Powa--Method for Coating and Product

Much of the research and development effort in the metal coating art is directed to the search for coating materials and methods of applying such materials which eliminate or appraoch elimination of volatile, organic solvents released in heat curing, which produce coatings at least comparable to conventional paints and methods of painting in appearance and durability, and which can be produced at a commercially feasible cost.

One proposal before the art is to replace liquid costing materials with coating materials in the form of dry, particulate solids commonly called "powder paint". These conventionally contain very low concentrations of volatile solvents, i.e., substantially less than any other paint system and of the order of 2% or slightly higher, and, in this regard, have much to recommend them. Inherent in their use, however, are certain problems of production and application which have retarded the extent of their adoption. One of these involves their use in conjunction with particulate metal pigments, ordinarily aluminum flakes. Automobiles coated with a so-called "metallic" finish, i.e., a topcoat of enamel or lacquer in which there is dispersed aluminum flakes in addition to conventional pigments, have found wide acceptance in the marketplace. For the most part, the problems incidental to employing aluminum flakes in conventional liquid paints, i.e., problems of paint manufacture and paint application, have been solved through years of experimentation and use. The problems of using aluminum flakes in dry powder are far more complex, particularly where some type of pulverizing step is a part of the paint manufacturing process and when application of the paint to a substrate is by electrostatic spray techniques. Further, while increased use of powder coatings in greater volume and improved methods of manufacture will reduce the present cost of quality powder coatings, their production in all of the colors demanded in the marketplace may be prohibitive.

Another approach to providing quality coatings in a low emission system has been the use of the so-called water-based coatings, i.e., aqueous resin solutions and aqueous resin emulsions. Conventionally, these contain a concentration of volatile organic solvents that is far below that in conventional liquid enamels and lacquers, i.e., resin solutions and resin dispersions or both in an organic solvent, but significantly higher than is found in powder coatings. Other problems encountered with water-based coatings include (1) problems of humidity control (2) problems of film fracture during the bake known as "popping", occur in areas receiving an unnecessarily thick coating, often the result of substrate contours, and (3) problems in obtaining finish coatings having a high gloss without special care and cost in formulation.

The invention hereinafter described in detail provides a method painting characterized by low solvent emissions, a capacity for producing coatings of high gloss while maintaining other requisite properties, and the production of substrates having unique qualities particularly suitable for variations in styling.

One object of this invention is to provide a method of coating wherein the organic solvent concentration of coating materials is reduced to a practical minimum while providing a high quality, high gloss finish at an acceptable cost.

Another object of this invention is to provide a method for employing metal pigments and powder coating materials in producing a finish coating which avoids pigment degradation in the manufacture of coating materials and the problems inherent in electrostatic application of powder containing aluminum flakes.

Another object of this invention is to provide a method of coating wherein water-based paints may be employed without humidity control, film-popping, or special formulation to obtain high gloss.

Another object of this invention is to provide coated substrates having unique properties.

While this invention is also effective for painting polymeric substrates under the same conditions hereinafter set forth for painting metal with due allowance for the maximum temperature tolerance of the substrate, this invention is primarily directed to the painting of metal.

The metal substrate to be used will ordinarily be steel which has received conventional preparations for finish coating, i.e., cleaning, phosphate treating and coating with a conventional primer paint to provide corrosion protection and enhance adhesion of the finish coat.

In the method of this invention, a substrate is provided with a protective and decorative finish coat in four essential steps.

In the first step of this method, the substrate is coated with a relatively thin, highly pigmented, water-based thermosetting enamel to an average film thickness between about 0.4 and about 1.2, preferably 0.5 to 1.0, mils (1 mil = 0.001 inch). The enamel will contain between about 6 and about 60 weight percent of combined pigments based on resin solids, i.e., about 6 to about 60 parts by weight particulate pigment to about 40 to about 94 parts by weight of film-forming material, the latter consisting essentially of thermosetting polymers conventionally called "paint binder resins" and crosslinking agents where such resins are not self-crosslinking. The variance will depend upon the type of "metallic" or "nonmetallic" finish desired, i.e., and concentration and type of pigments used.

In the second step, the thin, pigmented, water-based coating is at least partially heat cured by baking at a metal temperature in the range of about 200.degree. to about 350.degree., preferably 225.degree. to 275.degree.F. for a time in the range of about 5 to about 15 minutes.

In the third step, there is applied to the thin, pigmented, water-based coating a powder coatings that has average film thickness in the range of about 0.8 to about 1.7, preferably 1.0 to 1.5, mils and upon baking provides an essentially transparent overcoat. Ordinarily, the overcoat is pigment-free but in some embodiments, appearance is enhanced by the inclusion of small amounts of very small pigments which do not negative its transparency, e.g., transparent iron oxides.

In the fourth step, the powder coating and the underlying water-based coating are baked at a temperature in the range of about 300.degree. to about 350.degree., preferably 325.degree.-350.degree.F. for a time in the range of about 15 to about 30 minutes.

It wll be understood by those skilled in the art that in each of the baking steps, the time of baking is preferably inversely proportional to the temperature of the same within the ranges specified therefor.

Both the water-based coating material and the powder coating material may be applied by electrostatic spray means. The water-based coating material also may be applied by air spray, hydraulic spray, or a combination of electrostatic spray with either of the others.

The powder coating material used as the transparent overcoat may be any powder coating material providing substantial transparency when baked and may be either thermosetting or thermoplastic. Of necessity, it must be a coating material that will adhere to the basecoat and should have good "flow" or self-leveling properties.

Water-based coating systems and powder coating systems have advantages relative to each other which the method of this invention combines while eliminating certain disadvantages of each.

Relative to the solely water-based coating systems, the method of this invention provides the following advantages:

1. improved chemical resistance. The powder derived overcoat when free or essentially free of pigment and any easily attacked chemical linkages approaches an absolute maximum in chemical resistance for paints.

2. shorter line distance requires in spray booths. This follows from the fact that about 50% or more of the paint applied is powder which requires less line distance than water-based application and the fact that the basecoat is applied as a thin coating which is high in solids concentration.

3. shorter line distance in the curing ovens. Both the thin, high solids, basecoat and the clear powder overcoating can go directly into curing temperature without film popping. Whereas a thicker, less dense, coating characteristic of a solely water-based coating does not admit of ready water release and must pass through upward gradiations of heat before reaching the curing temperatures.

4. improved styling capability. Coatings obtained by the method of this invention have unique qualities that admit of a wider range of styling variations in automobiles and other articles of manufacture where color effect is an important factor in market acceptance. Surprisingly, coatings can be prepared by this method which demonstrate value change at an unusually low angle of incidence. Otherwise stated, the rate of change of color value, i.e., change from light to dark and vice versa, with respect to the angle of light inpingement is greater than with conventional automobile finish coats and greater than with either water-based coatings or powder coatings. Further, the segregation of the aluminum flakes in the basecoat admits of the use of coarser pigments, e.g., larger aluminum particles, without pigment protrusions from the completed coating. This provides additional flexibility for achieving desired polychromatic effects. This flexibility is further enhanced through the employment of small amounts of the aforementioned transparent pigments which, in effect, tint the transparent overcoat.

