Epoxide advancement process

Abstract: Coating compositions containing aqueous dispersion of higher molecular weight epoxy resin are produced by advancing the molecular weight of an aqueous dispersion of a low molecular weight epoxy resin having a number average molecular weight between about 360 and 2 000. The water dispersed low molecular weight epoxy resins are advanced in molecular weight by coreaction with a diphenol at temperatures above about 105°C and at pressures above about 34 475 N/m² over atmospheric (5 psig) to produce the aqueous dispersed high molecular weight epoxy resin. The aqueous dispersed high molecular weight epoxy resin can be further copolymerized with ethylenic monomers, if desired, to produce an acrylic epoxy emulsion binder useful in protective coatings.

Description: This invention relates to a process for advancing the molecular weight of low molecular weight epoxy resins in water to make a stable aqueous emulsion of high molecular weight epoxy resin, and to a coating composition comprising an aqueous dispersion of high molecular weight epoxy resin producible by the process. Coating compositions are organic compositions applied to substrates and cured to form continuous films. They ordinarily comprise a polymeric binder, pigments, and various additives, although some coating compositions contain little or no pigments and are known as clear coatings. Epoxy resins are particularly desirable for use as a polymeric binder in coating compositions, where they provide toughness, flexibility, adhesion, and chemical resistance. Water-dispersed coating compositions containing epoxy resins are especially desirable for interior can coating compositions. An important property of coatings for the interior of soft drink and beer cans, for instance, is that they must not alter the taste of the drink inside the can. Taste problems can occur in a variety of ways such as by leaching coating components into the drink, by absorption of flavour by the coating, by chemical reaction, or by a combination of these effects. United States Patent No. 4 212 781 discloses a non-aqueous process for modifying epoxy resin by reaction with addition polymerizable monomer in the presence of benzoyl peroxide at a suitable reaction temperature. This reaction produces a non-aqueous reaction mixture containing a blend of resinous materials comprising an epoxy resin, a carbon graft epoxy-acrylic polymer, and associatively-formed ungrafted addition polymer. The monomers include carboxylic acid functional monomers to provide sufficient acid functionality in the reaction mixture to enable stable dispersion of the resulting reaction product in a basic aqueous medium. To provide epoxy-derived binders for coating compositions, low molecular weight liquid epoxy resins are advanced in molecular weight to produce a high molecular weight epoxy resin preferably having a molecular weight above about 7000. The advancement is generally carried out by a fusion or organic solvent process in which low molecular weight epoxy resin, such as the diglycidyl ether of bisphenol A, is coreacted with a lesser amount of bisphenol A to give a high molecular weight epoxy resin. For example, a typical low molecular weight liquid epoxy resin having a molecular weight of about 380 can be advanced by reacting with bisphenol A at a weight ratio of about 66/33 weight parts epoxy resin/bisphenol A in about 15 weight parts of ethylene glycol monobutyl ether solvent and at a reaction temperature of about 175°C in the presence of an ethyl triphenyl phosphonium acetate catalyst at atmospheric pressure, as described in U.S. 4,212,781, to produce a high molecular weight epoxy resin. The high molecular weight epoxy acrylic copolymers can be emulsified into water if first dissolved in an organic solvent to a low viscosity. Solvent levels of 50 to 100 parts per 100 parts of epoxy-acrylic by weight are generally required because lower solvent levels tend to render the solvent mixture difficult to disperse into water. Typical epoxy suspensions are disclosed in U.S. 4,409,288 and U.S. 4,177,177, which first disperse high molecular weight epoxy resin into solvent which in turn are dispersed into water followed by stripping of the organic solvent. The organic solvent must be removed from the aqueous emulsion by distillation, which is an expensive and time consuming process. U.S. 4,122,067 discloses a process for reacting a polyepoxide with a dihydric phenol in water as a 40% to 95% aqueous dispersion and at temperatures between 80°C and 100°C using nonionic surfactants to produce water dispersed very low molecular weight epoxy resins. The epoxy resins are in the form of solid granular beads. Dispersion