Cationic, Advanced Epoxy Resin Compositions

1. Field of the Invention

The invention is concerned with cationic, advanced epoxy resin compositions, a method for their preparation and the use of such compositions in cathodic electrodeposition.

2. Description of the Prior Art

Electrodeposition has become an important method for the application of coating over the last two decades and continues to grow in popularity because of its efficiency, uniformity and environmental acceptance. Cathodic electrodeposition has become dominant in areas where highly corrosion-resistant coatings are required, such as in primers for automobile bodies and parts. Epoxy based systems provide the best overall performance in this application and are widely used.

Cathodic electrodeposition resins based on conventional epoxies obtained by reacting liquid diglycidyl ethers of bisphenol A with bisphenol A to produce higher molecular weight epoxy resins have known disadvantages. Such products tend to have excessively high softening points resulting in poor flow out. In addition, such products require excessive amounts of solvent during their preparation. In order to improve flow, it has been proposed to modify such conventional epoxy resins by reaction with a diol in the presence of a tertiary amine catalyst. Thus, Bosso et al., U.S. Pat. No. 3,839,252, describes modification with polypropylene glycol. Marchetti et al., U.S. Pat. No. 3,947,339, teaches modification with polyesterdiols or polytetramethylene glycols. Wismer et al., U.S. Pat. No. 4,419,467, describes still another modification with diols derived from cyclic polyols reacted with ethylene oxide. These various modifications, however, also have disadvantages. Tertiary amines or strong bases are required to effect the reaction between the primary alcohols and the epoxy groups involved. Furthermore, these reactions require long cook times and are subject to gellation because of competitive polymerization of the epoxy groups by the base catalyst. In addition epoxy resins containing low levels of chlorine are required to prevent deactivation of this catalyst.

Many coating formulations applied by electrodeposition include pigments to provide color, or opacity or application or film properties. U.S. Pat. No. 3,936,405, Sturni et al., describes pigment grinding vehicles especially useful in preparing stable, aqueous pigment dispersions for water-dispersible coating systems, particularly for application by electrodeposition. The final electrodepositable compositions, as described, contain the pigment dispersion and an ammonium or amine salt group solubilized cationic electrodepositable epoxy-containing vehicle resin and other ingredients typically used in electrodepositable compositions. Among the kinds of resins used are various polyepoxides such as polyglycidyl ethers of polyphenols, polyglycidyl ethers of polyhydric alcohols and polyepoxides having oxyalkylene groups in the epoxy molecule.

The automobile industry still has needs in the areas of controlled film thickness and lower temperature cure systems. The ability to build thicker, uniform films which are smooth and free of defects will allow the elimination of an intermediate layer of paint known as a primer surface or spray primer, previously required to yield a sufficiently smooth surface for the topcoat. Such an elimination results in removal of one paint cycle and provides more efficient operations. Thicker electrocoat primers may also provide improved corrosion resistance.

The present invention is directed to an advanced epoxy cationic resin having a charge density of from about 0.2 to about 0.6 milliequivalent of cationic charge per gram of resin prepared by reacting in the presence of a suitable catalyst

(A) a composition comprising (1) at least one diglycidyl ether of a polyetherpolyol and (2) at least one diglycidyl ether of a dihydric phenol with

(B) at least one dihydric phenol and optionally,

(C) a monofunctional capping agent; wherein components (A-1) and (A-2) are employed in quantities such that from about 10 to about 75, preferably from about 10 to about 50 and most preferably from about 15 to about 35, weight percent of the diglycidyl ethers contained in component (A) are contributed by Component (A-1) and from 25 to about 90, preferably from about 50 to about 90 and most preferably from about 65 to about 85, weight percent of such glycidyl ethers are contributed by component (A-2) and components (A) and (B) are employed in such quantities that the resultant advanced epoxy resin has an average epoxide equivalent weight of from about 350 to about 10,000 and preferably from about 600 to about 3,000, whereby there is formed an advanced epoxy resin having terminal oxirane groups and subsequently converting the oxirane groups to cationic groups by reacting the resin with a nucleophile and adding an organic acid and water at at least one point in the process.

The present invention is also directed to a coating composition comprising an aqueous dispersion of the above-described cationic, advanced epoxy resin, a method for making such compositions and a method for coating such compositions.

The cationic, advanced epoxy resin compositions of the invention contain the resins obtained from a selected advanced epoxy resin having terminal oxirane groups by reacting at least some of the epoxy (oxirane) groups of the resin with a nucleophile in and adding an organic acid and water at some point during the preparation.

The starting epoxy resin component for preparing the cationic, advanced epoxy resin compositions is an advanced resin prepared by reacting a composition comprising a glycidyl ether of a polyetherpolyol (A-1), a glycidyl ether of a dihydric phenol (A-2) with a dihydric phenol (B) and optionally, a monohydric capping agent (C). Glycidyl ethers of dihydric phenols useful for the preparation of these resins are those having at least one, and preferably an average of about two, vicinal epoxide groups per molecule. These polyepoxides can be produced by condensation of an epihalohydrin with a polyphenol in the presence of a basic acting substance.

Useful glycidyl ethers of polyphenols are represented by Formulae I and II: ##STR1## wherein A is a divalent hydrocarbon group having from 1 to 12, preferably 1 to 6 carbon atoms, ##STR2## or the like; each R' is independently hydrogen, a hydrocarbyl or hydrocarbyloxy group having from 1 to 4 carbon atoms, or a halogen, preferably chlorine or bromine; R is independently hydrogen or a hydrocarbyl group having from 1 to 3 carbon atoms; n has a value from zero to 1; and n' has a value from zero to about 40, preferably from 0.1 to 5.

