Patent Application
20050228124
The present invention relates generally to coating compositions and substrates coated with such compositions, as well as to a method for repairing such coated substrates.
Typically, automotive coatings processes include the application of several different coating layers onto an automobile body. These coating layers can include for example, an electrodeposition primer layer, a sealer layer, a basecoat layer, and a clearcoat layer. The coating compositions used to form each of these coating layers may be waterborne or solventborne compositions or in solid particulate form. Due to recent government VOC regulations, one or more of these coating layers typically is formed from waterborne coating compositions. Each of these original layers may require a thermal bake at a relatively high temperature to achieve complete cure of the coating. For example, an original clearcoat layer may be cured at a temperature within the range of 250° F. to 300° F. (121° C. to 149° C.), in order to achieve complete cure of this clearcoat layer, as well as full cure of any of the previously applied coating layers, e.g. a basecoat layer.
In certain circumstances, after the application and cure of all original coating layers is complete, there may be a flaw or defect present in one of the layers, such as a crater or a dirt particle, that requires repair of that particular area. This repair process typically involves removing the defect, such as by sanding, followed by re-application of one of more of the coating layers. Often times, a basecoat layer and a clearcoat layer are reapplied after the defect is removed. The bake temperature of one or more of the coating layers applied during this repair process may be lower than that used to cure the original layer. For example, a repair clearcoat layer may be capable of curing at temperatures, such as within the range of 160° F. to 180° F. (71° C. to 82° C.), in order to achieve complete cure.
One possible drawback to this repair process can be the poor water resistance properties of the repair coating layers resulting in coating defects e.g. blistering. Such blistering can result in a loss of adhesion between the coating layers, such as between the basecoat and clearcoat layers.
Therefore, it would be desirable to provide a coating composition, which is useful as both an original and a repair finish, contains low or no VOC or HAP (i.e. Hazardous Air Pollutant) materials, and provides improved water resistance properties demonstrated by improved blistering resistance and improved adhesion between the coating layers.
In one embodment, the present invention is directed to a coating composition comprising:
The present invention is also directed to a thermosetting composition comprising:
Further, the present invention is directed to a method of repairing a defect in a multi-layer coating comprising applying the coating composition of the present invention.
Other than in the operating examples, or where otherwise indicated, all numbers expressing quantities of ingredients, reaction conditions and so forth used in the specification and claims are to be understood as being modified in all instances by the term “about.” Accordingly, unless indicated to the contrary, the numerical parameters set forth in the following specification and attached claims are approximations that may vary depending upon the desired properties sought to be obtained by the present invention. At the very least, and not as an attempt to limit the application of the doctrine of equivalents to the scope of the claims, each numerical parameter should at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques.
Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, the numerical values set forth in the specific examples are reported as precisely as possible. Any numerical values, however, inherently contain certain errors necessarily resulting from the standard deviation found in their respective testing measurements.
Also, it should be understood that any numerical range recited herein is intended to include all sub-ranges subsumed therein. For example, a range of “1 to 10” is intended to include all sub-ranges between and including the recited minimum value of 1 and the recited maximum value of 10, that is, having a minimum value equal to or greater than 1 and a maximum value of equal to or less than 10. Because the disclosed numerical ranges are continuous, they include every value between the minimum and maximum values. Unless expressly indicated otherwise, the various numerical ranges specified in this application are approximations.
It should also be understood that, in this application, use of the singular includes the plural unless specifically stated otherwise.
As used herein, by “thermosetting composition” is meant one which “sets” irreversibly upon curing or crosslinking, wherein the polymer chains of the polymeric components are joined together by covalent bonds. This property is usually associated with a crosslinking reaction of the composition constituents often induced, for example, by heat or radiation. Hawley, Gessner G., The Condensed Chemical Dictionary, Ninth Edition., page 856; Surface Coatings, Vol. 2, Oil and Colour Chemists' Association, Australia, TAFE Educational Books (1974). Curing or crosslinking reactions also may be carried out under ambient conditions. Once cured or crosslinked, a thermosetting composition will not melt upon the application of heat and is insoluble in solvents. By contrast, a “thermoplastic composition” comprises polymeric components which are not joined by covalent bonds and thereby can undergo liquid flow upon heating and are soluble in solvents. Saunders, K. J., Organic Polymer Chemistry, pp. 41-42, Chapman and Hall, London (1973).
As used herein, the term “polymer” is meant to encompass prepolymers, oligomers, and includes without limitation both homopolymers and copolymers. Also, as used herein, the term “reactive” refers to a functional group that forms a covalent bond with another functional group under conditions sufficient to cure the composition. As used herein, the term “capable of reacting” with regard to a functional group refers to the capability of a functional group to form a covalent bond with another functional group.
As used herein, the term “polyisocyanate”, unless otherwise indicated, is intended to include blocked (or capped) isocyanates as well as unblocked (poly)isocyanates.
As used herein, the phrase components “are different from each other” refers to components which do not have the same chemical structure as other components in the composition.
As used herein, the term “glass transition temperature” refers to the temperature at which an amorphous material, such as glass or a high polymer, changes from a brittle vitreous state to a plastic state. For purposes of this invention, the glass transition temperature is theoretically calculated according to the equation described on page 29 in The Chemistry of Organic Film Former by D. H. Solomon, Wiley and Sons, 1967.
As used herein, the term “cure” as used in connection with a composition, e.g., “composition when cured,” shall mean that any crosslinkable components of the composition are at least partially crosslinked. In certain embodiments of the present invention, the crosslink density of the crosslinkable components, i.e., the degree of crosslinking, ranges from 5% to 100% of complete crosslinking.
As indicated, the present invention is directed to a coating composition comprising:
By “alkylol” is meant a hydrocarbon radical that contains one or more hydroxyl groups. By “alkylamino” is meant a hydrocarbon radical that contains one or more amine groups. As used herein, “(meth)acrylic acid” and like terms are intended to include acrylic acid and/or methacrylic acid. As used herein, when referring to the latex emulsion that includes crosslinked polymeric microparticles dispersed in an aqueous continuous phase, a “suitable” material is a material that may be used in or in preparing the latex emulsion that includes crosslinked polymeric microparticles dispersed in an aqueous continuous phase, so long as the material does not substantially affect the stability of the latex emulsion or the polymerization process.
Crosslinking monomers suitable for use as the crosslinking monomer (a) of latex emulsion (I) can include any monomer having two or more sites of reactive unsaturation, or any monomer that has a functional group capable of reacting to form crosslinks after polymerization. As used herein, functional groups that are capable of reacting to form crosslinks after polymerization refer to functional groups on a first polymer molecule that may react under appropriate conditions to form covalent bonds with functional groups on a second polymer molecule to form a crosslinked polymer. Functional groups that may react to form crosslinks include, but are not limited to N-alkoxymethyl amides, N-methylolamides, lactones, lactams, mercaptans, hydroxyls, epoxides and the like. Examples of such monomers include, but are not limited to, N-alkoxymethyl(meth)acrylamides, γ-(meth)acryloxytrialkoxysilane, N-methylol(meth)acrylamide, N-butoxymethyl(meth)acrylamide, (meth)acryliclactones, N-substituted (meth)acrylamide lactones, (meth)acryliclactams, and N-substituted (meth)acrylamide lactams and glycidyl (meth)acrylate.