at 40% to 75% are said to be unstable and result in large particles settling out of water while 75% to 95% dispersions result in much smaller particles but stable dispersions. Under these conditions, it has been found that mixtures of liquid epoxy and bisphenol coreact and advance the molecular weight only to about 1 000 where the reaction mixture becomes glassy and the reaction stops. US patent 4 212 776 discloses an epoxy ester produced by esterifying the epoxy group with a monocarboxylic acid followed by the copolymerization of monomers. The esterification is carried out in an organic solvent such as ketones. The epoxy is not advanced in molecular weight, nor is the epoxy reacted in water. It now has been found that aqueous emulsions of low molecular weight epoxy resin can be advanced in molecular weights with diphenols such as bisphenol-A while dispersed in water to produce small particle size stable aqueous dispersions of the high molecular weight epoxy resin in water. According to the present invention there is provided a process for producing a coating composition containing a stable aqueous emulsion of high molecular weight epoxy resin binder produced by the steps comprising: i) dispersing into water using a combination of anionic and non-ionic surfactants a combination of a) low molecular weight epoxy resin having a number average molecular weight between about 360 and 2 000 b) a diphenol to provide an aqueous dispersion of reactants; ii) advancing the molecular weight of the low molecular weight epoxy resin by reacting with the diphenol at temperatures above about 105°C and at pressures above about 34 475 N/m 2 above atmospheric (5 psig); to provide an aqueous dispersed high molecular weight epoxy resin having a number average molecular weight greater than 2 000, preferably between about 2 000 and 20 000. The process of this invention provides a convenient and economical method for producing a stable high molecular weight epoxy resin emulsion directly, having a non-volatile content which is suitable for interior can coating applications without the need for the cumbersome multi-step process of intermediate mixing with high levels of organic solvent, dispersion into water, and subsequent solvent stripping. A further advantage is that acrylic or methacrylic acid monomer can subsequently be copolymerized with other ethylenic monomers in the resulting aqueous dispersion of high molecular weight epoxy resin at relatively low levels to maintain dispersibility and stability of the resulting epoxy-acrylic copolymer in water. A further advantage relates to enhanced rheological properties including improved coating application properties as well as improved performance and sag resistance properties. The stable, high molecular weight, epoxy aqueous emulsion resulting from the process of this invention can be further coreacted directly with ethylenic unsaturated monomers, if desired, to produce epoxy emulsion copolymers suitable for use as a very low VOC (volatile organic content) aqueous dispersed coating composition. Low molecular weight epoxy resins are polyglycidyl ethers of bisphenol A having 1,2-epoxy equivalency between about 1.5 and 2.5, including mixtures of monoepoxides and diepoxides. Low molecular weight epoxy resins are predominantly linear chain molecules comprising the coreaction product of polynuclear dihydroxy phenols (known as bisphenols) with halohydrins to produce epoxy resins containing at least one and preferably two epoxy groups per molecule. The most common bisphenols are bisphenol-A, bisphenol-F, bisphenol-S and 4,4' dihydroxy biphenyl, with the most preferred being bisphenol-A. Halohydrins including epichlorohydrin, dichlorohydrin, and 1,2-dichloro-3-hydroxy propane with the most preferred being epichlorohydrin. Preferred low molecular weight epoxy resins comprising the coreaction product of excess molar equivalents of epichlorhydrin and bisphenol-A produce predominantly an epoxy group terminated linear molecular chain of containing 1 to 4 repeating copolymerized units of diglycidyl ether of bisphenol-A. The most preferred linear, low molecular weight epoxy resins for increasing molecular weight in accordance with this process are polyglycidyl ethers of bisphenol-A having terminating 1,2-epoxide groups and an epoxy equivalent weight between 180 and 800, and a number average molecular weight from about 360 to 2 000 as measured by gel permeation chromatography (GPC). Commercially available low molecular weight epoxy resins suitable for advancement in the process of the present invention include epoxy resins identified by trade marks and average molecular weights as follows: Dow Chemical DER 333 (380); DER 661 (525); and Shell Chemical epoxy resins EPON 828 (380); EPON 836 (625); EPON 1001 (525) and Ciba Geigy linear epoxy resins GT-7013 (1400); GT-7014 (1500); GT 7074 (2000); and GT-256 (1200). The most common diphenols are bisphenol-A, bisphenol-F, bisphenol-S, and 4,4'-dihydroxy biphenyl with the most preferred being bisphenol-A. Minor amounts of mono or poly phenols can be added if desired. Examples of monophenols are phenol, o, m, or p-cresol, 2,4-xylenol, 3,4-xylenol, 2,5-xylenol, cardanol, p-tert-butyl phenol. Examples ot other diphenols are o-dihydroxy-benzene, m-dihydroxybenzene and p-dihydroxybenzene, and 3,5-dihydroxytoluene. Examples of trihydric phenols are 1,3,5-trihydroxybenzene and 1,2,3-trihydroxybenzene. The low molecular weight epoxy resin is coreacted with diphenol at ratios typically between 1:2 and 2:1 equivalents of epoxy to phenol functionality with preferred ratios between 4:5 and 5:4. The low molecular weight epoxy resins and the diphenol coreactant are first dispersed into water by using a combination of anionic and nonionic surfactants to produce an aqueous emulsion of reactants. This gives dilute emulsions with greatly improved stability and cleanliness. Useful anionic surfactants include those hydrocarbons having anionic solubilizing groups such as carboxylates, sulphonates, sulphates, and phosphates. Among the anionic surfactants suitable for use in the present invention are the sulphates and sulphonates, such as sodium and potassium alkyl sulphates, aryl sulphates, and alkylaryl sulphates and sulphonates, including sodium 2-ethylhexyl sulphate, potassium 2-ethylhexyl sulphate, sodium nonyl sulphate, sodium undecyl sulphate, sodium tridecyl sulphate, sodium pentadecyl sulphate, sodium lauryl sulphate, sodium methylbenzene sulphonate, potassium methylbenzene sulphonate, sodium dodecylbenzene sulphonate, potassium toluene sulphonate and sodium xylene sulphonate; and sulphonated ethoxylated higher fatty alcohols as well as anionic surfactants such as potassium caprylate, potassium myristate, potassium palmitate, potassium stearate, potassium oleate, sodium decyl sulphonate, sodium dodecyl sulphonate, sodium tetradecyl sulphate, sodium lauryl sulphate, potassium dehydroabietate, sodium rosinate, alkyl sodium sulphosuccinate esters, and the like. Anionic surfactants are ordinarily utilized at the level of 0.1% to 5% based on the combined weight of epoxy and difunctional coreactant. Useful nonionic polymeric stabilizers including ethylene oxide chains and hydroxyl groups such as hydrolysed polyvinyl alcohol, hydroxyethyl cellulose, ethylene oxide copolymers or polypropylene glycol, as well as polyoxyethylene glycols reacted with polyglycidyl polyethers or polyhydric phenols. These non-ionic surfactants include alkylphenoxypoly (ethyleneoxy) ethanols having alkyl groups containing between 4 to 240 ethyleneoxy units, such as the heptylphenoxypoly(ethyleneoxy) ethanols, nonylphenoxypoly (ethyleneoxy) ethanols and dodecylphenoxypoly (ethyleneoxy ethanols, polyoxyalkylene derivatives of hexitol (including sorbitans, sorbides, mannitans and mannides) anhydride, partial long chain fatty acid esters, such as the polyoxyalkylene derivatives of sorbitan monolaurate, sorbitan monopalmitate, sorbitan monostearate, sorbitan tristearate, sorbitan monooleate and sorbitan trioleate; condensates of ethylene oxide with a hydrophobic base formed by condensing propylene oxide and propylene glycol; sulphur-containing condensates such as those prepared by condensing ethylene oxide with higher alkyl mercaptans, such as nonyl, dodecyl, or teradecyl mercaptan, or with alkylthiophenols wherein the alkyl substituent contains from 6 to 15 carbon atoms; ethylene oxide derivatives or long-chain carboxylic acids such as lauric, myristic, palmitic or oleic acid, or mixtures of acids, such as tall oil, and ethylene oxide derivatives of long-chain alcohols such as octyl, decyl, lauryl or cetyl alcohol. 0.1% to 10% by weight nonionic stabilizer can be used based on the weight epoxy and diphenol reactants. Dilute aqueous emulsions useful in the invention contain between 10% and 30% by weight reactants dispersed into water. Organic solvents can be used at low levels to reduce emulsion viscosity, if desired, and provide for more efficient emulsification of the low molecular weight epoxy resin. 