Polyphenols useful for the production of these polyepoxides include 2,2-bis(4-hydroxyphenyl)propane (bisphenol A), 1,1-bis(4-hydroxyphenyl)ethane, bis(4-hydroxyphenyl)methane (bisphenol F), p,p'-hydroxybiphenol, resorcinol, hydroquinone, or the like. The particularly preferred polyglycidyl ethers of polyphenols are the diglycidyl ether of bisphenol A and the oligomeric polyglycidyl ethers of bisphenol A.

The glycidyl ethers of polyetherpolyols useful in preparation of these epoxy resins are those having the structure: ##STR3## The glycidyl ethers of polyetherpolyols are produced by the condensation of an epihalohydrin with a polyetherpolyol having the structure:

wherein X is ##STR4## where R is hydrogen or an alkyl group having 1 to 6 carbon atoms, n has a value of 1 to 3 and m is a number having an average of from 2 to 50.

The polyetherpolyols may be produced by the polymerization of the appropriate alkylene oxide or of mixtures of various alkylene oxides to produce a chain having the desired R groups distributed among the units. Examples of useful polyetherpolyols are diethylene glycol, triethylene glycol, poly(ethylene glycol), dipropylene glycol, tripropylene glycol, poly(propylene glycol), di-1,2-butylene glycol, poly(1,2-butyleneoxide), poly(1,4-butanediol), and the like. The particularly preferred polyetherpolyols from which the diglycidyl ethers are derived are dipropylene glycol and poly(propylene glycol) in which the average value of m is between 5 and 20.

Some of the common methods of synthesis of the diglycidylethers of polyetherpolyols produce significant amounts of organic chloride-containing impurities. However, other processes are known for preparing products with lower levels of such impurities. While the low-chloride resins are not required for the practice of this invention, they may be used, if desired, for possible improvements in the process of preparing the resins, in the storage properties of the resins or formulated coatings made therefrom or in the performance properties of the products.

Mixtures containing the above two glycidyl ether components are reacted with a diphenol and, optionally, a capping agent to produce epoxy-functional resins having the desired epoxide(oxirane) group content which are used to prepare the resins of the invention. The effective proportions of the diglycidyl ether components range from about 10 to about 75 weight percent of the diglycidylether of a polyetherpolyol (A-1) and from about 25 to about 90 weight percent of the diglycidyl ether of a diphenol (A-2). However, better overall results are obtained with from about 10 to about 50 weight percent of the diglycidylether of a polyetherpolyol and from about 50 to about 90 weight percent of the diglycidylether of a phenol. Especially preferred is from about 15 to about 35 weight percent of the diglycidylether of a polyetherpolyol and correspondingly from about 65 to about 85 weight percent of the diglycidyl ether of a phenol. While products containing higher than 90 percent of the diglycidylether of a polyetherpolyol will electrodeposit to give high film build, their rupture voltage limits their use to the lower voltages which do not provide sufficient throwing power for many applications such as in electrocoating automobile bodies. The proportions of the glycidyl ether components (A=A-1+A-2) and the dihydric phenol (B) are selected to provide an average epoxy equivalent weight in the advanced epoxy resin of from about 350 to about 10,000, preferably from about 600 to about 3,000. Such proportions usually are in the range of from about 60 to about 90 weight percent of A and from about 10 to about 40 weight percent of B. Useful diphenolic compounds include those described above as suitable for production of polyepoxide. The preferred diphenol is bisphenol A. Also useful are the bisphenols produced by chain extension of the diglycidyl ether of a bisphenol with a molar excess of a bisphenol to produce a diphenolic functional oligomeric product.

The use of capping agents such as monofunctional phenolic compounds provides the advantageous ability to reduce the epoxide content of the resulting product without chain-extension reactions and thus allows independent control of the average molecular weight and the epoxide content of the resulting resin within certain limits. Use of a monofunctional compound to terminate a certain portion of the resin chain ends also reduces the average epoxy functionality of the reaction product. The monofunctional phenolic compound is typically used at levels of zero to 0.7 equivalent of phenolic hydroxyl groups per equivalent of epoxy which would remain after reaction of substantially all of the phenolic groups of the diphenol.

Examples of useful monofunctional capping agents are monofunctional phenolic compounds such as phenol, tertiary-butyl phenol, cresol, para-nonyl phenol, highr alkyl substituted phenols, and the like. Particularly preferred is para-nonyl phenol. The total number of phenolic groups and the ratio of difunctional to monofunctional phenolic compounds, if any are used, are chosen so that there will be a stoichiometric excess of epoxide groups. Ratios are also chosen so that the resulting product will contain the desired concentration of terminal epoxy groups and the desired concentration of resin chain ends terminated by the monophenolic compound after substantially all of the phenolic groups are consumed by reaction with epoxy groups. Usually, the amount of the capping agent is from about 1 percent to about 15 percent based on the total weight of the A and B components.

These amounts are dependent on the respective equivalent weights of the reactants and the relative amounts of the epoxy-functional components and may be calculated by methods known in the art. In the practice of this invention, the desired epoxide content of the reacion product useful for preparation of the cationic resin is typically between 1 and 5 percent, calculated as the weight percentage of oxirane groups, and preferably is from about 2 to about 4 percent. These levels are preferred because they provide, after conversion, the desired cationic charge density in the resinous products useful in cathodic electrodeposition. These cationic resins are produced by conversion of part or all of the epoxy groups to cationic groups as described below.

Reaction of the monofunctional compound with epoxy groups of the polyglycidylether components of the reaction mixture may be done prior to, substantially simultaneously with, or subsequent to the chain-extension reactions of the diphenolic compound and the polyglycidylether components. The preferred method is to have all of the reactants present simultaneously.

