CHLORINATED OR CHLOROSULFONATED ETHYLENE/VINYL ACETATE COPOLYMER FOR USE IN PAINTS

Abstract: A copolymer for use in corrosion-resistant paints which comprises a chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer made from an ethylene/vinyl acetate copo­ lymer resin having a melt index of about 300-10,000 and having a vinyl acetate content of from about 10-30 weight percent, said chlorinated or chlorosulfonated copolymer having a glass transition temperature of from about 15-50°C, a combined chlorine content of from about 42-56 weight percent, from about 2-6 acetate groups per 100 backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copo­ lymer, and, optionally, up to about 5 sulfonyl chloride groups per 100 backbone carbon atoms of the chlorosulfonated ethy­ lene/vinyl acetate copolymer and sufficient chlorine atoms at­ tached directly to the copolymer backbone to bring the total degree of substitution of the backbone carbon atoms of the chlorinated or chlorosulfonated copolymer to about 30-50%.

Description: TITLE CHLORINATED OR CH LOROSU LFONATE D ETHYLENE/VINYL ACETATE COPOLYMER FOR USE IN PAINTS BACKGROUND OF ThE INVENTION This application is a continuation-in-part of application Serial No. 608,861 filed ,ay 10, 1984. The present invention is directed to a novel chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer for use in sprayable corrosion-resistant paint compositions having a high solids content and a low viscosity, to a process for making the copolymers and to the paint compositions derived from these copolymers. Various polymers, such as chlorinated polyethylene rubber or chlorosulfonated polyethylene rubber, have been dissolved in solvents and mixed with conventional fillers and pigments to make sprayable corrosion-resistant paints. The sprayable corrosion-resistant paint compositions must have a viscosity low enough to be readily sprayable. It is also desirable to minimize the quantity of solvent for the polymer used in the paint composition. The paint compositions must contain sufficient solids to provide adequate covering characteristics and, perhaps, even more importantly, the paint when applied as a film to a substrate must be strong and capable of withstanding impact without cracking. Thus, the paint compositions must have adequate strength. Paint compositions containing high molecular weight polymers are known to provide better covering characteristics and have higher strength than paint compositions containing lower molecular weight polymers. However, such compositions are more difficult to spray on a substrate because their high molecular weights lead to higher solution viscosities. The paint compositions of the present invention contain a copolymer that results in sprayable paint compositions having a high solids content while, at the same time, they have a surprisingly low viscosity and, the paint compositions, when applied as a film to a substrate, exhibit excellent tensile strength which is an indication of the strength of the paint. SUMMARY OF THE INVENTION The present invention is directed to a copolymer for use in corrosion-resistant paints which comprises a chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer made from an ethylene/vinyl acetate copolymer resin having a melt index of from about 350-10,000 and having a vinyl acetate content of from about 10-30 weight percent, said chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer having a glass transition temperature of from about 15-50 C, a combined chlorine content of from about 42-56 weight percent, about 2-6 acetate groups per 100 backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer and, optionally, up to 5 sulfonyl chloride groups per 100 backbone carbon atoms of chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer, and sufficient chlorine atoms attached directly to the copolymer backbone carbon atoms to bring the total degree of substitution of the backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer to about 30-50%. The chlorinated ethylene/vinyl acetate copolymers are made by a process which comprises dissolving an ethylene/vinyl acetate copolymer resin having a vinyl acetate content of about 10-30 weight percent and a melt index of from about 350-10,000 in an organic solvent for the copolymer resin, adding a chlorinating agent and/or a chlorosulfonating agent to the resulting