Patent Application
20230312970
The present invention relates to an aqueous coating composition and a method for producing an aqueous coating composition.
Aqueous coating compositions are coating compositions containing an aqueous solvent. Generally, such an aqueous coating composition tends to be affected in the rate of solvent volatilization by the change of coating environment such as temperature and humidity in coating. The change of the rate of solvent volatilization may cause change of the appearance and/or the physical properties of a coating film formed by application.
One example of coping with such change of the coating environment may be a method of adjusting the rate of solvent volatilization by adjusting the amount of the solvent contained in the aqueous coating composition. For example, JP-A-2008-302274 (Patent Literature 1) discloses a method of determining a coating NV (nonvolatile content) according to the coating environment. As disclosed in Patent Literature 1, in the application of an aqueous coating composition, parameters such as the viscosity of the coating composition are often adjusted by adjusting the amount of the solvent of the aqueous coating composition, etc. according to the coating environment such as temperature and humidity However, such adjustment of parameters is complicated.
In the application of an aqueous coating composition, another means for reducing the influence of the coating environment may be the use of a thickener. For example, JP-A-2006-70095 (Patent Literature 2) discloses a multi-components aqueous coating composition comprising (I) a diluent and (II) a base coating material, wherein the diluent (I) comprises a thickener (A) and water, the base coating material (II) comprises a resin component (B), a thickener (C) and water, and the thickener (A) and the thickener (C) are selected from a combination of an inorganic thickener and a polyacrylic thickener, a combination of a urethane-associated thickener and a polyacrylic thickener, and a combination of a urethane-associated thickener and an inorganic thickener (claim 1). On the other hand, in the method of adjusting the viscosity using a thickener, it is possible to increase the viscosity of the coating composition, but it is difficult to design a coating composition having a low viscosity.
Incidentally, in the field of the application of a coating composition, there is an application method called “wet-on-wet” that can shorten the application process by applying a first coating composition, then applying a second coating composition without curing the resulting coating film, and then curing the two coating films simultaneously. However, the case where the first coating composition and the second coating composition are wet-on-wet applied is problematic in that the coating compositions are mixed at between the layers of the two uncured coating films (mix of layers) and, as a result, an undesirable phenomenon, namely, deterioration of coating film appearance may occur.
In the field of the application of an aqueous coating composition, there is desired a means for reducing the influence of the coating environment without impairing the appearance of a resulting coating film. The present invention solves the problems described above and the object thereof is to provide an aqueous coating composition which exhibits a small viscosity change and can form a coating film having a superior coating film appearance even when the amount of the solvent contained in the aqueous coating composition is reduced due to changes in the coating environment.
In order to solve the above-described problems, the present invention provides the following aspects.
[1]
An aqueous coating composition comprising an acrylic resin dispersion (A) and a melamine resin (B),
wherein
the acrylic resin dispersion (A) has a core/shell structure,
the acrylic resin dispersion (A) is a dispersion of a solution-polymerization product of a core part preparation monomer (a-1) and a shell part preparation monomer (a-2), wherein the shell part preparation monomer (a-2) includes an acid group-containing polymerizable monomer,
a mass ratio of a core part to a shell part of the acrylic resin dispersion (A) is in a range of core part/shell part=30/70 to 70/30,
the shell part of the acrylic resin dispersion (A) has an acid group, and a neutralization rate of the acid groups in the shell part is 50% or more,
a weight-average molecular weight of the acrylic resin dispersion (A) is in a range of 10,000 to 70,000,
the core part preparation monomer (a-1) has an acid value of 10 mg KOH/g or less, and the shell part preparation monomer (a-2) has an acid value of 10 mg KOH/g or more and 70 mg KOH/g or less,
a whole monomer mixture including the core part preparation monomer (a-1) and the shell part preparation monomer (a-2) has an acid value of 10 mg KOH/g or more and 30 mg KOH/g or less, a glass transition temperature of the acrylic resin dispersion (A) is in a range of −10 to 60° C., and the melamine resin (B) includes a hydrophobic melamine resin.
[2]
The aqueous coating composition defined above, wherein
the whole monomer mixture including the core part preparation monomer (a-1) and the shell part preparation monomer (a-2) has a hydroxyl value of 50 mg KOH/g or more and 150 mg KOH/g or less,
the core part preparation monomer (a-1) has a hydroxyl value of 50 mg KOH/g or more and 150 mg KOH/g or less, and
the shell part preparation monomer (a-2) has a hydroxyl value of 50 mg KOH/g or more and 150 mg KOH/g or less.
[3]
The aqueous coating composition defined above, further comprising one or more selected from the group consisting of a polyester resin dispersion and a polyurethane resin dispersion.
[4]
The aqueous coating composition defined above, wherein as to a viscosity of a dry coating film of the coating composition, viscosity η1 where a solid content in a dry coating film is 60% by mass and viscosity η2 where a solid content in a dried coating film is 90% by mass satisfy the following condition:
1≤η2/η1≤10, and
the viscosities η1 and η2 are viscosities measured at a temperature of 23° C. and a shear rate of 0.1 sec−1.
[5]
A method for producing an aqueous coating composition comprising an acrylic resin dispersion (A) having a core/shell structure and a melamine resin (B),
wherein
the acrylic resin dispersion (A) is produced through:
a step of solution-polymerizing a core part preparation monomer (a-1) to form a core part of the acrylic resin dispersion;
a step of solution-polymerizing, in the presence of the resulting core part, a shell part preparation monomer (a-2) including an acid group-containing polymerizable monomer to form a shell part of the acrylic resin dispersion; and
a step of desolvating the resulting solution-polymerization product, neutralizing it with a basic compound, and dispersing it in an aqueous medium,
a mass ratio of the core part to the shell part of the acrylic resin dispersion (A) is in a range of core part/shell part=30/70 to 70/30,
the shell part of the acrylic resin dispersion (A) has acid groups, wherein a neutralization rate of acid groups in the shell part is 50% or more,
a weight-average molecular weight of the acrylic resin dispersion (A) is in a range of 10,000 to 70,000,
the core part preparation monomer (a-1) has an acid value of 10 mg KOH/g or less, and the shell part preparation monomer (a-2) has an acid value of 10 mg KOH/g or more and 70 mg KOH/g or less,
a whole monomer mixture including the core part preparation monomer (a-1) and the shell part preparation monomer (a-2) has an acid value of 10 mg KOH/g or more and 30 mg KOH/g or less,
a glass transition temperature of the acrylic resin dispersion (A) is in a range of −10 to 60° C., and the melamine resin (B) includes a hydrophobic melamine resin.
[6]
A method for forming a multilayer coating film, comprising:
a step (1) of applying a first aqueous base coating composition onto a surface of an object to form an uncured first aqueous base coating film;
a step (2) of applying a second aqueous base coating composition onto the uncured first aqueous base coating film to form an uncured second aqueous base coating film;
a step (3) of applying a clear coating composition onto the uncured second aqueous base coating film to form an uncured clear coating film; and
a step (4) of heat-curing the uncured first aqueous base coating film, the uncured second aqueous base coating film, and the uncured clear coating film obtained in the steps (1) to (3) at a time to form a multilayer coating film, wherein
the first aqueous base coating composition is the aqueous coating composition defined above.
The aqueous coating composition defined above has a characteristic that it exhibits a small viscosity change even when the amount of the solvent contained in the coating composition is reduced. For this reason, the composition is advantageous in that it can be applied without suffering from great change in coating workability even when the amount of the solvent is reduced. The aqueous coating composition has an advantage that it can exhibit good coating workability even under various coating environments differing in temperature and/or humidity.
The aqueous coating composition comprises an acrylic resin dispersion (A) and a melamine resin (B). In the following, respective components are described in detail.
The aqueous coating composition comprises an acrylic resin dispersion (A). The acrylic resin dispersion (A) is characterized in that it has a core/shell structure and that it is a dispersion of a solution-polymerization product of a monomer mixture.
The acrylic resin dispersion (A) can be produced through:
a step of solution-polymerizing a core part preparation monomer (a-1) to form a core part of the acrylic resin dispersion;
a step of solution-polymerizing, in the presence of the resulting core part, a shell part preparation monomer (a-2) containing an acid group-containing polymerizable monomer to form a shell part of the acrylic resin dispersion;
a step of desolvating the resulting solution-polymerization product and neutralizing it with a basic compound; and
a step of mixing the neutralized polymerization product with an aqueous medium and dispersing it in the aqueous medium.