5. less sensitivity to sagging amd popping. This results from the water-dispersed basecoat being relatively thin and of high solids concentration.

6. less stringent humidity control. This also results from use of the relatively thin, high solids containing basecoat as opposed to a coating of full depth in a solely water-based system.

7. reduced solvent emission. As no more than about 50% of the total finish coat is provided by the water-based component, the total concentration of volatile, organic solvents is decreased proportionally since none need be present in the powder overcoat.

8. reduced usage of components in short supply. Certain materials used in the manufacture or formulation of water-based coatings are in relative short supply, e.g., amines, diethylene glycol monobutyl ether, etc. Reduction of the water-based fraction of these coatings to about 50% or less of that used in solely water-based coatings proportionally reduces the requirements for such materials.

9. improved appearance. The difficulties encountered in obtaining coatings of high gloss with water-based coatings are eliminated with the powder overcoat. Relative to water-based coatings, it is relatively simple to formulate transparent powder coatings which provide a high gloss finish. Further, the positioning of the pigments in the basecoat gives an appearance of depth not obtainable with solely water-based coatings.

10. improved "fill" properties. This relates to the capability of a coating material to obliterate substrate irregularities, e.g., metal scratches etc. High pigment loadings are conducive to hiding such irregularites but in a single coat system a compromise must be struck between achieving such hiding and obtaining a coating with good gloss. The one works against the other. The need for such a compromise is eliminated here with a heavily pigmented base coat to provide "hiding" and a transparent overcoat to provide gloss.

11. increased film durability. This results both from the dense, heavily pigmented undercoat and the chemical resistance of a clear, unpigmented or lightly pigmented powder overcoat.

12. less application problems and increased mottle resistance. This particularly true where metal pigments are employed. It is less difficult to obtain good particle orientation in a thin, highly pigmented, water-based coating than it is with a water-based coating of full depth. A mottled appearance in "metallic" finishes ordinarily results from poor aluminum flake orientation.

Relative to solely powder derived coatings, the method of this invention provides the following advantages:

1. improved chemical resistance. The powder derived overcoat can be free of pigment and any easily attacked chemical linkages and approaches an absolute maximum in chemical resistance for paints.

2. Reduced complexity of color change. In the method of this invention, the powder used, in all cases, is a clear or transparent material after baking. Color change with powder is far more complex than with liquid coatings, be they water-based or otherwise, for the reason that with powder one cannot blend out contaminants, i.e., if a small amount of white particles are applied with black particles, they will show up as white spots on a black surface.

3. Reduced manufacturing costs. The producton of unpigmented powder coatings is markedly less complex and less expensive than the production of pigmented powder coatings.

4. Admits of providing coatings characterized as medium and high metallics. This results from applying the metal particles with the basecoat which is relatively problem free in contrast to the metal orientation problems encountered when electrostatically spraying powder containing medium to high concentrations of metal particles.

5. Reduction of cross contamination. This relates to areas other than color change on the line wherein color contamination of pigmented powders results from manufacture or handling.

6. Improved film appearance. The clear overcoat gives a visual concept of depth when pigmentation is confined to the basecoat.

7. Facilitates painting plastic parts. The dense, basecoat apparently forms a tight seal against gases, e.g., unreacted monomer, which otherwise escape from plastic parts on baking. In a solely powder-derived coating, this release frequently causes bubbling and surface mar.

8. Improved durability. The transparent, powder-derived overcoat renders the coating less subject to deterioration resulting from continued exposure to ultra-violet light.

9. Reduces or eliminates size classification of powder. When conventionally pigmented powder is used, care is taken to remove the "fines", small particles of powder, to reduce the color contamination problem peculiar to pigmented powders.

Any water-based thermosetting paint which can be used in automobile topcoats and is curable under the time-temperature conditions hereinbefore set forth, may be used as the basecoat in the method of this invention.

The water-based enamels preferred for use in this invention are disclosed in U.S. patent application Ser. No. 476,114 filed June 3, 1974, now U.S. Pat. No. 3,919,154, Yun-Feng Chang, et al. The disclosures of this application are incorporated herein by reference.

The hybrid, water-based paint compositions preferred for use in this invention employ in combination a low molecular weight emulsion polymer and a low molecular weight solution polymer with the latter being present in an amount sufficient to contribute significantly to the composition of the polymeric binder, i.e., at least about 5 weight percent of this polymeric combination. Thus, they differ from the conventional emulsion type paints employing a water-soluble thickener polymer in at least three compositional respects irrespective of chemical functionality, namely (1) the emulsion polymers have significantly lower molecular weights, (2) the solution polymers have significantly lower molecular weights, and (3) the solution polymers are employed in significantly higher concentrations than are the water-soluble thickener polymers.

More specifically, the hybrid paint compositions of this invention, exclusive of optional components such as pigments, particulate fillers and catalysts, have a liquid continuous aqueous phase. About 30 to about 50% by weight of this phase, exclusive of the aforecited optional components, is made up of a mixture of (a) an amino resin crosslinking agent; (b) a mixture of at least two copolymers of acrylic monomers; and (c) an amine. The balance is water or, in certain embodiments, water and an organic solvent. The mixture of copolymers comprises (1) about 5 to about 95, preferably about 5 to about 50, and most preferably about 10 to about 30, parts by weight of a "solution polymer", i.e., a carboxy-functional copolymer of acrylic monomers that (i) is at least partially neutralized with an amine, (ii) is soluble in said aqueous phase, (iii) has average molecular weight (M.sub.n) in the range of about 3,000 to about 20,000, and (iv) has Tg in the range of - 15.degree. to 50.degree.C., and (2) about 5 to about 95, preferably about 50 to about 95, and most preferably about 50 to about 70 parts by weight of an "emulsion polymer", i.e., a copolymer of acrylic monomers having carboxy, hydroxy or carboxy and hydroxy functionality that (i) is essentially insoluble in said continuous phase, (ii) has average molecular weight (M.sub.n) in the range of about 3,000 to about 20,000 and (iii) has Tg of -15.degree. to 50.degree.C. The amino resin crosslinking agent is present in an amount in the range of about 15 to about 35 weight percent of the sum of the weight of solution polymer and the weight of emulsion polymer. The amine is a water-soluble amine and is present in an amount sufficient to solubilize the solution polymer in the aqueous phase at a pH range of about 7.1 to about 8.5. In certain embodiments, hereinafter illustrated, these hybrid compositions include organic cosolvents while in other embodiments such solvents are not present.

When applied to the substrate to be coated by spraying, these water-based paints including pigments, particulate fillers, and catalysts, if any, contain between about 50 and about 65% by weight water or in those embodiments wherein such solvents are used, water and organic cosolvents.

A number of methods can be used to prepare the water-based paints preferred for use in this invention.

In a first general method, at least one of the polymers, usually the solution polymer, is polymerized in solution in a water miscible or dilutable organic solvent while the other polymer, usually the emulsion polymer, is prepared by an emulsion polymerization in water. The resultant water-based paint will contain a conventional, essentially non-reactive, water-miscible or dilutable organic paint solvent. The concentration of organic solvent in such paints will be at least about 5% by volume of the volatile phase, i.e., organic solvent and water, and preferably in the range of about 10 to about 20 volume percent of the volatile phase.