solution to produce a chlorinated or chlorosulfonated ethylene vinyl acetate copolymer wherein the total degree of substitution of backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer is about 30-50% and, optionally, contains up to about 5 sulonyl chloride groups per 100 backbone carbon atoms of the copolymer. The chlorinated copolymer is especially useful for the preparation of sprayable paint compositions of high solids content and low viscosity. Such compositions comprise about 15-30% by weight, based on the weight of the total composition, of a chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer wherein said copolymer contains from about 42-56 weight percent combined chlorine, from about 2-6 acetate groups per 100 backbone carbon atoms of said chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer, and up to 5 sulfonyl chloride groups per 100 backbone carbon atoms of said chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer so that the total degree of substitution of the backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer is from about 30-50 percent, an organic solvent for the chlorinated or chlorosulfonated ethylene/viny) acetate copolymer, and from about 20-35% by weight fillers ana pigments, based on the weight of the total composition, said sprayable paint composition having a solution viscosity of about 300-5,000 cps measured on a Brookfield viscometer. DETAILED DESCRIPTION OF THE INVENTION The ethylenefvinyl acetate copolymer resin that is chlorinated or chlorosulfonated contains about 10-30 percent by weight, preferably about 16-26 percent by weight, copolymerized vinyl acetate and has a melt index of from 350-10,OG0, preferably about 400-3000. The melt index is determined by ASTM D1234-65T, revised 1965 (Condition E). The melt index of the ethylene/vinyl acetate copolymer resin that is chlorinated or chlorosulfonated must be between 350-10,000, If the melt index of the copolymer resin is less than 350, the chlorinated or chlorosulfonated copolymer will have too high a viscosity and when such copolymer is compounued in a paint composition, the resulting viscosity of the paint composition is, likewise, too high. If the ethylene/vinyl acetate copolymer resin has a melt index greater than 10,000, the chlorinated or chlorosulfonated copolymer elastomer is unduly soft and processing is difficult. The ethylene/vinyl acetate copolymer resin is dissolved in an organic solvent, such as a halogenated hydrocarbon, for example, chloroform, methylene chloride, tetrachloroethylene, cblorobenzene or, preferably, carbon tetrachloride. The ethylene/vinyl acetate copolymer resin is reactea with the chlorinating agent, gaseous chlorine alone or with the chlorosulfonating agent, sulfuryl chloride to introduce on the ethylene/vinyl acetate copolymer resin, chlorine alone or with sulfur, wherein the sulfur is present on the chlorinated copolymer as sulfonyl chloride groups. The amount ot gaseous chlorine and sulfuryl chloride used in the process is determined by the required degree of chlorination or the amount of sulfur desired as sulfonyl chloride groups on the chlorinated copolymer. Generally between about 0.5-2 parts by weight gaseous chlorine and 0-0.1 parts by weight sulfuryl chloride per part ethylene/vinyl acetate copolymer resin are used to incorporate the desired amounts of chlorine atoms and sulfonyl chloride groups on the copolymer. The temperature at which the chlorination or chlorosulfonation reaction is carried out may be varied over a wide range and is generally governed by the viscosity of the solution and the decomposition temperature of the conventional free radical catalyst used in the process. Usually the temperature is between about 80-1000C. Generally the chlorination or chlorosulfonation is conducted in the presence conventional free radical initiators such as 2,2'-azobis[2-methylpropane nitrile). The resulting chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer can be isolated by known means, preferably, drum drying. Other well known methods of isolation that can be used are, for example, precipitation, filtration and spray drying or solvent exchange to a nonchlorinated solvent. The resulting chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer has a glass transition temperature of from about 15-50 C and a combined chlorine content of from about 42-56, preferably 