WO2016043149A1 - Method for forming coating film - Google Patents

Method for forming coating film Download PDF

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Publication number
WO2016043149A1
WO2016043149A1 PCT/JP2015/075980 JP2015075980W WO2016043149A1 WO 2016043149 A1 WO2016043149 A1 WO 2016043149A1 JP 2015075980 W JP2015075980 W JP 2015075980W WO 2016043149 A1 WO2016043149 A1 WO 2016043149A1
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Prior art keywords
coating
coating film
water
moisture
water separation
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PCT/JP2015/075980
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French (fr)
Japanese (ja)
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環 川元
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日本ペイントホールディングス株式会社
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Priority claimed from JP2015130811A external-priority patent/JP6560036B2/en
Application filed by 日本ペイントホールディングス株式会社 filed Critical 日本ペイントホールディングス株式会社
Publication of WO2016043149A1 publication Critical patent/WO2016043149A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D3/00Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
    • B05D3/12Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by mechanical means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/24Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials for applying particular liquids or other fluent materials

Definitions

  • the present invention relates to a coating film forming method in which a coating film is formed by application of a water-based coating composition.
  • Liquid coating compositions can generally be roughly classified into two types: a solvent-based coating composition containing an organic solvent and an aqueous coating composition containing water as a main solvent.
  • the water-based coating composition has a small amount of organic solvent compared to the solvent-based coating composition, and therefore has a low environmental load. Therefore, use of water-based paint compositions is required in various coating fields.
  • the water-based paint composition contains water having a low evaporation rate as a solvent. Therefore, in the formation of the coating film, it is strongly influenced by the environment during the coating and drying of the aqueous coating composition. Specifically, for example, when the aqueous coating composition is applied and dried in a low temperature environment of 5 ° C. or lower, the evaporation of water as a solvent is very slow. Also, for example, when the aqueous coating composition is applied and dried in a high humidity environment with a humidity of 80% or more, the evaporation of water as a solvent is very slow.
  • Patent Document 1 JP 2012-229302 A (Patent Document 1) describes an aqueous paint solidification accelerator for road marking containing calcium acetate particles or magnesium acetate particles (Claim 1). And in this patent document 1, by using the water-based paint solidification accelerator for road marking, it is described that the drying time of the water-based paint for road marking applied to the road surface can be shortened and the solidification of the paint can be promoted. Has been.
  • the road marking water-based paint solidification accelerator is a coating apparatus that simultaneously applies the road marking water-based paint solidification accelerator and the road marking water-based paint to the road surface as described in claim 7 or 8.
  • the transferred water marking solidifying accelerator is diffused in the container through which the spray of the water marking for road marking passes as described in claim 9, and the road marking is displayed on the water marking paint for road marking. It is painted using a special coating device such as a coating device that mixes water-based paint solidification accelerators.
  • Patent Document 2 describes an aqueous paint fixing agent for road marking containing water-insoluble inorganic compound particles capable of generating heat by reacting with water (Claim 1). .
  • the water marking agent for road marking is applied to the road surface together with the water marking paint for road marking, or is applied by being sprayed on the coating film of the waterborne coating for road marking applied to the road surface. ).
  • Patent Document 3 describes an aqueous road marking paint characterized in that it includes solid polymer particles or inorganic compound particles that can absorb water ( Claim 1).
  • Patent Document 3 also discloses a method for accelerating the drying of a water-based road marking paint applied to a surface, which is solid polymer particles or inorganic compound particles that can absorb water, and is applied to the surface together with the paint or applied. A method comprising spraying on the applied paint is also described (claim 2).
  • the invention described in Patent Document 3 does not describe the water removal step in the present invention.
  • the present invention solves the above-mentioned conventional problems, and its object is to achieve the object even under conditions where it is difficult to form a dry coating film by coating with an aqueous coating composition, such as a low temperature condition or a high humidity condition. It is providing the method which can form the coating film which has the function to do.
  • a painting process for painting a water-based paint composition The coating film obtained by the above coating is separated into a top layer containing water and a coating layer, a coating film separating step, and the top layer containing water is removed by a method other than drying.
  • Process A method for forming a coating film.
  • the uppermost layer containing moisture preferably further contains a moisture absorbent.
  • an aspect further including a moisture absorbent mixing step of adding a moisture absorbent to the aqueous coating composition before the coating step can be mentioned.
  • the coating film forming method for example, further including a water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition before the coating step, The coating film separation step is brought about by the water separation accelerator.
  • a water separation accelerator mixing step for example, before the coating step, a water separation accelerator mixing step and a moisture absorbent mixing step are performed, Here, the water separation accelerator mixing step is performed before the moisture absorbent mixing step.
  • the water absorbent preferably has a water absorption of 1 g / g or more.
  • the moisture absorbent is preferably one or more selected from the group consisting of a superabsorbent resin, protein and polysaccharide.
  • the water separation promoter is preferably one or more selected from the group consisting of organic acids, inorganic acids, acid anhydrides, pH buffer solutions, metal salts, basic compounds, and polymer flocculants.
  • the water separation accelerator is preferably a polymer flocculant.
  • the polymer flocculant is preferably a polyhydroxysiloxane compound.
  • a water-removing process using a water-absorbing material wherein a water-absorbing material is used to remove moisture from the coating process obtained by coating the aqueous coating composition; A method of forming a coating film.
  • a water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition before the coating step An embodiment is mentioned.
  • the water-absorbing material is one or more water-absorbing agents selected from the group consisting of a superabsorbent resin, protein and polysaccharide, or a sheet, film, membrane, comprising the water-absorbing agent, A strip or foam sheet is preferred.
  • the coating film forming method of the present invention is characterized in that moisture contained in the coating film formed from the aqueous coating composition is removed by a method other than drying. Therefore, even in a coating environment where it is difficult to evaporate an aqueous medium contained in a coating film formed from an aqueous coating composition, such as a low temperature condition and / or a high humidity condition, a coating having a target function is provided. A film can be formed.
  • the method of the present invention makes it possible to form a coating film in any environment without being influenced by the coating environment.
  • the coating film forming method of the present invention is a method for forming a coating film by coating an aqueous coating composition, wherein water contained in the coating film formed from the aqueous coating composition is removed by a method other than drying. It is characterized by. Although it does not specifically limit as an aqueous coating material composition used in the coating-film formation method of this invention, For example, the following aqueous coating material composition is mentioned.
  • Aqueous coating composition examples of the aqueous coating composition used in the method of the present invention include an aqueous coating composition containing an aqueous resin dispersion.
  • the aqueous resin dispersion contained in the aqueous resin dispersion aqueous coating composition is a film-forming resin component.
  • aqueous resin dispersion for example, an acrylic resin emulsion, an acrylic resin dispersion, a silicone-containing acrylic resin emulsion, a urethane resin emulsion, a vinyl acetate resin emulsion, a fluororesin emulsion, a vinyl chloride resin emulsion, and the like can be used. These resins may be used alone or in combination of two or more.
  • an acrylic resin emulsion, an acrylic resin dispersion, or a silicone-containing acrylic resin emulsion is preferably used.
  • An acrylic resin emulsion that can be used as an aqueous resin dispersion can be prepared by emulsion polymerization of a polymerizable monomer in an aqueous medium.
  • polymerizable monomers used in the preparation of acrylic resin emulsions ⁇ , ⁇ -ethylenically unsaturated monomers having a carboxyl group, ⁇ , ⁇ -ethylenically unsaturated monomers having a hydroxyl group, and other ⁇ , ⁇ -ethylenically unsaturated monomers are used. Saturated monomers are mentioned. These monomers can be appropriately selected according to the object to be coated with the aqueous coating composition and the application.
  • ⁇ -ethylenically unsaturated monomer having a carboxyl group acrylic acid, methacrylic acid, acrylic acid dimer, crotonic acid, 2-acryloyloxyethylphthalic acid, 2-acryloyloxyethyl succinic acid, ⁇ -carboxy- Polycaprolactone mono (meth) acrylate, isocrotonic acid, ⁇ -hydro- ⁇ -((1-oxo-2-propenyl) oxy) poly (oxy (1-oxo-1,6-hexanediyl)), maleic acid, fumarate Examples thereof include acid and itaconic acid. Among these, acrylic acid and methacrylic acid are preferable. In this specification, “(meth) acryl” means both acrylic and methacrylic.
  • an ⁇ , ⁇ -ethylenically unsaturated monomer having a hydroxyl group may be used as necessary.
  • the ⁇ , ⁇ -ethylenically unsaturated monomer having a hydroxyl group include hydroxyethyl (meth) acrylate, hydroxypropyl (meth) acrylate, hydroxybutyl (meth) acrylate, allyl alcohol, methacrylic alcohol and / or (meth). Mention may be made of adducts of hydroxyethyl acrylate and ⁇ -caprolactone.
  • hydroxyethyl (meth) acrylate preferred are hydroxyethyl (meth) acrylate, hydroxybutyl (meth) acrylate and / or an adduct of hydroxyethyl (meth) acrylate and ⁇ -caprolactone.
  • ⁇ , ⁇ -ethylenically unsaturated monomers include (meth) acrylic acid esters (eg methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, (meth) acrylic acid n-butyl, isobutyl (meth) acrylate, t-butyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, lauryl methacrylate, phenyl acrylate, isobornyl (meth) acrylate, cyclohexyl methacrylate, (meth ) T-butyl cyclohexyl acrylate, dicyclopentadienyl (meth) acrylate, dihydrodicyclopentadienyl (meth) acrylate), polymerizable amide compounds (eg (meth) acrylamide, N-methylol (meth) ) Acryl
  • Dienes eg, butadiene, isoprene, etc.
  • polymerizable aromatic compounds eg, polymerizable nitriles, ⁇ -olefins, vinyl esters, and dienes. These can be appropriately selected according to the purpose.
  • a crosslinkable monomer may be used as the other ⁇ , ⁇ -ethylenically unsaturated monomer.
  • the crosslinkable monomer is a compound having two or more radically polymerizable ethylenically unsaturated groups in the molecule, such as divinylbenzene, ethylene glycol di (meth) acrylate, hexanediol di (meth) acrylate, Polyethylene glycol di (meth) acrylate, allyl (meth) acrylate, 1,4-butanediol di (meth) acrylate, 1,6-hexane di (meth) acrylate, neopentyl glycol di (meth) acrylate, pentaerythritol di (meth) )
  • Divinyl compounds such as acrylate, and triallyl cyanurate, pentaerythritol tri (meth) acrylate, trimethylolpropane tri (meth)
  • emulsion polymerization in an aqueous medium is performed by, for example, dissolving an emulsifier in an aqueous medium containing water or a hydrophilic organic solvent such as water and alcohol or glycol, and heating. Under stirring, the polymerization can be carried out by dropping a monomer mixture obtained by mixing an ⁇ , ⁇ -ethylenically unsaturated monomer used as a raw material and a polymerization initiator. The monomer mixture obtained by mixing the ⁇ , ⁇ -ethylenically unsaturated monomer used as the raw material may be pre-emulsified using an emulsifier and water.
  • Polymerization initiators that can be suitably used for emulsion polymerization include azo oily compounds (for example, azobisisobutyronitrile, 2,2′-azobis (2-methylbutyronitrile), and 2,2′- Azobis (2,4-dimethylvaleronitrile) and the like, and aqueous compounds (eg, anionic 4,4′-azobis (4-cyanovaleric acid), 2,2-azobis (N- (2-carboxyethyl)) -2-methylpropionamidine and cationic 2,2′-azobis (2-methylpropionamidine)); and redox oily peroxides (eg, benzoyl peroxide, parachlorobenzoyl peroxide, lauroyl peroxide and t-butyl perbenzoate) and aqueous peroxides (eg potassium persulfate and persulfate) Ammonium and the like) and the like.
  • azo oily compounds for example, azobisis
  • emulsifier those usually used by those skilled in the art can be used.
  • reactive emulsifiers such as Antox MS-60 (manufactured by Nippon Emulsifier Co., Ltd.), Eleminol JS-2 (manufactured by Sanyo Kasei Kogyo Co., Ltd.), Adekari Soap NE-20 (manufactured by Asahi Denka Co., Ltd.) and Aqualon HS-10 (Daiichi Kogyo Seiyaku Co., Ltd.) is particularly preferred.
  • a mercaptan such as lauryl mercaptan and a chain transfer agent such as ⁇ -methylstyrene dimer can be used as necessary.
  • the reaction temperature is determined by the initiator. For example, it is preferably 60 to 90 ° C. for an azo initiator and 30 to 70 ° C. for a redox system. In general, the reaction time is 1 to 8 hours.
  • the amount of initiator relative to the total amount of monomer mixture is generally from 0.1 to 5% by weight, preferably from 0.2 to 2% by weight.
  • the emulsion polymerization can be performed in multiple stages, for example, in two stages.
  • the two-stage emulsion polymerization first, a part of the mixture of ⁇ , ⁇ -ethylenically unsaturated monomers used as the raw material is emulsion polymerized, and then the remainder of the ⁇ , ⁇ -ethylenically unsaturated monomer mixture is further added.
  • it is a polymerization method in which emulsion polymerization is performed.
  • the volume average particle diameter of the acrylic resin emulsion is preferably 20 to 500 nm, and more preferably 50 to 200 nm.
  • the volume average particle diameter is a volume average particle diameter determined by a dynamic light scattering method. Specifically, an electrophoretic light scattering photometer ELS-800 (manufactured by Otsuka Electronics Co., Ltd.) is used. Can be measured.
  • the acrylic resin emulsion is preferably adjusted to pH 5 to 10 by neutralizing with a basic compound.