In a second general method both the solution polymer and the emulsion polymer are prepared by emulsion polymerizaton in water. The paints thus prepared are prepared without organic solvents and thus employed free of same. Organic solvents in the amounts used in the first general method may be added to the dispersion, if desired.

A third general method is the same as the first general method except for the difference that in carrying out the emulsion polymerization the surfactant, i.e., surface active agent or emulsifier, is replaced by a solution polymer hereinafter more fully described.

A fourth general method is the same as the second general method except for the difference that in carrying out one or both, preferably both, of the emulsion polymerization the surfactant is replaced by a solution polymer hereinafter more fully described.

The advantage provided by the third and fourth general methods is that elimination of the conventional surfactant eliminates the problem of incompatibility and water sensitivity associated with the use of surfactants.

A. The solution polymer in these paints has carboxy functionality and may also have hydroxy functonality and/or amide functionality. These polymers contain about 5 to about 30 mole percent of acrylic or methacrylic acid and 70 to 95 mole percent of olefinically unsaturated monomers copolymerizable with such acid component. Preferably, these other olefinically unsaturated monomers are monoacrylates or monomethacrylates. In the embodiment wherein the primary solution polymer has only carboxy functionality, these are preferably esters of acrylic acid or methacrylic acid and a C.sub.1 -C.sub.8 monohydric alcohol. C.sub.8 -C.sub.12 monovinyl hydrocarbons such as styrene, alpha methyl styrene, t-butyl styrene, and vinyl toluene may comprise up to about 30 mole percent of such polymer. Vinyl monomers such as vinyl chloride, acrylonitrile, methacrylonitrile and vinyl acetate may be included in the copolymer a modifying monomers. However, when employed, these modifying monomers should constitute only between about 0 and about 30 preferably 0 to about 15, mole percent of such polymer. In the embodiment wherein the solution polymer has both carboxy functionality and hydroxy functionality, the copolymer contains about 5 to about 25 mole percent of acrylic or methacrylic acid, about 5 to about 25 mole percent of a hydroxyalkylacrylate or methacrylate, e.g., hydroxyethyl acrylate, hydroxypropyl acrylate, hydroxyethyl methacrylate or hydroxypropyl methacrylate, and a remainder of the same monofunctional monomers as set forth above for the solely carboxy-functional polymer. In still another embodiment, the polymer has amide functionality in addition to carboxy functionality. Such a polymer contains about 5 to about 25 mole percent acrylic acid or methacrylic acid, about 5 to about 25 mole percent of acrylamide, methacrylamide, N-methylolacrylamide, N-methylolmethacrylamide, or the alkyl ether of a methylolacrylamide or a methylolmethacrylamide, e.g., N-isobutoxymethylolacrylamide, with the remainder of the same monofunctional monomers as set forth above for the solely carboxy-functional polymer. A portion of the amide functional monomers may be replaced with a equimolar amount of one of the aforementioned hydroxyacrylates or hydroxymethacrylates.

Other monomers not heretofore mentioned may be used in these polymers if used in limited concentrations. These include 2-acrylamide-2-methylpropanesulfonic acid and methacryloyloxyethylphosphate, which may comprise up to about 3% of such polymer.

B. the emulsion polymer in these paints has carboxy functionality, hydroxy functionality or carboxy and hydroxy functionality. These polymers contain 0 to 15 mole percent acrylic acid or methacrylic acid, preferably 0 to 10 mole percent, and 85 to 100 mole percent of other olefinically unsaturated monomers that are copolymerizable with each other and with the acid component when the latter is used. Such other olefinically unsaturated monomers are the same in type and of the same percentage distribution range as those heretofore disclosed for the solution polymer with the exception of the acid monomers content above noted.

In those embodiments, wherein both the solution polymer and the emulsion polymer have hydroxy functionality and carboxy functionality, it is preferred to have a greater concentration of carboxy functionality on the solution polymer relative to the emulsion polymer and a greater concentration of the hydroxy functionality on the emulsion polymer relative to the solution polymer.

Thus, the combinations involved include (a) a carboxy-functional solution polymer and a hydroxy-functional emulsion polymer, (b) a carboxy-functional solution polymer and a carboxy-functional emulsion polymer, (c) a carboxy-functional solution polymer and a carboxy-functional, hydroxy-functional emulsion polymer, (d) a carboxy-functional and hydroxy-functional solution polymer and a hydroxy-functional emulsion polymer, (e) a carboxy-functional, hydroxy-functional solution polymer and a carboxy-functional and hydroxy-functional emulsion polymer, (f) a carboxy-functional and amide-functional solution polymer and a hydroxy-functional emulsion polymer, (g) a carboxy-functional and amide-functional solution polymer and a carboxy-functional emulsion polymer, (h) a carboxy-functional and amide-functional solution polymer and a carboxy-functional and hydroxy-functional emulsion polymer, (i) a carboxy-functional, hydroxy-functional, and amide-functional solution polymer and a hydroxy-functional emulsion polymer, (j) a carboxy-functional, hydroxy-functional, amide-functional solution polymer and a carboxy-functional emulsion polymer, and (k) a carboxy-functional, hydroxy-functional, amide-functional solution polymer and a carboxy-functional, hydroxy-functional emulsion polymer. Amide functionality may also be incorporated into the emulsion polymer but this is more difficult to achieve efficiently than in the solution polymer, particularly in the case of modified amide functionality, e.g., N-methylolacrylamide.

C. the amino resin crosslinking agent, may be and is hereafter illustrated as a conventional amino resin crosslinking agent of the type long in use as a crosslinking agent in acrylic enamels, e.g., melamine-formaldehyde resins and urea-formaldehyde resins.

In preparing the water-soluble copolymer, the functional monomers and the remaining monothylenically unsaturated monomers are mixed and reacted by conventional free radical initiated polymerization in such proportions as to obtain the copolymer desired. A large number of free radical initiators are known to the art and are suitable for this purpose. These include benzoyl peroxide; t-butyl peroctoate; t-butyl perbenzoate; lauryl peroxide; t-butyl-hydroxy peroxide; acetylcyclohexane sulfonyl peroxide; diisobutyryl peroxide; di-(2-ethylhexyl) peroxydicarbonate; diisopropyl peroxydicarbonate; t-butylperoxypivalate; decanoyl peroxide; axobis(2-methyl propionitrile); etc. The polymerization is carried out in solution using a solvent which is miscible or dilutable with water. The solvent concentration at this stage is ordinarily about 30 to 60 weight percent of the polymerization solution. The polymerization is carried out at a temperature between about 45.degree.C. and the reflux temperature of the reaction mixture. Included among the suitable solvents are n-propyl alcohol, isopropyl alcohol, dioxane, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, ethylene glycol monobutyl ether, diethylene glycol monobutyl ether, diethylene glycol monomethyl ether acetate, diethylene glycol monoethyl ether, diethylene glycol monobutyl ether, ethylene glycol monomethyl ether acetate, diethylene glycol monoethyl ether acetate, etc. The copolymer thus obtained is neutralized with amine to a pH of about 6 to 10 and diluted to desired viscosity with water or organic solvent.