44-50, weight percent. The copolymer contains from about 2-6, usually 2.5-5.5, acetate groups per 100 backbone carbon atons of the copolymer. Optionally, the copolymer contains up to 5, usually 0.1-1, sulfonyl chloride groups per 100 backbone carbon atoms of the copolymer. The copolymer contains sufficient chlorine atoms attached directly to the copolymer backbone carbon atoms to bring the total degree of substitution of backbone carbon atoms of the copolymer to about 30-50%. The degree of substitution of the substituents on the chlorinated or chlorosultonated copolymer is critical, because of their effect on the glass transition temperature (Tg) of the copolymer. If the glass temperature is below about 150C, which occurs when the total degree of substitution is below about 30 percent, paint compositions containing the copolymers and conventional fillers and pigments, when applied as a film to a substrate are too soft and tacky and lack adequate tensile strength to form a strong film on a substrate. On the other hand, if the total degree of substitution of the backbone carbon atoms on the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer is more than about 50 percent, the glass transition is above about 50 C Paint compositions containing such copolymers when applied as a film to a substrate are too brittle and crack upon impact. If the amount of acetate groups on the copolymer is less than about 2 per 100 backbone carbon atoms or more than about 6 per 100 backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer, paint compositions containing the copolymer when applied as a film to a substrate are not strong and lack adequate tensile strength, even at the required degree of overall substitution. It is surprising that a chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer, made from an ethylene/vinyl acetate resin that has such a low molecular weight, as indicated by the melt index of the resin of from 300-10,000, would result in a chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer that when used as a component in corrosion-resistant paint compositions would result in a film that is especially strong, as indicated by its tensile strength, and because of the low molecular weight of the chlorinated or chlorosulfonated copolymer it can be readily applied to a substrate by spraying. The above-described chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer can be formulated into corrosion-resistant paint compositions by any conventional means with pigments and fillers on, for example, a ball mill. The pigments used can be any of the conventional types used in paint compositions comprising, for example, iron oxides, lead oxides, strontium chromate, carbon black, coal dust, titanium dioxide, talc, barium sulfate, as well as color pigments, including cadmium yellow, cadmium red, chromium yellow, and metallic pigments such as aluminum flake. Conventional fillers used in corrosionresistant paints can be incorporated in the composition. Representative fillers include calcium carbonate, clay, talc, etc. The corrosion-resistant paint composition of the present invention contains about 15-30 percent by weight, usually 12-26 percent by weight, based on the total weight of the composition of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer ana a solvent for the chlorinated copolymer. The solvent evaporates after the paint composition is applied to a substrate leaving the solid material to form a film or coating. The solvent is chosen so as to provide good viscosity and sprayability characteristics. The solvent also assists in the substrate wetting, promotes copolymer component compatibility, package stabilitv and coalescence or film formation. Representative solvents that can be used include aromatic hydrocarbons such as toluene and xylene, halogenated aliphatic compounds such as carbon tetrachloride, chlorobenzene, chloroform and methylene chloride, ketones such as methyl ethyl ketone and methyl isobutyl ketone, alcohols such as isopropyl alcohol, normal butyl alcohol, monoethers of glycols such as the monoethers of ethylene glycol and diethylene glycol, as well as mixtures of the above. The solvent is present in the composition in amounts of about 30-60 percent by weight based on the total weight of the solvent and the chlorinatea or chiorosulfonated ethylene/vinyl acetate copolymer component and the