Reactions of the above components to produce the epoxy resins are typically conducted by mixing the components and heating, usually in the presence of a suitable catalyst, to temperatures between 130.degree. and 200.degree. C., preferably between 150.degree. and 175.degree. C., until the desired epoxide content of the product is reached. The reaction optionally may be conducted in an appropriate solvent to reduce the viscosity, facilitate mixing and handling, and assist in controlling the heat of reaction.

Many useful catalysts for the desired reactions are known in the art. Examples of suitable catalysts include ethyltriphenylphosphonium actate.acetic acid complex, ethyltriphenylphosphonium chloride, bromide, iodide, or phosphate, and tetrabutylphosphonium acetate. The catalysts are typically used at levels of 0.01 to 0.5 mole percent of the epoxide groups.

Appropriate solvents include aromatic solvents, glycol ethers, glycol ether esters, high boiling esters or ketones, or mixtures. Other useful solvents will be apparent to those skilled in the art. Preferred solvents are ethylene glycol monobutylether and propylene glycol monophenylether. Solvent content may range from zero to about 30 percent of the reaction mixture. A solvent is usually chosen which is compatible with the subsequent cation-forming reactions and with the final coating composition so that the solvent does not require subsequent removal.

Unexpectedly, incorporation of these glycidyl ethers of polyetherpolyols into the epoxy resin confer to cathodically electrodepositable coating compositions produced therefrom the ability to build thicker films having controlled thickness during the electrodeposition process, as compared to a similar composition using an epoxy resin not containing the polyetherpolyol/glycidyl ether component. The ability to deposit thicker films is highly desirable for reducing the number of paint applications required while improving the corrosion resistance and appearance of the electrodeposited coating. The film thickness can be controlled by adjusting the amount of the diglycidylether or polyetherpolyol incorporated into the epoxy resin. Generally, thickness increases with increasing content of this component.

Another advantage is that the cationic epoxy resins containing the diglycidylether of a polyetherpolyol have a lower viscosity at a given temperature than unmodified cationic resins of the same molecular weight. This lower viscosity allows the use of higher molecular weight resins and/or less solvent to achieve a viscosity comparable to an unmodified resin. The lower viscosity resins allow the coating composition greater flowout during deposition and curing which results in better appearance. Alternatively, the lower viscosity resins enable curing at lower temperatures to give equivalent flow and appearance. Finally, coatings produced using these epoxy resins have greater flexibility due to incorporation of the diglycidylether of a polyetherpolyol component as component to those based on similar resins not containing that component.

The nucleophilic compounds which are used advantageously in forming the cations required by this invention are represented by the following classes of compounds, sometimes called Lewis bases:

(a) monobasic heteroaromatic nitrogen compounds,

(b) tetra(lower alkyl)thioureas,

(c) R.sub.1 --S--R.sub.2 wherein R.sub.1 and R.sub.2 individually are lower alkyl, hydroxy lower alkyl or wherein R.sub.1 and R.sub.2 are combined as one alkylene radical having 3 to 5 carbon atoms

(d) ##STR5## wherein R.sub.2 and R.sub.3 individually are lower alkyl, hydroxy lower alkyl, ##STR6## or are combined as one alkylene radical having from 3 to 5 carbon atoms, R.sub.4 is an alkylene group having from 2 to 10 carbon atoms, R.sub.5 and R.sub.6 individually are lower alkyl and R.sub.1 is hydrogen or lower alkyl, aralkyl or aryl, except that when R.sub.2 and R.sub.3 together are an alkylene group then R.sub.1 is hydrogen, lower alkyl or hydroxyalkyl and when either or both of R.sub.2 and R.sub.3 is ##STR7## then R.sub.1 is hydrogen, (e) ##STR8## wherein R.sub.1, R.sub.2 and R.sub.3 individually are lower alkyl, hydroxy lower alkyl or aryl.

In this specification the term lower alkyl means an alkyl having from 1 to 6 carbon atoms such as methyl, ethyl, propyl, isopropyl, n-butyl, isobutyl, n-pentyl, isopentyl, n-hexyl and isohexyl.

Representative specific nucleophilic compounds are pyridine, nicotinamide, quinoline, isoquinoline, tetramethyl thiourea, tetraethyl thiourea, hydroxyethylmethyl sulfide, hydroxyethylethyl sulfide, dimethyl sulfide, diethyl sulfide, di-n-propyl sulfide, methyl-n-propyl sulfide, methylbutyl sulfide, dibutyl sulfide, dihydroxyethyl sulfide, bis-hydroxybutyl sulfide, trimethylene sulfide, thiacyclohexane, tetrahydrothiophene, dimethyl amine, diethyl amine, dibutyl amine, N-methylethanolamine, diethanolamine and the ketimine derivatives of polyamines containing secondary and primary amino groups such as those produced by the reaction of diethylene triamine or N-aminoethylpiperazine with acetone, methyl ethyl ketone or methylisobutyl ketone; N-methylpiperidine, N-ethylpyrrolidine, N-hydroxyethylpyrrolidine, trimethylphosphine, triethylphosphine, tri-n-butylphosphine, trimethylamine, triethylamine, tri-n-propylamine, tri-isobutylamine, hydroxyethyldimethylamine, butyldimethylamine, tri-hydroxyethylamine, triphenylphosphorus, and N,N,N-dimethylphenethylamine.

Substantially any organic acid, especially a carboxylic acid, can be used in the conversion reaction to form onium salts so long as the acid is sufficiently strong to promote the reaction between the nucleophile and the vicinal epoxide group(s) on the resinous reactant. In the case of the salts formed by addition of acid to a secondary amine/epoxy resin reaction product, the acid should be sufficiently strong to protonate the resultant tertiary amine product to the extent desired.