In preparing the emulsion copolymer, the functional monomers are mixed and reacted by conventional free-radical initiated polymerization in aqueous emulsion to obtain the copolymer desired.

Conventional surfactants, chain transfer agents, and initiators are employed in the emulsion polymerization. The monomer charge is usually emulsified by one or more micelleforming compounds composed of a hydrophobic part, such as a hydrocarbon group containing six or more carbon atoms, and a hydrophilic part, such as hydroxyl groups, alkali metal, ammonium carboxylate groups, sulfonate groups, phosphate or sulfate partial ester groups, or a polyether chain. Exemplary emulsifying agents include alkali metal sulfonates of styrene, nahthalene, decyl benzene, and dodecyl benzene; sodium dodecyl sulfate; sodium stearate; sodium oleate; the sodium alkyl aryl polyether sulfates and phosphates; the ethylene oxide condensates of long chain fatty acids, alcohols, and mercaptans, and the alkali metal salts of rosin acids. These materials and the techniques of their employment in emulsion formation and maintenance are well known in the art. A chain transfer agent or mixture of chain transfer agents may be added to the reaction medium to limit the molecular weight of the copolymer; such chain transfer agents are generally mercaptans such as dodecanethiol, benzenethiol, 1-octanethiol, pentanethiol, and butanethiol. These are conventional materis and are employed in a conventional manner. The polymerization initiator is composed of one or more water-soluble, free-radical-generating species such as hydrogen peroxide or the sodium, potassium, or ammonium persulfates, perborates, peracetates, percarbonates and the like. The polymerization is carried out at a temperature between about 45.degree.C. and the reflux temperature of the reaction mixture. As is well known in the art, these initiators may be associated with activating systems such as redox systems which may incorporate mild reducing agents, such as sulfites and thiosulfites, and redox reaction promoters such as transistion metal ions, and that these allow the polymerization to be carried out at a lower temperature, e.g., 0.degree.C. or below. As, however, it is desirable to maintain a low concentration of non-polymeric ionic species in the finished paint formulation in order that the cured paint film may have optimum resistance to water, it is preferred to use a minimum concentration of such optional inorganic salts as ferrous sulfate, sodium bisulfite, and the like.

Those skilled in the art will be aware that other emulsifying agents, polymerization initiators and chain transfer agents may be used which are compatible with the polymerization system herein required and with the attainment of acceptable cured paint film properties.

As will be disclosed later herein, the solution polymer may also be prepared by emulsion polymerization. In such preparation, the resultant acid-functional copolymer latex is converted to a polymer solution by the addition of an appropriate base, usually ammonia or an organic amine. There are, however, different needs involved in the after-preparation employment of the emulsion polymer that is used as such in formulation of paint and the solution polymer which although prepared by emulsion polymerization is subsequently converted to a solution polymer and used as such. These needs should be taken into consideration in the prepartion procedure.

In the use of emulsion polymerization to produce a solution polymer, there is no need for the resulting latex to be stable under conditions different from those ensuing at the end of the polymerization process since the latex no longer exists, as such, after the polymer goes into solution upon neutralization. To facilitate such conversion to solution polymers, polymers prepared by emulsion polymerization for use as solution polymers ordinarily contain a higher concentration of carboxyl groups and a lower concentration of decidedly hydrophobic monomers, e.g., 2-ethylhexyl acrylate, relative to the corresponding concentrations in the polymers prepared by emulsion polymerization for use as such.

In contrast, latices which are used as such in the formulation of paint are required to remain essentially as stable latices throughout the processes of polymerization, paint formulation, and product distribution and use. This implies a requirement of stability, i.e., freedom from coagulum formation through time and under a variety of pH conditions, solvent environment, etc. These requirements are best met, and hence it is preferred to use, an alkali metal or ammonium persulfate either as the sole polymerization initiator, or as one constituent of a mixed initiator system. In those embodiments in which conventional surfactants, more specifically a combination of anionic and nonionic surfactants, to obtain a more stable latex. Such surfactant mixtures are well known in the art.

The polymer solution and the polymer latex prepared according to the aforedescribed procedures are subsequently converted into a paint using conventional paint formulation techniques. Typically, a mill base is prepared which comprises the bulk of the pigment and/or particulate filler of the paint formulation. The mill base is "let down" i.e., blended with the remaining polymeric and liquid constituents of the final formulation. A mill base, prepared by conventional sand grinding, ball milling, or pebble milling generally comprises all or a part of the water soluble resin, pigments, organic cosolvents, and may also comprise a quantity of amine in excess of that required to solubilize the solution polymer. To complete the paint, the polymer latex which has been neutralized to a pH range of 5.0 to 10, preferably 5 to 9, is added with mild agitation to the balance of the water required in the total formulation. The balance of the water-soluble resin, crosslinking agent, and millbase are added slowly with agitation. Additional quantities of pigment may be added subsequently as slurries in organic solvents or as separate mill bases to adjust the color as desired. The viscosity of the finished paint is determined and adjusted as required to obtain desired application properties.

Alternately, all or a portion of the (preferably neutralized) polymer latex, water, organic cosolvent, and amine may be added to the solution polymer and pigments prior to ball milling, sand grinding, or pebble milling. This procedure is advantageously employed to reduce the viscosity of mill bases prepared using the solution polymers of relatively high molecular weight.

Organic amines are used to neutralize carboxyl groups on the solution polymer and hence to render it soluble in the aqueous dispersion. They are also used to maintain the pH of the finished paint formulation above about 7, e.g., in the range of 7-10, preferably between 7 and 9.5, and with certain pigments such as aluminum flakes preferably between 7 and 9, to prevent premature reaction of the functional groups on the acrylic copolymer with the amino resin cross-linking agent. Those skilled in the art will be aware that in certain embodiments the paint dispersion can be made up at a pH outside the pH range for application and later adjusted to the desired pH shortly before it is applied. A portion of the amine, e.g., preferably between about 60 and 100% of the amount chemically equivalent to the carboxyl functionality of the polymer is added to the solution polymer directly. Advantageously, a small additional portion of amine is used to raise the pH of the emulsion polymer to about 5 to about 10, preferably 5 to 9, prior to finishing the paint formulation so that the mill base is not subjected to the low pH environment of the polymer latex (pH about 2.5).

Suitable amines are amines (1) which are soluble in the aqueous medium of the paint, (2) that ionize sufficiently in such aqueous medium to solubilize the solution polymer, (3) that ionize sufficiently in such aqueous medium when employed in suitable amounts to provide the paint dispersion with a pH of at least about 7, preferably 7.2 or higher, and thereby keep the rate of reaction between reactive groups of the amino resin (crosslinking agent) negligible prior to curing an (4) that allow for rapid curing of the enamel upon heating. Suitable amines include alkyl, alkanol and aryl primary, secondary and tertiary amines. Preferred are secondary and tertiaryalkyl and alkanol amines having a boiling point within the range of 80.degree.-200.degree.C. By way of example, these include N,N-dimethyl ethanolamine, N,N-diethylethanolamine, isopropanolamine, morpholine, N-methylmorpholine, N-ethylmorpholine, N-methylethanolamine, 2,6-dimethylmorpholine, methoxypropylamine, and 2-amino-2-methyl-1-propanol.