0% to 20% by weight or higher amounts of organic solvent based on the weight of coreactants can be added if desired. Small amounts of solvent can help to reduce the viscosity of the epoxy and diphenol mixture although appreciable amounts of organic solvents will increase the VOC level. Suitable useful solvents include aromatics, such as xylene; the higher ketones, such as diisobutyl ketone; and similar organic solvents. More polar solvents such as butyl and hexyl cellosolve can be used in lesser amounts but tend to cause emulsion instability. In preferred compositions, described further below, ethylenic monomers are used as organic solvents during the epoxy advancement reaction whereupon the ethylenic monomers are subsequently copolymerized in a later addition copolymerization step. The first stage emulsification of epoxy and diphenol reactants is best done at elevated temperatures from 50°C to 95°C to allow better emulsification of the reactants. Preferably the aqueous dispersion of low molecular weight epoxy resin to be advanced in molecular weight comprises between 10% and 30% by weight of low molecular weight epoxy resin. Advancement is preferably carried out at temperatures between 110°C and 150°C and preferably under pressures of between 68 950 N/m 2 and 482 650 N/m 2 above atmospheric (between 10 and 70 psig). Final emulsion solids can range from about 15% to 50% by weight of advanced epoxy resin with balance being water. Various hydroxide and tertiary amine catalysts can be used to control the epoxy/phenol reaction, such as metal hydroxides, and quaternary hydroxides, although tertiary amines are preferred, such as triethylamine, dimethyldodecylamine, benzyldimethylamine, and the like. Advancement of the low molecular weight epoxy resin seems to be fairly easy with tertiary amines such as triethyl amine, dimethyldodecyl amine, dimethylethanol amine, and the like but the more hydrophobic amines are preferred over the hydrophillic dimethylethanol amine. Strong bases such as potassium hydroxide and quaternary hydroxides, such as benzyltrimethyl ammonium hydroxide, can also be used, but are not preferred. Phosphines, such as triphenyl phosphine can be used, although these catalysts can be unstable at higher temperatures in the presence of water and may cause discolouration. Based on the weight of the epoxy plus phenol, 0.1 to 5% catalyst is sufficient to give a good reaction rate at 125°C. The presence of tertiary amines makes the emulsion slightly basic with a pH 8 to 9. Acidic pH's, less than 7, should be avoided, as epoxy resins can hydrolyse at a low Ph below about 7. The process of advancing molecular weights of low molecular epoxy resin in an aqueous polymerization medium in accordance with this invention, provides a convenient method for producing high molecular weight epoxy resin aqueous emulsions which do not require solvent stripping to obtain low VOC coatings. Low molecular weight epoxy resin, such as diglycidyl ether of bisphenol-A, provides a good solvent for difunctional phenols suitable for advancing epoxy resins, and these solutions can be easily emulsified in water with common surfactants. The advanced molecular weight epoxy resin comprises an emulsified high molecular weight epoxy resin having a number average molecular weight above 2 000 and preferably between 2 000 and 20 000. Number average molecular weights ordinarily can be measured by gel permeation chromatography (GPC) as set forth in ASTM D 3016-72 and ASTM D 3593-80. The high molecular weight epoxy emulsion products can then be reacted with acrylic monomer to form epoxy/acrylic blends and copolymer grafts which are suitable for use as a low to zero VOC coating composition such as interior two piece can coating. In accordance with a preferred aspect of this invention, the preformed high molecular weight epoxy resin dispersed in water is modified by copolymerizing ethylenic monomers in-situ with the aqueous dispersed high molecular weight epoxy resin to produce an aqueous polymeric blend of addition polymer and epoxy resin. The addition polymer portion of the epoxy-acrylic blend comprises polymerized ethylenically unsaturated monomers including functionally reactive and non-reactive monomers. Functionally reactive monomers include carboxyl functional monomers such as acrylic acid and lower alkyl substituted acrylic acids such as methacrylic acid and ethacrylic acid to provide carboxyl functionality for stabilizing the epoxy-acrylic copolymer mixture in water. The preferred acrylic acid is methacrylic acid. Small amounts of other functionally reactive monomers may be used such as hydroxy monomers for example 2-hydroxy ethyl methacrylate, amide monomers for example acrylamide, or N-methylol monomers illustrated by N-methylol acrylamide. Examples of non-reactive monomers are acrylate and methacrylate esters, such as ethyl acrylate, methyl methacrylate or isobutyl methacrylate, styrene, or vinyl toluene, vinyl acetate, vinyl chloride, vinylidene chloride, acrylonitrile, and generally alkyl esters of an acrylic acid, generally