As mentioned above, in one embodiment of the present invention, the crosslinking monomer can have two sites of reactive unsaturation. In a further embodiment, the crosslinking monomer may comprise ethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, tetraethylene glycol di(meth)acrylate, 1,3-butylene glycol di(meth)acrylate, trimethylolpropane tri(meth)acrylate, 1,4-butanediol di(meth)acrylate, neopentyl glycol di(meth)acrylate, 1,6-hexanediol di(meth)acrylate, pentaerythritol di(meth)acrylate, pentaerythritol tri(meth)acrylate, pentaerythritol tetra(meth)acrylate, glycerol di(meth)acrylate, glycerol allyloxy di(meth)acrylate, 1,1,1-tris(hydroxymethyl)ethane di(meth)acrylate, 1,1,1-tris(hydroxymethyl)ethane tri(meth)acrylate, 1,1,1-tris(hydroxymethyl)propane di(meth)acrylate, 1,1,1-tris(hydroxymethyl)propane tri(meth)acrylate, triallyl cyanurate, triallyl isocyanurate, triallyl trimellitate, diallyl phthalate, diallyl terephthalate, divinyl benzene, methylol (meth)acrylamide, triallylamine, and/or methylenebis (meth) acrylamide.
The crosslinking monomer (a) comprises at least 15 weight percent, or at least 20 weight percent, or at least 22.5 weight percent, or at least 25 weight percent of the monomer mix used to prepare the polymeric microparticles. Also, the crosslinking monomer comprises not more than 45 weight percent, or not more than 40 weight percent, or not more than 35 weight percent, or not more than 30 weight percent of the monomer mix used to prepare the polymeric microparticles. The level of the crosslinking monomer (a) used is determined by the desired properties that are to be incorporated into the resulting microparticle. The crosslinking monomer may be present in the monomer mix at any value or in any combination of the recited ranges inclusive of those values stated above.
Any polymerizable ethylenically unsaturated monomers having hydrophilic functional groups can be used as the monomer (b). In a particular embodiment of the present invention, polymerizable ethylenically unsaturated monomers having hydrophilic functional groups described by structures I and/or II above may be used as the monomer (b) provided that the monomer can be polymerized in a latex emulsion polymerization system and does not substantially affect the stability of the latex emulsion or the polymerization process.
Polymerizable ethylenically unsaturated monomers having hydrophilic functional groups suitable for use as the monomer (b) in the preparation of the polymeric microparticles of the present invention include, but are not limited to (meth)acrylamide, hydroxyethyl(meth)acrylate, hydroxypropyl(meth)acrylate, dimethylaminoethyl (meth)acrylate, allyl glycerol ether, methallyl glycerol ether and/or polyethyleneoxide allyl ether.
In an embodiment of the present invention, a particular advantage of the present crosslinked polymeric microparticles is that they do not require the presence of an alkaline material to swell the microparticles, thereby providing desired rheological properties. This eliminates the additional processing step of adding an alkaline material to promote particle swelling and renders the resulting rheological properties more predictable.
In another embodiment of the present invention, the polymerizable ethylenically unsaturated monomers having hydrophilic functional groups (b) include monomers described by structure (I) above.
In a further embodiment of the present invention, the polymerizable ethylenically unsaturated monomers having hydrophilic functional groups (b) include monomers described by structure (II) above.
The polymerizable ethylenically unsaturated monomer having hydrophilic functional groups (b) comprises at least 2 weight percent, or greater than 2 weight percent, or at least 5 weight percent, or greater than 5 weight percent, or at least 7 weight percent, or at least 8 weight percent of the monomer mix used to prepare the polymeric microparticles. The polymerizable ethylenically unsaturated monomer having hydrophilic functional groups comprises not more than 35 weight percent, or not more than 30 weight percent, or not more than 20 weight percent, or not more than 15 weight percent of the monomer mix used to prepare the polymeric microparticles. The level of the polymerizable ethylenically unsaturated monomer having hydrophilic functional groups used is determined by the properties that are to be incorporated into the resulting microparticle. The level of the polymerizable ethylenically unsaturated monomer having hydrophilic functional groups present in the monomer mix can range between any combination of the recited values inclusive of the recited values.
Polymerizable ethylenically unsaturated monomers suitable for use as the monomer (c) which, optionally, make up the remainder of the monomer mix, and which are different from the crosslinking monomer (a) and the monomer having hydrophilic functional groups (b), may be included in the polymeric microparticles of the present invention. Any suitable polymerizable ethylenically unsaturated monomer may be used, provided that it is capable of being polymerized in a latex emulsion polymerization system and does not substantially affect the stability of the latex emulsion or the polymerization process. Suitable polymerizable ethylenically unsaturated monomers include, but are not limited to, methyl(meth)acrylate, ethyl(meth)acrylate, propyl(meth)acrylate, N-butyl(meth)acrylate, t-butyl(meth)acrylate, 2-ethylhexyl(meth)acrylate, isobornyl (meth)acrylate, dimethylaminoethyl (meth)acrylate, styrene, (meth)acrylonitrile, lauryl (meth)acrylate, cyclohexyl (meth)acrylate, and/or 3,3,5-trimethylcyclohexyl (meth)acrylate.
The polymerizable ethylenically unsaturated monomer (c) may comprise at least 20 weight percent, or at least 30 weight percent, or at least 40 weight percent, or at least 50 weight percent of the monomer mix used to prepare the polymeric microparticles. The polymerizable ethylenically unsaturated monomers may comprise not more than 80 weight percent, or not more than 75 weight percent, or not more than 70.5 weight percent, or not more than 67 weight percent of the monomer mix used to prepare the polymeric microparticles. The level of the polymerizable ethylenically unsaturated monomer (c) which can be used is determined by the properties that are to be incorporated into the resulting microparticle. The level of the polymerizable ethylenically unsaturated monomer (c) present in the monomer mix may range between any combination of the recited values inclusive of the recited values.
In a particular embodiment of the present invention, the crosslinking monomer (a) comprises glycol di(meth)acrylates and/or glycol tri(meth)acrylates; the polymerizable ethylenically unsaturated monomer having hydrophilic functional groups (b) comprises (meth)acrylamide; and the polymerizable ethylenically unsaturated monomer (c) comprises an alkyl(meth)acrylate.
The latex emulsion (I) of crosslinked polymeric microparticles dispersed in an aqueous continuous phase is prepared by latex emulsion polymerization of (a), (b) and optionally, (c) as described above. In many cases, the monomer mixture of (a), (b) and (c) will readily disperse into stable monomer droplets and micelles as would be expected in a Smith-Ewart type of process. In such cases, no monomeric or polymeric emulsifiers and/or protective colloids are added to the latex emulsion, and the latex emulsion is substantially free of polymeric emulsifiers and/or protective colloids. It should be understood, however, that in some cases, a surface active agent may be added to the aqueous continuous phase to stabilize, or prevent coagulation or agglomeration of the monomer droplets, especially during polymerization.