  • the basic compounds are ammonia, methylamine, ethylamine, dimethylamine, diethylamine, trimethylamine, triethylamine, dimethylethanolamine, diethanolamine, diethylaminoethanol, triethanolamine, tetraethylammonium hydroxide, propylamine, dipropylamine, tripropylamine.
  • Amines such as butylamine, dibutylamine and tributylamine, and hydroxides such as sodium hydroxide and potassium hydroxide.
  • the neutralization is preferably performed by adding the basic compound to the system before or after emulsion polymerization.
  • the acrylic resin dispersion can be prepared, for example, by preparing an acrylic resin by solution polymerization of the polymerizable monomer, and then dispersing the obtained acrylic resin in water. More specifically, the acrylic resin dispersion contains the above ⁇ , ⁇ -ethylenically unsaturated monomer having a carboxyl group as an essential component, and after performing solution polymerization together with other ⁇ , ⁇ -ethylenically unsaturated monomers. It can be prepared by neutralizing with a basic compound and dispersing in water.
  • the solution polymerization is generally a method in which the mixture of the polymerizable monomers is stirred while being dropped into an organic solvent together with a polymerization initiator under heating conditions.
  • Solution polymerization can be carried out, for example, under conditions of a polymerization temperature of 60 to 160 ° C. and a dropping time of 0.5 to 10 hours.
  • the polymerizable monomer can be polymerized in two stages. By polymerizing the polymerizable monomer in two stages, a core-shell type acrylic resin dispersion comprising a core part and a shell part can be obtained.
  • the polymerization initiator is not particularly limited as long as it is used for normal polymerization, and examples thereof include azo compounds and peroxides. Generally, the amount of the polymerization initiator with respect to 100 parts by mass of the monomer mixture is 0.1 to 18 parts by mass, preferably 0.3 to 12 parts by mass.
  • the solvent that can be used here is not particularly limited as long as it does not adversely affect the reaction, and examples thereof include alcohols, ketones, ethers, and hydrocarbon solvents. Furthermore, in order to adjust the molecular weight, a mercaptan such as lauryl mercaptan and a chain transfer agent such as ⁇ -methylstyrene dimer can be used as necessary.
  • the number average molecular weight of the acrylic resin thus obtained by solution polymerization is preferably 4,000 to 20,000.
  • the number average molecular weight of the acrylic resin obtained by solution polymerization can be measured by gel permeation chromatography (GPC) using a polystyrene standard sample standard.
  • An acrylic resin dispersion can be obtained by removing the solvent as necessary from the acrylic resin obtained by the solution polymerization and neutralizing it by adding a basic compound.
  • the basic compound include the basic compounds listed above.
  • the amount of the basic compound added is preferably such an amount that the neutralization rate of the carboxyl group of the acrylic resin obtained by the solution polymerization is 60 to 100%. When the neutralization rate is less than 60%, the water dispersibility of the acrylic resin dispersion becomes low and the storage stability may be poor.
  • the acrylic resin dispersion preferably has a volume average particle diameter determined by a dynamic light scattering method in the range of 10 to 1000 nm.
  • the acrylic resin dispersion preferably has a volume average particle diameter of 10 to 1000 nm, and more preferably 100 to 800 nm.
  • silicone-containing acrylic resin emulsion examples include a polymer obtained by polymerization of a monomer composition further containing an alkoxysilyl group-containing polymerizable monomer in addition to the polymerizable monomer used in the preparation of the acrylic resin emulsion. Can do.
  • the alkoxysilyl group-containing polymerizable monomer is not particularly limited as long as it is a polymerizable monomer containing an alkoxysilyl group having 1 to 14 carbon atoms.
  • trimethoxysilylpropyl (meth) acrylate, triethoxysilylpropyl (meth) acrylate, vinyltrimethoxysilane, vinyltriethoxysilane and the like can be mentioned.
  • an organic silicone unit may be introduced into the silicone-containing acrylic resin emulsion.
  • a method for introducing the organosilicone unit a mixture of an organosilicone compound (for example, organosilane, a hydrolyzate of organosilane, a condensate of organosilane, etc.) and an acrylic polymerizable monomer is subjected to emulsion polymerization, hydrolysis, condensation reaction and Examples include a method of performing radical polymerization, a method of copolymerizing a monomer having a silicone functional group, and a method of bonding an organosilicone compound to the surface of acrylic polymer particles by reacting an organosilicone compound with an acrylic polymer. . Two or more methods described above may be combined.
  • the organosilane is not particularly limited, and examples thereof include tetraalkoxysilanes such as tetramethoxysilane, tetraethoxysilane, tetra-n-propoxysilane, tetra-i-propoxysilane, tetra-n-butoxysilane; Methoxysilane, methyltriethoxysilane, ethyltrimethoxysilane, ethyltriethoxysilane, n-propyltrimethoxysilane, n-propyltriethoxysilane, i-propyltrimethoxysilane, i-propyltriethoxysilane, n-butyltri Methoxysilane, n-butyltriethoxysilane, n-pentyltrimethoxysilane, n-hexyltrimethoxysilane, n-heptyltri
  • urethane resin emulsions in addition to the above, urethane resin emulsions, vinyl acetate resin emulsions, fluororesin emulsions, vinyl chloride resin emulsions and the like that are commonly used by those skilled in the art can also be used.
  • the amount of the aqueous resin dispersion contained in the aqueous coating composition is preferably 5 to 50 parts by mass with respect to 100 parts by mass of the aqueous coating composition as the resin solid content.
  • the aqueous resin dispersion may be a reaction curable resin that is cured by reacting with a curing agent, or may be a fusion resin that does not require a curing agent.
  • a curing agent for example, a carbodiimide curing agent, a melamine curing agent, an isocyanate curing agent, or the like can be used.
  • the aqueous coating composition in the present invention may contain other components as required in addition to the above components.
  • a film-forming aid for example, a film-forming aid, a thickener, a polyfunctional amine polymer, a coupling agent, a plasticizer, a crosslinked resin particle, a pigment, a surface conditioner, an antiseptic, an antifungal agent, an antifoaming agent, Examples thereof include a light stabilizer, an ultraviolet absorber, an antioxidant, and a pH adjuster.
  • the water-based paint composition contains water as a solvent.
  • the water-based coating composition may contain a hydrophilic organic solvent such as alcohol or glycol, if necessary, in addition to water.
  • the method for preparing the aqueous coating composition is not particularly limited, and can be prepared by stirring the above-described components with a stirrer or the like.
  • pigments or design materials are included in the aqueous coating composition, those having good dispersibility can be mixed with a stirrer, and as another method, a sand grind is added to a vehicle containing water, a surfactant or a dispersant. What was previously disperse
  • Coating Film Forming Method As one aspect of the coating film forming method of the present invention, A painting process for painting a water-based paint composition; The coating film obtained by the above coating is separated into a top layer containing water and a coating layer, a coating film separating step, and the top layer containing water is removed by a method other than drying. Process, The method of including is mentioned.
  • FIG. 1 is a schematic explanatory view showing this coating film forming method.
  • any method other than drying can be used.
  • the method of the present invention it is only necessary to include a moisture removing step of removing the uppermost layer containing moisture by a method other than drying, and in the method of the present invention, some moisture is removed by drying. It does not exclude that.
  • the coating film separation step the aspect in which the moisture contained in the coating film obtained by painting is evaporated somewhat corresponds to the method of the present invention as long as the water removal step is performed thereafter.
  • Arbitrary base material is mentioned as a to-be-coated object which coats water-based paint composition.
  • the substrate include metal, wood, plastics, rubber, stone, slate, concrete, mortar, fiber, paper, glass, porcelain, earthenware, film, and composites thereof. These substrates may be provided with a coating such as an undercoat coating as necessary.
  • any appropriate method can be used according to the type and shape of the article (base material) to be coated.
  • a method for applying the aqueous coating composition for example, commonly used coating methods such as dipping, brushing, flow coating, roller, roll coater, air spray, airless spray, curtain flow coater, roller curtain coater, die coater, etc. Can be used.
  • the aqueous coating composition is preferably applied so that the film thickness after removing water is 5 to 1000 ⁇ m, more preferably 20 to 300 ⁇ m.
  • the coating film obtained by coating the aqueous coating composition is separated into a water-containing uppermost layer and a coating film forming layer (coating film separation step).
  • coating film separation step examples include a method in which a coating film obtained by painting is allowed to stand for 2 seconds to 24 hours.
  • the uppermost layer containing moisture may contain only moisture, or may contain a moisture absorbent and / or a water separation accelerator described later. Further, the uppermost layer containing water may contain the above-mentioned additive contained in the aqueous coating composition, a slight amount of a film-forming component, and the like.
  • the coating film forming layer is a layer containing a coating film forming component contained in the aqueous coating composition.
  • the coating film forming component include the aqueous resin dispersion and other components as required.
  • the coating film forming layer may contain various additives in addition to the coating film forming component.
  • an aqueous coating composition As one means for bringing about and facilitating separation of the coating film obtained by coating into a water-containing uppermost layer and a film-forming layer, for example, before the coating step, an aqueous coating composition And a method of adding a water separation accelerator to the product (water separation accelerator mixing step).
  • the water separation accelerator include organic acids, inorganic acids, acid anhydrides, pH buffer solutions, metal salts, basic compounds, and polymer flocculants.
  • separation into the uppermost layer containing water and the coating film-forming layer means that an aqueous resin dispersion such as a resin emulsion is placed under a predetermined unstable condition, and a resin component, etc.
  • an aqueous resin dispersion such as a resin emulsion
  • a resin component etc.
  • the resin component constituting the aqueous resin dispersion and water are separated.
  • the basic mechanism of action is estimated as follows.
  • the water separation accelerator is a metal salt
  • the salt in the aqueous resin dispersion is fixed as hydrated water due to the strong hydration power of the salt, thereby reducing the stability of the aqueous resin dispersion.
  • the water separation accelerator is an organic acid, an inorganic acid, an acid anhydride, or a basic compound
  • a so-called coagulation action is considered to work. That is, the water separation accelerator exerts an electrical interaction with the ionic group of the aqueous resin dispersion by electrostatic attraction, so that the zeta potential on the surface of the aqueous resin dispersion particle is lowered and dehydrated. It is considered that the resin component becomes hydrophobic due to the coalescence of the particles, and the resin component of the aqueous resin dispersion is separated from the water.
  • the water separation accelerator is a polymer flocculant
  • the polymer chain of the polymer flocculant called a coagulation action together with these actions causes cross-linking adsorption to the resin component of the aqueous resin dispersion, and the polymer It is considered that separation of the resin component and moisture is promoted by bringing the aqueous resin dispersions together through a flocculant and making the resin component hydrophobic.
  • organic acid that can be used as a water separation accelerator
  • Monovalent carboxylic acids eg, acetic acid, benzoic acid, propionic acid, formic acid, etc.
  • Divalent carboxylic acids eg, maleic acid, fumaric acid, succinic acid, oxalic acid, etc.
  • Organic sulfonic acids for example, methanesulfonic acid, paratoluenesulfonic acid, benzenesulfonic acid, aminoethylsulfonic acid, etc.
  • Etc examples of the inorganic acid that can be used as the water separation accelerator include hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, and the like.
  • Examples of the acid anhydride that can be used as a water separation accelerator include those obtained by dehydration condensation of two molecules of the organic acid or inorganic acid.
  • Specific examples of the acid anhydride include, for example, acetic anhydride, benzoic anhydride, disulfuric acid (pyrosulfuric acid), pyrophosphoric acid (diphosphoric acid), diphosphorus pentoxide (phosphorus tetraoxide), and propionic anhydride.
  • an intramolecular dehydration condensate of the above divalent carboxylic acid can also be used. Examples of such condensates include maleic anhydride and fumaric anhydride.
  • Examples of the pH buffer that can be used as the water separation accelerator include acetate buffer, phosphate buffer, citrate buffer, Tris buffer, and borate buffer. Moreover, the buffer agent composition used for preparation of these pH buffer solutions may be added directly to the aqueous coating composition.
  • Examples of metal salts that can be used as a water separation accelerator include aluminum salts (eg, aluminum sulfate, polyaluminum chloride, etc.), iron salts (eg, polyferric sulfate, ferric chloride, etc.), sodium salts ( Examples thereof include sodium chloride, sodium sulfate, etc., calcium salts (eg, calcium chloride), magnesium salts (eg, magnesium chloride), and the like.
  • polymer flocculant that can be used as a water separation accelerator
  • cationic polymer flocculants dimethylaminoethyl methacrylate methylene chloride, diallyldimethylammonium chloride, aniline resin hydrochloride, polyamine derivatives, polythiourea acetate, polyethyleneaminotriazole, polyvinylbenzyltrimethylammonium chloride, polyethyleneimine, vinylpyridine
  • anionic polymer flocculants such as copolymer salts, sodium poly (meth) acrylate, maleic acid copolymer salt, itaconic acid copolymer salt, polyacrylamide partial hydrolyzate salt, sodium alginate, carboxy Methyl cellulose sodium salt, polyhydroxysiloxane compound, etc.
  • gelatin a copolymer of the above-mentioned anion unit and cation unit, etc. are used as the amphoteric polymer flocculant
  • polyacrylamide, polyoxyethylene, water-soluble urea, starch, etc. are appropriately used as the nonionic polymer flocculant. be able to.
  • the polyhydroxysiloxane compound which is a hydrolyzed condensate of alkoxysilane, has a relatively large pKa, so it does not cause abrupt aggregation that causes destabilization of the system, but has a relatively large polymer structure.
  • water separation accelerator that causes the above-mentioned cross-linking adsorption action more efficiently and causes rapid water separation by uniformly aggregating the entire system.