pigments and fillers present. The composition contains a relatively large amount of solids which provides good covering characteristics. The particular amount of solvent used is that amount which will result in a paint composition having a solution viscosity determined in 30 percent by weight xylene of about 300-5000 cps, usually, 400-1000 cps, measured on a Brookfield viscometer. Generally, the utiliation of the chlorinated or chlorosulfonated ethyleneZvinyl acetate copolymer allows the addition of about 20-35 percent by weight fillers ana pigments to give a total solids content of from 35-65 percent by weight. In addition, plasticizers, antioxidants, U.V. light absorbers, flow control agents and other formulating additives can be used in the sprayable paint composition if desired. These materials are optionally present in amounts up to 5 percent by weight based on the total solids in the corrosionresistant paint composition. The corrosion-resistant paint composition of the present invention is designed for application by spraying, although other conventional methods of coating, including brushing, dipping, and flow coating, can be employed if desired. However, the paint composition is especially formulated for spraying. Conventional spray techniques and equipment are utilized in the application of the corrosion-resistant paint composition. The paint composition can be applied over any substrate including wood, metal, glass, cloth, plastics, and the like, as well as over various primers. The paint compositions are particularly useful on substrates such as primed steel, aluminum, insulation material and the like. In general, coating thickness of the paint composition on the substrate will vary depending upon the particular application desired. In general, coatings from 0.1-2 mm have been found to be satisfactory in most applications. After application of the corrosion-resistant paint compositions to a substrate, the compositions can be cured. The compositions are not usually subjected to a heat cure cycle but, if desired, improvements in the properties are obtained when the compositions are cured at temperatures of about 400-1200C, for 5-60 minutes and, in most cases, from 600-1200C for about 10-30 minutes. Higher or lower temperatures with correspondingly shorter or longer times can be utilized. The exact cure schedule best employed depends upon the nature of the substrate. The corrosion-resistant paint composition has a high solids content and yet the viscosity of the composition is low enough that it can be applied to a substrate by conventional paint spraying techniques. The following examples illustrate preferred eiibodiments of the invention in which amounts are given in parts by weight, unless otherwise indicated. EXAMPLE 1 Into a 38 liter stirred autoclave were charged 1.4 kg ethylene/vinyl acetate copolymer resin (EVA) having a melt index of 400 and a vinyl acetate content of 25 weight percent, and 18.2 kg carbon tetrachloride. The autoclave was closed and the pressure set at 0.17 MPa. The reaction mixture was heated at lO0 C until the resin was dissolved, then the addition of 20 ml/min initiator solution (0.5 percent 2,2'-azobis- [2-methylpropane nitrile] in chloroform) was instituted. Chlorine gas was addea to the reaction mixture at a rate of 0.45 kg/hr, and simultaneously 1 liter (0.6 kg or 0.43 parts by weight per part copolymer resin) of sulfuryl chloriae was added over a period of 30 minutes. Addition of chlorine was continued until a total of 1 kg, i.e., 0.71 parts by weight per part copolymer resin, was added (2.2 hr). Following a degassing step to remove acid gas, enough stabilizer solution (pone 828 in carbon tetrachloride) was added to the autoclave to supply 23.5 g Epon 828 (condensation product of bisphenol A and epichlorohydrin with a neutralization equivalent of 180). The autoclave was cooled and discharged. The reaction mixture was filterea and the chlorosulfonated ethylene/vinyl acetate copolymer was isolated by drum drying. Analysis showed that the polymer contained 42.2 weight percent combined chlorine and 1.01 weight percent sulfur. Substitution of the polymer backbone with chlorine, acetate and sulfonyl chloride moieties was 40.13 percent comprising 4.90 acetate groups per hundrea backbone carbon atoms, 0.93 sulfonyl chloride groups per hundred backbone carbon atoms and 34.3 chlorine