A surface active agent can be present in the latex emulsion of the present invention at any level that stabilizes the emulsion. The surface active agent may be present at least 0.001 percent by weight, or at least 0.005 percent by weight, or at least 0.01 percent by weight, or at least 0.05 percent by weight based on the total weight of the latex emulsion. The surface active agent may be present at not more than 10 percent by weight, or not more than 7.5 percent by weight, or not more than 5 percent by weight, or not more than 3 percent by weight based on the total weight of the latex emulsion. The level of the surface active agent used is determined by the amount required to stabilize the latex emulsion. The surface active agent may be present in the latex emulsion at any level or in any range of levels inclusive of those stated above.
The surface active agent may be an anionic, cationic, or nonionic surfactant or dispersing agent, or compatible mixtures thereof, such as a mixture of an anionic and a nonionic surfactant. Such surfactants and dispersing agents are well known in the art, any of a variety of which may be suitable.
A free radical initiator typically is used in the latex emulsion polymerization process. Any suitable free radical initiator as are well known in the art may be used. Suitable free radical initiators include, but are not limited to thermal initiators, photoinitiators and oxidation-reduction initiators, all of which may be otherwise categorized as being water-soluble initiators or non-water-soluble initiators.
In one embodiment of the present invention, the average particle size of the polymeric microparticles may be at least 0.001 microns, or at least 0.005 microns, or at least 0.01, or at least 0.02 microns. The average particle size of the polymeric microparticles typically is not more than 1 micron, or not more than 0.9 microns or not more than 0.8 microns. The average particle size of the polymeric microparticles may be any value or in any range of values inclusive of those stated above
In another embodiment of the present invention, the latex emulsion of crosslinked polymeric microparticles dispersed in an aqueous continuous phase is prepared by a seeded latex emulsion polymerization process. Such a seeded latex emulsion polymerization process includes:
In certain embodiments of the present invention, the coating composition also comprises a polymer (II) comprising (i) a C8 to C20 alkyl ester of (meth)acrylic acid; (ii) a polymerizable ethylenically unsaturated monomer comprising a polar functional group; and (iii) optionally, a polymerizable ethylenically unsaturated monomer, wherein (i), (ii) and (iii) are different from each other; and wherein the polymer has a glass transition temperature of no more than −10° C.
The C8 to C20 alkyl ester of (meth)acrylic acid (i) of polymer (II) can comprise, for example, octyl (meth)acrylate, lauryl (meth)acrylate, cetyl (meth)acrylate, stearyl (meth)acrylate, behenyl (meth)acrylate, and/or eicosyl (meth)acrylate. In a particular embodiment, the C8 to C20 alkyl ester of (meth)acrylic acid comprises lauryl (meth)acrylate.
The C8 to C20 alkyl ester of (meth)acrylic acid used to prepare polymer (II) may be present at an amount of at least 50 weight percent and not more than 99.9 weight percent based on total weight of monomer solids.
In an embodiment of the present invention, the C8 to C20 alkyl ester of (meth)acrylic acid may comprise at least 50 weight percent, or at least 70 weight percent, or at least 90 weight percent based on the total weight of monomer solids used to prepare polymer (II). The C8 to C20 alkyl ester of (meth)acrylic acid may comprise not more than 99.9 weight percent, or not more than 95 weight percent, or not more than 85 weight percent based on the total weight of monomer solids used to prepare polymer (II). The level of the C8 to C20 alkyl ester of (meth)acrylic acid which can be used is determined by the properties that are to be incorporated into the resulting polymer (II). The level of the C8 to C20 alkyl ester of (meth)acrylic acid present in the monomer mix may range between any combination of the recited values inclusive of the recited values.
In addition to the C8 to C20 alkyl ester of (meth)acrylic acid as described above, polymer (II) comprises a polymerizable ethylenically unsaturated monomer comprising a polar functional group. As used herein, the term “polar functional group” refers to a functional group having a high dielectric constant and strong polarity. Any suitable polymerizable ethylenically unsaturated monomer having a polar functional group can be used.
The polar functional group can comprise, for example, carboxyl groups, hydroxyl groups, and/or amine groups. In an embodiment of the present invention, the polar functional group comprises a carboxyl group. In a particular embodiment, the ethylenically unsaturated monomer (ii) of polymer (II) comprises (meth)acrylic acid.
In certain embodiments, the ethylenically unsaturated monomer (ii) used to prepare polymer (II) is present at an amount of at least 0.1 weight percent and not more than 5 weight percent based on total weight of monomer solids.
In a particular embodiment of the present invention, the ethylenically unsaturated monomer (ii) may comprise at least 0.1 weight percent, or at least 1 weight percent, or at least 4 weight percent based on the total weight of monomer solids used to prepare polymer (II). The ethylenically unsaturated monomer (ii) also may comprise not more than 5 weight percent, or not more than 3 weight percent, or not more than 2 weight percent based on the total weight of monomer solids used to prepare polymer (II). The level of the ethylenically unsaturated monomer (ii) which can be used is determined by the properties that are to be incorporated into the resulting polymer (II). The level of the ethylenically unsaturated monomer (ii) present in the monomer mix may range between any combination of the recited values inclusive of the recited values.
In other embodiments, the polymer (II) optionally comprises a polymerizable ethylenically unsaturated monomer, wherein (i), (ii) and (iii) are different from each other. As previously discussed, any suitable polymerizable ethylenically unsaturated monomer may be used, provided that the polymer (II) has a glass transition temperature of no more than −10° C. Further, if present, these polymerizable ethylenically unsaturated monomers may be present in any suitable amount provided that the glass transition temperature of polymer (II) does not exceed −10° C. In a particular embodiment of the present invention, polymer (II) has a glass transition temperature of no more than −30° C.
In certain embodiments, polymer (II) is present in the coating composition at an amount of at least 2 weight percent, or at least 5 weight percent resin solids based on the total weight of resin solids of the coating composition. The polymer (II) may be present in the coating composition at an amount of not more than 30 weight percent, or not more than 15 weight percent resin based on the total weight of resin solids of the coating composition. The level of polymer (II) which can be used is determined by the properties that are to be incorporated into the resulting coating composition. The level of the polymer (II) present in the coating composition may range between any combination of the recited values inclusive of the recited values.
In addition to the dispersions of crosslinked microparticles and polymer described above, certain embodiments of the coating compositions of the present invention further comprise an aqueous polyurethane dispersion, comprising polyurethane-acrylate particles dispersed in an aqueous medium. Suitable polyurethane-acrylate particles can comprise the reaction product obtained by polymerizing the components of a pre-emulsion formed from:
The active hydrogen-containing polyurethane acrylate prepolymer (A) in the polyurethane-acrylate particles is present in an amount of at least 20 percent by weight, or at least 25 percent by weight, or at least 30 percent by weight, or at least 35 percent by weight or at least 40 percent by weight of the solids of the polyurethane-acrylate particles. Further, the active hydrogen-containing polyurethane acrylate prepolymer (A) may be present in an amount of up to 80 percent by weight, or up to 75 percent by weight, or up to 70 percent by weight, or up to 65 percent by weight or up to 60 percent by weight of the solids of the polyurethane-acrylate particles. The level of active hydrogen-containing polyurethane acrylate prepolymer (A) in the polyurethane-acrylate particles can be any value or range between any combination of these values inclusive of the recited values.