Monobasic acids are normally preferred (H.sup..sym. A.sup..crclbar.). Suitable organic acids include, for example, alkanoic acids having from 1 to 4 carbon atoms (e.g., acetic acid, propionic acid, etc.), alkenoic acids having up to 5 carbon atoms (e.g., acrylic acid, methacrylic acid, etc.) hydroxy-functional carboxylic acids (e.g., glycolic acid, lactic acid, etc.) and organic sulfonic acids (e.g., methanesulfonic acid), and the like. Presently preferred acids are lower alkanoic acids of 1 to 4 carbon atoms with lactic acid and acetic acid being most preferred. The anion can be exchanged, of course, by conventional anion exchange techniques. See, for example, U.S. Pat. No. 3,959,106 at column 19. Suitable anions are chloride, bromide, bisulfate, bicarbonate, nitrate, dihydrogen phosphate, lactate and alkanoates of 1-4 carbon atoms. Acetate and lactate are the most preferred anions.

The conversion reaction is normally conducted by merely blending the reactants together and maintaining the reaction mixture at an elevated temperature until the reaction is complete or substantially complete. The progress of the reaction is easily monitored. The reaction is normally conducted with stirring and is normally conducted under an atmosphere of inert gas (e.g., nitrogen). Satisfactory reaction rates occur at temperatures of from about 25.degree. C. to about 100.degree. C., with preferred reaction rates being observed at temperatures from about 60.degree. to about 80.degree. C.

Good results can be achieved by using substantially stoichiometric amounts of reactants although a slight excess or deficiency of the epoxy-containing resin or the nucleophile can be used. With weak acids, useful ratios of the reactants range from 0.5 to 1.0 equivalent of nucleophile per epoxide group of the resin and 0.6 to 1.1 equivalents of acid per epoxide. These ratios, when combined with the preferred epoxide content resins described above, provide the desired range of cationic charge density required to produce a stable dispersion of the coating composition in water. With still weaker acids (e.g., a carboxylic acid, such as acetic acid) a slight excess of acid is preferred to maximize the yield of onium salts. In preparing the compositions in which the cationic group being formed is an onium group, the acid should be present during the reaction of the nucleophile and the epoxy group of the resin. When the nucleophile is a secondary amine, the amine-epoxy reaction can be conducted first, followed by addition of the acid to form the salt and thus produce the cationic form of the resin.

For the onium-forming reactions, the amount of water that is also included in the reaction mixture can be varied to convenience so long as there is sufficient acid and water present to stabilize the cationic salt formed during the course of the reaction. Normally, it has been found preferable to include water in the reaction in amounts of from about 5 to about 30 moles per epoxy equivalent. When the nucleophile is a secondary amine, the water can be added before, during, or after the resin epoxy group/nucleophile reaction. The preferred range of charge density of the cationic, advanced epoxy resin is from about 0.2 to about 0.6 milliequivalent of charge per gram of the resin.

It has also been found advantageous to include minor amounts of water-compatible organic solvents in the reaction mixture. The presence of such solvents tends to facilitate contact of the reactants and thereby promote the reaction rate. In this sense, this particular reaction is not unlike many other chemical reactions and the use of such solvent modifiers is conventional. The skilled artisan will, therefore, be aware of which organic solvents can be included. One class of solvents that we have found particularly beneficial are the monoalkyl ethers of the C.sub.2 -C.sub.4 alkylene glycols. This class of compounds includes, for example, the monomethyl ether of ethylene glycol, the monobutyl ether of ethylene glycol, etc. A variety of these alkyl ethers of alkylene glycols are commercially available.

When a desired degree of reaction is reached, any excess nucleophile can be removed by standard methods, e.g., dialysis, vacuum stripping and steam distillation.

The cationic, advanced epoxy resins of this invention in the form of aqueous dispersions are useful as coating compositions, especially when applied by electrodeposition. The coating compositions containing the cationic resins of this invention as the sole resinous component are useful but it is preferred to include crosslinking agents in the coating composition so that the coated films, when cured at elevated temperatures, will be crosslinked and exhibit improved film properties. The most useful sites on the resin for crosslinking reactions are the secondary hydroxyl groups along the resin backbone. Materials suitable for use as crosslinking agents are those known to react with hydroxyl groups and include blocked polyisocyanates; amine-aldehyde resins such as melamine-formaldehyde, urea-formaldehyde, benzoguanine-formaldehyde, and their alkylated analogs; polyester resins; and phenol-aldehyde resins.

Particularly useful and preferred crosslinking agents are the blocked polyisocyanates which, at elevated temperatures, deblock and form isocyanate groups which react with the hydroxyl groups of the resin to crosslink the coating. Such crosslinkers are typically prepared by reaction of the polyisocyanate with a monofunctional active-hydrogen compound.

Examples of polyisocyanates suitable for preparation of the crosslinking agent are described in U.S. Pat. No. 3,959,106 to Bosso, et al., in Column 15, lines 1-24, incorporated by reference herein. Also suitable are isocyanate-functional prepolymers derived from polyisocyanates and polyols using excess isocyanate groups. Examples of suitable prepolymers are described by Bosso, et al., in U.S. Pat. No. 3,959,106, Column 15, lines 25-57, incorporated herein by reference. In the preparation of the prepolymers, reactant functionality, equivalent ratios, and methods of contacting the reactants must be chosen in accordance with considerations known in the art to provide ungelled products having the desired functionality and equivalent weight.

Preferred polyisocyanates are the isocyanurate trimer of hexamethylene diisocyanate, toluene diisocyanate, methylene diphenylene diisocyanate, isophorone diisocyanate and a prepolymer of toluene diisocyanate and trimethylolpropane.