atoms per hundred backbone carbon atoms of the chlorosulfonated ethylene vinyl/acetate copolymer. The glass transition temperature (Tg) was 430C. EXAMPLE 2 A chlorinated ethylene/vinyl acetate copolymer was prepared by the method described above in Example 1, except that 2.05 kg i.e. 1.46 parts by weight per part copolymer resin, gaseous chlorine was added to the reaction mixture over a period of 4.5 hr and no sulfuryl chloride was used. Analysis of the chlorinated ethylene/vinyl acetate copolymer showed the polymer contained 47 weight percent combined chlorine. Polymer backbone substitution totalled 46.05 percent comprising 4.90 acetate groups per hundred backbone carbon atoms and 41.15 chlorine atoms per hundred backbone carbon atoms of the chlorinated ethylene/vinyl acetate copolymer. EXAMPLE 3 A 3.8 liter stirred autoclave was charged with 0.34 kg ethylene/vinyl acetate copolymer resin having a melt index of 1000 and a vinyl acetate content 26 weight percent, 2.59 kg carbon tetrachloride, and 0.27 kg chloroform. The autoclave was closed and the pressure was set at 0.38 MPa. The reaction mixture was heated at 1050C until the resin dissolved. Then 4 ml of an initiator solution (0.5 percent 2,2'-azobis-[2-methylpropane nitrile] in chloroform) was added and the reaction mixture was allowed to cool to 900C while continuously adding gaseous chlorine at a rate of 0.72 g/min and initiator at a rate of 0.27 ml/min. Addition of sulfuryl chloride was begun and 420 ml was added over a period of 210 min. to give 0.73 parts by weight per part copolymer resin. Total addition time for the chlorine and initiator was 250 min. resulting in addition of .85 parts by weight chlorine per part copolymer resin. Following a gassing step to remove acid gas, enough stabilizer solution (upon 828 in carbon tetrachloride} was added to supply 9g Lpobb 828. The reactor was cooled and discharged and the product was isolated by drum drying. Analysis showed the polymer contained 43.1 weight percent combined chlorine and 0.91 weight percent sulfur. The total degree of backbone substitution with chlorine, acetate and sulfonyl chloride moieties was 41.85 percent comprising 5.14 acetate groups per hundred backbone carbon atoms, 0.91 sulfonyl chloride groups per hundred backbone carbon atoms and 35.86 chlorine atoms per hundred backbone carbon atoms. Glass transition temperature was 280C. EXAMPLE 4 A chlorinated ethylene/vinyl acetate copolymer was prepared according to the procedure described in Example 2, except 2.7 kg ethylene/vinyl acetate resin having a melt index of 2500 and a vinyl acetate content of 18 weight percent was used and 5.3 kg chlorine (i.e. 1.97 parts by weight chlorine per part copolymer resin was added over a period of 7.75 hr. and rate of initiator addition was 4 ml/min. The product contained 47.8 percent combined chlorine. Substitution of the polymer backbone totaled 43.52 percent comprising 3.34 acetate groups per hundred backbone carbon atoms and 40.18 chlorine atoms per hundred backbone carbon atoms. The glass transition tewperature of the product was 360C. COMPARATI VE EXAMPLE A Into a 3.8 liter stirred autoclave were charged 0.2 kg high density polyethylene (Melt Index 466), 2.07 carbon tetrachloride, 0.23 chloroform and 20 ml of a 1 percent solution of pyridine in carbon tetrachloride. The autoclave was closed and the pressure set at 0.27 MPa. The reaction mixture was heated at 1050C until the resin dissolved, then 8 ml of an initiator solution (0.5 percent, 2,2'-azobis-[2-methylpropane nitrile] in chloroform) was added. Simultaneously chlorine gas and sulfuryl chloride were introduced to the reaction mixture. A total of 189 ml sulfuryl chloride was added over a period of 1.5 hr. and the chlorine gas was adaed at a rate of 1.1 g/min until a total of 0.165 kg haa been added. At this point enough stabilizer solution (pone 828 in carbon tetrachloride) was added to supply 3.5 g Epon 828 (a condensation product of bisphenol A and epichlorohydrin). The reactor was cooled and discharged. The reaction mixture was filtered and the chlorosulfonated polyethylene product was washed twice with a 40 percent aqueous methanol solution, followed by a water wash. Isolation was done on a drum drier. Analysis showed the polymer contained 42.2 weight percent chlorine and 1.98 weight percent sulfur. The overall degree of polymer backbone