The core part preparation monomer (a-1) is a monomer mixture including a polymerizable monomer. Examples of the polymerizable monomer include:
(meth)acrylate monomers, which are esters of alkyl alcohols and (meth)acrylic acid, such as methyl (meth)acrylate, ethyl (meth)acrylate, n-propyl (meth)acrylate, n-butyl (meth)acrylate, t-butyl (meth)acrylate, isobutyl (meth)acrylate, 2-ethylhexyl (meth)acrylate or lauryl (meth)acrylate;
hydroxyl group-containing polymerizable monomers such as 2-hydroxyethyl (meth)acrylate, hydroxypropyl (meth)acrylate, 4-hydroxybutyl acrylate, diethylene glycol (meth)acrylate, caprolactone-modified hydroxy(meth) acrylate, and N-methylol acrylamide;
alicyclic polymerizable monomers such as dicyclopentanyl (meth)acrylate, dicyclopentenyl (meth)acrylate, dicyclopentenyloxyethyl (meth)acrylate, cyclohexyl (meth)acrylate, bornyl (meth)acrylate, isobornyl (meth)acrylate, 2-methyl-2-adamantyl (meth)acrylate, dicyclopentanyl (meth)acrylate, and cyclohexyl (meth)acrylate;
aromatic group-containing polymerizable monomers such as styrene, a-methylstyrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, p-tert-butylstyrene, itaconic acid esters (such as dimethyl itaconate), maleic acid esters (such as dimethyl maleate), fumaric acid esters (such as dimethyl fumarate), and vinyl acetate;
acid group-containing polymerizable monomers such as (meth)acrylic acid, 2-acryloyloxyethylphthalic acid, 2-acryloyloxyethylsuccinic acid, itaconic acid, maleic acid, and fumaric acid;
crosslinking monomers having two or more radically polymerizable ethylenically unsaturated groups in the molecule such as divinylbenzene, allyl (meth)acrylate, ethylene glycol di(meth)acrylate, 1,6-hexane diol di(meth)acrylate, 1,1,1-trishydroxymethylethane di(meth)acrylate, trimethylolpropane tri(meth)acrylate, triallyl isocyanurate, butadiene, and divinylbenzene;
polymerizable nitrile monomers such as (meth)acrylonitrile;
α-olefins such as ethylene and propylene;
vinyl ester monomers such as vinyl acetate, vinyl propionate, and vinyl versatate;
polymerizable amide monomers such as (meth)acrylamide, N-methylol(meth)acrylamide, N-butoxymethyl(meth)acrylamide, N,N-dimethyl(meth)acrylamide, N,N-dibutyl(meth)acrylamide, N,N-dioctyl(meth)acrylamide, N-monobutyl(meth)acrylamide, N-monooctyl(meth)acrylamide, 2,4-dihydroxy-4′-vinylbenzophenone, N-(2-hydroxyethyl)acrylamide, and N-(2-hydroxyethyl)methacrylamide; polymerizable glycidyl monomers such as glycidyl (meth)acrylate; and acid anhydride group-containing polymerizable monomers such as (meth)acrylic anhydride and maleic anhydride. The core part preparation monomer (a-1) includes two or more of the above-mentioned monomers.
In the present description, (meth)acryl shall mean both acryl and methacryl.
In the preparation of the core part of the acrylic resin dispersion (A), the acid anhydride group-containing polymerizable monomer is a component intended to react with a hydroxyl group of a polymer yielded through polymerization to form an ester linkage and introduce a polymerizable group into the polymerization product. That is, in the preparation of the core part, the acid anhydride group-containing polymerizable monomer is not used as a component for introducing an acid group into the core part, and is not a component for providing an acid group to the core part.
In the preparation of the core part of the acrylic resin dispersion (A), a polymerizable group can be introduced into the core part by the use of the acid anhydride group-containing polymerizable monomer. The polymerizable group introduced into the core part functions as a grafting part between the shell part and the core part during the polymerization of the shell part. The formation of the grafting part between the shell part and the core part is more preferable because it can effectively decrease the generation of mix of layers.
The core part preparation monomer (a-1) preferably includes two or more monomers selected from the group consisting of the (meth)acrylic acid ester monomer, the hydroxyl group-containing polymerizable monomer, the aromatic group-containing polymerizable monomer, the acid group-containing polymerizable monomer and the anhydride group-containing polymerizable monomer, and more preferably includes the (meth)acrylate monomer, the hydroxyl group-containing polymerizable monomer, the aromatic group-containing polymerizable monomer, the acid group-containing polymerizable monomer, and the acid anhydride group-containing polymerizable monomer.
The core part preparation monomer (a-1) even more preferably includes two or more monomers selected from the group consisting of styrene, n-butyl (meth)acrylate, methyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, hydroxyethyl (meth)acrylate, (meth)acrylic acid, and (meth)acrylic anhydride, and particularly preferably includes styrene, n-butyl (meth)acrylate, methyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, hydroxyethyl (meth)acrylate, (meth)acrylic acid, and (meth)acrylic anhydride.
The core part preparation monomer (a-1) preferably has an acid value of 10 mg KOH/g or less. The condition that the acid value of the core part preparation monomer (a-1) is 10 mg KOH/g or less is advantageous in that this can reduce a viscosity change when the amount of the solvent contained in the aqueous coating composition is reduced. The acid value of the acrylic resin is preferably in the range of 0 to 10 mg KOH/g, and more preferably in the range of 0 to 8 mg KOH/g.
The core part preparation monomer (a-1) preferably has a hydroxyl value of 50 mg KOH/g or more and 150 mg KOH/g or less. The condition that the hydroxyl value of the core part preparation monomer (a-1) is in the above range is advantageous in that the physical properties of a resulting coating film are improved. In addition, the condition that the hydroxyl value is 150 mg KOH/g or less is advantageous in that poor coating film appearance such as mix of layers can be more effectively prevented thereby. The hydroxyl value is more preferably 60 mg KOH/g or more and 140 mg KOH/g or less, and even more preferably 75 mg KOH/g or more and 130 mg KOH/g or less.
In the present description, the acid value and the hydroxyl value of a resin represent a solid acid value and a solid hydroxyl value, respectively, and are values measured by the method described in JIS K 0070. The number-average molecular weight and the weight-average molecular weight are values obtained by converting values measured by gel permeation chromatography (GPC) in terms of polystyrene standards.
Examples of the conditions for solution-polymerizing the core part preparation monomer (a-1) include an embodiment in which it is solution-polymerized in the presence of a polymerization initiator in an organic solvent. The polymerization temperature is preferably in the range of 70° C. to 200° C., and more preferably in the range of 90° C. to 170° C. The polymerization time is preferably 0.2 hours to 10 hours, and more preferably 1 hour to 6 hours.
The organic solvent to be used for the solution-polymerization is not particularly limited as long as it does not adversely affect the reaction, and a commonly used organic solvent can be used. Specific examples of the organic solvent include hydrocarbon solvents such as hexane, heptane, xylene, toluene, cyclohexane, and naphtha; ketone solvents such as methyl isobutyl ketone, methyl ethyl ketone, isophorone, and acetophenone; and ester solvents such as ethyl acetate, butyl acetate, isobutyl acetate, octyl acetate, ethylene glycol monomethyl ether acetate, and diethylene glycol monomethyl ether acetate. These may be used singly, or two or more of them may be used in combination.
As the polymerization initiator, those commonly used in radical polymerization can be used. Examples of the polymerization initiator include:
azo compounds such as azobisisobutyronitrile, 2,2′-azobis(2-methylbutyronitrile), 2,2′-azobis(2,4-dimethylvaleronitrile), 2,2′-azobis(4-methoxy-2,4-dimethylvaleronitrile), 2-phenylazo-4-methoxy-2,4-dimethylvaleronitrile, 2,2′-azobis{2-methyl-N-[1,1-bis(hydroxymethyl)-2-hydroxyethyl]propionamide}, 2,2′-azobis{2-methyl-N-[2-(1-hydroxyethyl)]propionamide}, 2,2′-azobis{2-methyl-N-[2-(1-hydroxybutyl)]propionamide}, 2,2′-azobis[2-(5-methyl-2-imidazolin-2-yl)propane] and salts thereof, 2,2′-azobis[2-(2-imidazolin-2-yl)propane] and salts thereof, 2,2′-azobis[2-(3,4,5,6-tetrahydropyrimidin-2-yl)propane] and salts thereof, 2,2′-azobis(1-imino-1-pyrrolidino-2-methylpropane) and salts thereof, 2,2′-azobis{2-[1-(2-hydroxyethyl)-2-imidazolin-2-yl]propane} and salts thereof, 2,2′-azobis(2-methylpropionamidine) and salts thereof, and 2,2′-azobis[N-(2-carboxyethyl)-2-methylpropionamidine]; and organic peroxides such as benzoyl peroxide, cumene hydroperoxide, tert-butyl hydroperoxide, tert-butyl peroxy-2-ethylhexanoate (hexanate hexanoate
), and tert-butyl peroxyisobutyrate. These may be used singly, or two or more of them may be used in combination.