Catalysts for the curing of resins described herein are not normally required to obtain satisfactory film properties. If desired, however, for purposes of lowering the film baking temperature or of further improving cured film properties, strong acid catalysts can be employed in an amount not in excess of 3% by weight of the total finished paint formulation. Said strong acid catalysts may be introduced either as copolymerizable species incorporated in one or both acrylic copolymers, e.g., 2-acrylamide-2-methylpropanesulfonic acid, or as a non-polymerizable additive, e.g., p-toluenesulfonic acid. It is generally preferred not to add such catalysts, however, as they may tend to increase the water sensitivity of the cured film and may deleteriously affect storage stability of the liquid paint.

In those embodiments wherein a volatile organic solvent is employed as a cosolvent, i.e., solution of the solution polymer also being affected by the use of a water-soluble amine, the following solvents are suitable for this use include: n-propyl alcohol, isopropyl alcohol, butanol, 2-butoxyethanol, 2(2-butoxy)ethoxyethanol, n-octyl alcohol, dioxane, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, ethylene glycol monobutyl ether, diethylene glycol monomethyl ether, diethylene glycol monoethyl ether, diethylene glycol monoethyl ether, diethylene glycol monobutyl ether, ethylene glycol monomethyl ether acetate, diethylene glycol monoethyl ether acetate, etc.

In this method, the water-soluble copolymer is produced by emulsion polymerization. The functional monomers are mixed and reacted by conventional free-radical initiated polymerization in aqueous emulsion to obtain the copolymer desired. The resulting acid-functional copolymer latex is converted to a polymer solution by the addition of an appropriate base, usually ammonia or an organic amine.

Conventional surfactants, chain transfer agents, and initiators are employed in the emulsion polymerization. The monomer charge is usually emulsified by one or more micelleforming compounds composed of a hydrophobic part, such as a hydrocarbon group containing six or more carbon atoms, and a hydrophilic part, such as hydroxyl group, alkali metal or ammonium carboxylate groups, phosphate or sulfate partial ester groups, sulfonate groups, or a polyether chain. Exemplary emulsifying agents include alkali metal sulfonates of styrene, naphthalene, decyl benzene and dodecyl benzene; sodium dodecyl sulfate; sodium stearate; sodium oleate, the sodium alkyl aryl polyether or sulfates and phosphates; the ethylene oxide condensates of long chain fatty acids, alcohols, and mercaptans, and the alkali metal salts of rosin acids. These materials and the techniques of their employment in emulsion formation and maintenance. As previously pointed out, however, when emulsion polymerization is used to product a solution polymer, there is no need for the resulting latex to be stable under conditions different from those ensuing at the end of the polymerization process since the latex no longer exists as such after the polymer goes into solution upon neutralization. To facilitate such conversion to solution polymers, polymers prepared by emulsion polymerization for use as a solution polymer ordinarily contain a higher concentration of carboxyl groups and a lower concentration of decidedly hydrophilic monomers, e.g., 2-ethylhexyl acrylate, relative to the corresponding concentrations in the polymers prepared for use as emulsion polymers. Further, the teaching hereinbefore set forth with respect to the choice of initiators when preparing the latter, i.e., using an alkali metal or ammonium persulfate either as the sole polymerization initiator or as one constitutent of a mixed initiator system to avoid coagulum formation through time and under a variety of pH conditions, solvent environment, etc., is applicable where the polymer is to be converted to a solution polymer. Such initiators may be used when preparing the solution polymer by emulsion polymerization but conventional peroxide inititors are quite suitable for this. Hence, this method offers an advantage, in this respect, in that the concentration of ionic inorganic contaminants, e.g., sulfate ions, in the paint formulation is reduced. A chain transfer agent or mixture of chain transfer agents may be added to the reaction medium to limit the molecular weight of the polymer, such chain transfer agents are generally mercaptans such as dodecanethiol, benzenethiol, 1-octanethiol, pentanethiol and butanethiol. These are conventional materials employed in a conventional manner. The polymerization initiator is composed of one or more water-soluble, free-radical-generating species such as hydrogen peroxide or the sodium, potassium or ammonium persulfates, perborates, peracetates, percarbonates and the like. As is well known in the art, these initiators may be associated with activating systems such as redox system which may incorporate mild reducing agents, such as sulfites and thiosulfites and redox reaction promoters such as transition metal ions. As hereinbefore mentioned, however, it is desirable to maintain a low concentration of non-polymeric ionic species in the finished paint formulation in order that the cured paint film may have optimum resistance to water. Hence, it is preferred to use a minimum concentration of such optional inorganic salts as ferrous sulfate, sodium bisulfite, and the like. Those skilled in the art will be aware that other emulsifying agents, polymerization initiators and chain transfer agents may be used which are compatible with the polymerization system herein required and with the attainment of acceptable cured paint film properties.

The emulsion copolymer may be prepared using the same procedures hereinbefore recited for preparation of the emulsion copolymer in part B. of the first general method.

The polymer solution and the polymer latex prepared according to the aforedescribed procedures may be subsequently converted into a paint using the same procedures hereinbefore recited for formulation of paint in part C. of the first general method.

The use of organic amines and amines which are suitable for such use are the same for this general method as hereinbefore described in detail in part D. of the first general method.

The use of catalysts and catalysts which are suitable for curing the resins hereinbefore described and hereinafter illustrated are the same for this general method as hereinbefore described in detail in part D. of the first general method.

The use and choice of cosolvents for use with this general method may be the same as hereinbefore described in part F. of the first general method.

The third general method for preparing the paints disclosed herein is identical with the first general method hereinbefore described in detail except for the difference that all or a part of the surfactant, i.e., surface active agent or emulsifier, employed in preparing the emulsion polymer, is replaced with a stabilizer polymer, that is identical with or similar to, the solution polymer heretofore described in the first and second general methods and employed as a primary constituent of the paints described herein.

The stabilizer polymer of the third and fourth general methods is carboxy functional and soluble in the aqueous phase of these paint dispersions and is either the same as the primary solution polymer, heretofore discussed, or similar to such solution polymer and compatible with the system. The average molecular weight (M.sub.n) of the stabilizer polymer may be the same as that of the primary solution polymer, i.e., between 3,000 and 20,000 but advisedly is of lower molecular weight than the primary solution polymer. Preferably, the average molecular weight of this third copolymer is in the range of about 3,000 to about 8,000. Its Tg is in the range of -15.degree. to 50.degree.C. When the stabilizer polymer is used in lieu of the surfactant to prepare either the solution polymer or the emulsion polymer, it is present in a concentration in the range of about 0.2 to about 10, preferably about 0.5 to about 5, weight percent based on the weight of polymer to be prepared.