substitution with chlorine and sulfonyl chloride moieties was 30.32 percent comprising 1.57 sulfonyl chloride groups per hundred backbone carbon atoms and 28.75 chlorine atoms per hundred backbone carbon atoms. The glass transition temperature of the polymer was 100C. COMPARATIVE EXAMPLE B The process described in Example 1 was repeated except that the ethylene/vinyl acetate copolymer resin had a melt index of 150 and a vinyl acetate content of 18 weight percent and a total of 0.55 kg gaseous chlorine was added over a period of 1.5 hr to the reaction mixture. The chlorosulfonated ethylene/vinyl acetate copolymer had a combined chlorine content of 35.2 weight percent and a sulfur content of 1.24 weight percent. The overall total degree of polymer backbone substitution with chlorine, acetate and sulfonyl chloride moieties was 28.36 percent comprising 3.34 acetate groups per hundred backbone carbon atoms, 0.97 sulfonyl chloride groups per hundred backbone carbon atoms and 24.05 chlorine atoms per hundred backbone carbon atoms. The glass transition temperature was Soc. Properties of the polymers of Examples 1-4 and Comparative Examples A-D are shown in Table I. TABLE I Com- Com para- para Example Example Example Example tive tive Sample 1 2 3 4 Ex. A Ex. B Starting Poly Resin EVA EVA EVA EVA ethy- EVA Melt lene Index 400 400 1000 2500 466 150 Weight % Vinyl 25 25 26 18 0 18 Acetate Starting Resin Product Chloro Chlori- Chloro- Chlori- Chloro- Chloro sulfo- nated sulfo- nated sulfo- sulto nated EVA nated EVA natea natea EVA EVA Poly- EVA ethy lene Weight % Chlorine 42.2 47 43.1 47.9 42.2 35.2 Combined Product % Backbone Carbon Atoms Substituted with C1 34.30 41.15 35.86 40.18 28.75 24.05 Weight % 1.0 0 0.9 0 2.0 1.2 Sulfur Product TABLE I Continued Com- Com para- para Example Example Example Example tive tive Sample 1 2 3 4 EX. A Ex. B t Backbone Carbon Atoms Sub stituted with -SOCl 0,93 0 0.86 0 1.57 0.97 % Backbone Carbon Atoms Sub stituted with -OCOCH3 4.90 4.90 5.14 3.34 0 3.34 Degree of Substitution** 40.13 46.05 41.85 43.52 30.32 28.36 Solution Viscosity (cps) 33% in Tbluene 250 480 220* 137* 750 715 Tg 43 - 28 36 10 5 *In xylene **Percentage of polymers backbone substituted with chlorine atoms, acetate groups and optionally sulfonyl chloride groups. The chlorosulfonated and chlorinated ethylene/vinyl acetate copolymers prepared from the polymers of Examples 1-4, and Comparative Examples A and B were formulated into corrosion-resistant paints by ballmilling the formulations shown in Table II. Amounts given are in parts by weight. TABLE II Ex. Ex. Ex. Ex. Comp. Ex. Comp. Ex. Sample 1 2 3 4 A B Polymer 200 75 100 100 100 300 80 80 30 40 40 40 120 CaCO3 160 60 50 50 80 240 PbO 40 15 20 - 20 60 MgO 10 Mercapto- 1 0.7 -- - 1 3 benzthiazole disulfide Staybelite -- -- -- 3 9 Resin (Hydrogenated Resin Tenlo 70- 1 -- -- - -- - (Polyethylene glycol ester and fatty amides Dispersing Agent) Nuosperse (Dispersing Agent) Tetramethyl 3 -- -- - - -thiuram disulfide Teluene 500 180 -- - 287 550 Xylene -- -- 250 250 -- - The corrosion-resistant paints described in Table II were cast onto a Teflons fluorocarbon film and dried. The polymer films were tested for tensile strength after the polymer paint compositions were cured at 1000C for 20 minutes according to ASTM D412. The viscosity and percent solids of the paints and tensile strength of films are shown in Table III. TABLE III Paint Ex. Ex. Ex. Ex. Comp. Comp. Properties 1 2 3 4 A B Viscosity (cps) 380 900 420 255 1175 3650 Neight Percent Solids 49.2 50.1 45.6 44.6 46 57.1 Film Properties TB (MPa) 13.8 17.1 12.4 13.6 2.1 4.6 The test results indicate that the paint compositions made according to the present invention have a low viscosity in spite of the fact that the solids content is high. In addition, the tensile strength is high indicating that the film is strong and will not break. Comparative Example indicates that a chlorosulfonated polyethylene made from polyethylene having a melt index of 466 exhibits poor film strength, as shown by its TB of 2.1 MPa. Comparative Example B indicates that a chlorosulfonated ethylene/vinyl acetate copolymer made from an ethylene/vinyl acetate copolymer resin having a melt index of 150 and chlorinated to a degree of substitution of only 28.36 percent results in a polymer film having inadequate strength, as indicated by its tensile strength value.