In the solution-polymerization, a chain transfer agent may be used, if necessary. By using a chain transfer agent, the molecular weight of a resulting polymerization product can be prepared. As the chain transfer agent, known chain transfer agents, for example, mercaptans such as n-dodecyl mercaptan, tert-dodecyl mercaptan, n-octyl mercaptan, n-tetradecyl mercaptan, and n-hexyl mercaptan; halogen compounds such as carbon tetrachloride and ethylene bromide; and α-methylstyrene dimer can be used. These may be used singly, or two or more of them may be used in combination. For example, using a-methylstyrene dimer, which is an addition-fragmentation chain transfer agent, at the time of forming a core part is advantageous in that polymer chains composed of radically polymerizable monomers having different compositions can be grafted thereby.
Examples of a preferable embodiment of the preparation of a core part include an embodiment where the core part preparation monomer (a-1) includes a hydroxyl group-containing polymerizable monomer and an acid anhydride group-containing polymerizable monomer, and a monomer of the core part preparation monomer (a-1) other than the acid anhydride group-containing polymerizable monomer is polymerized and then a hydroxyl group of the resulting polymerization product is reacted with an anhydride group of the acid anhydride group-containing polymerizable monomer, and thus a polymerizable group is introduced into the polymer. This is advantageous in that a polymerizable group which serves as a grafting part during shell polymerization can thereby be introduced into a core part.
Next, the shell part of an acrylic resin dispersion is formed by solution-polymerizing a shell part preparation monomer (a-2) including an acid group-containing polymerizable monomer in the presence of the core part obtained above. The shell part preparation monomer (a-2) to be used for forming the shell part includes an acid group-containing polymerizable monomer as described above.
Examples of the acid group-containing polymerizable monomer contained in the shell part preparation monomer (a-2) include (meth)acrylic acid, 2-acryloyloxyethylphthalic acid, 2-acryloyloxyethylsuccinic acid, itaconic acid, maleic acid, fumaric acid, and (meth)acrylic anhydride. As the acid group-containing polymerizable monomer, it is preferable to use one or more selected from the group consisting of (meth)acrylic acid, (meth)acrylic anhydride, maleic acid, and itaconic acid.
In the preparation of the shell part of the acrylic resin dispersion (A), an acid anhydride group-containing polymerizable monomer such as (meth)acrylic anhydride is used not for forming an ester linkage by reacting a hydroxyl group with an acid anhydride group, but as a polymerizable monomer like other polymerizable monomers. Therefore, in the preparation of the shell part, the acid anhydride group-containing polymerizable monomer is used as an acid group-containing polymerizable monomer that provides an acid group to a polymerization product after polymerization.
Examples of the monomer other than the acid group-containing polymerizable monomer contained in the shell part preparation monomer (a-2) include a (meth)acrylate monomer, a hydroxyl group-containing polymerizable monomer, an alicyclic polymerizable monomer, an aromatic group-containing polymerizable monomer, crosslinking monomers, polymerizable nitrile monomers, α-olefins, vinyl ester monomers, and polymerizable amide monomers. As these monomers, the above-mentioned monomers can be used.
The shell part preparation monomer (a-2) preferably includes one or more acid group-containing polymerizable monomers selected from the group consisting of (meth)acrylic anhydride and (meth)acrylic acid, and one or more selected from the group consisting of the above-mentioned (meth)acrylate monomer, hydroxyl group-containing polymerizable monomer, and aromatic group-containing polymerizable monomer.
The shell part preparation monomer (a-2) more preferably includes the acid group-containing polymerizable monomer and one or more monomers selected from the group consisting of styrene, n-butyl (meth)acrylate, methyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, hydroxyethyl (meth)acrylate, and particularly preferably includes styrene, n-butyl (meth)acrylate, methyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, hydroxyethyl (meth)acrylate, and (meth)acrylic acid.
The shell part preparation monomer (a-2) preferably has an acid value of 10 mg KOH/g or more and 70 mg KOH/g or less. The condition that the acid value of the shell part preparation monomer (a-2) is in the above range is advantageous in that this can reduce a viscosity change when the amount of the solvent contained in the aqueous coating composition is reduced. The acid value is preferably in the range of 10 to 60 mg KOH/g, more preferably in the range of 20 to 60 mg KOH/g, and even more preferably in the range of 20 to 50 mg KOH/g.
The shell part preparation monomer (a-2) preferably has a hydroxyl value of 50 mg KOH/g or more and 150 mg KOH/g or less. The condition that the hydroxyl value of the shell part preparation monomer (a-2) is in the above range is advantageous in that a good reactivity with a melamine resin (B) can be secured and a good physical performance can be secured in a resulting coating film. The hydroxyl value is more preferably 60 mg KOH/g or more and 140 mg KOH/g or less, and even more preferably 70 mg KOH/g or more and 130 mg KOH/g or less.
Examples of the conditions for solution-polymerizing the shell part preparation monomer (a-2) include an embodiment in which it is solution-polymerized in the presence of a polymerization initiator in an organic solvent. The polymerization temperature is preferably in the range of 70° C. to 200° C., and more preferably in the range of 90° C. to 170° C. The polymerization time is preferably 0.2 hours to 10 hours, and more preferably 1 hour to 6 hours. As an organic solvent and a polymerization initiator to be used for the solution-polymerization and a chain transfer agent that may be used if necessary, those mentioned above can be used.
In the core part preparation monomer (a-1) and the shell part preparation monomer (a-2), the whole monomer mixture including the core part preparation monomer (a-1) and the shell part preparation monomer (a-2) preferably has an acid value of 10 mg KOH/g or more and 30 mg KOH/g or less. The condition that the acid value of the whole monomer mixture is in the above range is an advantageous in that good coating film properties of a formed coating film can be secured.
The whole monomer mixture including the core part preparation monomer (a-1) and the shell part preparation monomer (a-2) preferably has a hydroxyl value of 50 mg KOH/g or more and 150 mg KOH/g or less. The condition that the hydroxyl value of the whole monomer mixture is in the above range is an advantageous in that good coating film properties of a formed coating film can be secured.
In the above procedure, a solution-polymerization product having a core/shell structure can be obtained. The acrylic resin dispersion (A) can be prepared by desolvating the thus-obtained solution-polymerization product, then neutralizing it with a basic compound, and dispersing it in an aqueous medium. In the preparation of the dispersion, the stability of the dispersion is improved by neutralizing all or a part of the acid groups in the shell part of the solution-polymerization product having a core/shell structure with a basic compound. As to the neutralization with a basic compound, it is permitted that the resulting solution-polymerization product is desolvated and then neutralized with a basic compound and the neutralized solution-polymerization product is mixed with an aqueous medium and dispersed in the aqueous medium, and it is also permitted that the resulting (solution-)polymerized product is mixed with an aqueous medium containing a basic compound and dispersed in the aqueous medium.
Examples of the basic compound to be used for the neutralization include amine compounds such as ammonia, triethylamine, propylamine, dibutylamine, amylamine, 1-aminooctane, 2-dimethylaminoethanol, ethylaminoethanol, 2-diethylaminoethanol, 1-amino-2-propanol, 2-amino-1-propanol, 2-amino-2-methyl-1-propanol, 3-amino-1-propanol, 1-dimethylamino-2-propanol, 3-dimethylamino-1-propanol, 2-propylaminoethanol, ethoxypropylamine, aminobenzyl alcohol, and morpholine, and inorganic compounds such as sodium hydroxide and potassium hydroxide. These may be used singly, or two or more of them may be used in combination.
The neutralization rate of the acid groups in the shell part by the basic compound (that is, the equivalent ratio of the basic compound to the acid groups) is 50% or more. The neutralization rate is preferably 60 to 100%. The condition that the neutralization rate of the acid groups in the shell part is in the above range is advantageous in that viscosity change decreases even when the amount of the solvent contained in the coating composition is reduced.
The mass ratio of the core part to the shell part of the acrylic resin dispersion (A) is in the range of core part/shell part=30/70 to 70/30. The mass ratio is preferably in the range of core part/shell part=35/65 to 65/35, and more preferably in the range of 40/60 to 60/40. When the mass ratio core part/shell part is out of the range of 30/70 to 70/30, there is a possibility that a large viscosity change occurs when the amount of the solvent contained in the coating composition is reduced.
The weight-average molecular weight of the acrylic resin dispersion (A) is in the range of 10,000 to 70,000. When the weight-average molecular weight of the acrylic resin dispersion (A) is less than 10,000, mix of layers may occur during wet-on-wet application. When the weight-average molecular weight is greater than 70,000, there is a possibility that a large viscosity change occurs when the amount of the solvent contained in the coating composition is reduced. The weight-average molecular weight is preferably in the range of 13,000 to 60,000, and more preferably in the range of 15,000 to 50,000.
The glass transition temperature of the acrylic resin dispersion (A) is in the range of −10 to 60° C. More preferably, the glass transition temperature is in the range of −5 to 50° C. The condition that the glass transition temperature of the acrylic resin dispersion (A) is in the above range is advantageous in that the resulting coating composition exhibits a small viscosity change and an aqueous coating composition capable of forming a coating film having a superior coating film appearance can be prepared therefrom.