Suitable blocking agents include alcohols, phenols, oximes, lactams, and N,N-dialkylamides or esters of alpha-hydroxyl group containing carboxylic acids. Examples of suitable blocking agents are described in U.S. Pat. No. 3,959,106 to Bosso, et al., in Column 15, line 58, through Column 16, line 6, and in U.S. Pat. No. 4,452,930 to Moriarity. Particularly useful are the oximes of ketones, also known as ketoximes, due to their tendency to deblock at relatively lower temperatures and provide a coating composition which can be cured at significantly lower temperatures. The particularly preferred ketoxime is methyl ethyl ketoxime.

These cationic resins of the invention, when formulated with certain preferred ketoxime-blocked polyisocyanates, provide coating compositions which cure at significantly lower temperatures than those of the prior art.

The blocked polyisocyanates are prepared by reacting equivalent amounts of the isocyanate and the blocking agent in an inert atmosphere such as nitrogen at temperatures between 25.degree. to 100.degree. C., preferably below 70.degree. C. to control the exothermic reaction. Sufficient blocking agent is used so that the product contains no residual, free isocyanate groups. A solvent compatible with the reactants, product, and the coating composition may be used such as a ketone or an ester. A catalyst may also be employed such as dibutyl tin dilaurate.

The blocked polyisocyanate crosslinking agents are incorporated into the coating composition at levels corresponding to from about 0.2 to about 2.0 blocked isocyanate groups per hydroxyl group of the cationic resin. The preferred level is from about 0.5 to about 1.0 blocked isocyanate group per resin hydroxyl group.

A catalyst optionally may be included in the coating composition to provide faster or more complete curing of the coating. Suitable catalysts for the various classes of crosslinking agents are known to those skilled in the art. For the coating compositions using the blocked polyisocyanates as crosslinking agents, suitable catalysts include dibutyl tin dilaurate, dibutyl tin diacetate, dibutyl tin oxide, stannous octanoate, and other urethane-forming catalysts known in the art. The preferred catalyst is dibutyl tin dilaurate. Amounts used typically range between 0.1 and 3 weight percent of binder solids.

Unpigmented coating compositions are prepared by blending the cationic resinous product with the crosslinking agent and optionally any additives such as catalysts, solvents, surfactants, flow modifiers, defoamers, or other additives. This mixture is then dispersed in water by any of the known methods. A particularly preferred method is the technique known as phase-inversion emulsification, wherein water is slowly added with agitation to the above mixture, usually at temperatures ranging from ambient to 70.degree. C., until the phases invert to form an organic phase-in-water dispersion. The solids content of the aqueous dispersion is usually between 5 and 30 percent by weight and preferably between 10 and 25 percent by weight for application by electrodeposition.

Pigmented coating compositions are prepared by adding a concentrated dispersion of pigments and extenders to the unpigmented coating compositions. This pigment dispersion is prepared by grinding the pigments together with a suitable pigment grinding vehicle in a suitable mill as known in the art.

Pigments and extenders known in the art are suitable for use in these coatings including pigments which increase the corrosion resistance of the coatings. Examples of useful pigments or extenders include titanium dioxide, talc, clay, lead oxide, lead silicates, lead chromates, carbon black, strontium chromate, and barium sulfate.

Pigment grinding vehicles are known in the art. A preferred pigment grinding vehicle for use in this invention consists of a water-soluble cationic resinous product, water, and a minor amount of glycol ether solvent. The cationic resinous product is prepared by reacting an epichlorohydrin/bisphenol A condensation product having an epoxide group content of about 8 percent with a nucleophile, an acid, and water in a similar fashion as described above for the cationic resins used in the preferred embodiment of the invention. The water-soluble product may be diluted with water to form a clear solution useful as a pigment grinding vehicle.

The pH and/or conductivity of the coating compositions may be adjusted to desired levels by the addition of compatible acids, bases, and/or electrolytes known in the art. Other additives such as solvents, surfactants, defoamers, anti-oxidants, bactericides, etc. may also be added to modify or optimize properties of the compositions or the coating in accordance with practices known to those skilled in the art.

Although the coating compositions of the invention may be applied by any conventional technique for aqueous coatings, they are particularly useful for application by cathodic electrodeposition, wherein the article to be coated is immersed in the coating composition and made the cathode, with a suitable anode in contact with the coating composition. When sufficient voltage is applied, a film of the coating deposits on the cathode and adheres. Voltage may range from 10 to 1,000 volts, typically 50 to 500. The film thickness achieved generally increases with increasing voltage. In the case of the coating compositions of the invention, thicker films are achieved by incorporation of the diglycidyl ether of a polyetherpolyol into the epoxy resin used to produce the cationic resins of the invention. Also, control over the final thickness may be exercised by adjusting the amount of that component used. Current is allowed to flow for between a few seconds to several minutes, typically two minutes over which time the current usually decreases. Any electrically conductive substrate may be coated in this fashion, especially metals such as steel and aluminum. Other aspects of the electrodeposition process, such as bath maintenance, are conventional. After deposition, the article is removed from the bath and typically rinsed with water to remove that coating composition which does not adhere.

The uncured coating film on the article is cured by heating at elevated temperatures, ranging from about 200.degree. to about 400.degree. F., for periods of about 1 to about 60 minutes. For the embodiments of the invention using the ketoxime-blocked polyisocyanate curing agents, satisfactory cure of the resulting coating can be achieved at cure schedules as low as 250.degree. F. for 30 minutes, as compared to 325.degree. to 350.degree. F. for 20 to 30 minutes for systems typically used in the art. Although the ketoxime-blocked polyisocyanates have been cited in the prior art as being capable of curing cathodically electrodepositable compositions at relatively lower temperatures, no examples of reduction to practice have been found which achieved cure at less than 325.degree. F. Thus, this aspect of the invention represents a significant improvement over the prior art.