Claims: CLAIMS 1. A copolymer for use in corrosionresistant paints which comprises a chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer made from an ethylene/vinyl acetate copolymer resin having a melt index of about 350-10,000 and having a vinyl acetate content of from about 10-30 weight percent, said chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer having a glass transition temperature of from about 15-50 C, a combined chlorine content of from about 42-56 weight percent, about 2-6 acetate groups per 100 backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer and, optionally, up to about 5 sulfonyl chloride groups per 100 backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer, and sufficient chlorine atoms attached directly to the copolymer backbone carbon atoms to bring the total degree of substitution of the backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer to about 30-50%. 2. A copolymer of Claim 1 wherein the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer contains from about 2.5-5.5 acetate groups per 100 backbone carbon atoms of the ethylene/vinyl acetate copolymer. 3. A copolymer of Claim 1 wherein the chlorosulfonated ethylene/vinyl acetate copolymer contains from about 0.1-1 sulfonyl chloride groups per 100 backbone carbon atoms of the chlorosulfonated ethylene/vinyl acetate copolymer. 4. A copolymer of Claims 1 or 2 wherein the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer is made from an ethylene/vinyl acetate copolymer resin having a melt index from about 400-3,000. 5. A copolymer of Claim 3 wherein the chlorosulfonated ethylene/vinyl acetate copolymer has a combined chlorine content of from about 44-50 percent by weight and said copolymer is made from an ethylene/vinyl acetate copolymer resin having a melt index of from 400-3,000. 6. A process for making a chlorinated ethylene/vinyl acetate copolymer which comprises dissolving an ethylene/vinyl acetate copolymer resin having a vinyl acetate content of about 10-30 weight percent and a melt index of from about 350-10,000 in an organic solvent for the copolymer resin, adding a chlorinating agent or chlorosulfonating agent to the resulting solution to produce a chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer wherein the total degree of substitution of the backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer is about 30-508 and, optionally, contains up to about 5 sulfonyl chloride groups per 100 backbone carbon atoms of the copolymer. 7. A process of Claim 6 wherein the ethylene/vinyl acetate copolymer resin has a vinyl acetate content of from about 16-26 weight percent. 8. A process of Claims 6 or 7 wherein the melt index of the ethylene/vinyl acetate copolymer resin is from about 400-3,000. 9. A process of Claim 6 wherein up to about 0.6 parts by weight sulfuryl chloride is added to the resulting solution. 10. A sprayable paint composition of high solids content and low viscosity comprising 15-30 percent by weight, based on the weight of the total composition, of a chlorinated or chlorosulfonate ethylene/vinyl acetate copolymer wherein said copolymer contains about 42-56 weight percent combined chlorine, from about 2-6 acetate groups per 100 backbone carbon atoms of said chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer, up to 5 sulfonyl chloride groups per 100 backbone carbon atoms of said chlorinated or chlorosulfonated ethylene/vinyl acetate so that the total degree of substitution of the backbone carbon atoms of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer is from about 30-50%, an organic solvent for the chlorinated or chlorosulfonated ethylene/vinyl acetate copolynier, and from about 20-35 percent by weight fillers and pigments, based on the weight of the total composition, the sprayable paint composition having a solution viscosity of about 300-5,000 cps. measure on a Brookfield viscometer. 11. A composition of Claim 10 containing about 12-26 percent by weight of a chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer. 12. A composition of Claim 10 wherein the chlorosulfonated ethylene/vinyl acetate copolymer contains from about 0.1-1 sulfonyl chloride groups per 100 backbone carbon atoms of said copolymer. 13. A composition of Claim 10 wherein the solution viscosity of the sprayable composition 15 from about 400-1000 cps. 14. A composition of Claim 1U wherein the organic solvent is present in an amount of about 30-60 percent by weight based upon the total weight of the chlorinated or chlorosulfonated ethylene/vinyl acetate copolymer, solvent, fillers and pigments. 15. A composition of Claim 10 having a total solids content of from about 35-65 percent by weight.

Inventors: DAWES, JAMES WILKINSON, SMITH, JOHN FREDERICK
Applicants: E.I. DU PONT DE NEMOURS AND COMPANY
Application year: 1985
Main classification: C08F8
IPC codes: C08F8