One examples of a means for adjusting the glass transition temperature of the acrylic resin dispersion (A) to within the above range may be an example in which the core part preparation monomer (a-1) includes one or more of styrene, α-methylstyrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, and p-tert-butylstyrene. The core part of the resulting acrylic resin dispersion has a styrene structure in this case, which is therefore advantageous in that the glass transition temperature of the acrylic resin dispersion (A) can be suitably adjusted.
The amount of the acrylic resin dispersion (A) contained in the aqueous coating composition is preferably 10 to 90 parts by mass, more preferably 15 to 80 parts by mass, and even more preferably 20 to 80 parts by mass, based on 100 parts by mass of the total resin solid content. The condition that the amount of the acrylic resin dispersion (A) is in the above range is advantageous in that the viscosity change is small and good coating workability is exhibited.
The aqueous coating composition contains a melamine resin (B). The melamine resin (B) is a component that functions as a curing agent in the aqueous coating composition. The melamine resin (B) has a structure in which groups R5 to R10 are bonded via three nitrogen atoms to a melamine nucleus (triazine nucleus) as represented by the following formula (1). The melamine resin is generally constituted by a polynuclear body in which a plurality of melamine nuclei are bonded to each other. On the other hand, the melamine resin may be a mononuclear body composed of one melamine nucleus. The structure of the melamine nucleus constituting the melamine resin can be represented by the following formula (1).
In the above formula (1), R1 to R6 may be the same or different and each represent a hydrogen atom amino group), CH2OH (methylol group), CH2OR7, or a binding part to another melamine nucleus. R7 is an alkyl group, preferably an alkyl group having 1 to 4 carbon atoms such as a methyl group, an ethyl group, a propyl group, and a butyl group.
Melamine resins can generally be broadly classified into water-soluble melamine resin and hydrophobic melamine resin. Here, the water-soluble melamine resin satisfies all of the following conditions (i) to (iii).
(i) The melamine resin has a number-average molecular weight of 1,000 or less.
(ii) In the above formula (1), at least one of R1 to R6 is a hydrogen atom (imino group) or CH2OH (methylol group). That is, the total amount of the average imino group content and the average methylol group content is 1.0 or more.
(iii) When R1 to R6 are each CH2OR7 in R1 to R6 in the above formula (1), R7 is a methyl group.
The number-average molecular weight of the melamine resin is a value measured by GPC.
The hydrophobic melamine resin is a melamine resin other than the water-soluble melamine resin. That is, one that satisfies any of the following conditions (iv) to (vi) corresponds to the hydrophobic melamine resin.
(iv) The number-average molecular weight of the melamine resin is greater than 1,000.
(v) The total amount of the average imino group content and the average methylol group content is 1.0 or less.
(vi) In R1 to R6 in the above formula (1), two or more of R1 to R6 are CH2OR7 and R7 is an alkyl group having 1 to 4 carbon atoms, provided that at least one R7 constituting R1 to R6 is an alkyl group having 2 to 4 carbon atoms.
The melamine resin (B) preferably includes a hydrophobic melamine resin, and the melamine resin (B) is more preferably a hydrophobic melamine resin. There is an advantage that the use of a hydrophobic melamine resin can effectively prevent the generation of a mix of layers during wet-on-wet application.
Commercially available products may be used as the melamine resin (B). Specific examples of the commercially available products include CYMEL Series (trade name) manufactured by Allnex, specifically, CYMEL 202, CYMEL 204, CYMEL 211, CYMEL 232, CYMEL 235, CYMEL 236, CYMEL 238, CYMEL 250, CYMEL 251, CYMEL 254, CYMEL 266, CYMEL 267, CYMEL 285 (these are melamine resins having both a methoxy group and a butoxy group);
MYCOAT 506 (manufactured by Mitsui Cytec Ltd., a melamine resin having a butoxy group alone); and U-VAN 20N60 and U-VAN 20SE (U-VAN (trade name) Series manufactured by Mitsui Chemicals, Inc.).
These may be used singly, or two or more of them may be used in combination. Of these, CYMEL 202, CYMEL 204, CYMEL 211, CYMEL 250, CYMEL 254, and MYCOAT 212 are more preferable.
The amount of the melamine resin (B) contained in the aqueous coating composition is preferably 10 to 60 parts by mass, and more preferably 20 to 50 parts by mass, based on 100 parts by mass of the total resin solid content. The condition that the amount of the melamine resin (B) is in the above range is advantageous in that a good curing performance of the aqueous coating composition can be secured.
The aqueous coating composition may contain other resin components, as necessary. Examples of such other resin components include a polyester resin dispersion and a polyurethane resin dispersion.
As the polyester resin dispersion, for example, a dispersion of a polyester resin having two or more hydroxyl groups in one molecule, which is called a polyester polyol, can be suitably used. The condition that the aqueous coating composition comprises the polyester resin dispersion is advantageous in that the coating workability is improved and the appearance of a resulting coating film is improved. Such a polyester resin is prepared by making a polyhydric alcohol and a polybasic acid or an anhydride thereof undergo polycondensation (an esterification reaction), and a polyester resin dispersion can be prepared by mixing and stirring the resulting polyester resin with a basic compound and an aqueous medium.
Examples of a polyhydric alcohol that can be used in the preparation of the polyester resin include ethylene glycol, diethylene glycol, polyethylene glycol, propylene glycol, dipropylene glycol, polypropylene glycol, neopentyl glycol, 1,2-butanediol, 1,3-butanediol, 2,3-butanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, hydrogenated bisphenol A, hydroxyalkylated bisphenol A, 1,4-cyclohexane dimethanol, 2,2-dimethyl-3-hydroxypropyl-2,2-dimethyl-3-hydroxypropionate, 2,2,4-trimethyl-1,3-pentanediol, N, N-bis-(2-hydroxyethyl)dimethylhydantoin, polytetramethylene ether glycol, polycaprolactone polyol, glycerin, sorbitol, trimethylolethane, trimethylolpropane, trimethylolbutane, hexanetriol, pentaerythritol, dipentaerythritol, and tris-(hydroxyethyl) isocyanate. These polyhydric alcohols may be used singly, or two or more of them may be used in combination.
Examples of a polybasic acid or an anhydride thereof include phthalic acid, phthalic anhydride, tetrahydrophthalic acid, tetrahydrophthalic anhydride, hexahydrophthalic acid, hexahydrophthalic anhydride, methyltetrahydrophthalic acid, methyltetrahydrophthalic anhydride, himic anhydride, trimellitic acid, trimellitic anhydride, pyromellitic acid, pyromellitic anhydride, isophthalic acid, terephthalic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, adipic acid, azelaic acid, sebacic acid, succinic acid, succinic anhydride, lactic acid, dodecenylsuccinic acid, dodecenylsuccinic anhydride, cyclohexane-1,4-dicarboxylic acid, and carbic anhydride. These polybasic acids or anhydrides thereof may be used singly, or two or more of them may be used in combination.
As the polyester resin dispersion, a dispersion of a polyester resin modified with a lactone, an oil or fat, a fatty acid, melamine resin, urethane resin, or the like can also be used. For example, the dispersion of a polyester resin modified with an oil or fat or a fatty acid is a polyester resin modified using an oil or fat such as castor oil, dehydrated castor oil, coconut oil, corn oil, cottonseed oil, linseed oil, perilla oil, poppy oil, safflower oil, soybean oil, and tung oil, or a fatty acid extracted from these oils and fats. In the production of the fat, oil or fatty acid-modified polyester resin, it is preferable to add the above-mentioned fat or oil and/or fatty acid in an amount up to about 30 parts in total by mass based on 100 parts by mass of the polyester resin.
The polyester resin dispersion preferably has a number-average molecular weight of 800 to 10,000, and more preferably 1,000 to 8,000 in terms of polystyrene determined by GPC measurement.
The polyester resin dispersion preferably has a solid hydroxyl value of 20 to 350 mg KOH/g, more preferably 30 to 300 mg KOH/g, and even more preferably 40 to 200 mg KOH/g.
When the aqueous coating composition comprises a polyester resin dispersion, the content of the polyester resin dispersion is preferably in the range of 5 to 60 parts by mass, and more preferably in the range of 5 to 50 parts by mass, based on 100 parts by mass of the total resin solid content.
The polyurethane resin dispersion can be prepared by dispersing, in water, a polyurethane resin prepared by using a polyol compound, a compound having an active hydrogen group and a hydrophilic group in its molecule, an organic polyisocyanate, and, if necessary, a chain extender and a polymerization terminator.