  • basic compounds that can be used as a water separation accelerator include ammonia, methylamine, ethylamine, dimethylamine, diethylamine, trimethylamine, triethylamine, dimethylethanolamine, diethanolamine, diethylaminoethanol, triethanolamine, tetraethylammonium hydroxide, Examples include amines such as propylamine, dipropylamine, tripropylamine, butylamine, dibutylamine and tributylamine, and hydroxides such as sodium hydroxide and potassium hydroxide. These water separation promoters may be used alone or in combination of two or more.
  • the water separation accelerator it is preferable to use at least one selected from the group consisting of organic acids (eg, acetic acid, propionic acid, etc.), acid anhydrides (eg, acetic anhydride, propionic anhydride, etc.) and polymer flocculants. .
  • the water separation accelerator it is more preferable to use an anionic polymer flocculant which is one type of polymer flocculant, and it is more preferable to use a polyhydroxysiloxane compound.
  • Preparation of a polyhydroxysiloxane compound more preferably used as a water separation accelerator is generally obtained by hydrolysis or condensation of a raw material selected from mono-, di-, tri-, and tetraalkoxysilanes alone or from a plurality thereof. .
  • a specific manufacturing method The well-known means described in patent 3599277, 5048395 grade
  • an amount that impairs the stability of the film-forming resin component is added. Specifically, it is preferably added in an amount of 0.01 to 50 parts by mass, more preferably 0.1 to 20 parts by mass with respect to 100 parts by mass of the aqueous coating composition. There exists a possibility that the effect as a water-separation promoter may not fully be exhibited as it is less than 0.01 mass part. If it exceeds 50 parts by mass, various coating film properties such as the curability and water resistance of the coating film may be deteriorated.
  • a method for adding a water separation accelerator to the aqueous coating composition a general mixing method can be used.
  • the uppermost layer containing water obtained by the coating film separating step is removed by a method other than drying (moisture removing step).
  • “removing the uppermost layer containing moisture by a method other than drying” means removing moisture contained in the coating film formed from the aqueous coating composition by a method other than drying after coating. Means. Specific examples of such a method include, for example, a method in which the uppermost layer containing moisture is washed away by gravity by tilting a coating film obtained by painting, or the uppermost layer containing a moisture absorbent is removed by hand or air. Examples of the removal method include removal or removal using an optional instrument as necessary, and a method of removing moisture by absorbing moisture in the uppermost layer into the moisture-absorbing material.
  • a water absorbent mixing step of adding a water absorbent to the aqueous coating composition may be performed before the coating step.
  • the moisture absorbent is contained in the uppermost layer containing moisture.
  • the moisture absorbent include an agent having a water absorption of 1 g / g or more. The amount of water absorption can be measured in accordance with the water absorption amount test method for high water absorption resin of JIS K 7223-1996.
  • the water absorbent include a highly water-absorbent resin, protein, polysaccharide and the like.
  • superabsorbent resins that can be used as moisture absorbents include polyacrylates (eg, sodium polyacrylate, potassium polyacrylate), polyvinyl alcohol, polyacrylamide, polyoxyethylene, polysulfonate, polyglutamic acid. Resins such as salts are listed.
  • the protein that can be used as a moisture absorbent include gelatin, glue, albumin, casein, gluten, and sericin.
  • a common material may be used for the water separation accelerator and the water absorbent. More specifically, a polymer flocculant which is an example of a water separation accelerator is used, and the same material may be used as a moisture absorbent.
  • a polymer flocculant, which is an example of a water separation accelerator is a component that causes separation of water from aqueous resin dispersion particles by, for example, salting out or coagulating action of added functional groups. This is because such an action is common in terms of action mechanism with the moisture absorption effect provided by the moisture absorbent in that water is fixed and separated and removed from the resin component.
  • the moisture absorbent is preferably in the form of particles or powder.
  • the particulate or powder moisture absorber include a moisture absorber having a volume average particle diameter of 100 nm to 1 mm.
  • the volume average particle diameter of the moisture absorbent can be measured by a laser light scattering method or the like. Specifically, it can be measured using a laser diffraction particle size distribution analyzer SALD-2200 (manufactured by Shimadzu Corporation). You may adjust a water
  • the water absorbent it is preferable to use at least one selected from the group consisting of proteins (for example, gelatin) and polysaccharides (for example, starch, hydroxyethyl cellulose, etc.).
  • proteins for example, gelatin
  • polysaccharides for example, starch, hydroxyethyl cellulose, etc.
  • the water absorbent When the water absorbent is added to the aqueous coating composition, it is preferably added in an amount of 0.1 to 100 parts by mass, and an amount of 0.1 to 30 parts by mass with respect to 100 parts by mass of the aqueous coating composition. It is more preferable to add at. If the amount is less than 0.1 parts by mass, moisture may not be sufficiently absorbed.
  • a general mixing method can be used as a method of adding a water absorbent to the aqueous coating composition.
  • the moisture absorbent may be subjected to an immersion treatment in which it is previously immersed in an organic solvent before being added to the aqueous coating composition.
  • the organic solvent for example, one or more selected from the group consisting of poorly water-soluble organic solvents and water-insoluble organic solvents can be used.
  • performing the immersion treatment for example, an aspect in which 0.5 to 10 parts by mass of the organic solvent is used for 1 part by mass of the moisture absorbent and the organic solvent is brought into contact with the organic solvent for 0.5 minutes to 24 hours. It is done.
  • the poorly water-soluble organic solvent means an organic solvent having a solubility at 20 ° C. of 10 mg / L or more and less than 10 g / L, and the water-insoluble organic solvent has a solubility at 20 ° C. of less than 10 mg / L. It means an organic solvent.
  • the water separation promoter mixing step is more preferably performed before the water absorbent mixing step.
  • a water-removing process using a water-absorbing material wherein a water-absorbing material is used to remove moisture from the coating process obtained by coating the aqueous coating composition;
  • the method of including is mentioned.
  • the moisture absorbing material is brought into contact with the moisture absorbing material from above the coating film obtained by painting to absorb moisture into the moisture absorbing material, thereby removing moisture.
  • FIG. 2 is a schematic explanatory view showing this coating film forming method.
  • the moisture-absorbing material used for removing moisture is not limited to the shape shown in FIG. 2, and any shape can be used.
  • the above-described moisture absorbent can be cited.
  • a material having a shape such as a sheet, a film, a membrane, a strip, and a foamed sheet, which is configured to include the moisture absorbent, can be used.
  • a material having such a shape for example, a material such as a commercially available sheet can be used.
  • the above-mentioned moisture absorbent can also be used after being processed into a shape such as a sheet or a film.
  • a water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition may be further included before the coating step.
  • the water separation accelerator the water separation accelerator described above can be used.
  • the coating film forming method of the present invention is characterized by removing water contained in the aqueous coating composition by a method other than drying. Therefore, a coating film can be formed even in a coating environment where it is difficult to evaporate the aqueous medium contained in the aqueous coating composition, such as a low temperature condition and / or a high humidity condition. According to the method of the present invention, it is possible to form a coating film having a desired function in any environment without being influenced by the coating environment.
  • the coating film forming method of the present invention may be used for forming a single layer coating film or may be used for forming a multilayer coating film.
  • coat a coating composition further with respect to the coating film which performed the said water removal process are mentioned, for example.
  • the water removal step may be performed as necessary.
  • the coating film forming method of the present invention is used in the formation of a multilayer coating film, in addition to the above-mentioned advantages, there are further advantages such as prevention of problems such as mixed layers.
  • MKC silicate MS51 (condensate of tetramethoxysilane manufactured by Mitsubishi Chemical Co., SiO 2 content 51%, degree of condensation is 5 as an average value) 10.71 g of aluminum chelate D (aluminum chelate compound manufactured by Kawaken Fine Chemical Co., Ltd.) (76% isopropanol solution) 0.44 g and methanol 28.70 g were added and dissolved. After the temperature was raised to 40 ° C., 40.18 g of water was gradually added over 2 hours and stirred, followed by aging at 40 ° C. for 2 hours to obtain a polyhydroxysiloxane solution having a concentration of 9.6%.
  • Example 1 10 g of core-shell acrylic resin dispersion (manufactured by Nippon Paint Co., Ltd., solid content 44%, acid value 20 mg-KOH / g) was weighed in a glass bottle, and 0.18 g of special grade acetic anhydride (reagent) was added as a water separation accelerator, Homogenously mixed by shaking 10 times by hand at room temperature. Immediately thereafter, it was painted on a test piece at room temperature with a 10 mil doctor blade.
  • acetic anhydride acetic anhydride
  • a highly water-absorbent resin particle (trade name: Aquakeep 10SH-PF, manufactured by Sumitomo Seika Co., Ltd., water absorption: 500 g / g, volume average particle diameter: 26 ⁇ m) as a moisture absorbing material on the coating film 2 g was added. After 5 minutes, the uppermost layer containing moisture was removed with a finger to obtain a desired coating film having a dry film thickness of 100 ⁇ m.
  • the water absorption amount of the highly water-absorbent resin particles was measured in accordance with the water absorption amount test method for the highly water-absorbent resin of JIS K 7223-1996. Specifically, 0.2 g of the substance is put in a tea bag, immersed in deionized water for 3 hours, suspended for 10 minutes and drained immediately, and the weight is measured. It was.
  • Example 2 The moisture absorbent is gelatin (trade name; Cook Gelatin, manufactured by Morinaga & Co., Ltd., water absorption: 17 g / g, volume average particle size: 697 ⁇ m), and the timing of removing the uppermost layer containing moisture is 15 A coating film having a target dry film thickness of 100 ⁇ m was obtained in the same manner as in Example 1 except that the change was made after minutes.
  • the gelatin used was pulverized in advance using a pestle in a mortar for 2 minutes.
  • the water absorption of gelatin was determined in the same manner as in Example 1.
  • Example 3 10 g of the same dispersion as described in Example 1 was weighed into a glass bottle, 0.18 g of acetic anhydride was added as a water separation accelerator, and then the mixture was uniformly mixed by shaking by hand 10 times at room temperature. Immediately thereafter, it was painted on a test piece at room temperature with a 10 mil doctor blade. Fifteen minutes later, the test piece was tilted to remove the uppermost layer containing moisture, and a desired coating film having a dry film thickness of 100 ⁇ m was obtained.
  • Example 4 10 g of the same dispersion as described in Example 1 was weighed into a glass bottle, 0.18 g of acetic anhydride was added as a water separation accelerator, and then the mixture was uniformly mixed by shaking by hand 10 times at room temperature. Immediately thereafter, 8 g of gelatin was added as a water absorbent, and the mixture was shaken by reciprocating 10 times and mixed uniformly. Immediately after that, it was uniformly cast on the test piece at room temperature. After coating, the mixture was allowed to stand at room temperature for 1 hour, and the uppermost layer that contained water and became a film was removed with a spoon. Thus, a coating film having a target dry film thickness of 200 ⁇ m was obtained.
  • the gelatin shown above was filtered by impregnating 10 g of toluene in advance with 8 g of gelatin (trade name: Cook Gelatin, Morinaga & Co., Ltd., water absorption: 17 g / g). And then used.
  • Example 5 A target coating film having a dry film thickness of 200 ⁇ m was obtained in the same manner as in Example 4 except that the standing conditions were changed to a temperature of 5 ° C. and a humidity of 50%.
  • Example 6 A target coating film having a dry film thickness of 200 ⁇ m was obtained in the same manner as in Example 4 except that the standing conditions were changed to a temperature of 23 ° C. and a humidity of 83%.
  • Example 7 The target dry film was obtained in the same manner as in Example 4 except that the water absorbent was changed to 2 g of hydroxyethyl cellulose (trade name: SP-850, manufactured by Daicel, water absorption 20 g / g, volume average particle size: 92 ⁇ m). A 200 ⁇ m thick coating film was obtained.
  • the hydroxyethyl cellulose shown above was used after filtering what impregnated 2 g of hydroxyethyl cellulose in 4 g of toluene in advance. Further, the water absorption amount of hydroxyethyl cellulose was determined in the same manner as in Example 1.
  • Example 8 A coating film having a target dry film thickness of 200 ⁇ m was obtained in the same manner as in Example 4 except that 2.29 g of the polyhydroxysiloxane solution prepared in Production Example 1 was used as the water separation accelerator.
  • Comparative Example 1 10 g of the same dispersion as described in Example 1 was weighed in a glass bottle and coated on a test piece at room temperature with a 10 mil doctor blade. After coating, it was allowed to stand at room temperature for 1 hour to obtain a coating film having a dry film thickness of 100 ⁇ m. In addition, the water removal process was not performed.
  • Comparative Example 2 A coating film having a dry film thickness of 100 ⁇ m was obtained in the same manner as in Comparative Example 1 except that the standing conditions were changed to a temperature of 5 ° C. and a humidity of 50%. In addition, the water removal process was not performed.
  • Comparative Example 3 A coating film having a dry film thickness of 100 ⁇ m was obtained in the same manner as in Comparative Example 2 except that the standing time was changed to 5 hours.
  • Comparative Example 4 A coating film having a dry film thickness of 100 ⁇ m was obtained in the same manner as in Comparative Example 1 except that the standing conditions were changed to a temperature of 23 ° C. and a humidity of 83%. In addition, the water removal process was not performed.
  • Comparative Example 5 A coating film having a dry film thickness of 100 ⁇ m was obtained in the same manner as in Comparative Example 4 except that the standing time was changed to 5 hours. In addition, the water removal process was not performed.