All of the coating compositions of the invention provide useful cathodically electrodepositable coatings having improved flowout, film build, and flexibility properties due to the incorporation of the diglycidyl ether of a polyetherpolyol component.

In the following examples, epoxy resins were used as starting materials which are characterized as follows:

Epoxy Resin A is a condensation product of bisphenol A and epichorohydrin having an epoxide equivalent weight of 187.

Epoxy Resin B is a condensation product of dipropylene glycol and epichlorohydrin having an epoxide equivalent weight of 185.

Epoxy Resin C is a condensation product of a polypropylene glycol having an average molecular weight of 375 to 425 and epichlorohydrin, the product having an epoxide equivalent weight of 323.

Epoxy Resin D is a condensation product of epichlorohydrin and a polypropylene glycol having an average molecular weight of 375 to 425. The product has an epoxide equivalent weight of 333 and contains less than 0.3 percent chlorine in the form of organic chloride impurities and inorganic chlorides.

Curing Agent A is a blocked polyisocyanate available from Mobay Chemical Company as Desmodur KL5- 2540. The material is believed to be the reaction product of methyl ethyl ketoxime and a polyisocyanate which is substantially the isocyanurate trimer of hexamethylene diisocyanate. The product is supplied as a 75 percent solution of the blocked polyisocyanate in propylene glycol monomethylether acetate.

Into a one-liter, round-bottomed flask fitted with a nitrogen inlet, thermometer, mechanical stirrer, condenser, and an addition funnel was charged 262.3 parts by weight of toluene diisocyanate (80/20 mixture of 2,4/2,6 isomers) under a nitrogen atmosphere. The diisocyanate was stirred and heated to 60.degree. C. A mixture of 160.2 parts of Polyglycol P425 (The Dow Chemical Company) and 0.35 parts of T-12 catalyst (M & T Chemicals) was added over a period of one hour at a rate which maintained the reaction mixture near 60.degree. C. The mixture was maintained at 60.degree. C. for an additional 40 minutes after completion of the addition, then 196.8 parts of methyl ethyl ketoxime was added over a period of 100 minutes at 60.degree. C. After about one-third of the ketoxime has been added, addition of 135.2 parts of propylene glycol monomethyl ether acetate (2-methoxy propyl acetate) was begun and proceeded concurrently with the ketoxime addition. After completion of these two simultaneous additions, infrared analysis showed no detectable unreacted isocyanate. The product was diluted by addition of 19.5 parts of 2-ethyl hexanol.

Into a one-liter, round-bottomed flask fitted with a nitrogen inlet, thermometer, condenser, mechanical stirrer, and an addition funnel was charged 626.3 parts of Spencer Kellog's Spenkel P49-A6-60, a 60 percent solution of an isocyanate terminated prepolymer from toluene diisocyanate and trimethylolpropane dissolved in methoxypropyl acetate. The solution was stirred at ambient temperatures (22.degree. to 24.degree. C.) and 0.62 parts of T-12 catalyst was added. Two hundred parts of 2-ethylhexanol was added dropwise over a period of 2 hours. The temperature of the reaction mixture was allowed to rise to 50.degree. to 60.degree. C. during the addition. The reaction mixture was then cooled to ambient temperature over 2 hours. The infrared spectrum of the product showed no residual unreacted isocyanate groups. The product solution was approximately 68.9 percent non-volatile.

Into a two liter, round-bottom flask fitted with a nitrogen inlet, thermometer, mechanical stirrer, and condenser were charged Epoxy Resin A and Epoxy Resin B or Epoxy Resin C, and bisphenol A in the preparations shown in Table I. The mixture was stirred under a nitrogen atmosphere and heated to 85.degree. to 90.degree. C. to form a clear mixture. A solution containing 70 percent by weight of ethyl triphenyl phosphonium acetate.acetic acid complex in methanol in the amount shown in Table I was added at 90.degree. C. The mixture was then heated to 150.degree. C. at a rate of 1.degree. to 2.degree. C. per minute and then allowed to exotherm. The peak exotherm temperature was controlled to below 190.degree. C. by cooling. The temperature was then allowed to fall to 175.degree. C. and then maintained at 175.degree. C. until 70 minutes past peak exotherm, when the desired epoxide content was reached. The epoxide equivalent weight of each product is shown in Table I.

For each of Resins R and S, para-nonylphenol, in the amount shown in Table I, was included in the material charged to the round-bottomed flask. Comparative material A was prepared in the same manner as Resins N-Q from the components shown in Table I.

The resin products summarized in Table I were converted to a cationic resin in the following manner.

Into a two-liter, round-bottomed flask fitted with a nitrogen inlet, thermometer, mechanical stirrer, condenser, and addition funnel was charged some of each of the epoxy resin product shown in Table I and a glycol ether in the kinds and amounts shown in Table II. The mixture was heated under nitrogen to between 110.degree. to 130.degree. C. and stirred to form a solution. The solution was cooled to the reaction temperature and an aqueous mixture of nicotinamide, lactic acid, and water was added over a period of 30 minutes to produce an opaque, whitish, viscous mixture. The reaction temperature was maintained throughout the addition. Thirty minutes after completion of this addition, additional water was added over 30 minutes. The reaction mixture was maintained at the reaction temperature for a reaction time of 3 hours after completion of the first addition. The products were clear, light yellow, highly viscous solutions. Comparative Example A was prepared in this same manner from comparative Material A in the amounts and kinds of ingredients shown in Table II.