The polyol compound is not particularly limited as long as it is a compound having two or more hydroxyl groups, and examples thereof include polyhydric alcohols such as ethylene glycol, propylene glycol, 1,4-butanediol, 1,6-hexanediol, trimethylolpropane, and glycerol; polyether polyols such as polyethylene glycol, polypropylene glycol, and polytetramethylene ether glycol; polyester polyols obtained from a dicarboxylic acid such as adipic acid, sebacic acid, itaconic acid, maleic anhydride, phthalic acid, and isophthalic acid, and a glycol such as ethylene glycol, triethylene glycol, propylene glycol, butylene glycol, tripropylene glycol, and neopentyl glycol; polycaprolactone polyol; polybutadiene polyol; polycarbonate polyol; and polythioether polyol. The polyol compound may be used singly, or two or more thereof may be used in combination.
Examples of the compound having an active hydrogen group and a hydrophilic group in the molecule include compounds known as compounds containing active hydrogen and an anionic group {an anionic group or an anion-forming group (a group that reacts with a base to form an anionic group and, in this case, that is converted into an anionic group by neutralizing with a base before, during or after a urethanization reaction)} (those disclosed in JP-B-42-24192 and JP-B-55-41607; specific examples include dimethylolalkanoic acids such as α,α-dimethylolpropionic acid and α,α-dimethylolbutyric acid), compounds known as compounds having active hydrogen and a cationic group in the molecule (e.g., those disclosed in JP-B-43-9076), and compounds known as compounds having active hydrogen and a nonionic group (e.g., those disclosed in JP-B-48-41718; specifically, polyethylene glycol and alkylalcohol alkylene oxide adducts, etc.).
The organic polyisocyanate is not particularly limited as long as it has two or more isocyanate groups in its molecule, and examples thereof include aliphatic diisocyanates such as 1,4-tetramethylene diisocyanate, 1,6-hexamethylene diisocyanate, 2,2,4-trimethylhexamethylene diisocyanate, 3-isocyanatomethyl-3,5,5-trimethylcyclohexyl isocyanate, dicyclohexylmethane-4,4′-diisocyanate, methylcyclohexyl-2,4-diisocyanate, methylcyclohexyl-2, 6-diisocyanate, xylylene diisocyanate, 1,3-bis(isocyanate) methylcyclohexane, tetramethylxylylene diisocyanate, transcyclohexane-1,4-diisocyanate, and lysine diisocyanate; aromatic diisocyanates such as 2,4-toluylene diisocyanate, 2,6-toluylene diisocyanate, diphenylmethane-4,4′-diisocyanate, 1,5′-naphthene diisocyanate, tolidine diisocyanate, diphenylmethylmethane diisocyanate, tetraalkyldiphenylmethane diisocyanate, 4,4′-dibenzyldiisocyanate, and 1,3-phenylene diisocyanate; and triisocyanates such as lysine ester triisocyanate, triphenylmethane triisocyanate, 1,6,11-undecane triisocyanate, 1,8-diisocyanato-4,4-isocyanatomethyloctane, 1,3,6-hexamethylene triisocyanate, and bicycloheptane triisocyanate. These polyisocyanate compounds may be used in the form of a dimer or trimer thereof (isocyanurate linkage), and may be reacted with an amine and used as a biuret. Moreover, it is also possible to use polyisocyanates having a urethane linkage resulting from reacting such polyisocyanate compounds with polyols.
The chain extender that may be added if necessary in the preparation of the polyurethane resin dispersion is not particularly limited as long as it contains two or more active hydrogen groups, and examples thereof include low molecular weight polyols (e.g., ethylene glycol, propylene glycol, 1,4-butanediol, 3-methylpentanediol, 2-ethyl-1,3-hexane diol, and trimethylolpropane), polyamines (e.g., ethylenediamine, hexamethylenediamine, diethylenetriamine, hydrazine, xylylenediamine, and isophoronediamine), and water.
Examples of the polymerization terminator include a compound having one active hydrogen in its molecule (for example, monoalcohol and monoamine) or a monoisocyanate compound.
The reaction method of the polyurethane resin may be any method of a one-shot method in which the respective components are reacted at once and a multistage method in which the respective components are reacted in steps {a method of producing the resin by reacting part of an active hydrogen-containing compound (e.g., macromolecular polyol) with a polyisocyanate, thereby forming an NCO terminated prepolymer, and then reacting the remainder of the active hydrogen-containing compound}. The reaction of synthesizing the polyurethane resin is performed usually at 40 to 140° C., and preferably 60 to 120° C. In order to accelerate the reaction, there may be used a catalyst that is usually used for a urethanization reaction, such as a tin-based catalyst including dibutyltin laurate and tin octylate or an amine-based catalyst including triethylenediamine. In addition, the above reaction may be carried out in an organic solvent that is inert to isocyanate (e.g., acetone, toluene, dimethylformamide, etc.), and the solvent may be added either during the reaction or after the reaction.
The polyurethane resin dispersion can be prepared by treating a resulting polymer with a known method (a method of forming an anionic group by neutralization with a base in the case of an anion-forming group, a method of forming a cationic group with a quaternizing agent or a method of forming a cationic group by neutralization with an acid in the case of a cation-forming group) and then dispersing the polymer in water.
When the aqueous coating composition comprises a polyurethane resin dispersion, the content of the polyurethane resin dispersion is preferably in the range of 5 to 60 parts by mass, and more preferably in the range of 5 to 50 parts by mass, based on 100 parts by mass of the total resin solid content.
The aqueous coating composition of the present invention may comprise other components as necessary in addition to the above-described components. Examples of such other components include pigments, film-forming assistants, surface conditioners, antiseptic agents, fungicides, defoaming agents, light stabilizers, ultraviolet absorbers, antioxidants, and pH adjusters.
The pigment is not particularly limited, and examples thereof include: organic coloring pigments such as azo chelate pigments, insoluble azo pigments, condensed azo pigments, monoazo pigments, disazo pigments, diketopyrrolopyrrole pigments, benzimidazolone pigments, phthalocyanine pigments, indigo pigments, thioindigo pigments, perinone pigments, perylene pigments, dioxane pigments, quinacridone pigments, isoindolinone pigments, naphthol pigments, pyrazolone pigments, anthraquinone pigments, anthrapyrimidine pigments, and metal complex pigments; inorganic coloring pigments such as chrome yellow, yellow iron oxide, chromium oxide, molybdate orange, red iron oxide, titanium yellow, zinc flower, carbon black, titanium dioxide, cobalt green, phthalocyanine green, ultramarine, cobalt blue, phthalocyanine blue, and cobalt violet; mica pigments (titanium dioxide-coated mica, colored mica, metal-plated mica); graphite pigment, alumina flake pigment, metal titanium flakes, stainless flakes, plate-like iron oxide, phthalocyanine flakes, metal-plated glass flakes, other colored and colored flat pigments; and extender pigments such as titanium oxide, calcium carbonate, barium sulfate, barium carbonate, magnesium silicate, clay, talc, silica, and calcined kaolin.
The method for preparing the aqueous coating composition is not particularly limited, and the aqueous coating composition can be prepared by stirring the above-described components with a stirrer or the like. When a pigment, etc. are contained in the aqueous coating composition, those having good dispersibility can be mixed with a stirrer, and as another method, those previously dispersed in a vehicle containing water, a surfactant, a dispersant, etc. with a sand grind mill or the like can be added.
The aqueous coating composition is not particularly limited in its application method and drying conditions, and those which are commonly well-known can be applied. The aqueous coating composition can be used for various uses, and it exhibits superior performance especially under normal temperature drying to forced drying conditions. The forced drying generally means heating at about 80° C., but may be heating up to about 150° C., for example.
The object to which the aqueous coating composition of the present invention is applied is not particularly limited, and examples thereof include metal substrates such as iron, stainless steel and the like and surface-treated products thereof, cement substrates such as gypsum, and plastic substrates such as polyesters and acrylic plastics. Further examples include various objects for construction such as building materials and structures, various objects for the automobile industry such as automobile bodies and parts, and various objects for industrial fields such as electric appliances and electronic parts.
The aqueous coating composition is preferably in an embodiment where as to the viscosity of a dry coating film of the coating composition, the viscosity η1 in which the solid content in a dry coating film is 60% by mass and the viscosity η2 in which the solid content in a dried coating film is 90% by mass satisfy the following condition:
1≤η2/η1≤10.
The viscosities η1 and η2 are shear viscosities measured at a temperature of 23° C., at a shear rate of 0.1 s−1 using a rotary viscoelasticity analyzer.
The method of measuring the viscosity by increasing the solid content of an uncured coating material may, for example, be the following method. A coated sheet with an uncured coating film formed thereon is adjusted to have solid contents of 60±3% and 90±3% using, for example, a vacuum desolvation apparatus and the viscosity is measured at a temperature of 23° C. and a shear rate of 0.1 s−1 using a rotary viscoelasticity analyzer.
In the present description, for example, “the solid content in a dry coating film is 60% by mass” means that a state where the solid content is 60±3% by mass, and for example, “the solid content in a dry coating film is 90% by mass” means that a state where the solid content is 90±3% by mass.