The hydrophobic polymerizable ethylenically unsaturated monomers (B) in the polyurethane-acrylate particles are present in an amount of at least 20 percent by weight, or at least 25 percent by weight, or at least 30 percent by weight, or at least 35 percent by weight or at least 40 percent by weight of the solids of the polyurethane-acrylate particles. Further, the hydrophobic polymerizable ethylenically unsaturated monomers (B) may be present in an amount of up to 80 percent by weight, or up to 75 percent by weight, or up to 70 percent by weight, or up to 65 percent by weight or up to 60 percent by weight of the solids of the polyurethane-acrylate particles. The level of hydrophobic polymerizable ethylenically unsaturated monomers (B) in the polyurethane-acrylate particles can be any value or range between any combination of these values inclusive of the recited values.
The crosslinking monomer (C) in the polyurethane-acrylate particles is present in an amount of at least 1 percent by weight, or at least 2 percent by weight, or at least 3 percent by weight, or at least 4 percent by weight or at least 5 percent by weight of the solids of the polyurethane-acrylate particles. Further, the crosslinking monomer (C) may be present in an amount of up to 20 percent by weight, or up to 17.5 percent by weight, or up to 15 percent by weight, or up to 12.5 percent by weight or up to 10 percent by weight of the solids of the polyurethane-acrylate particles. The level of crosslinking monomer (C) in the polyurethane-acrylate particles can be any value or range between any combination of these values inclusive of the recited values.
The value of (A)+(B)+(C) can be 100%, but will be less than 100% when other components as are known to those skilled in the art are also included in the polyurethane-acrylate particles.
The polyol of (i) may be one or more polyols selected from a polyether polyol, a polyester polyol, an acrylic polyol, or a mixture thereof. In an embodiment of the present invention, the polyol is one or more polyether polyols described by structure VII:
where R1 is H or C1-C5 alkyl including mixed substituents for example, n is from 1 to 200 and m is from 1 to 5. Examples of suitable polyetherpolyols that may be used include, but are not limited to, poly(oxytetramethylene) glycols; poly(oxyethylene) glycols; poly(oxy-1,2-propylene) glycols; 1,6-hexanediol; poly(tetrahydrofuran); trimethylolpropane; sorbitol; pentaerythritol; the reaction products of ethylene glycol with a mixture of 1,2-propylene oxide and ethylene oxide; the reaction products obtained by the polymerization of ethylene oxide, propylene oxide and tetrahydrofuran and mixtures of polyols can be used as polyol (i).
In another embodiment of the present invention, the polymerizable ethylenically unsaturated monomer comprising a hydroxyl group of (ii) may be one or more monomers described by structure VIII:
The polyisocyanate (iv) may be an aliphatic polyisocyanate, an aromatic polyisocyanate, or mixtures thereof. Examples of polyisocyanates that may be used as polyisocyanate (iv) include, but are not limited to, isophorone diisocyanate, 4,4′-diphenylmethane diisocyanate, 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, tolylene diisocyanate, 1,4-tetramethylene diisocyanate, 1,6-hexamethylene diisocyanate, 1,4-cyclohexyl diisocyanate, alpha, alpha-xylylene diisocyanate, 4,4′-methylene-bis(cyclohexyl isocyanate), 1,2,4-benzene triisocyanate, and polymethylene polyphenyl isocyanate. Mixtures of such polyisocyanates also can be used.
The hydrophobic polymerizable ethylenically unsaturated monomers (B) may be any suitable hydrophobic polymerizable ethylenically unsaturated monomers. As used herein, by “hydrophobic monomer”, is meant a monomer that is “substantially insoluble” in water. By “substantially insoluble” in water what is meant is that a monomer has a solubility in distilled water of less than 6 g/100 g at 25° C. determined by placing 3 g of water and 0.18 g of monomer in a test tube at 25° C. and shaking the test tube. On visual examination, if two distinct layers form, the monomer is considered to be hydrophobic. If a cloudy solution forms, the turbidity of the mixture is measured using a turbidimeter or nephelometer (for example, Hach Model 2100 AN, Hach Company, Loveland, Colo.). A reading of greater than 10 nephelometric turbidity units (NTU) indicates that the monomer is considered to be hydrophobic. Examples of suitable hydrophobic monomers include, but are not limited to, methyl(meth)acrylate, ethyl(meth)acrylate, propyl(meth)acrylate, N-butyl(meth)acrylate, t-butyl(meth)acrylate, 2-ethylhexyl(meth)acrylate, isobornyl (meth)acrylate, glycidyl (meth)acrylate, N-butoxy methyl (meth)acrylamide, styrene, (meth)acrylonitrile, lauryl (meth)acrylate, cyclohexyl (meth)acrylate, and 3,3,5-trimethylcyclohexyl (meth)acrylate. Mixtures of such hydrophobic monomers also can be used.
The crosslinking monomer (C) has two or more sites of polymerizable ethylenic unsaturation. Any suitable crosslinking monomer may be used to prepare the polyurethane-acrylate particles of the present aqueous polyurethane dispersion. For example, suitable crosslinking monomers include, but are not limited to, ethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, tetraethylene glycol di(meth)acrylate, 1,3-butylene glycol di(meth)acrylate, trimethylolpropane tri(meth)acrylate, 1,4-butanediol di(meth)acrylate, neopentyl glycol di(meth)acrylate, 1,6-hexanediol di(meth)acrylate, pentaerythritol di(meth)acrylate, pentaerythritol tri(meth)acrylate, pentaerythritol tetra(meth)acrylate, glycerol di(meth)acrylate, glycerol allyloxy di(meth)acrylate, 1,1,1-tris(hydroxymethyl)ethane di(meth)acrylate, 1,1,1-tris(hydroxymethyl)ethane tri(meth)acrylate, 1,1,1-tris(hydroxymethyl)propane di(meth)acrylate, 1,1,1-tris(hydroxymethyl)propane tri(meth)acrylate, triallyl cyanurate, triallyl isocyanurate, triallyl trimellitate, diallyl phthalate, diallyl terephthalate, divinyl benzene, methylol (meth)acrylamide, triallylamine, and methylenebis (meth) acrylamide. Mixtures of such crosslinking monomers also can be used.
As those skilled in the art of polymer science can appreciate, the incorporation of the various components of the active hydrogen-containing polyurethane acrylate prepolymer can occur in a statistically predictable manner. In preparing the active hydrogen-containing polyurethane acrylate prepolymer, an excess of hydroxyl functionality from compounds (i), (ii) and (iii) is present relative to isocyanate functionality from the polyisocyanate of (iv). This results in the formation of polymer molecules having end groups having hydroxyl functionality from (i) or (iii), and/or an end group containing a polymerizable ethylenically unsaturated group from (ii). The distribution and amount of the carboxylic group of the compound of (iii) on the resulting polyurethane acrylate prepolymer determines the hydrophobic-hydrophilic balance of the prepolymer.