Into a 5-liter, round-bottom flask fitted with a nitrogen inlet, thermometer, mechanical stirrer and condenser was charged 1,763.7 parts by weight of Epoxy Resin A, 588.4 parts of Epoxy Resin C, 852.7 parts of bisphenol A, and 363.4 parts of 95 percent para-nonyl phenol. The mixture was stirred under nitrogen atmosphere and heated to 90.degree. C. to form a clear mixture. A solution containing 70 percent by weight of ethyl triphenyl phosphonium acetate.acetic acid complex in methanol (4.6 parts) was added at 90.degree. C. The mixture was heated to 150.degree. C. over a period of 29 minutes and allowed to exotherm to 184.degree. C. The temperature was then maintained at 175.degree. C. for 95 minutes past exotherm. The mixture was cooled to 130.degree. C. and an additional 2.3 parts of the phosphonium acetate solution was added. The temperature was raised to 175.degree. C. over 35 minutes and maintained at 175.degree. C. for 50 minutes. The epoxy resin product was then cooled and the solid pulverized. The epoxide equivalent weight of the product (Epoxy Resin T) was 1,660 g/equivalent.

Seven hundred fifty parts of Epoxy Resin T and 83.3 parts of propylene glycol monophenyl ether were charged to a similar reactor and heated under nitrogen to 110.degree. C. to form an epoxy resin solution. The solution was cooled to 85.degree. C. and a mixture of 40.2 parts of N,N-dimethylethanolamine, 54.2 parts of 75 percent lactic acid, and 101.6 parts of deionized water was added dropwise over 35 minutes at 80.degree. to 85.degree. C. The reaction mixture was maintained at 80.degree. C. for 7.25 hours. The cationic resin product was a viscous, light yellow solution.

A portion (750 parts) of Epoxy Resin T and 83.3 parts of propyleneglycol monophenyl ether were charged to a reactor as described in Example 7 and heated under nitrogen to 82.degree. C. N-methyl-2-aminoethanol (33.9 parts) was added dropwise with cooling over 40 minutes. The temperature was allowed to climb to 95.degree. C. during the course of the addition. The reaction mixture was then maintained at 100.degree. C. for 3.5 hours to produce a viscous, yellow resin in solution. Portions of this resin were converted to cationic form during preparation of unpigmented coating compositions therefrom in Examples 18, 23 and 24.

A solution (826.3 parts) was prepared by heating under nitrogen to 90.degree. C. Epoxy Resin T and propyleneglycol monophenyl ether in the same proportions in a similar reactor as described in Examples 7 and 8. Methyl isobutyl ketone (61.5 parts) was added dropwise at 80.degree. C. The resulting resin solution was then heated to 150.degree. C. at ambient pressure and 37.6 parts of a solvent-water azeotrope was collected in a Dean-Stark trap. The solution was cooled to 75.degree. C. Versamine K11 (115.6 parts), which is a ketimine derivative of a polyamine containing both primary and secondary amine groups was added dropwise over a period of 65 minutes at 70.degree. to 79.degree. C. The reaction mixture was then maintained at 80.degree. to 84.degree. C. for one hour to produce a viscous, yellow resin solution. Portions of this resin were converted to cationic form during preparation of coating compositions therefrom in Examples 19, 25 and 26.

Into a 1-liter, round-bottomed flask fitted with a nitrogen inlet, thermometer, condenser, mechanical stirrer, and addition funnel was charged 108.8 parts of Epoxy Resin A, 36.3 parts Epoxy Resin D, 52.5 parts bisphenol A, and 22.4 parts 95 percent para-nonyl phenol. The mixture was heated under nitrogen to 95.degree. C. and 0.28 part of a 70 percent solution in methanol of ethyl triphenyl phosphonium acetate.acetic acid complex was added. The mixture was heated to 150.degree. C. over a period of 30 minutes and then allowed to exotherm to 170.degree. C. The temperature was then maintained at 175.degree. C. for 70 minutes after peak exotherm. The epoxide equivalent weight of the product at this point was 1,690 g/equivalent. The product was cooled to 115.degree. C. and diluted with 24.4 parts of propylene glycol monophenyl ether to produce Epoxy Resin U in solution.

The epoxy resin solution was cooled to 90.degree. C. and a mixture of 11.9 parts of nicotinamide, 14.9 parts 75 percent lactic acid, and 29.4 parts of deionized water was added dropwise over a period of 39 minutes at between 72.degree. to 85.degree. C. The reaction mixture then was maintained at 70.degree. C. for 7.5 hours to produce a cationic resin solution.

Into a two liter, round-bottomed flask fitted with a nitrogen inlet, thermocouple temperature indicator, mechanical stirrer, condenser, and an addition funnel was charged the resin solution as shown in Table III. This solution was heated under nitrogen atmosphere to 60.degree. to 75.degree. C. and stirred while the curing agent and T-12 catalyst (M & T Chemicals) were added and blended with the resin. For Examples 18, 19 and 23-26, lactic acid was added to convert the resin to the cationic form. The mixture was cooled to 60.degree. to 63.degree. C. and dropwise addition of deionized water was begun. The water was added at a rate which permitted thorough mixing with the viscous mixture to form a water-in-resin dispersion in which no separated water layer was apparent. The temperature of the mixture was steadily decreased as the addition proceeded such that the temperature was 40.degree. to 50.degree. C. when the mixture inverted, as noted by a drop in viscosity, to form a resin in water dispersion. The dispersion was then cooled to ambient temperature while diluting with the remainder of the water. The amounts of the ingredients are shown in Table III.