The stabilizer polymer may be prepared by any of several methods, including (1) the method used to prepare the solution polymer of the first general method of paint preparation, i.e., polymerization in solution in a water miscible or dilutable organic solvent; (2) the method used to prepare the solution polymer for the second general method of paint preparation, i.e., emulsion polymerication using an emulsifier or surfactant; (3) emulsion polymerization using in lieu of a surfactant a small amount of the intended polymer from a previous preparation; and (4) a method of emulsion polymerization described hereinafter which employs neither surfactant nor a water soluble polymer in lieu thereof. In the latter, conventional chain transfer agents and polymerization initiators are used as described hereinbefore for the preparation of a solution polymer by emulsion polymerization. A mixture of monomers including carboxy-functional monomers and a chain transfer agent is added slowly to a stirred mixture of initiator and water maintained at a suitable reaction temperature, e.g., between 45.degree. and 95.degree.C. It is preferred to add simultaneously with the monomer mixture an additional quantity of polymerization initiator to sustain a sufficient initiator concentration throughout the polymerization. The polymer latex so obtained is filtered and neutralized with ammonia or water-soluble amine to render it water soluble.

The fourth general method for preparing the paints disclosed herein is identical with the second general method hereinbefore described in detail except for the difference that all of a part of the surfactant used to prepare the solution polymer, the emulsion polymer or, preferable, both the solution polymer and the emulsion polymer is replaced by a stabilizer polymer, such as heretofore described in detail in the description of the third general method.

The preferred powder coating material used in the method of this invention is a thermosetting copolymer of acrylic monomers which is either self-crosslinking, or preferably, is intimately mixed with a monomeric or polymeric crosslinking agent, e.g., an epoxy-functional copolymer of acrylate and methacrylate monomers and, as crosslinking agent, azelaic acid.

The preferred film-formers for this purpose include thermosettable copolymer systems comprising: (a) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a C.sub.4 -C.sub.20, saturated, straight chain, aliphatic, dicarboxylic acid crosslinking agent -- exemplified by U.S. patent application Ser. No. 172,236 filed Aug. 16, 1971; now U.S. Pat. No. 3,752,870 (b) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a mixture of about 90 to 98 percent by equivalent weight of a C.sub.4 -C.sub.20, saturated, straight chain, aliphatic dicarboxylic acid and about 10 to about 2 percent by equivalent weight of a C.sub.10 -C.sub.22, saturated, straight chain, aliphatic, monocarboxylic acid -- exemplified by U.S. Pat. No. 3,730,930; (c) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a diphenol having a molecular weight in the range of about 110 to about 550 -- exemplified by U.S. patent application Ser. No. 172,228, filed Aug. 16, 1971, now U.S. Pat. No. 3,758,634; (d) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a carboxy terminated polymer -- exemplified by U.S. patent application Ser. No. 172,229 filed Aug. 16, 1971, now U.S. Pat. No. 3,781,380; (e) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent a phenolic hydroxy terminated polymer -- exemplified by U.S. patent application Ser. No. 172,225 filed Aug. 16, 1971, now U.S. Pat. No. 3,787,520; (f) an epoxy-functional, carboxy-functional, self-crosslinkable copolymer of ethylenically unsaturated monomers -- exemplified by U.S. patent application Ser. No. 172,238 filed Aug. 16, 1971, now U.S. Pat. No. 3,770,848; (g) a hydroxy-functional, carboxy-functional, copolymer of monoethylenically unsaturated monomers -- exemplified by U.S. patent application Ser. No. 172,237 filed Aug. 16, 1971, now U.S. Pat. No. 3,787,340; (h) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor an anhydride of a dicarboxylic acid -- exemplified by U.S. patent application Ser. No. 172,224 filed Aug. 16, 1971, now U.S. Pat. No. 3,781,379; (i) a hydroxy-functional copolymer of monoethylenically unsaturated monomers and as crosslinking agent therefor a compound selected from dicarboxylic acids, melamines, and anhydrides -- exemplified by U.S. patent application Ser. No. 172,223 filed Aug. 16, 1971, abandoned in favor of continuation-in-part application Ser. No. 407, 128 filed Oct. 17, 1972 in turn abandoned in favor of continuation-in-part application Ser. No. 526,546 filed Nov. 25, 1974 and continuation-in-part application Ser. No. 526,547 filed Nov. 25, 1974; (J) an 25, 1974; (k) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a compound containing tertiary nitrogen atoms -- exemplified by U.S. patent application Ser. No. 172,222 filed Aug. 16, 1971, now U.S. Pat. No. 3,758,635; (k) a copolymer of an alpha-beta unsaturated carboxylic acid and an ethylenically unsaturated compound and as crosslinking agent therefor an epoxy resin having two or more epoxy groups per molecule -- as exemplified by U.S. patent application Ser. No. 172,226 filed Aug. 16, 1971, now U.S. Pat. No. 3,758,633; (l) a self-crosslinkable, epoxy-functional, anhydride-functional copolymer of olefinically unsaturated monomers -- exemplified by U.S. patent application Ser. No. 172,235 filed Aug. 16, 1971, now U.S. Pat. No. 3,758,632; (m) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a carboxy terminated polymer, e.g., a carboxy terminated polymer, e.g., a carboxy terminated polyester -- exemplified by application Ser. No. 223,746 filed Feb. 4, 1972, abandoned in favor of continuation-in-part application Ser. No. 489,271 filed Aug. 5, 1974; (n) an epoxy-functional copolymer of vinyl monomers and as crosslinking agent therefor a dicarboxylic acid -- exemplified by U.S. patent application Ser. No. 228,262 filed Feb. 22, 1972, now U.S. Pat. No. 3,787,521; (o) an epoxy-functional and hydroxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a C.sub.4 -C.sub.20, saturated, straight chain, aliphatic dicarboxylic acid -- exemplified by U.S. patent application Ser. No. 394,874 filed Sept. 6, 1973, abandoned in favor of continuation-in-part application Ser. No. 552,676 filed Feb. 24, 1975; (p) an epoxy-functional copolymer of monovinyl monomers with optional hydroxy and/or amide functionality and as crosslinking agent therefor (1) a C.sub.4 -C.sub.20, saturated, straight chain, aliphatic dicarboxylic acid and (2) a polyanhydride-exemplified by U.S. patent application Ser. No. 394,881 filed Sept. 6, 1973, abandoned in favor of continuation-in-part application Ser. No. 552,456, continuation-in-part application Ser. No. 552,457 and continuation-in-part application Ser. No. 552,471 all filed Feb. 24, 1975; (q) an epoxy-functional, amide-functional copolymer of monovinyl monomers and as crosslinking agent therefor an anhydride of a dicarboxylic acid -- exemplified by U.S. patent application Ser. No. 394,880 filed Sept. 6, 1973, abandoned in favor of continuation-in-part application Ser. No. 552,472 filed Feb. 24, 1975; (r) an epoxy-functional, hydroxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor an anhydride of a dicarboxylic acid -- exemplified by U.S. patent application Ser. No. 394,879 filed Sept. 6, 1973, abandoned in favor of continuation-in-part application Ser. No. 552,511 filed Feb. 24, 1975; (s) an epoxy-functional, amide-functional copolymer of monovinyl monomers and as cross-linking agent therefor a carboxy-terminated polymer -- exemplified by U.S. patent application Ser. No. 394,875 filed Sept. 6, 1973, abandoned in favor of continuation-in-part application Ser. No. 552,518 filed Feb. 24, 1975; (t) an epoxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a monomeric or polymeric anhydride and a hydroxy carboxylic acid -- exemplified by U.S. patent application Ser. No. 394,878 filed Sept. 6, 1973, abandoned in favor of continuation-in-part application Ser. No. 552,079 filed Feb. 24, 1975; (u) an epoxy-functional, amide-functional copolymer of monovinyl monomers and as crosslinking agent therefor a monomeric or polymeric anhydride and a hydroxy carboxylic acid -- exemplified by U.S. patent application Ser. No. 394,877 filed Sept. 6, 1973, abandoned in favor of continuation-in-part application Ser. No. 552,078 filed Feb. 24, 1975; and (v) an epoxy-functional, hydroxy-functional copolymer of monovinyl monomers and as crosslinking agent therefor a monomeric or polymeric anhydride and a hydroxy carboxylic acid -- exemplified in U.S. patent application Ser. No. 394,876 filed Sept. 6, 1973, abandoned in favor of continuation-in-part application Ser. No. 552,077 filed Feb. 24, 1975.