  • the result of the comparative example 1 is an evaluation result of the coating film obtained by leaving it at room temperature for 1 hour after coating. From the results of Comparative Example 1, it can be seen that even when the room temperature condition is not used, when the water removal step is not performed, a good coating film cannot be obtained only by standing for 1 hour.
  • the results of Examples 1 to 8 are all evaluation results of the coating film immediately after being formed according to the above examples. In the examples of the present invention, it was confirmed that even when the same paint as in Comparative Example 1 was used, a good coating film could be formed by removing moisture by a method other than drying. .
  • the result of the comparative example 2 is an evaluation result of the coating film obtained by being allowed to stand for 1 hour in a coating environment where the evaporation of the aqueous medium is difficult under low temperature conditions.
  • the result of the comparative example 4 is an evaluation result of the coating film obtained by leaving still for 1 hour in the coating environment where the evaporation of the aqueous medium is difficult under high humidity conditions. In the coating environment of these comparative examples 2 and 4, even when it was allowed to stand for another 4 hours to promote the volatilization of water (Comparative Example 3 and Comparative Example 5), the coating film remained sticky. .
  • Example 5 and 6 in addition to being in the coating environment of Comparative Examples 2 and 4, since the coating film thickness is thick and the total water content in the coating film is large, doctor blade coating On the other hand, the coating film is formed by a coating method that is more disadvantageous in film formation. In Examples 5 and 6, it was confirmed that a good coating film without sticky feeling could be obtained even though the coating film was formed using a coating method with higher hurdles on film formation. .
  • a coating film having a desired function is formed even in a coating environment where it is difficult to evaporate an aqueous medium contained in an aqueous coating composition such as a low temperature condition and / or a high humidity condition. There is an advantage that it becomes possible to do.

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Abstract

The purpose of the present invention is to provide a method with which it is possible to form a coating film even under conditions, such as low temperature conditions and/or highly humid conditions, in which it is difficult to form a coating film by applying an aqueous coating composition. The present invention relates to a method for forming a coating film, the method comprising: a coating step for coating with an aqueous coating composition; a coating film separation step for separating the coating film obtained by said coating into a moisture-containing uppermost layer and a coating film formation layer; and a moisture removal step for removing the moisture-containing uppermost layer by a method other than drying.

Description

塗膜形成方法Coating method
 本発明は、水性塗料組成物の塗装によって塗膜を形成する、塗膜形成方法に関する。 The present invention relates to a coating film forming method in which a coating film is formed by application of a water-based coating composition.
 液状の塗料組成物は、一般に、有機溶媒を含む溶剤型塗料組成物と、水を主たる溶媒とする水性塗料組成物の2種に大別することができる。水性塗料組成物は一般に、溶剤型塗料組成物と比較して有機溶媒の含有量が少ないため、環境に対する負荷が少ない。そのため、様々な塗装分野において、水性塗料組成物の使用が求められている。 Liquid coating compositions can generally be roughly classified into two types: a solvent-based coating composition containing an organic solvent and an aqueous coating composition containing water as a main solvent. In general, the water-based coating composition has a small amount of organic solvent compared to the solvent-based coating composition, and therefore has a low environmental load. Therefore, use of water-based paint compositions is required in various coating fields.
 一方で、水性塗料組成物は、蒸発速度の低い水を溶媒として含む。そのため、塗膜形成においては、水性塗料組成物塗装および乾燥時の環境の影響を強く受けることとなる。具体的には、例えば5℃以下の低温環境で水性塗料組成物を塗装および乾燥する場合は、溶媒である水の蒸発が非常に遅くなる。また、例えば湿度80%以上の高湿度環境で水性塗料組成物を塗装および乾燥する場合も、溶媒である水の蒸発が非常に遅くなる。このような低温および/または高湿条件においては、水性塗料組成物の塗装後において、溶媒である水が十分に蒸発できないため、塗膜の強度が上がらず、目的とする機能を有する塗膜を得ることができないという不具合があった。 On the other hand, the water-based paint composition contains water having a low evaporation rate as a solvent. Therefore, in the formation of the coating film, it is strongly influenced by the environment during the coating and drying of the aqueous coating composition. Specifically, for example, when the aqueous coating composition is applied and dried in a low temperature environment of 5 ° C. or lower, the evaporation of water as a solvent is very slow. Also, for example, when the aqueous coating composition is applied and dried in a high humidity environment with a humidity of 80% or more, the evaporation of water as a solvent is very slow. Under such low temperature and / or high humidity conditions, after the application of the aqueous coating composition, water as a solvent cannot sufficiently evaporate, so that the strength of the coating film does not increase and a coating film having the intended function is obtained. There was a problem that it could not be obtained.
 特開2012-229302号公報(特許文献1)には、酢酸カルシウムの粒子、又は、酢酸マグネシウムの粒子を含む、路面標示用水性塗料固化促進剤について記載されている(請求項1)。そしてこの特許文献1には、路面標示用水性塗料固化促進剤を用いることによって、路面に塗布された路面標示用水性塗料の乾燥時間を短縮し、その塗料の固化を促進することができることが記載されている。一方で、この路面標示用水性塗料固化促進剤は、請求項7または8に記載されるような、路面標示用水性塗料固化促進剤と路面標示用水性塗料とを同時に路面に塗布する塗装装置、または、請求項9に記載されるような、路面標示用水性塗料のスプレーが通過する容器内に、移送された該路面標示用水性塗料固化促進剤を拡散させ、路面標示用水性塗料に路面標示用水性塗料固化促進剤を混合させる塗装装置などといった、特殊な塗装装置を用いて塗装される。 JP 2012-229302 A (Patent Document 1) describes an aqueous paint solidification accelerator for road marking containing calcium acetate particles or magnesium acetate particles (Claim 1). And in this patent document 1, by using the water-based paint solidification accelerator for road marking, it is described that the drying time of the water-based paint for road marking applied to the road surface can be shortened and the solidification of the paint can be promoted. Has been. On the other hand, the road marking water-based paint solidification accelerator is a coating apparatus that simultaneously applies the road marking water-based paint solidification accelerator and the road marking water-based paint to the road surface as described in claim 7 or 8. Alternatively, the transferred water marking solidifying accelerator is diffused in the container through which the spray of the water marking for road marking passes as described in claim 9, and the road marking is displayed on the water marking paint for road marking. It is painted using a special coating device such as a coating device that mixes water-based paint solidification accelerators.
 特開2004-244467号公報(特許文献2)には、水と反応することで発熱可能な非水溶性の無機化合物粒子を含む路面標示用水性塗料定着剤について記載されている(請求項1)。この路面標示用水性塗料定着剤は、路面標示用水性塗料とともに路面に塗布するか、または路面に塗布された路面標示用水性塗料の塗膜上に散布することによって用いられている(請求項4)。 Japanese Patent Application Laid-Open No. 2004-244467 (Patent Document 2) describes an aqueous paint fixing agent for road marking containing water-insoluble inorganic compound particles capable of generating heat by reacting with water (Claim 1). . The water marking agent for road marking is applied to the road surface together with the water marking paint for road marking, or is applied by being sprayed on the coating film of the waterborne coating for road marking applied to the road surface. ).
 特開平9-235489号公報(特許文献3)には、固形ポリマー粒子または無機化合物の粒子であって、水を吸収できるものを含むことを特徴とする、水性道路マーキング塗料について記載されている(請求項1)。特許文献3にはまた、表面に施した水性道路マーキング塗料の乾燥を促進する方法であって、固形ポリマー粒子または無機化合物の粒子であって水を吸収できるものを、表面に塗料とともに、または塗布された塗料の上にスプレーすることを含む方法についても記載されている(請求項2)。一方で特許文献3記載の発明においては、本願発明における水分除去工程については記載されていない。 Japanese Patent Application Laid-Open No. 9-235489 (Patent Document 3) describes an aqueous road marking paint characterized in that it includes solid polymer particles or inorganic compound particles that can absorb water ( Claim 1). Patent Document 3 also discloses a method for accelerating the drying of a water-based road marking paint applied to a surface, which is solid polymer particles or inorganic compound particles that can absorb water, and is applied to the surface together with the paint or applied. A method comprising spraying on the applied paint is also described (claim 2). On the other hand, the invention described in Patent Document 3 does not describe the water removal step in the present invention.
特開2012-229302号公報JP 2012-229302 A 特開2004-244467号公報JP 2004-244467 A 特開平9-235489号公報Japanese Patent Laid-Open No. 9-235489
 本発明は上記従来の課題を解決するものであり、その目的とするところは、低温条件または高湿度条件などの、水性塗料組成物の塗装による乾燥塗膜形成が困難な条件においても、目的とする機能を有する塗膜を形成することができる方法を提供することにある。 The present invention solves the above-mentioned conventional problems, and its object is to achieve the object even under conditions where it is difficult to form a dry coating film by coating with an aqueous coating composition, such as a low temperature condition or a high humidity condition. It is providing the method which can form the coating film which has the function to do.
 上記課題を解決するため、本発明は下記態様を提供する。
[1]
 水性塗料組成物を塗装する塗装工程、
 上記塗装によって得られた塗膜を、水分を含有する最上層および塗膜形成層に分離する、塗膜分離工程、および
 上記水分を含有する最上層を、乾燥以外の方法によって除去する、水分除去工程、
を包含する、塗膜形成方法。
[2]
 上記水分を含有する最上層は、さらに水分吸収剤を含むのが好ましい。
[3]
 上記塗膜形成方法の1態様として、例えば、上記塗装工程の前に、水性塗料組成物に水分吸収剤を加える、水分吸収剤混合工程をさらに包含する態様が挙げられる。
[4]
 上記塗膜形成方法の1態様として、例えば、上記塗装工程の前に、水性塗料組成物に水分離促進剤を加える、水分離促進剤混合工程をさらに包含し、
 上記塗膜分離工程は、上記水分離促進剤によってもたらされる、
態様が挙げられる。
[5]
 上記塗膜形成方法の1態様として、例えば、上記塗膜形成方法において、上記塗装工程の前に、水分離促進剤混合工程および水分吸収剤混合工程が行われ、
ここで、上記水分離促進剤混合工程は、上記水分吸収剤混合工程の前に行われる、
態様が挙げられる。
[6]
 上記水分吸収剤は、吸水量1g/g以上であるのが好ましい。
[7]
 上記水分吸収剤は、高吸水性樹脂、タンパク質および多糖類からなる群から選択される1種またはそれ以上であるのが好ましい。
[8]
 上記水分離促進剤は、有機酸、無機酸、酸無水物、pH緩衝液、金属塩、塩基性化合物および高分子凝集剤からなる群から選択される1種またはそれ以上であるのが好ましい。
[9]
 上記水分離促進剤が高分子凝集剤であるのが好ましい。
[10]
 上記高分子凝集剤がポリヒドロキシシロキサン化合物であるのが好ましい。
[11]
 本発明の塗膜形成方法の他の1態様として、
 水性塗料組成物を塗装する塗装工程、および
 上記塗装によって得られた塗膜から、水分を、水分吸収材料を用いて除去する、水分吸収材料による水分除去工程、
を包含する、塗膜形成方法、が挙げられる。
[12]
 上記塗膜形成方法の1態様として、例えば、上記塗装工程の前に、水性塗料組成物に水分離促進剤を加える、水分離促進剤混合工程をさらに包含する、
態様が挙げられる。
[13]
 上記水分吸収材料は、高吸水性樹脂、タンパク質および多糖類からなる群から選択される1種またはそれ以上の水分吸収剤、または上記水分吸収剤を含んで構成される、シート、フィルム、膜、ストリップまたは発泡シートであるのが好ましい。
In order to solve the above problems, the present invention provides the following aspects.
[1]
A painting process for painting a water-based paint composition;
The coating film obtained by the above coating is separated into a top layer containing water and a coating layer, a coating film separating step, and the top layer containing water is removed by a method other than drying. Process,
A method for forming a coating film.
[2]
The uppermost layer containing moisture preferably further contains a moisture absorbent.
[3]
As one aspect of the coating film forming method, for example, an aspect further including a moisture absorbent mixing step of adding a moisture absorbent to the aqueous coating composition before the coating step can be mentioned.
[4]
As one aspect of the coating film forming method, for example, further including a water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition before the coating step,
The coating film separation step is brought about by the water separation accelerator.
An embodiment is mentioned.
[5]
As one aspect of the coating film forming method, for example, in the coating film forming method, before the coating step, a water separation accelerator mixing step and a moisture absorbent mixing step are performed,
Here, the water separation accelerator mixing step is performed before the moisture absorbent mixing step.
An embodiment is mentioned.
[6]
The water absorbent preferably has a water absorption of 1 g / g or more.
[7]
The moisture absorbent is preferably one or more selected from the group consisting of a superabsorbent resin, protein and polysaccharide.
[8]
The water separation promoter is preferably one or more selected from the group consisting of organic acids, inorganic acids, acid anhydrides, pH buffer solutions, metal salts, basic compounds, and polymer flocculants.
[9]
The water separation accelerator is preferably a polymer flocculant.
[10]
The polymer flocculant is preferably a polyhydroxysiloxane compound.
[11]
As another aspect of the coating film forming method of the present invention,
A water-removing process using a water-absorbing material, wherein a water-absorbing material is used to remove moisture from the coating process obtained by coating the aqueous coating composition;
A method of forming a coating film.
[12]
As one aspect of the coating film forming method, for example, further including a water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition before the coating step,
An embodiment is mentioned.
[13]
The water-absorbing material is one or more water-absorbing agents selected from the group consisting of a superabsorbent resin, protein and polysaccharide, or a sheet, film, membrane, comprising the water-absorbing agent, A strip or foam sheet is preferred.