A statistical distribution of three types of prepolymer molecules can result from the preparation of the polyurethane acrylate prepolymer. One type of prepolymer that can be formed is a first surfactant-like prepolymer, which has a hydroxyl and/or carboxylic functional group at one end of the prepolymer and a polymerizable ethylenically unsaturated group at the opposite end of the prepolymer. Additionally, a second surfactant-like prepolymer can result, which has a hydroxyl and/or carboxylic functional group at both ends of the prepolymer. Another type of prepolymer that can result is a hydrophobic prepolymer that does not contain any carboxylic acid groups, which has polymerizable ethylenically unsaturated groups at both ends of the prepolymer molecule.
It should be understood that for the purposes of the present invention, the reaction product (A) is considered to be a mixture of the aforementioned three types of prepolymers as well as any unreacted portions of components (i), (ii), (iii) and (iv) and any reaction by-products.
During the preparation of the aqueous polyurethane dispersion, the hydrophobic polymerizable ethylenically unsaturated monomers (B) and the crosslinking monomer (C) are added to the active hydrogen-containing polyurethane acrylate prepolymer (A) and passed through a high shear fluid processor for deagglomeration and dispersion of uniform submicron particles, resulting in a stable emulsion or dispersion. Suitable processors include, but are not limited to those sold under the trade name Microfluidizer®, available from the Microfluidics™ division of MFIC Corporation, Newton, Mass. The submicron particles that are formed contain the monomers (B) and (C) and the various prepolymers (A) as described above.
A further embodiment of the present invention is directed to a thermosetting composition comprising:
The thermosetting composition may be in any suitable physical form, for example in liquid form, such as a solution, dispersion or emulsions, and in solid form, for example, a dry, particulate powder. In a particular embodiment of the present invention, the thermosetting composition is a coating composition.
In the thermosetting composition of the present invention, the first reactant (I) can include any suitable reactive functional groups. For example, the functional groups can comprise one or more of epoxy, carboxylic acid, hydroxy, amide, oxazoline, aceto acetate, isocyanate, methylol, amino, methylol ether, and carbamate. Likewise, the functional groups of the curing agent (II) can include any suitable reactive functional groups, provided such groups are reactive with those of the first reactant (I). For example, the functional groups of the curing agent (II) can comprise one or more of epoxy, carboxylic acid, hydroxy, isocyanate, capped isocyanate, amine, methylol, methylol ether, and beta-hydroxyalkylamide. Generally, the functional groups of (I) and (II) will be different from and reactive with each other.
Examples of the first reactant (I) which are suitable for use in the thermosetting compositions of the present invention include, but are not limited to, film-forming polymers with at least one reactive functional group such as those discussed immediately above with respect to the first reactant (I). Such polymers can include any of a variety of functional polymers known in the art. For example, suitable hydroxyl group-containing polymers can include acrylic polyols, polyester polyols, polyurethane polyols, polyether polyols, and mixtures thereof. Examples of other suitable film-forming polymers with at least one functional group include those described in U.S. application Ser. No. 10/126,903 filed Apr. 19, 2002, entitled “Coating Compositions Containing Polyurethane Dispersions And Highly Crosslinked Polymer Particles,” which is hereby incorporated by reference. When desired, appropriate mixtures of film-forming polymers may be used as the first reactant (I).
As aforementioned, in addition to the first reactant (I), the latex emulsion of crosslinked polymeric microparticles (III), and the polymer (IV), the thermosetting composition of the present invention further includes a curing agent (II) having functional groups reactive with the functional groups of the first reactant (I).
Dependent upon the reactive functional groups of the first reactant (I), the curing agent (II) can be selected from an aminoplast resin, a polyisocyanate, a blocked isocyanate, a polyepoxide, a polyacid, an anhydride, an amine, a polyol, a carboxylic acid, an hydroxy containing compound, a methylol containing compound, a methylol ether containing compound, a beta-hydroxyalkylamide, and mixtures of any of the foregoing.
Examples of curing agents suitable for use in the compositions of the present invention are described in U.S. application Ser. No. 10/126,903, filed Apr. 19, 2002, entitled “Coating Compositions Containing Polyurethane Dispersions And Highly Crosslinked Polymer Particles,” which is hereby incorporated by reference.
In certain embodiments of the present invention, the latex emulsion of crosslinked microparticles (III) has functional groups reactive with the functional groups of the curing agent (II). The latex emulsion (III) can include any suitable reactive functional groups, provided such groups are reactive with those of the curing agent (II).
When desired, appropriate mixtures of curing agents may be used. It should be mentioned that the thermosetting compositions can be formulated as a one-component composition where a curing agent such as an aminoplast resin and/or a blocked isocyanate compound such as those described above is admixed with other composition components. The one-component composition can be storage stable as formulated. Alternatively, the thermosetting composition can be formulated as a two-component composition where a polyisocyanate curing agent such as those described above can be added to a pre-formed admixture of the other composition components just prior to application. The pre-formed admixture can comprise curing agents-such as aminoplast resins and/or blocked isocyanate compounds such as those described above.
It would be understood by those skilled in the art that the amount of first reactant (I) and curing agent (II) suitable for use in the present compositions depends on the curing conditions of the coating as well as desired properties of the cured coating.
In a particular embodiment of the present invention, the thermosetting composition comprises the following components:
In another embodiment of the present invention, the thermosetting coating composition is a basecoat composition that may include one or more effect pigments. Nonlimiting examples of suitable effect pigments include, for example, metallic pigments such as aluminum flake and copper bronze flake, and micaceous pigments, for example, metal oxide coated mica. In an embodiment of the present invention the thermosetting coating composition can provide improved flake orientation of metallic or micaceous pigments, resulting in improved coating appearance and enhanced Flop Index ratings as described below. The level of effect pigments present in the thermosetting composition of the present invention can vary dependent upon the other composition components, the desired color, and/or the end use of substrate to be coated.
Besides the metallic pigments, the basecoat compositions can contain nonmetallic color and/or filler pigments conventionally used in surface coatings such as, for example, inorganic pigments such as titanium dioxide, iron oxide, chromium oxide, lead chromate, and carbon black; and organic pigments such as phthalocyanine blue and phthalocyanine green.
Optional ingredients in the basecoat composition can comprise those which are well known in the art of formulating surface coatings, and can comprise surface active agents, flow control agents, thixotropic agents, fillers, anti-gassing agents, organic co-solvents, catalysts, and other customary adjuvants. Nonlimiting examples of these materials and suitable amounts are described in U.S. Pat. Nos. 4,220,679; 4,403,003; 4,147,769; and 5,071,904.
In a particular embodiment of the present invention, the thermosetting composition further comprises an aqueous polyurethane dispersion in addition to components (I), (II), (III) and (IV). The inclusion of polyurethane dispersions in aqueous coating compositions for improving smoothness, flow and leveling of the coating film is known in the art. Any suitable polyurethane dispersion may be used in the present thermosetting composition. Examples of suitable polyurethane dispersions include, but are not limited to, those disclosed in U.S. Pat. No. 5,071,904 to Martin et al. (col. 4, line 40 to col. 9, line 8); U.S. Pat. No. 6,291,564 to Faler et al. (col. 3, line 32 to col. 4, line 52); U.S. Pat. No. 6,281,272 to Baldy et al. (col. 15, lines 52-66, see Table 1 footnote 9); U.S. Pat. No. 4,880,867 to Gob et al. (col. 7, line 29 to col. 12, line 68); and U.S. Pat. No. 6,025,031 to Lettmann et al. (col. 6, lines 30 to 43) the noted portions of which are herein incorporated by reference.