For Examples 11-14, the pH was adjusted to about 7.6 with a 10 weight percent solution of N,N-diethyl-2-aminoethanol in water. The conductivity was adjusted to about 1,500 micromho/cm with a 10 weight percent solution of ammonium acetate in water. Comparative Example B was prepared in the same manner as Examples 11-14.

Water was added to the products of Examples 11-26 to adjust the non-volatile content to approximately 18 percent by weight which were then used as unpigmented coating compositions.

Pigmented coating compositions of Examples 27-38 and Comparative Example C were prepared by adding, with stirring, the concentrated pigment dispersion shown in Table IV and described below to the unpigmented coating compositions of the examples shown in Table IV. Sufficient pigment dispersion was added to yield a pigment-to-binder ratio of 0.2 by weight in the final paint. The pigment dispersions were made by using a pre-prepared pigment grinding vehicle.

Pigment grinding vehicle A was prepared by charging into a two-liter, round-bottomed flask fitted with a nitrogen inlet, thermometer, mechanical stirrer and condenser 340.3 parts by weight of Epoxy Resin A and 109.7 parts of bisphenol A. The mixture was stirred under a nitrogen atmosphere and heated to 90.degree. C. to form a clear mixture. A solution containing 70 percent by weight of ethyl triphenyl phosphonium acetate in methanol (0.6 parts) was added. The mixture was then heated to 150.degree. C. at a rate of 1.degree. to 2.degree. C. per minute and then allowed to exotherm to 170.degree. C. The temperature was raised to 175.degree. C. and maintained for 30 minutes, at which time the epoxide content of the resin was 8.1 percent by weight. The resin was cooled to 130.degree. C., diluted with 50.0 parts of ethylene glycol monobutyl ether, and cooled to 75.degree. C. to give an epoxy resin solution. A mixture of 77.5 parts of nicotinamide, 72.4 parts of lactic acid, and 212.5 parts of water was added to the resin solution over 65 minutes at 73.degree. to 79.degree. C. The mixture was then reacted 3 hours at 76.degree. to 79.degree. C. The resulting clear, light yellow, cationic resin solution was diluted to approximately 40 percent non-volatiles with 673.1 parts of water to produce a clear, yellow solution useful as a pigment grinding vehicle.

Pigment Grinding Vehicle B was prepared in the same kind of reactor by first preparing an epoxy resin solution from the same components in the same ratios by the same procedure as described for Pigment Grinding Vehicle A. Then the solution (750 parts) was heated to 82.degree. C. and a mixture of 85.7 parts of N,N-dimethyl-2-aminoethanol, 154.6 parts of a solution containing 75 percent of lactic acid and 288.9 parts of deionized water was added thereto over a period of 55 minutes at 75.degree. to 82.degree. C. The reaction mixture was maintained at 80.degree. C. for an additional 4.3 hours, then was cooled to 70.degree. C. and maintained at that temperature for 11 hours. The product was diluted with water to produce a cationic resin (Pigment Grinding Vehicle B) as a solution having a non-volatile content of 30 percent.

Pigment Grinding Vehicle C was prepared by making the epoxy resin solution in the same manner and same proportions. The epoxy resin solution (422 parts) was heated to 65.degree. C. Then 47.1 parts of N-methyl-2-aminoethanol was added dropwise over 22 minutes with cooling to maintain the temperature at 65.degree. to 74.degree. C. The temperature then was maintained at 80.degree. C. for 3 hours. A solution (75.4 parts) which contained 75 percent of lactic acid was diluted with water (100 parts) and then the resulting solution was added at 75.degree. to 80.degree. C. to the reaction mixture at 75.degree. to 80.degree. C. Thereafter dilution of the product with additional water (458.7 parts) provided a cationic resin solution containing 40 percent non-volatiles (Pigment Grinding Vehicle C).

A concentrated pigment dispersion (Pigment Dispersion A) was prepared by placing a pigment blend (100 parts by weight) comprised of 35 parts of clay, 35 parts of titanium dioxide, 20 parts of lead silicate, and 10 parts of carbon black in a metal paint can along with 75 parts of Pigment Grinding Vehicle A. Enough chrome-plated steel pellets (about 2 mm diameter by 5 mm long) were added to comprise about one-third of the final bulk volume. The pigments were ground and dispersed in the vehicle by placing the can on a paint shaker for 45 minutes. Water was then added and blended in to reduce the viscosity slightly and the grinding pellets removed by filtration. The final pigment dispersion contained 57 percent pigment by weight.

Concentrated Pigment Dispersion B was prepared by the same procedure using lead silicate, carbon black, lead chromate, titanium dioxide, and clay. The dispersion was further diluted with water to a final pigment content of 55.7 percent by weight.

Pigment Dispersion C was prepared using Pigment Grinding Vehicle B in the procedure described for Pigment Dispersion A. The dispersion was diluted further with water to a final pigment content of 56.3 percent by weight.

Pigment Dispersion D was prepared using Pigment Grinding Vehicle C in the procedure described for Pigment Dispersion A. The resulting dispersion was diluted further with water to a final pigment content of 54 percent by weight.

The coating compositions were placed in a stainless steel tank, agitated, and maintained at 80.degree. F. Unpolished steel test panels having Bonderite 40 treatment and P60 rinse available from Parker were immersed in the tank and connected as the cathode to a D.C. voltage source, with the tank walls serving as the anode. The desired voltage was applied for two minutes, then the panels were removed, rinsed with deionized water, and baked at 275.degree. F. for 30 minutes. Film thicknesses at various voltages are shown in Table V for unpigmented and pigmented compositions.

In all cases, the resins of the invention provided thicker films than the comparative examples which did not contain a diglycidylether of a polyetherpolyol. The thickness also generally increased with increasing proportions of that component.