 本発明の塗膜形成方法は、水性塗料組成物から形成された塗膜中に含まれる水分を、乾燥以外の方法によって除去することを特徴とする。そのため、低温条件および/または高湿度条件などの、水性塗料組成物から形成された塗膜中に含まれる水媒体の蒸発が困難である塗装環境下であっても、目的とする機能を有する塗膜を形成することが可能となる。本発明の方法によって、塗装環境に左右されることなく、あらゆる環境下において塗膜を形成することが可能となる。 The coating film forming method of the present invention is characterized in that moisture contained in the coating film formed from the aqueous coating composition is removed by a method other than drying. Therefore, even in a coating environment where it is difficult to evaporate an aqueous medium contained in a coating film formed from an aqueous coating composition, such as a low temperature condition and / or a high humidity condition, a coating having a target function is provided. A film can be formed. The method of the present invention makes it possible to form a coating film in any environment without being influenced by the coating environment.
本発明の塗膜形成方法の1態様を示す概略説明図である。It is a schematic explanatory drawing which shows 1 aspect of the coating-film formation method of this invention. 本発明の塗膜形成方法の他の1態様を示す概略説明図である。It is a schematic explanatory drawing which shows another one aspect | mode of the coating-film formation method of this invention.
 本発明の塗膜形成方法は、水性塗料組成物を塗装して塗膜を形成する方法において、水性塗料組成物から形成された塗膜中に含まれる水分を、乾燥以外の方法によって除去することを特徴とする。本発明の塗膜形成方法において用いられる水性塗料組成物として、特に限定されるものではないが、例えば下記の水性塗料組成物が挙げられる。 The coating film forming method of the present invention is a method for forming a coating film by coating an aqueous coating composition, wherein water contained in the coating film formed from the aqueous coating composition is removed by a method other than drying. It is characterized by. Although it does not specifically limit as an aqueous coating material composition used in the coating-film formation method of this invention, For example, the following aqueous coating material composition is mentioned.
水性塗料組成物
 本発明の方法において用いられる水性塗料組成物として、例えば、水性樹脂分散体を含む水性塗料組成物が挙げられる。
Aqueous coating composition Examples of the aqueous coating composition used in the method of the present invention include an aqueous coating composition containing an aqueous resin dispersion.
  水性樹脂分散体
 水性塗料組成物に含まれる水性樹脂分散体は、塗膜形成樹脂成分である。水性樹脂分散体として、例えば、アクリル樹脂エマルション、アクリル樹脂ディスパージョン、シリコーン含有アクリル樹脂エマルション、ウレタン樹脂エマルション、酢酸ビニル樹脂エマルション、フッ素樹脂エマルション、塩化ビニル樹脂エマルションなどを用いることができる。これらの樹脂は単独で用いてもよく、2種以上を併用してもよい。水性樹脂分散体としては、アクリル樹脂エマルション、アクリル樹脂ディスパージョンまたはシリコーン含有アクリル樹脂エマルションを用いるのが好ましい。
The aqueous resin dispersion contained in the aqueous resin dispersion aqueous coating composition is a film-forming resin component. As the aqueous resin dispersion, for example, an acrylic resin emulsion, an acrylic resin dispersion, a silicone-containing acrylic resin emulsion, a urethane resin emulsion, a vinyl acetate resin emulsion, a fluororesin emulsion, a vinyl chloride resin emulsion, and the like can be used. These resins may be used alone or in combination of two or more. As the aqueous resin dispersion, an acrylic resin emulsion, an acrylic resin dispersion, or a silicone-containing acrylic resin emulsion is preferably used.
 水性樹脂分散体として用いることができるアクリル樹脂エマルションは、水性媒体中で重合性モノマーを乳化重合することによって調製することができる。アクリル樹脂エマルションの調製に用いられる重合性モノマーとして、カルボキシル基を有するα,β-エチレン性不飽和モノマー、水酸基を有するα,β-エチレン性不飽和モノマー、およびその他のα,β-エチレン性不飽和モノマーが挙げられる。これらのモノマーは、水性塗料組成物を塗装する被塗物および用途に応じて適宜選択することができる。 An acrylic resin emulsion that can be used as an aqueous resin dispersion can be prepared by emulsion polymerization of a polymerizable monomer in an aqueous medium. As polymerizable monomers used in the preparation of acrylic resin emulsions, α, β-ethylenically unsaturated monomers having a carboxyl group, α, β-ethylenically unsaturated monomers having a hydroxyl group, and other α, β-ethylenically unsaturated monomers are used. Saturated monomers are mentioned. These monomers can be appropriately selected according to the object to be coated with the aqueous coating composition and the application.
 カルボキシル基を有するα,β-エチレン性不飽和モノマーとして、アクリル酸、メタクリル酸、アクリル酸二量体、クロトン酸、2-アクリロイルオキシエチルフタル酸、2-アクリロイルオキシエチルコハク酸、ω-カルボキシ-ポリカプロラクトンモノ(メタ)アクリレート、イソクロトン酸、α-ハイドロ-ω-((1-オキソ-2-プロペニル)オキシ)ポリ(オキシ(1-オキソ-1,6-ヘキサンジイル))、マレイン酸、フマル酸、イタコン酸などを挙げることができる。これらの中で好ましいものは、アクリル酸、メタクリル酸である。なお、本明細書において「(メタ)アクリル」とはアクリルとメタクリルとの両方を意味するものとする。 As an α, β-ethylenically unsaturated monomer having a carboxyl group, acrylic acid, methacrylic acid, acrylic acid dimer, crotonic acid, 2-acryloyloxyethylphthalic acid, 2-acryloyloxyethyl succinic acid, ω-carboxy- Polycaprolactone mono (meth) acrylate, isocrotonic acid, α-hydro-ω-((1-oxo-2-propenyl) oxy) poly (oxy (1-oxo-1,6-hexanediyl)), maleic acid, fumarate Examples thereof include acid and itaconic acid. Among these, acrylic acid and methacrylic acid are preferable. In this specification, “(meth) acryl” means both acrylic and methacrylic.
 アクリル樹脂エマルションの調製において、必要に応じてさらに、水酸基を有するα,β-エチレン性不飽和モノマーを用いてもよい。水酸基を有するα,β-エチレン性不飽和モノマーとしては、(メタ)アクリル酸ヒドロキシエチル、(メタ)アクリル酸ヒドロキシプロピル、(メタ)アクリル酸ヒドロキシブチル、アリルアルコール、メタクリルアルコールおよび/または(メタ)アクリル酸ヒドロキシエチルとε-カプロラクトンとの付加物を挙げることができる。これらの中で好ましいものは、(メタ)アクリル酸ヒドロキシエチル、(メタ)アクリル酸ヒドロキシブチルおよび/または(メタ)アクリル酸ヒドロキシエチルとε-カプロラクトンとの付加物である。 In the preparation of the acrylic resin emulsion, an α, β-ethylenically unsaturated monomer having a hydroxyl group may be used as necessary. Examples of the α, β-ethylenically unsaturated monomer having a hydroxyl group include hydroxyethyl (meth) acrylate, hydroxypropyl (meth) acrylate, hydroxybutyl (meth) acrylate, allyl alcohol, methacrylic alcohol and / or (meth). Mention may be made of adducts of hydroxyethyl acrylate and ε-caprolactone. Among these, preferred are hydroxyethyl (meth) acrylate, hydroxybutyl (meth) acrylate and / or an adduct of hydroxyethyl (meth) acrylate and ε-caprolactone.
 その他のα,β-エチレン性不飽和モノマーとしては、(メタ)アクリル酸エステル(例えば(メタ)アクリル酸メチル、(メタ)アクリル酸エチル、(メタ)アクリル酸n-プロピル、(メタ)アクリル酸n-ブチル、(メタ)アクリル酸イソブチル、(メタ)アクリル酸t-ブチル、(メタ)アクリル酸2-エチルヘキシル、メタクリル酸ラウリル、アクリル酸フェニル、(メタ)アクリル酸イソボルニル、メタクリル酸シクロヘキシル、(メタ)アクリル酸t-ブチルシクロヘキシル、(メタ)アクリル酸ジシクロペンタジエニル、(メタ)アクリル酸ジヒドロジシクロペンタジエニルなど)、重合性アミド化合物(例えば、(メタ)アクリルアミド、N-メチロール(メタ)アクリルアミド、N-ブトキシメチル(メタ)アクリルアミド、N,N-ジメチル(メタ)アクリルアミド、N,N-ジブチル(メタ)アクリルアミド、N,N-ジオクチル(メタ)アクリルアミド、N-モノブチル(メタ)アクリルアミド、N-モノオクチル(メタ)アクリルアミド2,4-ジヒドロキシ-4’-ビニルベンゾフェノン、N-(2-ヒドロキシエチル)アクリルアミド、N-(2-ヒドロキシエチル)メタクリルアミドなど)、重合性芳香族化合物(例えば、スチレン、α-メチルスチレン、ビニルケトン、t-ブチルスチレン、パラクロロスチレンおよびビニルナフタレンなど)、重合性ニトリル(例えば、アクリロニトリル、メタクリロニトリルなど)、α-オレフィン(例えば、エチレン、プロピレンなど)、ビニルエステル(例えば、酢酸ビニル、プロピオン酸ビニルなど)、ジエン(例えば、ブタジエン、イソプレンなど)、重合性芳香族化合物、重合性ニトリル、α-オレフィン、ビニルエステル、およびジエンを挙げることができる。これらは目的に応じて適宜選択することができる。 Other α, β-ethylenically unsaturated monomers include (meth) acrylic acid esters (eg methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, (meth) acrylic acid n-butyl, isobutyl (meth) acrylate, t-butyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, lauryl methacrylate, phenyl acrylate, isobornyl (meth) acrylate, cyclohexyl methacrylate, (meth ) T-butyl cyclohexyl acrylate, dicyclopentadienyl (meth) acrylate, dihydrodicyclopentadienyl (meth) acrylate), polymerizable amide compounds (eg (meth) acrylamide, N-methylol (meth) ) Acrylamide, N-butoxymethyl (meth) acrylic 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, N- (2-hydroxyethyl) methacrylamide, etc.), polymerizable aromatic compounds (for example, styrene, α-methylstyrene, vinyl ketone, t-butylstyrene, parachlorostyrene, vinylnaphthalene, etc.), polymerizable nitriles (eg, acrylonitrile, methacrylonitrile, etc.), α-olefins (eg, ethylene, propylene, etc.), vinyl esters (eg, vinyl acetate, propionic acid) Vinyl etc. ), Dienes (eg, butadiene, isoprene, etc.), polymerizable aromatic compounds, polymerizable nitriles, α-olefins, vinyl esters, and dienes. These can be appropriately selected according to the purpose.
 上記その他のα,β-エチレン性不飽和モノマーとして、架橋性モノマーを用いてもよい。ここで架橋性モノマーは、分子内に2つ以上のラジカル重合可能なエチレン性不飽和基を有する化合物であり、例えば、ジビニルベンゼン、エチレングリコールジ(メタ)アクリレート、ヘキサンジオールジ(メタ)アクリレート、ポリエチレングリコールジ(メタ)アクリレート、アリル(メタ)アクリレート、1,4-ブタンジオールジ(メタ)アクリレート、1,6-ヘキサンジ(メタ)アクリレート、ネオペンチルグリコールジ(メタ)アクリレート、ペンタエリスリトールジ(メタ)アクリレートなどのジビニル化合物、そして、トリアリルシアヌレート、ペンタエリスリトールトリ(メタ)アクリレート、トリメチロールプロパントリ(メタ)アクリレート、ジペンタエリスリトールヘキサ(メタ)アクリレートなどが挙げられる。架橋性モノマーは、上記のモノマーの組合せであってもよい。 A crosslinkable monomer may be used as the other α, β-ethylenically unsaturated monomer. Here, the crosslinkable monomer is a compound having two or more radically polymerizable ethylenically unsaturated groups in the molecule, such as divinylbenzene, ethylene glycol di (meth) acrylate, hexanediol di (meth) acrylate, Polyethylene glycol di (meth) acrylate, allyl (meth) acrylate, 1,4-butanediol di (meth) acrylate, 1,6-hexane di (meth) acrylate, neopentyl glycol di (meth) acrylate, pentaerythritol di (meth) ) Divinyl compounds such as acrylate, and triallyl cyanurate, pentaerythritol tri (meth) acrylate, trimethylolpropane tri (meth) acrylate, dipentaerythritol hexa (meth) acrylate, etc. . The crosslinkable monomer may be a combination of the above monomers.
 アクリル樹脂エマルションの調製における、水性媒体中での乳化重合は、例えば、水、または、水とアルコールまたはグリコールなどのような親水性の有機溶媒とを含む水性媒体中に、乳化剤を溶解させ、加熱撹拌下、原料として使用するα,β-エチレン性不飽和モノマーを混合したモノマー混合物および重合開始剤を滴下することにより行うことができる。原料として使用するα,β-エチレン性不飽和モノマーを混合したモノマー混合物は、乳化剤と水とを用いて予め乳化しておいてもよい。 In the preparation of an acrylic resin emulsion, emulsion polymerization in an aqueous medium is performed by, for example, dissolving an emulsifier in an aqueous medium containing water or a hydrophilic organic solvent such as water and alcohol or glycol, and heating. Under stirring, the polymerization can be carried out by dropping a monomer mixture obtained by mixing an α, β-ethylenically unsaturated monomer used as a raw material and a polymerization initiator. The monomer mixture obtained by mixing the α, β-ethylenically unsaturated monomer used as the raw material may be pre-emulsified using an emulsifier and water.