the lower alkyl esters, that is, those esters in which the esterifying group contains from 1 to 4 carbon atoms, and particularly ethyl acrylate. Other useful monomers include other C 1-15 alkyl acrylates esters and methacrylate esters such as, for example, propyl acrylate, isopropyl acrylate, butyl acrylate, isobutyl acrylate, tertiary butyl acrylate, pentyl acrylate, decyl acrylate, lauryl acrylate, isobornyl acrylate, methyl methacrylate, butyl methacrylate, isobutyl methacrylate, hexyl methacrylate, 2-ethyl hexyl methacrylate, octyl methacrylate, and nonyl methacrylate. Other useful monomers are those readily available monomers having vinyl unsaturation such as vinyl esters including vinyl acetate, vinyl propionate, vinyl butyrates, vinyl benzoates, vinyl isopropyl acetates and similar vinyl esters, vinyl halides, including vinyl chloride, vinyl fluoride, and vinylidene chloride; vinyl aromatic hydrocarbons including styrene, methyl styrenes and similar lower alkyl styrenes, chlorostyrene, vinyl toluene, vinyl naphthalene, divinyl benzene; vinyl aliphatic hydrocarbon monomers including alpha olefins such as ethylene, propylene, isobutylene, and cyclohexene as well as conjugated dienes such as 1,3-butadiene, methyl-2-butadiene, 1,3-piperylene, 2,3-dimethyl butadiene, isoprene, cyclohexadiene, cyclopentadiene, and dicyclopentadiene; and vinyl alkyl ethers including methyl vinyl ether, isopropyl vinyl ether, n-butyl vinyl ether, and isobutyl vinyl ether. In a preferred aspect of this invention, carboxyl functional monomers including lower alkyl substituted acrylic acids can be pre-reacted with epoxy resins by esterifying the carboxyl group with an epoxy oxirane group to produce an epoxy-ester prepolymer or intermediate polymer containing pendant double bond unsaturation. Thereafter, the epoxy-ester prepolymer can be further reacted with additional ethylenic monomers by emulsion addition copolymerization of the pendant double bonds with ethylenic double bonds in the ethylenic monomers previously described. The resulting copolymer is an epoxy-ester graft copolymer. In practice, the epoxy resin and the mixture of polymerizable ethylenic monomers are reacted together in the presence of a free radical initiator, preferably of the peroxide type, more preferably benzoyl peroxide. Typical and useful free radical initiators include cumene hydroperoxide, benzoyl peroxide, t-butyl perbenzoate, t-butyl peroxide, lauryl peroxide, methyl ethyl ketone peroxide, chlorobenzoyl peroxide, and the like. Other useful initiators include azobis initiators such as azobis derivatives of dimethylvaleronitrile, phenylmethane, isobutyronitrile, butyronitrile, cyclohexane carbonitrile, isobutyrate, trimethyl pentane and methyl propane. The amount of free radical catalyst is expressed in terms of percentage by weight of benzoyl peroxide based on the total weight of the polymerizable monomer. The amount of peroxide catalyst should be at least 0.5%, and preferably between 1% and 10% weight of benzoyl peroxide or other peroxide initiator based on monomer weight. The reaction temperature preferably is maintained in the range from 30°C to 130°C, although the temperature may be adjusted within a relatively wide range to accommodate the reactivity of the monomer mixture. After the monomers are added, the reaction mixture is normally held for up to three hours at the reaction temperature to assure complete monomer conversions. The in-situ polymerization of the monomers produces an in-situ formed carboxyl functional polymer containing at least 1%, and preferably between 5% and 25% of polymerized monoethylenically unsaturated carboxylic acid monomer based on the total weight of monomers copolymerized. The viscosity of the epoxy-acrylic polymeric blend can be controlled or adjusted by adding base such as tertiary amine, a metal hydroxide, or preferably ammonia. Preferably, polymerizable ethylenic monomers are used to replace solvent in the low molecular weight epoxy/bisphenol solution. Monomer can thus function as a solvent to lower viscosity and enhance emulsification, but then later polymerizes in the presence of the epoxy emulsion. Styrene is particularly well suited for this use as it can thermally polymerize during the epoxy advancement reaction without the use of a free radical initiator. Hence, zero VOC advanced epoxy/acrylic polymer blend emulsions can thereby be produced. The epoxy-acrylic matrix polymeric blend composition comprises by weight between 2% and 90% acrylic copolymer and between 10% and 98% epoxy resin. If desired, the epoxy-acrylic blend can be mixed with a water dispersible crosslinking component such as aminoplast whereby the resulting composition can be