In the present description, “a dry coating film of a coating composition” means a state where at least a part of the solvent contained in the coating composition has been evaporated after the coating composition has been applied to an object to be coated.
The condition that the viscosities η1 and η2 of an aqueous coating composition satisfy the above-defined condition means that a small viscosity change is exhibited even when the amount of the solid content in a dry coating film is in the above range and the amount of the solvent contained in the coating composition is reduced. The condition that a small viscosity change is exhibited even when the amount of the solvent is reduced is advantageous in that the change in coating workability exhibited when the viscosity has changed can be reduced. Such an aqueous coating composition has an advantage that it can exhibit good coating workability even under various coating environments differing in temperature and/or humidity.
The aqueous coating composition can be suitably used, for example, in forming a multilayer coating film. The method of forming a multilayer coating film may be, for example, the following method.
A method for forming a multilayer coating film, comprising a step (1) of applying a first aqueous base coating composition onto a surface of an object to form an uncured first aqueous base coating film, a step (2) of applying a second aqueous base coating composition onto the uncured first aqueous base coating film to form an uncured second aqueous base coating film, a step (3) of applying a clear coating composition onto the uncured second aqueous base coating film to form an uncured clear coating film, and a step (4) of heat-curing the uncured first aqueous base coating film, the uncured second aqueous base coating film, and the uncured clear coating film obtained in the steps (1) to (3) at a time to form a multilayer coating film.
The method of forming a multilayer coating film is a method in which application is performed sequentially when a coating film is in an uncured state, and this is a so-called wet-on-wet application method. Wet-on-wet application is advantageous in terms of economy and environmental impact because it can omit a baking drying oven.
In the above forming method, the aqueous coating composition can be suitably used as the first aqueous base coating composition.
The first aqueous base coating composition can be applied by application methods commonly used in the coating field. Examples of such application methods include multistage application, preferably two-stage application, with use of air electrostatic spray application, or application combining air electrostatic spray application and a rotary atomization type electrostatic applicator. The thickness of the first aqueous base coating film is preferably in the range of 3 to 40 μm.
Drying or preheating may, if necessary, be carried out after applying the first aqueous base coating composition and before applying the second aqueous base coating composition.
In another embodiment, after the application of the first aqueous base coating composition, the resulting coating film may be heat cured and then followed by the application of the second aqueous base coating composition onto the cured first aqueous base coating film.
As the second aqueous base coating composition, for example, an aqueous base coating composition usually used for the coating of automobile bodies can be used. Examples of such a second aqueous base coating composition include one containing a coating film-forming resin, a curing agent, a pigment such as a glitter pigment, a coloring pigment, and an extender pigment, and additives which are solved or dispersed in an aqueous medium. The second aqueous base coating material is not particularly limited with respect to its form as long as it is aqueous and, for example, it may be in the form of a water-soluble form, a water-dispersion form, an emulsion form, or the like.
The second aqueous base coating material may be applied by the same method as that of the first aqueous base coating material. The thickness of the second aqueous base coating film is preferably in the range of 3 to 20 μm. Drying or preheating may, if necessary, be carried out after applying the second aqueous base coating composition and before applying the clear coating composition.
In another embodiment, after the application of the second aqueous base coating composition, the resulting coating film may be heat cured and then followed by the application of a clear coating composition onto the cured second aqueous base coating film.
As the clear coating composition, for example, a composition that is usually used as a clear coating composition for an automobile body can be used. Examples of such a clear coating composition include a composition comprising a coating film-forming resin and, if necessary, a curing agent and other additives with them being dispersed or dissolved in a medium. Examples of the coating film-forming resin include an acrylic resin, a polyester resin, an epoxy resin, and an urethane resin. These can be used in combination with a curing agent such as an amino resin and/or an isocyanate resin. From the viewpoints of transparency or acid-resistant etching property, it is preferable to use a combination of an acrylic resin and/or a polyester resin and an amino resin, or an acrylic resin and/or a polyester resin having a carboxylic acid/epoxy curing system.
The application of the clear coating composition can be carried out using an application method known to those skilled in the art according to the mode of application of the clear coating composition. In general, the dry film thickness of a clear coating film to be formed by applying the above-described clear coating composition is preferably 10 to 80 μm, and more preferably 20 to 60 μm.
By heat curing an uncured clear coating film resulting from the application of a clear coating composition, a cured clear coating film can be formed. When the clear coating composition has been applied onto an uncured second aqueous base coating film, the uncured coating film is to be heat cured by heating. The heat curing temperature is preferably set to 80 to 180° C., and more preferably 120 to 160° C., from the viewpoint of curability and physical properties of a resulting multilayer coating film. The heat curing time may be set arbitrarily according to the above-mentioned temperature. Examples of the heat curing conditions include conditions where heating is performed at a heat curing temperature of 120° C. to 160° C. for 10 minutes to 30 minutes.
The present invention will be described hereafter in more detail by way of examples, to which the present invention is not intended to be limited. In the following examples, all designations of “part(s)” and “%” are on a mass basis, unless otherwise stated.
Preparation Step 1
A reactor equipped with a stirring device, a cooling device, and a heating device was charged with 210 parts by mass of butyl acetate and heated to 120° C. Thereafter, a monomer mixture composed of 73.65 parts by mass of styrene (ST), 178.96 parts by mass of methyl methacrylate (MMA), 75.94 parts by mass of n-butyl acrylate (BA), 64.45 parts by mass of 2-ethylhexyl acrylate, 105.00 parts by mass of hydroxyethyl methacrylate (HEMA), and 2.0 parts by mass of acrylic acid (AA) and a solution prepared by dissolving 70 parts by mass of tert-butyl peroxy-2-ethylhexanoate in 45 parts by mass of butyl acetate were dropped from two lines at constant rates over 90 minutes. While maintaining the reaction vessel at 120° C., 10 parts by mass of methacrylic anhydride was added and kept for 2 hours. Thereafter, the mixture was cooled to 60° C. to obtain a core polymer (core part).
Preparation Step 2
Subsequently, 210 parts by mass of butyl acetate was charged into a reactor equipped with a cooling device and a heating device and heated to 120° C. Thereafter, a monomer mixture composed of 835.00 parts by mass of the core polymer obtained in the step 1, 73.65 parts by mass of styrene (ST), 178.96 parts by mass of methyl methacrylate (MMA), 75.94 parts by mass of n-butyl acrylate (BA), 64.45 parts by mass of 2-ethylhexyl acrylate (2-EHA), 105.00 parts by mass of hydroxyethyl methacrylate (HEMA), and 20.0 parts by mass of acrylic acid (AA) and a solution prepared by dissolving 140 parts by mass of tert-butyl peroxy-2-ethylhexanoate in 120 parts by mass of butyl acetate were dropped from two lines at constant rates over 90 minutes.
Preparation Step 3
The reaction mixture was kept at 120° C. for 30 minutes, and a solution prepared by dissolving 3 parts by mass of tert-butyl peroxy-2-ethylhexanoate in 80 parts by mass of butyl acetate was dropped from a single line at a constant rate over 30 minutes. After stirring at 120° C. for 60 minutes, the mixture was cooled to 70° C. to synthesize a core-shell polymer. The resulting core-shell polymer had a resin solid content of 58.5% by mass, and a weight-average molecular weight of 25,000. The composition, the weight-average molecular weight, the acid value determined by calculation, and the hydroxyl value of the core-shell polymer are shown in Table 1.
Preparation Step 4
Subsequently, 170 parts by mass of dipropylene glycol monomethyl ether was added for dilution. Until the solid content reached 85% by mass, butyl acetate was distilled off from the resulting core-shell polymer under reduced pressure. After adding 27.21 parts by mass of dimethylethanolamine (DMEA) thereto, 1680 parts by mass of water was added to prepare acrylic resin dispersion (1). The resin solid content of the resulting acrylic resin dispersion (1) was 36.5% by mass.
The special values determined from the resin solid content and the composition of the resulting dispersion are shown in the following table.
The average particle diameter is a volume-average particle diameter D50, which is a value measured with a dispersion diluted with ion-exchanged water such that an appropriate signal level is attained using a laser Doppler type particle size analyzer (“Microtrac UPA150” manufactured by Nikkiso Co., Ltd.). The weight-average molecular weight is a value obtained by converting a value measured by gel permeation chromatography (GPC) in terms of polystyrene standards.
Acrylic resin dispersions (A)(2) to (11) were produced in the same manner as in Example 1, except that the charged amounts of the respective raw materials were changed to the values shown in Table 1.