 乳化重合に好適に用いることができる重合開始剤としては、アゾ系の油性化合物(例えば、アゾビスイソブチロニトリル、2,2’-アゾビス(2-メチルブチロニトリル)および2,2’-アゾビス(2,4-ジメチルバレロニトリル)など)、および水性化合物(例えば、アニオン系の4,4’-アゾビス(4-シアノ吉草酸)、2,2-アゾビス(N-(2-カルボキシエチル)-2-メチルプロピオンアミジンおよびカチオン系の2,2’-アゾビス(2-メチルプロピオンアミジン));並びにレドックス系の油性過酸化物(例えば、ベンゾイルパーオキサイド、パラクロロベンゾイルパーオキサイド、ラウロイルパーオキサイドおよびt-ブチルパーベンゾエートなど)、および水性過酸化物(例えば、過硫酸カリおよび過硫酸アンモニウムなど)などが挙げられる。 Polymerization initiators that can be suitably used for emulsion polymerization include azo oily compounds (for example, azobisisobutyronitrile, 2,2′-azobis (2-methylbutyronitrile), and 2,2′- Azobis (2,4-dimethylvaleronitrile) and the like, and aqueous compounds (eg, anionic 4,4′-azobis (4-cyanovaleric acid), 2,2-azobis (N- (2-carboxyethyl)) -2-methylpropionamidine and cationic 2,2′-azobis (2-methylpropionamidine)); and redox oily peroxides (eg, benzoyl peroxide, parachlorobenzoyl peroxide, lauroyl peroxide and t-butyl perbenzoate) and aqueous peroxides (eg potassium persulfate and persulfate) Ammonium and the like) and the like.
 乳化剤は、当業者に通常使用されているものを用いることができる。乳化剤として、反応性乳化剤である、アントックス(Antox)MS-60(日本乳化剤社製)、エレミノールJS-2(三洋化成工業社製)、アデカリアソープNE-20(旭電化社製)およびアクアロンHS-10(第一工業製薬社製)などが特に好ましい。また、分子量を調節するために、ラウリルメルカプタンのようなメルカプタンおよびα-メチルスチレンダイマーなどのような連鎖移動剤を必要に応じて用いることができる。 As the emulsifier, those usually used by those skilled in the art can be used. As emulsifiers, reactive emulsifiers such as Antox MS-60 (manufactured by Nippon Emulsifier Co., Ltd.), Eleminol JS-2 (manufactured by Sanyo Kasei Kogyo Co., Ltd.), Adekari Soap NE-20 (manufactured by Asahi Denka Co., Ltd.) and Aqualon HS-10 (Daiichi Kogyo Seiyaku Co., Ltd.) is particularly preferred. In order to adjust the molecular weight, a mercaptan such as lauryl mercaptan and a chain transfer agent such as α-methylstyrene dimer can be used as necessary.
 反応温度は開始剤により決定され、例えば、アゾ系開始剤では60~90℃であり、レドックス系では30~70℃で行うことが好ましい。一般に、反応時間は1~8時間である。モノマー混合物の総量に対する開始剤の量は、一般に0.1~5質量%であり、好ましくは0.2~2質量%である。上記乳化重合は多段階で行うことができ、例えば、2段階で行うことができる。2段階乳化重合は、まず上記原料として使用するα,β-エチレン性不飽和モノマーを混合したもののうちの一部を乳化重合し、次いで上記α,β-エチレン性不飽和モノマー混合物の残りをさらに加えて乳化重合を行う重合方法である。2段階重合を行うことによって、コア部とシェル部とからなるコアシェル型アクリル樹脂エマルションを得ることができる。 The reaction temperature is determined by the initiator. For example, it is preferably 60 to 90 ° C. for an azo initiator and 30 to 70 ° C. for a redox system. In general, the reaction time is 1 to 8 hours. The amount of initiator relative to the total amount of monomer mixture is generally from 0.1 to 5% by weight, preferably from 0.2 to 2% by weight. The emulsion polymerization can be performed in multiple stages, for example, in two stages. In the two-stage emulsion polymerization, first, a part of the mixture of α, β-ethylenically unsaturated monomers used as the raw material is emulsion polymerized, and then the remainder of the α, β-ethylenically unsaturated monomer mixture is further added. In addition, it is a polymerization method in which emulsion polymerization is performed. By performing two-stage polymerization, a core-shell type acrylic resin emulsion composed of a core part and a shell part can be obtained.
 上記アクリル樹脂エマルションは、体積平均粒子径が20~500nmであるのが好ましく、50~200nmであるのがより好ましい。ここで体積平均粒子径とは、動的光散乱法によって決定される体積平均粒子径であり、具体的には、電気泳動光散乱光度計ELS-800(大塚電子社製)などを使用して測定することができる。 The volume average particle diameter of the acrylic resin emulsion is preferably 20 to 500 nm, and more preferably 50 to 200 nm. Here, the volume average particle diameter is a volume average particle diameter determined by a dynamic light scattering method. Specifically, an electrophoretic light scattering photometer ELS-800 (manufactured by Otsuka Electronics Co., Ltd.) is used. Can be measured.
 上記アクリル樹脂エマルションは、貯蔵安定性の観点から、塩基性化合物で中和することにより、pH5~10に調整することが好ましい。上記塩基性化合物は、アンモニア、メチルアミン、エチルアミン、ジメチルアミン、ジエチルアミン、トリメチルアミン、トリエチルアミン、ジメチルエタノールアミン、ジエタノールアミン、ジエチルアミノエタノール、トリエタノールアミン、テトラエチルアンモニウムヒドロキシド、プロピルアミン、ジプロピルアミン、トリプロピルアミン、ブチルアミン、ジブチルアミン、トリブチルアミンなどのアミン類ならびに水酸化ナトリウム、水酸化カリウムなどの水酸化物が挙げられる。上記中和は、乳化重合の前または後に、上記塩基性化合物を系に添加することによって行うことが好ましい。 From the viewpoint of storage stability, the acrylic resin emulsion is preferably adjusted to pH 5 to 10 by neutralizing with a basic compound. The basic compounds are ammonia, methylamine, ethylamine, dimethylamine, diethylamine, trimethylamine, triethylamine, dimethylethanolamine, diethanolamine, diethylaminoethanol, triethanolamine, tetraethylammonium hydroxide, propylamine, dipropylamine, tripropylamine. , Amines such as butylamine, dibutylamine and tributylamine, and hydroxides such as sodium hydroxide and potassium hydroxide. The neutralization is preferably performed by adding the basic compound to the system before or after emulsion polymerization.
 アクリル樹脂ディスパージョンは、例えば、上記重合性モノマーを溶液重合してアクリル樹脂を調製し、その後、得られたアクリル樹脂を水中に分散させることによって調製することができる。より具体的には、アクリル樹脂ディスパージョンは、上記カルボキシル基を有するα,β-エチレン性不飽和モノマーを必須成分とし、それ以外のα,β-エチレン性不飽和モノマーとともに溶液重合を行った後、塩基性化合物で中和し、水中に分散させることによって調製することができる。 The acrylic resin dispersion can be prepared, for example, by preparing an acrylic resin by solution polymerization of the polymerizable monomer, and then dispersing the obtained acrylic resin in water. More specifically, the acrylic resin dispersion contains the above α, β-ethylenically unsaturated monomer having a carboxyl group as an essential component, and after performing solution polymerization together with other α, β-ethylenically unsaturated monomers. It can be prepared by neutralizing with a basic compound and dispersing in water.
 上記溶液重合は、加熱条件下において、上記重合性モノマーの混合物を、重合開始剤と共に有機溶媒中へ滴下しながら撹拌する方法が一般的である。溶液重合は、例えば、重合温度60~160℃、滴下時間0.5~10時間の条件で行うことができる。上記重合性モノマーは、2段階に分けて重合させることもできる。重合性モノマーを、2段階に分けて重合を行うことによって、コア部とシェル部とからなるコアシェル型アクリル樹脂ディスパージョンを得ることができる。 The solution polymerization is generally a method in which the mixture of the polymerizable monomers is stirred while being dropped into an organic solvent together with a polymerization initiator under heating conditions. Solution polymerization can be carried out, for example, under conditions of a polymerization temperature of 60 to 160 ° C. and a dropping time of 0.5 to 10 hours. The polymerizable monomer can be polymerized in two stages. By polymerizing the polymerizable monomer in two stages, a core-shell type acrylic resin dispersion comprising a core part and a shell part can be obtained.
 上記重合開始剤は、通常の重合に用いられるものであれば特に限定されず、例えば、アゾ系化合物または過酸化物が挙げられる。一般に、モノマー混合物100質量部に対する重合開始剤の量は0.1~18質量部であり、好ましくは0.3~12質量部である。 The polymerization initiator is not particularly limited as long as it is used for normal polymerization, and examples thereof include azo compounds and peroxides. Generally, the amount of the polymerization initiator with respect to 100 parts by mass of the monomer mixture is 0.1 to 18 parts by mass, preferably 0.3 to 12 parts by mass.
 また、ここで用い得る溶媒は反応に悪影響を与えないものであれば特に限定されず、例えば、アルコール、ケトン、エーテルおよび炭化水素系溶媒などが挙げられる。さらに、分子量を調節するために、ラウリルメルカプタンのようなメルカプタン、および、α-メチルスチレンダイマーなどのような連鎖移動剤を必要に応じて用いることができる。 The solvent that can be used here is not particularly limited as long as it does not adversely affect the reaction, and examples thereof include alcohols, ketones, ethers, and hydrocarbon solvents. Furthermore, in order to adjust the molecular weight, a mercaptan such as lauryl mercaptan and a chain transfer agent such as α-methylstyrene dimer can be used as necessary.
 このように溶液重合で得られるアクリル樹脂の数平均分子量は、4,000~20,000であるのが好ましい。本明細書において、溶液重合で得られるアクリル樹脂の数平均分子量は、ポリスチレン標準サンプル基準を用いたゲルパーミエーションクロマトグラフィ(GPC)で測定することができる。 The number average molecular weight of the acrylic resin thus obtained by solution polymerization is preferably 4,000 to 20,000. In this specification, the number average molecular weight of the acrylic resin obtained by solution polymerization can be measured by gel permeation chromatography (GPC) using a polystyrene standard sample standard.
 上記溶液重合で得られたアクリル樹脂は、必要に応じて溶剤を除去した後、塩基性化合物を加えて中和して水性化することにより、アクリル樹脂ディスパージョンを得ることができる。上記塩基性化合物としては、先に挙げた塩基性化合物が挙げられる。上記塩基性化合物を加える量は、上記溶液重合で得られたアクリル樹脂が有するカルボキシル基の中和率が60~100%となる量であることが好ましい。中和率が60%未満となる量である場合は、アクリル樹脂ディスパージョンの水分散性が低くなり、貯蔵安定性に劣るおそれがある。 An acrylic resin dispersion can be obtained by removing the solvent as necessary from the acrylic resin obtained by the solution polymerization and neutralizing it by adding a basic compound. Examples of the basic compound include the basic compounds listed above. The amount of the basic compound added is preferably such an amount that the neutralization rate of the carboxyl group of the acrylic resin obtained by the solution polymerization is 60 to 100%. When the neutralization rate is less than 60%, the water dispersibility of the acrylic resin dispersion becomes low and the storage stability may be poor.
 アクリル樹脂ディスパージョンは、動的光散乱法によって決定される体積平均粒子径が10~1000nmの範囲内であることが好ましい。体積平均粒子径が上記範囲内であることによって、水分散体の安定性が良好となり、さらに、得られる塗膜の外観が良好となるという利点がある。
 上記アクリル樹脂ディスパージョンは、体積平均粒子径が10~1000nmであるのが好ましく、100~800nmであるのがより好ましい。
The acrylic resin dispersion preferably has a volume average particle diameter determined by a dynamic light scattering method in the range of 10 to 1000 nm. When the volume average particle diameter is in the above range, there is an advantage that the stability of the aqueous dispersion is improved and the appearance of the obtained coating film is improved.
The acrylic resin dispersion preferably has a volume average particle diameter of 10 to 1000 nm, and more preferably 100 to 800 nm.
 シリコーン含有アクリル樹脂エマルションは、例えば、アクリル樹脂エマルションの調製において用いられる上記重合性モノマーに加えて、アルコキシシリル基含有重合性モノマーを更に含有するモノマー組成物の重合によって得られる重合体などを挙げることができる。 Examples of the silicone-containing acrylic resin emulsion include a polymer obtained by polymerization of a monomer composition further containing an alkoxysilyl group-containing polymerizable monomer in addition to the polymerizable monomer used in the preparation of the acrylic resin emulsion. Can do.
 上記アルコキシシリル基含有重合性モノマーは、炭素数1~14のアルコキシシリル基を含有する重合性モノマーであれば特に限定されず、例えば、(メタ)アクリル酸トリメトキシシリルプロピル、(メタ)アクリル酸トリエトキシシリルプロピル、(メタ)アクリル酸トリブトキシシリルプロピル、(メタ)アクリル酸ジメトキシメチルシリルプロピル、(メタ)アクリル酸メトキシジメチルシリルプロピル、ビニルトリメトキシシラン、ビニルトリエトキシシラン、ビニルジメトキシメチルシラン、ビニルメトキシジメチルシラン、ビニルトリス(β-メトキシエトキシ)シランなどを挙げることができる。これらは1種類または2種類以上を混合して使用することができる。これらのうち、特に、(メタ)アクリル酸トリメトキシシリルプロピル、(メタ)アクリル酸トリエトキシシリルプロピル、ビニルトリメトキシシラン、ビニルトリエトキシシランなどを挙げることができる。 The alkoxysilyl group-containing polymerizable monomer is not particularly limited as long as it is a polymerizable monomer containing an alkoxysilyl group having 1 to 14 carbon atoms. For example, trimethoxysilylpropyl (meth) acrylate, (meth) acrylic acid Triethoxysilylpropyl, tributoxysilylpropyl (meth) acrylate, dimethoxymethylsilylpropyl (meth) acrylate, methoxydimethylsilylpropyl (meth) acrylate, vinyltrimethoxysilane, vinyltriethoxysilane, vinyldimethoxymethylsilane, Examples thereof include vinylmethoxydimethylsilane and vinyltris (β-methoxyethoxy) silane. These can be used alone or in combination of two or more. Among these, in particular, trimethoxysilylpropyl (meth) acrylate, triethoxysilylpropyl (meth) acrylate, vinyltrimethoxysilane, vinyltriethoxysilane and the like can be mentioned.