heat cured to crosslink with carboxyl functionality of the epoxy-acrylic copolymer. On a polymer weight basis, the coating composition can contain between 0% and 15% (advantageously between 1% and 10%) aminoplast crosslinking resin mixed with between 85% and 100% of the above-indicated epoxy-acrylic matrix polymer composition. Referring next to the aminoplast crosslinking resins, aminoplasts are melamine or melamine derivatives such as methylol melamine or similar alkylated melamine formaldehyde resins. Aminoplasts further include benzo guanamine, acetoguanamine, as well as ureaformaldehyde. Commercially available aminoplasts which are water-soluble or water-dispersible for the instant purpose include Cymel 301, Cymel 303, Cymel 370, and Cymel 373 (all being products of American Cyanamid, Stamford, USA, said aminoplasts being melamine based, (e.g. hexamethoxy-methyl melamine for Cymel 303), and Beettle 80 (products of American Cyanamid which are methylated or butylated ureas). Other suitable aminoplast resins are of the type produced by reaction of aldehyde and form guanamines; ammeline; 2-chloro-4,6-diamine-1,3,5-triazine; 2-phenyl-p-oxy-4,6-diamino-1,3,5-tri-azine; and 2,4,6-triethyl-triamino-1,3,5-triazine. The mono, di-, or tri-aryl melamines, such as 2,4,6-triphenyl-triamino-1,3,5-triazine, are preferred. Other aldehydes used to react with the amino compound to form the resinous material are crotonic aldehyde, acrolein, or compounds which generate aldehydes, such as hexamethylene-tetramine, paraldehyde, and the like. The water-dispersed coating compositions can be produced by mixing together the high molecular weight epoxy-acrylic copolymer with water-dispersed crosslinker. The aminoplast polymer can be dispersed into water by mechanical mixing. The amount of water contained in the coating composition containing the epoxy-acrylic copolymer, and the aminoplast resin depend on the viscosity desired, which in turn, relates to the method of application. For spraying, preferably the coating composition contains between 10% and 30% by weight polymeric solids relative to 70% to 90% water. For applications other than spraying, the aqueous polymeric dispersions can contain between 10% and 40% by weight water. The coating composition of the present invention can be pigmented and/or opacified with known pigments and opacifiers. For many uses, including food use, the preferred pigment is titanium dioxide. The aqueous coating compositions can be used in a coating process which comprises applying a layer of the composition to a substrate and subsequently causing or allowing the layer to dry or cure. The aqueous coating composition can be applied satisfactorily by conventional methods known in the coating industry. Thus, spraying, rolling, dipping, and flow coating application methods can be used for both clear and pigmented films, although spraying is preferred. After application onto the substrate, the coating can be cured thermally at temperatures in the range from 95°C to 235°C or higher for time sufficient to effect complete curing as well as volatilizing of any fugitive component in the coating. For metal sheet substrates intended as beverage containers and particularly for carbonated beverages such as beer, the coating should be applied at a rate in the range from 0.0775 to 2.325 milligrams of polymer coating per square centimetre (0.5 to 15 milligrams per square inch) of exposed metal surface. To attain the foregoing, the water-dispersible coating as applied should be as thick as 2.5 to 25µm (0.1 to 1 mil). For a better understanding of the present invention, the following examples are provided. In this application, all parts are parts by weight, all percentages are weight percentages, and temperatures are degrees Centigrade, unless otherwise expressly noted. Pressures have been measured in pounds per square inch above atmospheric pressure (psig) and have been converted to N/m 2 on the basis of 1 psig = 6 895 N/m 2 . Viscosities were measured in poise or centipoise and were converted to N s/m 2 on the basis of 1 poise = 0.1 N s/m 2 . EEW means epoxide equivalent weight. Grit is agglomerated material that could be filtered out. NVM is non-volatile material by weight. EXAMPLE 1 (comparative example) A low molecular weight epoxy resin was advanced in molecular weight, but not in accordance with this invention, by the following procedure. Raw Material Weight Aromatic hydrocarbon solvent (Aromatic 2000) 189 Epoxy resin (Shell Epon 1009, EEW 3000) 18 Bisphenol A 376 Epoxy resin (Shell Epon 828, EEW 188) 564 Sodium C 14-16 olefin sulphonate surfactant (trade mark A246L) 2.5 Water 100 Water containing 0.5 g triethylamine catalyst 100.5 The aromatic