The polyurethane dispersion is present in the thermosetting coating composition of the present invention in an amount sufficient to provide a smooth cured coating as measured using a Byk Gardner wave scan instrument. See https://bvk-gardnerusa.com/html/Bvk/references/Applications/Application 4/application 4.h. For purposes of the present invention, the shortwave values correlate to the surface smoothness of a basecoat in a basecoat/clearcoat system.
Another embodiment of the present invention is directed to a coated substrate comprising:
The coating composition can be applied to the substrate by any conventional coating technique such as brushing, rolling, spraying, dipping, or flowing. Spray techniques and equipment for air spraying, airless spray, and electrostatic spraying in either manual or automatic methods known in the art can be used.
During application of the coating composition to the substrate, the film thickness of the coating formed on the substrate can range from 0.1 to 5 mils (2.54 to 127 micrometers). In another embodiment, the film thickness of the coating formed on the substrate can range 0.1 to 1 mils (2.54 to 25.4 micrometers), and can be 0.4 to 0.6 mils (10.2 to 15.2 micrometers). The coated substrate can be heated to a temperature and for a time sufficient to effect cure of the thermosetting composition applied thereto.
In another embodiment of the present invention, the composition is cured at ambient conditions.
Another embodiment of the present invention is directed to a method of repairing a defect in a multi-layer coating comprising:
The first base coating composition may include a pigmented basecoat composition. The first base coating layer can be fully cured or alternatively given a drying step in which solvent is driven out of the film by heating or an air drying period before application of the second coating layer. Suitable drying conditions may depend on the particular coating composition, and on the ambient humidity, but a drying time from 1 to 15 minutes at a temperature within the range of 70° F. to 200° F. (21° C. to 93° C.), or within the range of 160° F. to 180° F. (71° C. to 82° C.), can be adequate.
The first topcoat layer, which may include a substantially pigment-free (or clear) coating composition, can be applied to the first base coating layer by any conventional coating technique as described above, including, but not limited to, compressed air spraying, electrostatic spraying, and either manual or automatic methods. The first topcoat layer can be applied directly to the first base coating layer prior to drying or curing thereof; or to a dried first base coating layer, or to a cured first base coating layer. The two coatings can be heated to cure both coating layers simultaneously, i.e. to form a cured multi-layer coating. Typical curing temperatures are within the range of 50° F. to 475° F. (10° C. to 246° C.), or within the range of 250° F. to 300° F. (121° C. to 149° C.) for 1 to 30 minutes. The thickness (dry film thickness) of the first topcoat layer can range from 1 to 6 mils (25 to 150 micrometers).
When a defect is present in the cured multi-layer coating, the defect may be removed by any suitable method, such as by sanding, followed by re-application of one or more coating layers, the first and second base coating layers can be deposited from any of the coating compositions of the present invention. The first and second base coating compositions can be the same or different. Suitable drying conditions may depend on the particular coating composition, and on the ambient humidity, but a drying time from 1 to 15 minutes at a temperature within the range of 70° F. to 200° F. (21° C. to 93° C.), or within the range of 160° F. to 180° F. (71° C. to 82° C.), can be adequate.
The first and second topcoat layers may be formed from the same or different topcoat composition. A second topcoat layer may be applied over at least a portion of the second base coating layer and, optionally, over any of the previously applied layers. In one embodiment, the second topcoat layer is different from the first topcoat layer. The second topcoat layer can be applied directly to the second base coating layer prior to drying or curing thereof; or to a dried second base coating layer, or to a cured second base coating layer. The two coatings can be heated to cure both coating layers simultaneously, i.e. to form a cured multi-layer coating. The second topcoat layer may be heated at a temperature within the range of 180° F. to 200° F. (82° C. to 93° C.) for 30 to 45 minutes to effect cure. Alternatively, the second topcoat layer can be cured at room temperature. The thickness (dry film thickness) of the second topcoat layer can range from 1 to 6 mils (25 to 150 micrometers).
In another embodiment of the present invention, a second substantially pigment free topcoat composition can be applied directly to the first topcoat layer to form a “clear-on-clear” topcoat. The first topcoat coating composition can be applied over the first base coating layer as described above. The second topcoat coating composition which may be the same or different from the first topcoat composition can be applied to a cured or to a dried first topcoat before the first basecoat layer and first topcoat layer have been cured. The first base coating layer, the first topcoat layer and the second topcoat layer can then be heated to cure the three coatings simultaneously.
In one embodiment of the present invention, the base coating composition used to form the first base coating layer (and/or the second base coating composition used to form the second base coating layer), contains metallic or reflective pigments as are known in the art for use in color coats of the so-called color-plus-clear systems. These are the so-called “glamour finishes” whereby a differential light reflection effect, dependent upon the viewing angle, is achieved. This “flip-flop” effect can be attributed to the proper orientation (i.e., alignment parallel to the substrate surface) of the metallic and/or other reflective pigment in the base coating layer. Appearance properties such as gloss and distinctness of image, and smoothness, for the most part, can be attributed to the unpigmented topcoat (i.e., the clearcoat). The basecoat composition, which contains metallic and/or other reflective pigments, is formulated to maximize the “flip-flop” effect; and the top coating composition, which is substantially pigment-free, is formulated to maximize appearance properties such as gloss.
The above-described pigmented film-forming compositions are storage stable compositions which provide multi-layer composite coatings suitable for automotive color-plus-clear applications. The reflective pigment-containing base coats exhibit excellent “flip-flop” effect and excellent water resistance and appearance properties.
The coating composition of the present invention, when used as a metallic base coat composition, provides excellent metallic flake orientation as measured by Flop Index and include primarily HAPS compliant solvents. Further, the coatings derived from the present basecoat composition can be used with a wide variety of clearcoat chemistries and are able to maintain good metallic appearance by minimizing soak in or strike in. Also the coating compositions exhibit improved blistering resistance and interlayer adhesion properities.
As mentioned above, the multilayer composite coatings of the present invention can comprise two or more transparent topcoats applied over the base coat layer. It should be understood that when employed, the second transparent topcoat and the first transparent topcoat coating compositions can be the same or different provided that, when applied wet-on-wet, one topcoat does not substantially interfere with the curing of the other for example by inhibiting solvent/water evaporation from a lower layer. Moreover, the first topcoat, the second topcoat or both can be the coating composition of the present invention. Alternatively, only one of the first topcoat and the second topcoat is formed from the curable coating composition of the present invention.
In this instance, the topcoat that does not comprise the coating composition of the present invention can include any of the art recognized crosslinkable coating compositions comprising at least one coating material and at least one curing agent.
It should be mentioned that the coating compositions of the present invention can be advantageously formulated as a “monocoat”, that is, a coating which forms essentially one coating layer when applied to a substrate. The monocoat coating composition can be pigmented. Nonlimiting examples of suitable pigments can include any of those mentioned above. When employed as a monocoat, the coating compositions of the present invention can be applied (by any of the conventional application techniques discussed above) in two or more successive coats, and, in certain instances can be applied with only an ambient flash period between coats. The multi-coats when cured can form essentially one coating layer.