 さらに、シリコーン含有アクリル樹脂エマルションは、有機シリコーン単位を導入してもよい。有機シリコーン単位を導入する方法としては、有機シリコーン化合物(例えば、オルガノシラン、オルガノシランの加水分解物、オルガノシランの縮合物など)およびアクリル重合性モノマーの混合物を乳化重合し加水分解、縮合反応およびラジカル重合を行う方法、シリコーン官能基を有するモノマーを共重合する方法、アクリル重合体に対して有機シリコーン化合物を反応させることにより、アクリル重合体粒子表面に有機シリコーン化合物を結合させる方法などが挙げられる。上記の2以上の方法を組み合わせるものであってもよい。 Furthermore, an organic silicone unit may be introduced into the silicone-containing acrylic resin emulsion. As a method for introducing the organosilicone unit, a mixture of an organosilicone compound (for example, organosilane, a hydrolyzate of organosilane, a condensate of organosilane, etc.) and an acrylic polymerizable monomer is subjected to emulsion polymerization, hydrolysis, condensation reaction and Examples include a method of performing radical polymerization, a method of copolymerizing a monomer having a silicone functional group, and a method of bonding an organosilicone compound to the surface of acrylic polymer particles by reacting an organosilicone compound with an acrylic polymer. . Two or more methods described above may be combined.
 上記オルガノシランとしては、特に限定されず、例えば、テトラメトキシシラン、テトラエトキシシラン、テトラ-n-プロポキシシラン、テトラ-i-プロポキシシラン、テトラ-n-ブトキシシランなどのテトラアルコキシシラン類;メチルトリメトキシシラン、メチルトリエトキシシラン、エチルトリメトキシシラン、エチルトリエトキシシラン、n-プロピルトリメトキシシラン、n-プロピルトリエトキシシラン、i-プロピルトリメトキシシラン、i-プロピルトリエトキシシラン、n-ブチルトリメトキシシラン、n-ブチルトリエトキシシラン、n-ペンチルトリメトキシシラン、n-ヘキシルトリメトキシシラン、n-ヘプチルトリメトキシシラン、n-オクチルトリメトキシシラン、ビニルトリメトキシシラン、ビニルトリエトキシシラン、シクロヘキシルトリメトキシシラン、シクロヘキシルトリエトキシシラン、フェニルトリメトキシシラン、フェニルトリエトキシシラン、3-クロロプロピルトリメトキシシラン、3-クロロプロピルトリエトキシシラン、3,3,3-トリフルオロプロピルトリメトキシシラン、3,3,3-トリフルオロプロピルトリエトキシシラン、3-アミノプロピルトリメトキシシラン、3-アミノプロピルトリエトキシシラン、2-ヒドロキシエチルトリメトキシシラン、2-ヒドロキシエチルトリエトキシシラン、2-ヒドロキシプロピルトリメトキシシラン、2-ヒドロキシプロピルトリエトキシシラン、3-ヒドロキシプロピルトリメトキシシラン、3-ヒドロキシプロピルトリエトキシシラン、3-メルカプトプロピルトリメトキシシラン、3-メルカプトプロピルトリエトキシシラン、3-イソシアナートプロピルトリメトキシシラン、3-イソシアナートプロピルトリエトキシシラン、3-グリシドキシプロピルトリメトキシシラン、3-グリシドキシプロピルトリエトキシシラン、2-(3,4-エポキシシクロヘキシル)エチルトリメトキシシラン、2-(3,4-エポキシシクロヘキシル)エチルトリエトキシシラン、3-(メタ)アクリルオキシプロピルトリメトキシシラン、3-(メタ)アタクリルオキシプロピルトリエトキシシラン、3-ウレイドプロピルトリメトキシシラン、3-ウレイドプロピルトリエトキシシランなどのトリアルコキシシラン類;ジメチルジメトキシシラン、ジメチルジエトキシシラン、ジエチルジメトキシシラン、ジエチルジエトキシシラン、ジ-n-プロピルジメトキシシラン、ジ-n-プロピルジエトキシシラン、ジ-i-プロピルジメトキシシラン、ジ-i-プロピルジエトキシシラン、ジ-n-ブチルジメトキシシラン、ジ-n-ブチルジエトキシシラン、ジ-n-ペンチルジメトキシシラン、ジ-n-ペンチルジエトキシシラン、ジ-n-ヘキシルジメトキシシラン、ジ-n-ヘキシルジエトキシシラン、ジ-n-ヘプチルジメトキシシラン、ジ-n-ヘプチルジエトキシシラン、ジ-n-オクチルジメトキシシラン、ジ-n-オクチルジエトキシシラン、ジ-n-シクロヘキシルジメトキシシラン、ジ-n-シクロヘキシルジエトキシシラン、ジフェニルジメトキシシラン、ジフェニルジエトキシシランなどのジアルコキシシラン類のほか、メチルトリアセチルオキシシラン、ジメチルジアセチルオキシシランなどを挙げることができる。 The organosilane is not particularly limited, and examples thereof include tetraalkoxysilanes such as tetramethoxysilane, tetraethoxysilane, tetra-n-propoxysilane, tetra-i-propoxysilane, tetra-n-butoxysilane; Methoxysilane, methyltriethoxysilane, ethyltrimethoxysilane, ethyltriethoxysilane, n-propyltrimethoxysilane, n-propyltriethoxysilane, i-propyltrimethoxysilane, i-propyltriethoxysilane, n-butyltri Methoxysilane, n-butyltriethoxysilane, n-pentyltrimethoxysilane, n-hexyltrimethoxysilane, n-heptyltrimethoxysilane, n-octyltrimethoxysilane, vinyltrimethoxysilane, vinyl Triethoxysilane, cyclohexyltrimethoxysilane, cyclohexyltriethoxysilane, phenyltrimethoxysilane, phenyltriethoxysilane, 3-chloropropyltrimethoxysilane, 3-chloropropyltriethoxysilane, 3,3,3-trifluoropropyltri Methoxysilane, 3,3,3-trifluoropropyltriethoxysilane, 3-aminopropyltrimethoxysilane, 3-aminopropyltriethoxysilane, 2-hydroxyethyltrimethoxysilane, 2-hydroxyethyltriethoxysilane, 2- Hydroxypropyltrimethoxysilane, 2-hydroxypropyltriethoxysilane, 3-hydroxypropyltrimethoxysilane, 3-hydroxypropyltriethoxysilane, 3-mercaptop Pyrtrimethoxysilane, 3-mercaptopropyltriethoxysilane, 3-isocyanatopropyltrimethoxysilane, 3-isocyanatopropyltriethoxysilane, 3-glycidoxypropyltrimethoxysilane, 3-glycidoxypropyltriethoxysilane 2- (3,4-epoxycyclohexyl) ethyltrimethoxysilane, 2- (3,4-epoxycyclohexyl) ethyltriethoxysilane, 3- (meth) acryloxypropyltrimethoxysilane, 3- (meth) atacryl Trialkoxysilanes such as oxypropyltriethoxysilane, 3-ureidopropyltrimethoxysilane, 3-ureidopropyltriethoxysilane; dimethyldimethoxysilane, dimethyldiethoxysilane, diethyldimethoxysila Diethyldiethoxysilane, di-n-propyldimethoxysilane, di-n-propyldiethoxysilane, di-i-propyldimethoxysilane, di-i-propyldiethoxysilane, di-n-butyldimethoxysilane, di- -N-butyldiethoxysilane, di-n-pentyldimethoxysilane, di-n-pentyldiethoxysilane, di-n-hexyldimethoxysilane, di-n-hexyldiethoxysilane, di-n-heptyldimethoxysilane, Di-n-heptyldiethoxysilane, di-n-octyldimethoxysilane, di-n-octyldiethoxysilane, di-n-cyclohexyldimethoxysilane, di-n-cyclohexyldiethoxysilane, diphenyldimethoxysilane, diphenyldiethoxy Dialkoxysilanes such as silane , Methyl triacetyl silane, dimethyl acetyloxy silane and the like.
 水性樹脂分散体としては、上記以外にも、当業者において通常用いられる、ウレタン樹脂エマルション、酢酸ビニル樹脂エマルション、フッ素樹脂エマルション、塩化ビニル樹脂エマルションなどを用いることもできる。 As the aqueous resin dispersion, in addition to the above, urethane resin emulsions, vinyl acetate resin emulsions, fluororesin emulsions, vinyl chloride resin emulsions and the like that are commonly used by those skilled in the art can also be used.
 水性塗料組成物中に含まれる水性樹脂分散体の量は、樹脂固形分量として、水性塗料組成物100質量部に対して5~50質量部であるのが好ましい。 The amount of the aqueous resin dispersion contained in the aqueous coating composition is preferably 5 to 50 parts by mass with respect to 100 parts by mass of the aqueous coating composition as the resin solid content.
  その他の成分
 上記水性樹脂分散体は、硬化剤と反応して硬化する反応硬化型樹脂であってもよく、硬化剤を必要としない融着型樹脂であってもよい。硬化剤として、例えば、カルボジイミド硬化剤、メラミン硬化剤、イソシアネート硬化剤などを用いることができる。
Other Components The aqueous resin dispersion may be a reaction curable resin that is cured by reacting with a curing agent, or may be a fusion resin that does not require a curing agent. As the curing agent, for example, a carbodiimide curing agent, a melamine curing agent, an isocyanate curing agent, or the like can be used.
 本発明における水性塗料組成物は、上記成分に加えて、必要に応じた他の成分を含んでもよい。他の成分として、例えば、造膜助剤、増粘剤、多官能アミン重合体、カップリング剤、可塑剤、架橋樹脂粒子、顔料、表面調整剤、防腐剤、防かび剤、消泡剤、光安定剤、紫外線吸収剤、酸化防止剤、pH調整剤などが挙げられる。 The aqueous coating composition in the present invention may contain other components as required in addition to the above components. As other components, for example, a film-forming aid, a thickener, a polyfunctional amine polymer, a coupling agent, a plasticizer, a crosslinked resin particle, a pigment, a surface conditioner, an antiseptic, an antifungal agent, an antifoaming agent, Examples thereof include a light stabilizer, an ultraviolet absorber, an antioxidant, and a pH adjuster.
 水性塗料組成物は、水を溶媒として含む。水性塗料組成物は、水に加えて、アルコールまたはグリコールなどのような親水性の有機溶媒を必要に応じて含んでもよい。 The water-based paint composition contains water as a solvent. The water-based coating composition may contain a hydrophilic organic solvent such as alcohol or glycol, if necessary, in addition to water.
 水性塗料組成物の調製法としては特に限定されず、上述した各成分を、攪拌機などにより攪拌することによって調製することができる。水性塗料組成物中に顔料または意匠材料が含まれる場合は、分散性のよいものは攪拌機により混合することができ、他の方法として、水、界面活性剤または分散剤などを含むビヒクルにサンドグラインドミルなどを用いて予め分散させたものを加えることもできる。 The method for preparing the aqueous coating composition is not particularly limited, and can be prepared by stirring the above-described components with a stirrer or the like. When pigments or design materials are included in the aqueous coating composition, those having good dispersibility can be mixed with a stirrer, and as another method, a sand grind is added to a vehicle containing water, a surfactant or a dispersant. What was previously disperse | distributed using the mill etc. can also be added.
塗膜形成方法
 本発明の塗膜形成方法の1態様として、
 水性塗料組成物を塗装する塗装工程、
 上記塗装によって得られた塗膜を、水分を含有する最上層および塗膜形成層に分離する、塗膜分離工程、および
 上記水分を含有する最上層を、乾燥以外の方法によって除去する、水分除去工程、
を包含する方法が挙げられる。
Coating Film Forming Method As one aspect of the coating film forming method of the present invention,
A painting process for painting a water-based paint composition;
The coating film obtained by the above coating is separated into a top layer containing water and a coating layer, a coating film separating step, and the top layer containing water is removed by a method other than drying. Process,
The method of including is mentioned.
 図1は、この塗膜形成方法を示す概略説明図である。水分を除去する方法は、乾燥以外の方法であれば任意の方法を用いることができる。 FIG. 1 is a schematic explanatory view showing this coating film forming method. As a method for removing moisture, any method other than drying can be used.
 なお本発明の方法においては、水分を含有する最上層を、乾燥以外の方法によって除去する、水分除去工程が包含されていればよく、そして本発明の方法において、乾燥によって多少の水分が除去されることを排除するものではない。具体的には、塗膜分離工程において、塗装によって得られた塗膜に含まれる水分が、多少蒸発する態様についても、その後に水分除去工程が行われる限り、本発明の方法に該当する。 In the method of the present invention, it is only necessary to include a moisture removing step of removing the uppermost layer containing moisture by a method other than drying, and in the method of the present invention, some moisture is removed by drying. It does not exclude that. Specifically, in the coating film separation step, the aspect in which the moisture contained in the coating film obtained by painting is evaporated somewhat corresponds to the method of the present invention as long as the water removal step is performed thereafter.