solvent, Epon 1009, bisphenol A, and Epon 828 were heated moderately to dissolve the bisphenol-A and form a uniform mixture. The mixture was then added to the first addition of water containing surfactant and mixed in with a high shear Ross ME-100 (trade mark) emulsifier at 10,000 rpm for 5 minutes. Then the second addition of water containing triethyl amine was mixed with ordinary mixing for about 6 hours while heating at about 95°C. The NVM was 17.6. The product was a very low molecular weight epoxy resin of soft toffee consistency indicating the advancement reaction progress slowly and moderately. See Table 1. EXAMPLE 2 A low molecular weight was advanced in molecular weight in accordance with the process of this invention. Raw Material Weight Aromatic hydrocarbon (Aromatic 2000) 189 Epoxy resin (Shell Epon 1009, EEW 3000) 18 Bisphenol A 376 Epoxy resin (Shell Epon 828, EEW 188) 564 Sodium C 14-16 olefin sulphonate surfactant 5 Polyvinyl alcohol (mol.wt. 77 000) 2 Water 200 Water containing 1 g triethylamine catalyst 401 The aromatic solvent, Epon 1009, bisphenol-A and Epon 828 were heated moderately and then added to the water containing surfactant under high shear as in Example 1. Then the mixture was added to a pressure reactor along with the water containing triethylamine, where the contents were heated under ordinary mixing at a temperature of about 125°C under 206 850 N/m 2 (30 psig) pressure for 4 hours. The NVM was 22.1%. The product was a high molecular weight epoxy resin of solid consistency. See Table I. Melt viscosities of advanced epoxy resins produced in Examples 1 and 2 were compared with commercial epoxy resins measured at 175°C on an ICI (trade mark) cone and plate viscometer and the comparisons are reported in Table 1. Sample Epoxy Eqv. Wt. Viscosity poise N s/m 2 Epon 828 188 < 5 < 0.5 Epon 1004 1000 57 5.7 Epon 1009 3000 > 500 > 50 Example 1 - < 5 < 0.5 Example 2 - > 500 > 50 The foregoing Table 1 indicates that significantly higher molecular weight epoxy resins can be prepared as stable aqueous emulsion by the process of Example 2 under pressure and at temperatures above 100°C. EXAMPLE 3 (comparative example) A low molecular weight epoxy resin was prepared according to Example 2, except that polyvinyl alcohol nonionic surfactant was omitted. The emulsion was not stable at 125°C resulting in undesirable and useless agglomeration of the emulsion. EXAMPLE 4 A low molecular weight epoxy resin was advanced in molecular weight according to the procedure of Example 2, except diisobutyl ketone was used as an organic solvent in the first step in place of the aromatic hydrocarbon. Reaction temperature was 125°C and pressure was 206 850 N/m 2 (30 psig). The result was a high molecular weight epoxy resin stably dispersed in water as indicated in Table 2. EXAMPLE 5 A low molecular weight epoxy resin was advanced in molecular weight according to the procedure in Example 2, except that 1.5 g of benzyl dimethyl amine was used as a catalyst instead of triethyl amine. Reaction temperature was 125°C and pressure was 206 850 N/m 2 (30 psig). A stable, aqueous dispersed, high molecular weight epoxy resin resulted as indicated in Table 2. EXAMPLE 6 A low molecular weight epoxy resin was advanced in molecular weight according to Example 2, except that the reaction temperature under pressure of 344 750 N/m 2 (50 psig) was 140°C for 4 hours. A stable, aqueous dispersed, high molecular weight epoxy resin resulted as indicated in Table 2. Example Filtered Grit NVM ICI CONE AND PLATE 175°C Viscosity poise N s/m 2 3 total agglomeration 4 42 g 18.1% >500 >50 5 7.2 g 21.2% >500 >50 6 10.1 g 20.4% >500 >50 EXAMPLE 7 Low molecular weight epoxy resin was advanced in molecular weight in a manner similar to Example 2. Raw Material Weight (grams) a) Bisphenol-A 479.4 Epoxy resin (Epon 828, EEW 188) 752 b) Aromatic solvent (Aromatic 2000) 33 Mixture (a) 167 c) Surfactant (A246L) 5 Polyvinyl alcohol (Airool 350) 2 Water 200 d) Water (deionized) 400 Triethylamine 1 The raw material components were processed according to Example 2 at a pressure of 206 850 N/m 2 (30 psig) and at a temperature of 125°C for 4 hours. EXAMPLE 8 Low molecular weight epoxy resin was advanced in molecular weight in a manner similar to Example 2, except that polyvinyl alcohol was replaced with 2 g of hydroxy ethyl cellulose (trade mark Natrosol 250-MR). A stable aqueous emulsion of high molecular epoxy resin resulted at 20.1% NVM and 18.3 g grit. EXAMPLE 9 The intermediate from Ex. 6 was used to make an aqueous emulsion in a manner similar to Ex. 2 and was further copolymerized with ethylenic monomers as described below. 