Other thermoset film-formers suitable for use in the powder coating materials used in this invention include, but not by way of limitation, thermosettable systems in which the polymeric component is a polyester, a polyepoxide, or urethanemodified polyesters, polyepoxides and acrylics. As with the acrylics heretofore more specifically described, these may be self-crosslinking polymers or may be a combination of functional polymer and a coreactable monomeric compound which serves as crosslinking agent.

The preferred thermosettable powder paints known to applicants for automotive topcoats consist essentially of an epoxy-functional copolymer of olefinically unsaturated monomers and a crosslinking agent therefor. Such paints may contain flow control agents, catalysts, etc. in very small quantities.

The copolymer referred to in the preceding paragraph has average molecular weight (M.sub.n) in the range of about 1500 to about 15,000 and glass transition temerature in the range of about 40.degree.C. to about 90.degree.C. The epoxy functionality is provided by employing a glycidyl ester of a monoethylenically unsaturated carboxylic acid, e.g., glycidyl acrylate or glycidyl methacrylate, as a constituent monomer of the copolymer. This monomer should comprise about 5 to about 20 weight percent of the total. Additional functionality, e.g., hydroxy functionality or amide functionality, may also be employed by inclusion of a C.sub.5 -C.sub.7 hydroxy acrylate or methacrylate, e.g., ethyl acrylate, ethyl methacrylate, propyl acrylate, or propyl methacrylate, or an alpha-beta olefinically unsaturated amide, e.g., acrylamide or methacrylamide, among the constitutent monomers. When such additional functionality is used, the monomers providing it comprise about 2 to about 10 weight percent of the constituent monomers. The balance of the copolymer, i.e., about 70 to about 93 weight percent of the constituent monomers, are made up of monofunctional, olefinically unsaturated monomers, i.e., the sole functionality being ethylenic unsaturation. These monofunctional, olefinically unsaturated monomers are, at least in major proportion, i.e., in excess of 50 weight percent of the constituent monomers, acrylic monomers. The preferred monofunctional acrylic monomers for this purpose are esters of C.sub.1 -C.sub.8 monohydric alcohols and acrylic or methacrylic acid, e.g., methyl methacrylate, ethyl acrylate, propyl methacrylate, butyl acrylate, butyl methacrylate, hexyl acrylate and 2-ethylhexyl acrylate. In this preferred embodiment, the remainder, if any, aside from the aforementioned epoxy, hydroxy and amide functional monomers which also have olefinic unsaturation functionality used up in the polymerization formation of the copolymer, is preferably made up to C.sub.8 -C.sub.12 monovinyl hydrocarbons, e.g., styrene, vinyl toluene, alpha methyl styrene and tertiary butyl styrene. Other vinyl monomers which are suitable in minor amounts, i.e., between 0 and 30 weight percent of the constituent monomers, include vinyl chloride, acrylonitrile, methacrylonitrile, and vinyl acetate.

The crosslinking agents employed with the aforedescribed copolymer will have functionality that will react with the functionality of the copolymer. Thus, all of the crosslinking agents heretofore mentioned in the recital of powder paint patents and patent applications, e.g., C.sub.4 -C.sub.20 saturated, aliphatic dicarboxylic acids, mixtures of C.sub.4 -C.sub.20 saturated aliphatic dicarboxylic acids and monocarboxylic acids of carbon number in the same range, carboxy terminated copolymers having molecular weight (M.sub.n) in the range of 650 to 3000, monomeric anhydrides preferably anhydrides having a melting point in the range of about 35.degree. to 140.degree.C., e.g., phthalic anhydride, maleic anhydride, cyclohexane-1, 2-dicarboxylic anhydride, succinic anhydride, etc., homopolymers or monomeric anhydrides, and mixtures of such anhydrides and hydroxy acids having a melting point in the range 40.degree. to 150.degree.C., are suitable for use as cross-linking agents for these copolymers. The disclosures of all patents and patent applications recited herein are incorporated herein by reference. In general, these crosslinking agents are employed in amounts such as to provide between about 0.3 and about 1.5, preferably between about 0.8 and about 1.2, functional groups which are reactable with functional groups on the copolymer per functional groups on the copolymer.

In certain embodiments of this invention, it may be desirable to use for the overcoat thermoplastic powder coating materials. These could be one of the known thermoplastic coating materials, epoxy, polyester or acrylic, and still provide a transparent overcoat for the pigmented undercoat derived from a water-based paint. To date, however, thermosetting powders have been preferred for use as automobile finish coats.

The best acrylic, thermoplastic, powder coatings known to applicants are copolymers of alpha-beta olefinically unsaturated monomers. These are made up either solely or predominantly of acrylic monomers, i.e., in excess of 51 weight percent acrylic monomers, the balance is made up of C.sub.8 -C.sub.12 monovinyl hydrocarbons, e.g., styrene, vinyl toluene, alpha methyl styrene and tertiary butyl styrene. The acrylates and methacrylates used in either of these embodiments are preferably esters of a C.sub.1 -C.sub.8 monohydric alcohol and acrylic acid or methacrylic acid or a mixture of acrylic and methacrylic acids. One such copolymer contains about 76 to about 81 mole percent methyl methacrylate 1 to 3 mole percent acrylic acid or methacrylic acid or a mixture of acrylic and methacrylic acids, and 16 to 23 mole percent butyl methacrylate. Also, one may use a modified thermoplastic powder coating wherein a small amount of crosslinking is provided for. Such a coating material is exemplified by U.S. patent application Ser. No. 442,291 filed Feb. 12, 1974 by S. S. Labana et al.

The term "vinyl monomer" as used herein means a monomeric compound having in its molecular structure the functional group ##EQU1## wherein X is a hydrogen atom or a methyl group.

The term "copolymer" as used herein means a polymer formed from two or more different monomers.

"Alpha-beta unsaturation" as used herein includes both the olefinic unsaturation that is between two carbon atoms which are in the alpha and beta positions relative to an activating groups such as a carboxyl group, e.g., the olefinic unsaturation of maleic anhydride, and the olefinic unsaturation between the two carbon atoms which are in the alpha and beta positions with respect to the terminus of an aliphatic carbon-to-carbon chain, e.g., the olefinic unsaturation of acrylic acid, methyl methacrylate or styrene.

