)                                        
                  193    217 217 220   221  220  223 220  --              
Extrusion Rate (g/min.)                                                   
                  220    208 274 294   234  218  230 250  --              
Extrusion Appearance                                                      
                  Small  Very                                             
                             Very                                         
                                 Slight                                   
                                       Rough                              
                                            Smooth                        
                                                 Very                     
                                                     Very Smooth          
                  Bumps/Sticky                                            
                         Nervy                                            
                             Nervy                                        
                                 Roughness                                
                                       Nervy     Rough                    
                                                     Smooth               
Compression Set (100° C./22 hrs.)                                  
                  67     39  17  20    28   59   45  34   83              
ASTM D-395 Method B                                                       
Oil Resistance (100° C./166 hrs.)                                  
                  205    82  79  74    82   71   75  69   52              
ASTM #3 Oil - % Volume Swell                                              
Hardness - Shore A                                                        
                  56     42  43  51    57   76   50  67   94              
Deformation % - 121° C./1 hr.                                      
                  73     54  56  43    40   24   39  33   11              
2000 g. Load                                                              
Clash-Berg Stiffness, psi                                                 
                  50,900 29,000                                           
                             33,900                                       
                                 52,800                                   
                                       41,100                             
                                            63,500                        
                                                 52,400                   
                                                     87,900               
                                                          111,400         
Modulus of Rigidity at -35° C.                                     
__________________________________________________________________________
 .sup.1 Compound also contains stabilizer 5, costabilizer 3, filler 8 and 
 antioxidant 0.5                                                          
 .sup.2 Control from Example #2  pressed at 320° F.                
 
    
     While in accordance with the Patent Statutes, the best mode and preferred embodiment has been set forth, the scope of the invention is not limited thereto, but rather by the scope of the attached claims.