In an additional embodiment of the present invention, the coating composition described above can be present as a resinous phase dispersed in an aqueous phase. In this form, the coating composition can be used in a method of electrocoating a conductive substrate. In this method of electrocoating a conductive substrate serves as an electrode in an electrical circuit comprising an electrode and a counter electrode, the substrate being immersed in the composition thermosetting. The method includes passing electric current between the cathode and the anode to cause deposition of the electrocoating composition on the substrate as a substantially continuous film. The present invention is also directed to a substrate coated using the above-described method.
When the present coating composition is used in an electrocoating operation, the first reactant having reactive functional groups and/or the curing agent may additional include an ionic or salt group. The ionic group may be cationic or anionic. When the ionic group is cationic, it may be, for example, one or more of amine salts, quaternary ammonium and quaternary sulfonium groups. The cationic salt group may be derived from an epoxy group-containing monomer which after polymerization has been post-reacted with an amine salt or an amine and acid.
The present invention will further be described by reference to the following examples. The following examples are merely illustrative of the invention and are not intended to be limiting. All quantities, percentages and ratios are on a weight basis unless otherwise indicated.
This example describes the preparation of a polyester polymer used as a component in the coating compositions of the present invention. The polyester was prepared from the following ingredients as described below.
1A dimerdiacid available from Cognis.
The polyester polymer was prepared in a four-neck round bottom flask equipped with a thermometer, mechanical stirrer, condenser, dry nitrogen sparge and a heating mantle. The first four ingredients were heated to a temperature of 180° C. and stirred in the flask until 257 grams of distillate was collected and the acid value dropped to the range of 22-25. The material was then cooled to a temperature of 130° C. and the butyl ether of propylene glycol was added.
The final product was a liquid having Gardner-Holdt viscosity of Z5-Z6, a non-volatile content of 71.1% (as measured at 110° C. for one hour), and a weight average molecular weight of 23,125 as measured by gel permeation chromatography using polystyrene standards.
This example describes the preparation of an aqueous polyurethane dispersion containing polyurethane acrylate particles dispersed in an aqueous medium of the present invention.
A latex containing a hydrophilic polyurethane prepolymer was prepared by adding 313.3 g of N-methylpyrrolidine; 234.4 g of hydroxyethyl methacrylate; 241.5 g of dimethylol proprionic acid; 2.3 g of 2,6-Di-tert-butyl 4-methyl phenol; 2.3 g of triphenyl phosphate; and 2.3 g of dibutyl tin dilaurate to a four necked round bottom flask fitted with a thermocouple, mechanical stirrer, and condenser and heated to 100° C. in to obtain a homogeneous solution. Then 1200.0 g of polytetrahydrofuran (molecular weight 1000) was added. To this mixture at 90 to 100° C., 666.9 g isophorone diisocyanate was added over 90 minutes. The isocyanate container was rinsed with 153.0 g of butyl acrylate. The reaction mixture was stirred at 90° C. until all the isocyanate groups were reacted. Then 1100.0 g of butyl acrylate was added and cooled to ambient temperature.
Based on the ratios of monomers used, the theoretical distribution of compositions for this prepolymer is 25% diol (second surfactant-like prepolymer), 25% diacrylate (hydrophobic prepolymer), and 50% monofunctional in hydroxyl and acrylate (second surfactant-like prepolymer).
An aqueous polyurethane dispersion was prepared as described below from the following ingredients:
2Nonionic surfactant, 70% in water, available from RHODIA, Paris, France.
3Biocide containing 9.3% 1,2-Benzisothiazolin-3-one as active Ingredient, available from Syngenta Corporation, Wilmington, DE.
Charge 1 was mixed in a stainless steel beaker until homogeneous and the mixture was microfluidized, by passing once through a Microfluidizer® M110T (Microfluidics™ division of MFIC Corporation, Newton, Mass.) at 8000 psi into a stainless steel beaker and rinsed with 600 g of water. The microfluidized mixture was transferred to a round bottom flask fitted with a thermometer, mechanical stirrer, and condenser, sparged with nitrogen gas. Feed 1 was added to the flask and stirred for one minute. Then, Feed 2 was added to the flask over 30 minutes, an exothermic reaction was observed. The polymer was cooled to 30° C. and Feed 3 was added.
The final product was 40% solids by weight (as measured at 110° C. for one hour) and had a pH within the range of 7.5 to 9.0.
The following example describes the preparation of a latex emulsion containing crosslinked polymeric microparticles of the present invention. The aqueous dispersion was prepared as described below from the following ingredients. Amounts listed below indicate parts by weight (grams) unless otherwise noted.
4Anionic surfactant, available as AOT-75 from Cytec Industries, Inc.
5Anionic surfactant, available as Alipal CO-436 from GAF.
6Proxel GXL from Avecia Chemicals.
Charge 1 was added to a reactor fitted with thermocouple, agitator, and reflux condenser. The contents of the reactor were heated to a temperature of 83° C. at which time Feed A was added over a one (1) minute period, followed by a hold period of two (2) minutes. Feed B was then added over a one (1) minute period and the contents of the flask were held at a temperature of 83° C. for a period of 10 minutes. Feed C was then added over a 120-minute period. Approximately 10 minutes after the start of the Feed C addition, Feed D was added over a 120-minute period. Upon completion of the addition of Feed D, the reaction mixture was held at a temperature of 83° C. for 60 minutes, followed by cooling of the reaction product to ambient temperature. At ambient temperature Feed E was then added.
The final product was 30% solids by weight (as measured at 110° C. for one hour) and had a particle size of 0.1 micron (as measured using a Horiba LA-900 Laser Scattering Particle Size Distribution Analyzer, available from Horiba Instruments, Irvine, Calif.).
The polymer of Example D was prepared as described below from the following ingredients:
Charge 1 was added to a four-necked round bottom flask fitted with a thermocouple, mechanical stirrer, and condenser and heated to reflux. At this temperature, Feed 1 was added over 180 minutes. Fifteen minutes after the start of Feed 1, Feed 2 was added over 210 minutes. After a hold of 45 minutes, Feed 4 was added over 120 minutes. Fifteen minutes later, Feed 3 was added over 90 minutes. Then, the mixture was held for one hour, and Feed 5 was added while cooling the mixture to ambient temperature.
The final product was 70% solids by weight (as measured at 110° C. for one hour). The theoretical Tg (glass transition temperature) of this polymer was −62° C., calculated according to the equation described on page 29 in The Chemistry of Organic Film Former by D. H. Solomon, Wiley and Sons, 1967.
Two silver waterborne basecoat coating samples (Sample 1 and Sample 2) were prepared using the components listed in Table 1 below. Weights of all components are listed in grams. The “Premix Portion” was first prepared with all materials added under agitation in the order listed in Table 1. Then the “Basecoat Portion” was prepared using the “Premix Portion” at the amounts indicated by Table 1. Sample 1 was prepared without the polymer of Example D. Sample 2 was prepared with the polymer of Example D.