A reactor equipped with a cooling device and a heating device was charged with 466 parts by mass of butyl acetate and heated to 120° C. Thereafter, a monomer mixture composed of 50.00 parts by mass of styrene (ST), 298.61 parts by mass of methyl methacrylate (MMA), 225.01 parts by mass of n-butyl acrylate (BA), 155.86 parts by mass of 2-ethylhexyl acrylate (2-EHA), 231.98 parts by mass of hydroxyethyl methacrylate (HEMA), and 38.53 parts by mass of acrylic acid (AA) and a solution prepared by dissolving 15 parts by mass of tert-butyl peroxy-2-ethylhexanoate in 120 parts by mass of butyl acetate were dropped from two lines at constant rates over 90 minutes.
The reaction mixture was kept at 120° C. for 30 minutes, and a solution prepared by dissolving 3 parts by mass of tert-butyl peroxy-2-ethylhexanoate in 80 parts by mass of butyl acetate was dropped from a single line at a constant rate over 30 minutes. After stirring at 120° C. for 60 minutes, the mixture was cooled to 70° C. to synthesize acrylic polyol. The resulting acrylic polyol had a resin solid content of 60% by mass and a weight-average molecular weight of 24,000. The composition, the weight-average molecular weight, the acid value determined by calculation, and the hydroxyl value of the acrylic polyol are shown in Table 1.
Subsequently, 175 parts by mass of dipropylene glycol monomethyl ether was added for dilution. Until the solid content reached 85% by mass, butyl acetate was distilled off from the resulting acrylic polyol under reduced pressure. After adding 47.67 parts by mass of dimethylethanolamine) thereto, 2700 parts by mass of water was added to prepare acrylic resin dispersion (12). The resin solid content of the resulting aqueous dispersion was 30.0% by mass. The special values determined from the resin solid content and the composition of the resulting acrylic resin dispersion are shown in the following table.
Deionized water (633 parts) was added to a reaction vessel, and the temperature was raised to 80° C. while mixing and stirring in a nitrogen stream. Subsequently, a first-stage monomer mixture composed of 75.65 parts by mass of styrene (ST), 178.96 parts by mass of methyl methacrylate (MMA), 75.94 parts by mass of n-butyl acrylate (BA), 64.45 parts by mass of 2-ethylhexyl acrylate (2-EHA), and 105.00 parts by mass of hydroxyethyl methacrylate (HEMA), a monomer emulsion composed of 25.00 parts of Aqualon HS-10 (polyoxyethylene alkylpropenylphenyl ether sulfate, produced by DKS Co. Ltd.), 25.00 parts of ADEKA REASOAP NE-20 (α-[1-[(allyloxy)methyl]-2-(nonylphenoxy)ethyl]-ω-hydroxyoxyethylene, produced by ADEKA Corp.), and 400 parts of deionized water, and an initiator solution composed of 1.2 parts of ammonium persulfate and 500 parts of deionized water were dropped in parallel into the reaction vessel over 1.5 hours. After the completion of the dropping, aging was carried out at that temperature for 1 hour.
Furthermore, at 80° C., a second-stage monomer mixture of 53.65 parts by mass of styrene (ST), 178.96 parts by mass of methyl methacrylate (MMA), 75.94 parts by mass of n-butyl acrylate (BA), 64.45 parts by mass of 2-ethylhexyl acrylate (2-EHA), 105.00 parts by mass of hydroxyethyl methacrylate (HEMA), and 22 parts by mass of acrylic acid, a monomer emulsion composed of 10 parts of Aqualon HS-10 and 250 parts of deionized water, and an initiator solution composed of 3.0 parts of ammonium persulfate and 500 parts of deionized water were dropped in parallel into the reaction vessel over 1.5 hours. After the completion of the dropping, aging was carried out at that temperature for 2 hours.
Subsequently, the mixture was cooled to 40° C. and filtered through a 400 mesh filter, and then 100 parts of deionized water and 1.6 parts of dimethylaminoethanol were added to adjust to pH 6.5, and thus an acrylic resin emulsion having an average particle diameter of 150 nm, a nonvolatile content of 35%, a solid acid value of 20 mg KOH/g, and a hydroxyl value of 100 mg KOH/g was obtained.
Tripropylene glycol methyl ether (23.89 parts) and 161.1 parts of propylene glycol methyl ether were added to a reaction vessel, and the temperature was raised to 120° C. while mixing and stirring in a nitrogen stream. Subsequently, a monomer mixture composed of 100.00 parts by mass of styrene (ST), 198.92 parts by mass of methyl methacrylate (MMA), 391.48 parts of butyl acrylate (BA), 13.40 parts of 2-ethylhexyl acrylate (EHA), 231.98 parts of 2-hydroxyethyl methacrylate, and 64.22 parts of acrylic acid was prepared, and the monomer mixture and an initiator solution composed of 100 parts of tripropylene glycol methyl ether and 20 parts of tert-butyl peroxy-2-ethylhexanoate (hexanate hexanoate
) were dropped in parallel into the reaction vessel over 3 hours. After the completion of the dropping, aging was carried out at that temperature for 0.5 hours.
Furthermore, an initiator solution composed of 50 parts of tripropylene glycol methyl ether and 3 parts of tert-butyl peroxy-2-ethylhexanoate (hexanate hexanoate
) was dropped into the reaction vessel over 0.5 hours. After the completion of the dropping, aging was carried out at that temperature for 2 hours.
After removing the solvent to a solid content of 85% with a desolvation apparatus, 2070 parts of deionized water and 79.4 parts of dimethylaminoethanol were added to obtain a water-soluble acrylic resin solution. The water-soluble acrylic resin solution obtained had a nonvolatile content of 30%, a solid acid value of 50 mg KOH/g, and a hydroxyl value of 100 mg KOH/g.
A normal reaction vessel for polyester resin production equipped with a stirrer, a thermometer, a reflux condenser, a nitrogen inlet tube, etc. was charged with 19 parts of isophthalic acid, 36 parts of hexahydrophthalic anhydride, 7 parts of trimethylolpropane, 12 parts of neopentyl glycol, 26 parts of 1,6-hexanediol, and 0.1 parts of dibutyltin oxide as a catalyst, and the temperature of the mixture was raised from 150° C. to 230° C. over 3 hours and maintained at 230° C. for about 5 hours. After cooling to 135° C., 7.7 parts of trimellitic anhydride was added and stirred for 1 hour to obtain a polyester resin having a solid acid value of 50 mg KOH/g, a solid hydroxyl value of 45 mg KOH/g, and a number-average molecular weight of 2500. After cooling to 90° C., 7.3 parts of dimethylethanolamine and 225 parts of ion-exchanged water were added to obtain a polyester resin dispersion having a solid content of 30%.
In a 1-L flask equipped with a stirrer, a nitrogen inlet tube, a temperature controller, a condenser, and a dropping funnel, 40.2 parts by weight of dimethylolpropionic acid, 30 parts by weight of triethylamine, and 312 parts by weight of N-methylpyrrolidone were heated and melted at 90° C. Subsequently, 290 parts by weight of isophorone diisocyanate and 700 parts by weight of polyhexamethylene carbonate diol (number-average molecular weight: 1,000) were added thereto, followed by stirring for 10 minutes, and then 1.03 parts by weight of dibutyltin dilaurate was added. Next, the temperature of the reaction system was raised to 95° C., and the reaction was carried out at that temperature for 1 hour to prepare a urethane prepolymer solution. A 5-L flask equipped with a stirrer, a nitrogen inlet tube, a temperature controller, a condenser, and a dropping funnel was charged with 1757 parts by weight of deionized water and 9.2 parts by weight of hydrazine hydrate, and, while stirring the mixture, the urethane prepolymer solution was added thereto. After the addition, the mixture was further stirred for 30 minutes to obtain a polyurethane resin dispersion. The resulting resin dispersion was a cloudy stable aqueous dispersion, and the acid value of the resin solid was 16.3. In addition, the nonvolatile content of the resin dispersion was 33%.
After preliminarily mixing 4.5 parts of a dispersant Disperbyk 190 (nonionic and anionic dispersant manufactured by BYK-Chemie GmbH), 0.5 parts of a defoaming agent BYK-011 (defoaming agent manufactured by BYK-Chemie), 22.9 parts of ion-exchanged water, and 72.1 parts of titanium dioxide, a glass bead medium was added in a paint conditioner, and mixed and dispersed at room temperature until the particle size reached 5 μm or less, and thus a pigment-dispersing paste was obtained.
After mixing 138.7 parts of the pigment-dispersing paste obtained in Production Example 17, 166.2 parts of the acrylic resin dispersion (1) obtained in Production Example 1, 33.3 parts of the polyester resin dispersion obtained in Production Example 15, 30.3 parts of the polyurethane resin dispersion obtained in Example 16, and 28.6 parts of melamine resin (1) (CYMEL 250, melamine resin manufactured by Allnex, nonvolatile content: 70%) as a curing agent, 1 part of ADEKA NOL UH814 (trade name; urethane-associated thickener manufactured by ADEKA Corporation) as a viscosity-adjusting agent, 5 parts of ethylene glycol mono-2-ethylhexyl ether, and 5 parts of 2-ethylhexanol as hydrophilic organic solvents were mixed and stirred, and thus aqueous coating composition (1) was obtained.