This invention will be more fully understood from the following illustrative examples:

An automobile body which, after passing through a seven-stage phosphate treatment to surface condition the metal, has been prime and guide coated to an average depth of about 1.5 mils is finish coated in accordance with the method of this invention.

In this instance, the prime coat is a pigmented, polycarboxylic acid resin paint which electrodeposited upon the metal substrate to an average depth of about 0.8 mil in accordance with the method of U.S. Pat. No. 3,230,162 to Allan E. Gilchrist. After the prime coat has been baked to cure, there is applied over the prime coat a guide coat pigmented to a color quite different from the prime coat. In this instance, the guide coat is a conventional epoxy ester thermoset paint, i.e., a di- or poly-epoxide (Bishenol A -- Epichlorohydrin type) which has been reacted with soya fatty acids and mixed as a major fraction with a minor fraction of a melamineformaldehyde resin which serves as a crosslinking agent. This guide coat is applied by spraying to an average depth of about 0.7 mil. The guide coat is baked to cure and sanded. It is then ready for the finish coat.

1. The Emulsion Polymer (Acrylic Copolymer Latex)

To a flask equipped with a water condenser, agitator and thermometer are charged 770 parts by weight deionized water, 1.9 parts by weight ammonium persulfate and 22 parts by weight of Triton X-200. This charge is then heated to 95.degree.C.

An aqueous emulsion of acrylic monomers is formed by mixing the styrene, butyl methacrylate, propyl methacrylate, and acrylic acid with the n-octyl mercaptan, 52 parts by weight Triton X-305, 22 parts by weight of Triton X-200, 648 parts by weight of deionized water and 5 parts by weight of ammonium persulfate.

The emulsion of acrylic monomers is added dropwise to the heated charge over a 3 hour period during which the charge is maintained at 95.degree.C. The reaction mixture is held under continued agitation for 2 hours at 95.degree.C. after addition of the monomers is complete. The reaction mixture is then allowed to cool to 35.degree.C. When the temperature of the reaction mixture reaches 35.degree.C., there is added a mixture of the dimethyl ethanol amine and 49 parts by weight deionized water. The resulting product is a stable, milky white liquid dispersion with a nonvolatile content of 44-45%, a viscosity of 50 centipoise, and a pH of 5.

2. The solution Polymer (water soluble acrylic copolymer)

Into a flask equipped with a water condenser, agitator and thermometer is charged 488 parts by weight of diethylene glycol monobutyl ether and this is heated to 150.degree. to 155.degree.C. The styrene, butyl methacrylate, 2-ethylhexyl acrylate, hydroxypropyl methacrylate, acrylic acid, 45 parts by weight 5-butyl perbenzoate and 110 parts by weight of ethylene glycol monobutyl ether are mixed and added dropwise to the flask over a 3 hour period while the temperature of the reaction mixture is maintained at 150.degree.-155.degree.C. The reaction mixture is continuously agitated for 1 hour after monomer addition is complete. At the end of this hour, there are added three parts by weight of t-butyl perbenzoate and 13 parts by weight of diethylene glycol monobutyl ether. The reaction mixture is maintained under agitation and a temperature of 150.degree. to 155.degree.C. for 1 hour. It is then allowed to cool to 100.degree.C. at which time 111 parts by weight of dimethylethanol amine and 389 parts by weight of deionized water are added to the flask. The resulting product is a clear amber polymeric material with a nonvolatile content of 60% and a G-H Bubble Viscosity of 2-5 to 2-6.

To a flask equipped with an agitator, thermometer, water conderser and monomer addition funnel is charged 1520 parts by weight of toluene. The toluene is heated to reflux at about 110.degree.C. The methyl methacrylate, butyl methacrylate, glycidyl methacrylate, t-butyl peroctoate and 300 parts by weight toluene are mixed and added dropwise to the refluxing toluene through the monomer addition tunnel over a 3 hour period while agitation and reflux are maintained. Reflux is then continued for an additional 3 hours. The resulting product is a clear resinous material with a nonvolatile content of 50% and a G-H Bubble Viscosity of E. The product is devolatized by heat exchange and separated to recover the copolymer.

A "silver" colored, metal-pigmented, basecoat is prepared by mixing the following materials in the order of listing under continuous agitation:

This water-based material has a total solids content of about 45% and the pigment concentration by weight is about 6.4% based on the weight of solids.

The above ingredients are intimately mixed and this mixture is extruded at 100.degree.C. from a kneading extruder. The solid thus obtained is pulverized and sieved through a 200 mesh screen.

A basecoat of the water-based coating material of C is diluted with deionized water to a spraying viscosity of 25 seconds number 4 Ford Cup and applied to the substrate to an average depth of about 0.8 mil by electrostatic spray. This basecoat is heat cured by baking at 225.degree.F. (metal temperature) for 10 minutes.

After the substrate has cooled to room temperature, powder coating material from D is applied over the basecoat to an average depth of about 1.5 mils by electrostatic spray. This powder coating material is heat cured by baking at 350.degree.F. (metal temperature) for 25 minutes.

The resultant layered coating is smooth. It exhibits exceptionally high gloss and the appearance of having unusual depth.

The procedure of Example 1 is repeated except for the difference that the water-based coating material is prepared from the following materials:

This dark blue water-based material has a total solids content of about 41% and the total pigment concentration by weight is about 16% based on the weight of solids. As in the preceding example, this material is diluted to spraying viscosity prior to application to a substrate.

The resultant layered coating is smooth. It exhibits exceptionally high gloss and the appearance of having unusual depth.

The procedure of Example 1 is repeated except for the difference that the water-based coating material is prepared from the following materials:

This white water-based material has a total solids content of about 55% and the total pigment concentration is about 60% based on weight of solids. As in the preceding examples, this material is diluted to a spraying viscosity prior to application to a substrate.

The resultant layered coating is smooth. It exhibits exceptionally high gloss and has the appearance of having unusual depth.

The procedure of Example 1 is repeated except for the difference that the water-based coating material is prepared from the following materials:

This pastel blue, water-based material has a total solids content of about 40% and the total pigment concentration is about 20% based on weight of solids. As in the preceding examples, this material is diluted to a spraying viscosity prior to application to a substrate.

The resultant layered coating is smooth. It exhibits exceptionally high gloss and has the appearance of having unusual depth.

The term "acrylic monomer" as used herein means a compound selected from the group consisting of glycidyl acrylate, glycidyl methacrylate, acrylic acid, hydroxyethyl acrylate, hydroxypropyl acrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, esters of acrylic acid and a C.sub.1 -C.sub.8 monohydric alcohol, and esters of methacrylic acid and a C.sub.1 -C.sub.8 monohydric alcohol.

The term "acrylic copolymer" means a copolymer of monoethylenically unsaturated compounds at least a major portion of which are acrylic monomers.

The term "major portion" means in excess of 50 weight percent of the entity referred to.

The term "minor portion" means less than 50 weight percent of the entity referred to.

Many modifications of the foregoing examples will be apparent to those skilled in the art in view of this specification. It is intended that all such modifications which fall within the scope of this invention as defined in the claims shall be considered to be a part of this invention.

Any and all disclosures appearing in the claims and not specifically appearing in the same words in the body of this specification are herewith incorporated in the body of this specification by reference.