300 g. From EX.6 above 10 g. methacrylic acid 5 g. styrene 0.5 g. benzoyl peroxide Materials were mixed at 20°C and warmed under nitrogen to 80°C and held for 5 hours. 7 g of 28% ammonia solution was added in 10 g water and then cooled. Sample from Ex.6 above had a Brookfield viscosity of 0.02 Ns/m 2 (20 centipoise) with a #3 spindle at 50 rpm. The resulting resin had a viscosity of 0.34 Ns/m 2 (340 centipoise) under the same conditions. No settling of viscosity change in either sample was noted after 1 month. The emulsion of this example was drawn down on A1 sheet with a #14 wire wound bar, and baked 2 minutes at 193°C (380°F). The cured film properties were as follows:- Film Properties Appearance: Clear, glossy, smooth, hard, no crawling Sag: None noted Water Resistance: 30 minutes at 82°C (180°F) gave slight blush, but good adhesion over A1 and no film softening. EXAMPLES 10 AND 11 The following low molecular weight epoxy resins were processed according to the method of Example 2, except for the surfactant combination which differs as indicated below: The (a) components were premixed into (b) components using high shear 10 000 rpm for 5 minutes at 90°C. Part (c) was then added and the mixture heated at 125°C at 206 850 N/m 2 (30 psig) for 4 hours. The resulting resins had the following properties: NVM Grit Ex. 11 0.5% NVM over 150 g polymer grit Ex. 12 13.8% NVM 75 g polymer grit

Claims: A process for producing a coating composition containing a stable aqueous emulsion of high molecular weight epoxy resin binder produced by the steps comprising: (i) dispersing into water using a combination of anionic and non-ionic surfactants a combination of: a) low molecular weight epoxy resin having a number average molecular weight between 360 and 2000; b) a diphenol, to produce an aqueous dispersion of reactants; (ii) advancing the molecular weight of the low molecular weight epoxy resin by reacting with the diphenol at temperatures above 105°C and at pressures more than 34 475 N/m 2 above atmospheric (5 psig), to provide an aqueous dispersed high molecular weight epoxy resin, having a number average molecular weight of greater than 2000. The process of Claim 1 where the aqueous emulsion contains between 10% and 30% by weight of reactants dispersed in water. The process of Claim 1 where the diphenol is reacted with the low molecular weight epoxy resin at temperatures between 110°C and 150°C. The process of Claim 1 where the diphenol is reacted with the low molecular weight epoxy resin at pressures between 68 950 and 482 650 N/m 2 (10 psig and 70 psig). The process of Claim 1 also comprising the step; i) modifying the aqueous dispersion of high molecular weight epoxy resin by copolymerizing ethylenic monomers in-situ with the aqueous dispersed high molecular weight epoxy resin to produce an aqueous polymeric blend of addition polymer and epoxy resin. The process of Claim 5 where the ethylenic monomers comprise a carboxyl functional monomer, and said carboxyl functional monomer is pre-reacted with the epoxy resin to produce an epoxy-ester prepolymer or intermediate polymer containing pendant double bond unsaturation. The process of Claim 6 where the epoxy ester prepolymer is further reacted with additional ethylenic monomers by emulsion addition copolymerization of the pendant double bonds with ethylenic double bonds in the additional ethylenic monomers. The process of Claim 7 where the ethylenic monomers are copolymerized by addition copolymerization to produce an aqueous emulsion mixture of high molecular weight epoxy resin and addition copolymer. The process of Claim 5 where the emulsion copolymerized monomers plus high molecular weight epoxy resin comprises a matrix polymeric binder, and the copolymerized monomer comprises by weight between 2% and 90% based on the weight of the matrix polymeric binder. The process of Claim 9 where the matrix polymeric binder is mixed with an aminoplast to provide a composition which can be heat cured, containing on a polymer weight basis between 0% and 15% aminoplast. A coating composition containing a stable aqueous emulsion of high molecular weight epoxy resin binder, having a number average molecular weight of greater than 2000 and produced by the process of Claim 1 to 10. A coating process which comprises applying a layer of the composition claimed in Claim 11 to a substrate and subsequently causing or allowing the layer to dry or cure. A substrate when coated by the process of Claim 12 comprising a coating derived from the composition as claimed in Claim 11.

Inventors: BODE DANIEL, CRAUN GARY PIERCE, BODE, DANIEL, CRAUN, GARY PIERCE
Applicants: GLIDDEN CO, THE GLIDDEN COMPANY
Application year: 1993
Main classification: C08G59
IPC codes: C08F283, C08G59, C09D151