Aqueous coating compositions (2) to (33) were prepared in the same procedures as in Example 1, except that the acrylic resin dispersion, the polyester resin dispersion, the polyurethane resin dispersion, and the curing agent (melamine resin) were compounded in the amounts shown in the following tables.
The following evaluation tests were carried out using the aqueous coating compositions (1) to (33) obtained in the above Examples and Comparative Examples. The results obtained are shown in the following tables.
The viscosity of a coating film was measured in accordance with the following procedure.
The aqueous coating compositions prepared in Examples and Comparative Examples were dried to each have solid contents of 60±3% and 90±3% by using a vacuum desolvation apparatus (ARV-310) manufactured by THINKY Corporation. Subsequently, viscosity was measured at a temperature of 23° C. and a shear rate of 0.1 s−1 using a viscometer (MCR-301) manufactured by Anton Paar GmbH.
As a parameter indicating a rate of viscosity change, 42/41 was evaluated where the viscosity at which the solid content in a dry coating film is 60±3% by mass is represented by η1 and the viscosity at which the solid content in the dry coating film is 90±3% by mass is represented by η2. Evaluation criteria were as follows.
Evaluation Criteria for Viscosity (η2/η1)
⊚: 1≤η2/η1≤5 (There is almost no difference in viscosity between the solid contents of 60% by mass and 90% by mass.)
∘: 5<η2/η1≤10 (There is a slight difference in viscosity between the solid contents of 60% by mass and 90% by mass.)
Δ: 10<η2/η1≤15 (There is a viscosity difference between the solid contents of 60% by mass and 90% by mass.)
x: 15<η2/η1 (There is a very large difference in viscosity between the solid contents of 60% by mass and 90% by mass.)
Dull steel sheet treated with zinc phosphate was electrodeposited with POWERNIX 150 (trade name, cationic electro-deposition coating manufactured by Nippon Paint Co., Ltd.) such that the dry coating film was 20 μm thick, heat cured at 160° C. for 30 minutes, and then cooled, and thus a cured electrodeposition coating film was formed.
On the resulting electrodeposition coating film, any one of the aqueous coating compositions (1) to (33) was applied with a rotary atomization type electrostatic applicator such that the dry film thickness was 20 μm thick, and subsequently, AQUAREX AR-2100NH-700 (trade name, aqueous metallic base coating material manufactured by Nippon Paint Co., Ltd.) as a second aqueous base coating composition was applied with a rotary atomization type electrostatic applicator such that the dry film thickness was 10 μm in thickness, followed by preheating at 80° C. for 3 minutes.
The aqueous coating composition was applied under two different conditions, namely, through the step of applying it under the wet condition defined by a temperature of 15° C. and a humidity of 80% and then applying the second base coating composition under the condition of 23° C. and 60%, and through the step of applying the aqueous coating composition under the dry condition defined by a temperature of 30° C. and a humidity of 50% and then applying the second base coating composition under the condition of 23° C. and 60%. The aqueous coating composition was applied after an interval of 6 minutes from the application of the second base coating composition.
Further, PU EXCEL 0-2100 (trade name, two-component clear coating material manufactured by Nippon Paint Co., Ltd.) as a clear coating composition was applied to the coated sheet with a rotary atomization type electrostatic applicator such that the dry film thickness was 35 μm thick, followed by heat curing at 140° C. for 30 minutes, and thus two types of multilayer coating film specimens differing in the application condition for the aqueous coating composition (1).
The aqueous coating compositions (1) to (33), the second aqueous base coating composition, and the clear coating material were diluted under the following conditions.
The finished appearance of the resulting multilayer coating films was evaluated by measuring SW (measurement wavelength: 300 to 1,200 μm) using a wave-scan DOI (manufactured by BYK-Gardner). The difference in appearance between the appearance SW (WET) of a coating film applied under wet conditions and the appearance SW (DRY) of a coating film applied under dry conditions was used as an evaluation criterion.
Evaluation Criteria for Coating Film Appearance
⊚: SW (DRY)−SW (WET)≤2 (There is almost no difference in appearance between the wet condition and the dry condition.)
∘: 2<SW (DRY)−SW (WET)≤5 (There is a slight difference in appearance between the wet condition and the dry condition, but there is no problem.)
Δ: 5<SW (DRY)−SW (WET)≤10 (There is a large difference in appearance between the wet condition and the dry condition.)
x: 10<SW (DRY)−SW (WET) (There is a very large difference in appearance between the wet condition and the dry condition.)
The layer miscibility of the multilayer coating films prepared under the wet condition was evaluated using a flip-flop property. In a multilayer coating film good in layer miscibility, the orientation of the aluminum flakes contained in the second base coating is orderly arranged on the aqueous coating composition applied on a substrate, and the film is strong in flip-flop property. In a multilayer coating film poor in layer miscibility, the orientation of the aluminum flakes contained in the second base coating is randomly arranged on the aqueous coating composition applied on a substrate, and the film lacks flip-flop property.
As to the flip-flop property, L values at 15° (front) and 1100 (shade) were measured by using an X-Rite MA68II (manufactured by X-Rite Inc.). The larger the difference is, the better the flip-flop property is.
Evaluation Criteria for Layer Miscibility (Flip-Flop Property)
⊚: 100≤L value (15°)−L value (110°) (The L value difference between the front and the shade is large, and the flip-flop property is strong.)
∘: 90≤L value (15°)−L value (110°)<100 (The L value between the front and the shade is slightly large, and the flip-flop property is slightly strong.)
Δ: 80≤L value (15°)−L value (110°)<90 (Mix of layers occurred, and the flip-flop property is weak.)
x: L value (15°)−L value (110°)<80 (Mix of layers occurred violently, and the film lacks flip-flop property.)
The components shown in the above tables are as follows.
All of the aqueous coating compositions of the Examples were confirmed to exhibit a small viscosity change caused by change in solid content. Furthermore, all of the aqueous coating compositions of the Examples were reduced in generation of mix of layers between coating film layers, and were confirmed to be good in coating film appearance.
Comparative Example 1 is an example in which an acrylic resin emulsion was used instead of the acrylic resin dispersion. In this example, there was a large viscosity change caused by change in solid content, and the coating film appearance was also confirmed to be poor.
Comparative Example 2 is an example in which a water-soluble acrylic resin was used instead of the acrylic resin dispersion. In this example, generation of mix of layers between coating film layers was observed.
Comparative Example 3 is an example in which a water-soluble melamine resin was used instead of the hydrophobic melamine resin. In this example, generation of mix of layers between coating film layers was observed.
Comparative Example 4 is an example using an acrylic resin dispersion having no core/shell structure. In this example, there was a large viscosity change caused by change in solid content, and the coating film appearance was also confirmed to be poor.
Comparative Examples 5, 10, 15, 16 and 17 are examples in which the mass ratio of the acrylic resin dispersion is out of the range of core part/shell part=30/70 to 70/30. Also in these examples, there was a large viscosity change caused by change in solid content, and the coating film appearance was also confirmed to be poor.
Comparative Examples 6 and 11 are examples in which the acid value of the core part of the acrylic resin dispersion is greater than 10 mg KOH/g. In these examples, there was a slightly large viscosity change caused by change in solid content, and the coating film appearance was also confirmed to be slightly poor.
Comparative Examples 7 and 12 are examples in which the acid value of the whole monomer mixture including the core part preparation monomer (a-1) and the shell part preparation monomer (a-2) is out of the range of 10 mg KOH/g or more and 30 mg KOH/g or less. In this example, there was a large viscosity change caused by change in solid content, and the coating film appearance was also confirmed to be poor.
Comparative Examples 8 and 13 are examples in which the weight-average molecular weight of the acrylic resin dispersion is greater than 70,000. In this example, there was a large viscosity change caused by change in solid content, and the coating film appearance was also confirmed to be poor.
Comparative Examples 9 and 14 are examples in which the glass transition temperature of the acrylic resin dispersion is higher than 60° C. In this example, there was a large viscosity change caused by change in solid content, and the coating film appearance was also confirmed to be poor.
Comparative Example 18 is an example in which the neutralization rate of the acid groups in the shell part of the acrylic resin dispersion is less than 50%. In this example, there was a large viscosity change caused by change in solid content, and the coating film appearance was also confirmed to be poor.
The aqueous coating composition described above has the advantage that it exhibits a small viscosity change and coating can be performed without causing a large change in coating workability even when the amount of the solvent contained in the coating composition is reduced. The aqueous coating composition also has an advantage that deterioration in coating film appearance such as mix of layers can be reduced.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2018-122348 | Jun 2018 | JP | national |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 17255628 | Dec 2020 | US |
| Child | 18206220 | US |