7Pigment paste of a 1:1 w/w ratio of Sparkle Silver 5271-AR and Alpate Miraglow 7670-NS.
8A 60/36/4 w/w solution of LUBRIZOL 2062/diisopropanolamine/propylene glycol butyl ether. LUBRIZOL 2062 is available from the Lubrizol Co., Cleveland, OH.
9Mineral Spirits available from Shell Chemical Co., Houston, TX.
10A 2% (w/w) aqueous solution of Laponite RD, available from Southern Clay Products, Gonzales, Texas.
11Acrylic thickener 1:1 (w/w) aqueous solution available from Rohm and Haas, Philadelphia, PA.
Two mica-containing silver waterborne basecoat coating samples (Sample 3 and Sample 4) were prepared using the components listed in Table 2 below. All components are listed in grams. The “Premix Portion” was first prepared with all materials added under agitation in the order listed in Table 2. Then the “Basecoat Portion” was prepared using the “Premix Portion” at the amounts indicated by Table 2. Sample 3 was prepared without the polymer of Example D. Sample 4 was prepared with the polymer of Example D.
12Pigment paste of a 5.86:10.13 w/w ratio of Stapa Metallux 2154 and Stapa Metallux R 875
13Iriodim 9505 Red Violet
14A 60/36/4 w/w solution of LUBRIZOL 2062/diisopropanolamine/Propylene glycol Butyl ether. LUBRIZOL 2062 is available from the Lubrizol Co., Cleveland, OH.
15A 2% (w/w) aqueous solution of Laponite RD, available from Southern Clay Products, Gonzales, Texas.
16Acrylic thickener 1:1 (w/w) aqueous solution available from Rohm and Haas, Philadelphia, PA.
The viscosity of each coating composition (Samples 1 through 4) was reduced to a spray viscosity of 33 to 37 seconds (DIN #4 cup) with deionized water.
Samples 1 and 2 were each spray applied in a humidity and temperature controlled spray booth at 60% relative humidity (“RH”) and 70° F. (21° C.) onto cold rolled steel substrates which had been previously electrocoated with ED5000 and primed with 1177225A gray primer (both products available commercially from PPG Industries, Inc.), the primed panels having been prepared by ACT Laboratories Inc., of Hillsdale Mich. Each coating composition was spray-applied using the SATA LP90 gun with a MSB nozzle and 135 air cap.
Samples 1 and 2 were spray applied such that the dry or cured film thickness of each coating was in the range of 0.4 to 0.6 mils (10.2 to 15.2 micrometers) thickness. These coated test panels were allowed an ambient air flash period of 3 minutes at 70° F.(21° C.)/60% RH, followed by heating for 3 minutes at 176° F. (80° C.) to further dehydrate the coating.
After dehydration, a two-component clearcoat composition 74984/74985 (available from PPG Industries, Inc.) was mixed at a weight ratio of 3 to 1 and spray applied over the panels coated with Samples 1 and 2. This clearcoat was spray applied such that between 1.4 and 1.6 mils (35.6 to 40.6 micrometers) of dry clearcoat film thickness was achieved. Following application of this clearcoat, the coated test panels were allowed an ambient air flash of 10 minutes at 70° F.(21° C.)/60% RH, followed by heating for 30 minutes at 285° F. (140° C.). All panels were allowed to cure at ambient conditions (70° F.(21° C.)/60% RH) for an additional 24 hours.
Next, Samples 1 and 2 were re-applied to each of their respective coated panels. In other words, if the panel was originally coated with Sample 1, Sample 1 was re-applied to that same panel. Both Samples 1 and 2 were sprayed so that the dry or cured film thickness was in the range of 0.4 to 0.6 mils (10.2 to 15.2 micrometers) thickness.
All coated test panels were again allowed an ambient air flash period of 3 minutes at 70° F.(21° C.)/60% RH, followed by heating for 3 minutes at 176° F. (80° C.) to further dehydrate the coating. Next, a two-component clearcoat composition 74971/74972 (available from PPG Industries, Inc.) was mixed at a weight ratio of 2 to 1 and spray applied over the panels. This clearcoat was spray applied such that between 1.4 and 1.6 mils (35.6 to 40.6 micrometers) of dry clearcoat film thickness was achieved. Following application of this clearcoat, the coated test panels were allowed an ambient air flash of 10 minutes at 70° F.(21° C.)/60% RH, followed by heating for 45 minutes at 185° F. (85° C.). All panels were allowed to cure at ambient conditions (70° F.(21° C.)/60% RH) for an additional 72 hours before testing.
Samples 3 and 4 were each spray applied in a humidity and temperature controlled spray booth at 60% relative humidity (“RH”) and 70° F. (21° C.) onto cold rolled steel substrates which had been previously electrocoated with ED5000 and primed with 1177225A gray primer (both products available commercially from PPG Industries, Inc.), the primed panels having been prepared by ACT Laboratories Inc., of Hillsdale Mich. Each coating composition was spray-applied using the SATA LP90 gun with a MSB nozzle and 135 air cap.
Samples 3 and 4 were spray applied such that the dry or cured film thickness of each coating was in the range of 0.4 to 0.6 mils (10.2 to 15.2 micrometers) thickness. These coated test panels were allowed an ambient air flash period of 3 minutes at 70° F.(21° C.)/60% RH, followed by heating for 3 minutes at 176° F. (80° C.) to further dehydrate the coating.
After dehydration, a one-component clearcoat composition High Teck 97060 (available from PPG Industries, Inc.) was spray applied over the panels coated with Samples 3 and 4. This clearcoat was spray applied such that between 1.4 and 1.6 mils (35.6 to 40.6 micrometers) of dry clearcoat film thickness was achieved. Following application of this clearcoat, the coated test panels were allowed an ambient air flash of 10 minutes at 70° F.(21° C.)/60% RH, followed by heating for 30 minutes at 285° F. (140° C.). All panels were allowed to cure at ambient conditions (70° F.(21° C.)/60% RH) for an additional 72 hours before testing.
Panels coated with Samples 1 and 2 (including the repair process detailed above) were tested in humidity and evaluated for blistering. Panels coated with Samples 3 and 4 were tested in humidity and watersoak and evaluated for blistering and adhesion as described below.
17Blistering was rated on a 1-10 scale; 1 = no blisters and 10 = very large and/or very dense blisters.
18Humidity test is performed using a Chrysler Box cabinet at 100° C. and 100% Relative Humidity for a 10 day duration. Panels were tested immediately unpon removal from the cabinet.
19Water soak test is a water immersion test. Coated panels are immersed in 63° C. water for 48 hours and then tested immediately upon removal from the water.
20Adhesion was performed according to ASTM D3359. The higher the number, the better the adhesion.
Whereas particular embodiments of this invention have been described above for purposes of illustration, it will be evident to those skilled in the art that numerous variations of the details of the present invention may be made without departing from the invention as defined in the appended claims.
This application is a Continuation-in-Part of U.S. application Ser. No. 10/126,903, filed Apr. 19, 2002, entitled “Coating Compositions Containing Polyurethane Dispersions And Highly Crosslinked Polymer Particles,” which is hereby incorporated by reference.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 10126903 | Apr 2002 | US |
| Child | 11089163 | Mar 2005 | US |