 水性塗料組成物を塗装する被塗物として、任意の基材が挙げられる。基材としては、例えば、金属、木材、プラスティックス、ゴム、石材、スレート、コンクリート、モルタル、繊維、紙、ガラス、磁器、陶器、フィルム、およびこれらの複合体などが挙げられる。これらの基材は、必要に応じて、下塗り塗膜などの塗膜が予め設けられていてもよい。 Arbitrary base material is mentioned as a to-be-coated object which coats water-based paint composition. Examples of the substrate include metal, wood, plastics, rubber, stone, slate, concrete, mortar, fiber, paper, glass, porcelain, earthenware, film, and composites thereof. These substrates may be provided with a coating such as an undercoat coating as necessary.
 水性塗料組成物の塗装方法としては、被塗物(基材)の種類および形状などに応じた、任意の適切な方法を用いることができる。水性塗料組成物を塗装する方法として、例えば、浸漬、刷毛、流し塗り、ローラー、ロールコーター、エアースプレー、エアレススプレー、カーテンフローコーター、ローラーカーテンコーター、ダイコーターなどの一般に用いられている塗装方法などを用いることができる。 As a coating method of the water-based paint composition, any appropriate method can be used according to the type and shape of the article (base material) to be coated. As a method for applying the aqueous coating composition, for example, commonly used coating methods such as dipping, brushing, flow coating, roller, roll coater, air spray, airless spray, curtain flow coater, roller curtain coater, die coater, etc. Can be used.
 水性塗料組成物は、水分除去後の膜厚として5~1000μmとなるように塗装することが好ましく、20~300μmとなるように塗装することがより好ましい。 The aqueous coating composition is preferably applied so that the film thickness after removing water is 5 to 1000 μm, more preferably 20 to 300 μm.
 水性塗料組成物の塗装によって得られた塗膜を、水分を含有する最上層および塗膜形成層に分離させる(塗膜分離工程)。この塗膜分離工程として、例えば、塗装により得られた塗膜を、2秒~24時間の間、静置する方法などが挙げられる。 The coating film obtained by coating the aqueous coating composition is separated into a water-containing uppermost layer and a coating film forming layer (coating film separation step). Examples of the coating film separating step include a method in which a coating film obtained by painting is allowed to stand for 2 seconds to 24 hours.
 水分を含有する最上層は、水分のみを含んでもよく、または後述する水分吸収剤および/または水分離促進剤を含んでもよい。また水分を含有する最上層は、水性塗料組成物中に含まれる上記添加剤や、若干量の塗膜形成成分等を含んでもよい。 The uppermost layer containing moisture may contain only moisture, or may contain a moisture absorbent and / or a water separation accelerator described later. Further, the uppermost layer containing water may contain the above-mentioned additive contained in the aqueous coating composition, a slight amount of a film-forming component, and the like.
 塗膜形成層は、水性塗料組成物中に含まれる塗膜形成成分を含む層である。塗膜形成成分として、上記水性樹脂分散体、そして必要に応じたその他の成分などが挙げられる。塗膜形成層は塗膜形成成分に加えて、各種添加剤を含んでもよい。 The coating film forming layer is a layer containing a coating film forming component contained in the aqueous coating composition. Examples of the coating film forming component include the aqueous resin dispersion and other components as required. The coating film forming layer may contain various additives in addition to the coating film forming component.
 塗装によって得られた塗膜の、水分を含有する最上層および塗膜形成層への分離をもたらし、そしてこの分離を促進させる手段の1つとして、例えば、上記塗装工程の前に、水性塗料組成物に水分離促進剤を加える(水分離促進剤混合工程)方法が挙げられる。水分離促進剤として、例えば、有機酸、無機酸、酸無水物、pH緩衝液、金属塩、塩基性化合物、高分子凝集剤などが挙げられる。 As one means for bringing about and facilitating separation of the coating film obtained by coating into a water-containing uppermost layer and a film-forming layer, for example, before the coating step, an aqueous coating composition And a method of adding a water separation accelerator to the product (water separation accelerator mixing step). Examples of the water separation accelerator include organic acids, inorganic acids, acid anhydrides, pH buffer solutions, metal salts, basic compounds, and polymer flocculants.
 ここでいう分離、具体的には水分を含有する最上層および塗膜形成層への分離、とは、樹脂エマルションなどの水性樹脂分散体を所定の不安定条件下に置くことで、樹脂成分などを意図的に凝集させ析出させることによって、水性樹脂分散体を構成する樹脂成分と水分とを分離させることを意味する。このような分離において、例出する水分離促進剤がどのようなメカニズムで機能するかについては明らかにされていない部分も多いが、基本的な作用機構は、以下のように推定される。水分離促進剤が金属塩である場合は、塩の強い水和力により水性樹脂分散体中の水を水和水として固定化し、水性樹脂分散体の安定化を低下させる塩析作用によるものと考えられる。また、水分離促進剤が、有機酸、無機酸、酸無水物または塩基性化合物である場合は、いわゆる凝析作用が働くものと考えられる。すなわち、水分離促進剤が静電引力により水性樹脂分散体のイオン性基に電気的相互作用を及ぼすことで、水性樹脂分散体粒子表面のゼータ電位が低下し、脱水和され、水性樹脂分散体粒子同士の合一により樹脂成分が疎水化し、水性樹脂分散体の樹脂成分が水から分離されていくと考えられる。また、水分離促進剤が高分子凝集剤である場合には、これらの作用とともに凝結作用といわれる高分子凝集剤の高分子鎖が水性樹脂分散体の樹脂成分に対する橋かけ吸着をおこし、高分子凝集剤を介して水性樹脂分散体同士を合一させ、樹脂成分を疎水化させることで、樹脂成分と水分との分離が促進されると考えられる。 Separation here, specifically, separation into the uppermost layer containing water and the coating film-forming layer means that an aqueous resin dispersion such as a resin emulsion is placed under a predetermined unstable condition, and a resin component, etc. By intentionally aggregating and precipitating the water, the resin component constituting the aqueous resin dispersion and water are separated. In such separation, there are many parts that have not been clarified as to what kind of mechanism the water separation promoter to be described functions in, but the basic mechanism of action is estimated as follows. When the water separation accelerator is a metal salt, the salt in the aqueous resin dispersion is fixed as hydrated water due to the strong hydration power of the salt, thereby reducing the stability of the aqueous resin dispersion. Conceivable. In addition, when the water separation accelerator is an organic acid, an inorganic acid, an acid anhydride, or a basic compound, a so-called coagulation action is considered to work. That is, the water separation accelerator exerts an electrical interaction with the ionic group of the aqueous resin dispersion by electrostatic attraction, so that the zeta potential on the surface of the aqueous resin dispersion particle is lowered and dehydrated. It is considered that the resin component becomes hydrophobic due to the coalescence of the particles, and the resin component of the aqueous resin dispersion is separated from the water. In addition, when the water separation accelerator is a polymer flocculant, the polymer chain of the polymer flocculant called a coagulation action together with these actions causes cross-linking adsorption to the resin component of the aqueous resin dispersion, and the polymer It is considered that separation of the resin component and moisture is promoted by bringing the aqueous resin dispersions together through a flocculant and making the resin component hydrophobic.
 水分離促進剤として用いることができる有機酸として、例えば、
一価カルボン酸(例えば、酢酸、安息香酸、プロピオン酸、蟻酸など)、
二価カルボン酸(例えば、マレイン酸、フマル酸、コハク酸、シュウ酸など)、
有機スルホン酸(例えば、メタンスルホン酸、パラトルエンスルホン酸、ベンゼンスルホン酸、アミノエチルスルホン酸など)、
などが挙げられる。
 水分離促進剤として用いることができる無機酸として、例えば、塩酸、硝酸、硫酸、リン酸などが挙げられる。
 水分離促進剤として用いることができる酸無水物として、上記有機酸または無機酸の2分子が脱水縮合したものを挙げることができる。酸無水物の具体例として、例えば、無水酢酸、無水安息香酸、二硫酸(ピロ硫酸)、ピロリン酸(二リン酸)、五酸化二リン(十酸化四リン)、無水プロピオン酸などが挙げられる。
 酸無水物としてさらに、上記二価カルボン酸の分子内脱水縮合物も用いることができる。このような縮合物として、例えば、無水マレイン酸、無水フマル酸などが挙げられる。
 水分離促進剤として用いることができるpH緩衝液として、例えば、酢酸緩衝液、リン酸緩衝液、クエン酸緩衝液、トリス緩衝液、ホウ酸緩衝液などが挙げられる。また、これらのpH緩衝液の調製に用いられる緩衝剤組成物を、水性塗料組成物に直接添加する態様であってもよい。
 水分離促進剤として用いることができる金属塩として、例えば、アルミニウム塩(例えば、硫酸アルミニウム、ポリ塩化アルミニウムなど)、鉄塩(例えば、ポリ硫酸第二鉄、塩化第二鉄など)、ナトリウム塩(例えば、塩化ナトリウム、硫酸ナトリウムなど)、カルシウム塩(例えば、塩化カルシウムなど)、マグネシウム塩(例えば、塩化マグネシウムなど)などが挙げられる。
 水分離促進剤として用いることができる高分子凝集剤として、例えば、
カチオン系高分子凝集剤では、ジメチルアミノエチルメタアクリレートメチレンクロライド塩、ジアリルジメチルアンモニウムクロライド、アニリン樹脂塩酸塩、ポリアミン誘導体、ポリチオウレア酢酸塩、ポリエチレンアミノトリアゾール、ポリビニルベンジルトリメチルアンモニウムクロライド、ポリエチレンイミン、ビニルピリジン共重合物塩など、そして、アニオン系高分子凝集剤では、ポリ(メタ)アクリル酸ナトリウム、マレイン酸共重合物塩、イタコン酸共重合物塩、ポリアクリルアミド部分加水分解物塩、アルギン酸ナトリウム、カルボキシメチルセルロースナトリウム塩、ポリヒドロキシシロキサン化合物など、
が挙げられる。他にも、両性高分子凝集剤として、ゼラチン、上記アニオン単位とカチオン単位との共重合体など、ノニオン系高分子凝集剤としてポリアクリルアミド、ポリオキシエチレン、水溶性ウレア、デンプンなどを、適宜用いることができる。中でもアルコキシシランの加水分解縮合物であるポリヒドロキシシロキサン化合物は、比較的pKaが大きいため、系の不安定化を起こす急激な凝集を起こすことはないが、比較的大きな高分子構造を有しているので、前述の橋かけ吸着作用をより効率的にもたらし、均一に系全体の凝集が進行することで、速やかな水分離を起こす優れた水分離促進剤である。
 水分離促進剤として用いることができる塩基性化合物として、例えば、アンモニア、メチルアミン、エチルアミン、ジメチルアミン、ジエチルアミン、トリメチルアミン、トリエチルアミン、ジメチルエタノールアミン、ジエタノールアミン、ジエチルアミノエタノール、トリエタノールアミン、テトラエチルアンモニウムヒドロキシド、プロピルアミン、ジプロピルアミン、トリプロピルアミン、ブチルアミン、ジブチルアミン、トリブチルアミンなどのアミン類ならびに水酸化ナトリウム、水酸化カリウムなどの水酸化物が挙げられる。
 これらの水分離促進剤は、1種を単独で用いてもよく、2種以上を併用してもよい。
As an organic acid that can be used as a water separation accelerator, for example,
Monovalent carboxylic acids (eg, acetic acid, benzoic acid, propionic acid, formic acid, etc.),
Divalent carboxylic acids (eg, maleic acid, fumaric acid, succinic acid, oxalic acid, etc.),
Organic sulfonic acids (for example, methanesulfonic acid, paratoluenesulfonic acid, benzenesulfonic acid, aminoethylsulfonic acid, etc.),
Etc.
Examples of the inorganic acid that can be used as the water separation accelerator include hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, and the like.
Examples of the acid anhydride that can be used as a water separation accelerator include those obtained by dehydration condensation of two molecules of the organic acid or inorganic acid. Specific examples of the acid anhydride include, for example, acetic anhydride, benzoic anhydride, disulfuric acid (pyrosulfuric acid), pyrophosphoric acid (diphosphoric acid), diphosphorus pentoxide (phosphorus tetraoxide), and propionic anhydride. .
As the acid anhydride, an intramolecular dehydration condensate of the above divalent carboxylic acid can also be used. Examples of such condensates include maleic anhydride and fumaric anhydride.
Examples of the pH buffer that can be used as the water separation accelerator include acetate buffer, phosphate buffer, citrate buffer, Tris buffer, and borate buffer. Moreover, the buffer agent composition used for preparation of these pH buffer solutions may be added directly to the aqueous coating composition.
Examples of metal salts that can be used as a water separation accelerator include aluminum salts (eg, aluminum sulfate, polyaluminum chloride, etc.), iron salts (eg, polyferric sulfate, ferric chloride, etc.), sodium salts ( Examples thereof include sodium chloride, sodium sulfate, etc., calcium salts (eg, calcium chloride), magnesium salts (eg, magnesium chloride), and the like.
As a polymer flocculant that can be used as a water separation accelerator, for example,
For cationic polymer flocculants, dimethylaminoethyl methacrylate methylene chloride, diallyldimethylammonium chloride, aniline resin hydrochloride, polyamine derivatives, polythiourea acetate, polyethyleneaminotriazole, polyvinylbenzyltrimethylammonium chloride, polyethyleneimine, vinylpyridine In the case of anionic polymer flocculants such as copolymer salts, sodium poly (meth) acrylate, maleic acid copolymer salt, itaconic acid copolymer salt, polyacrylamide partial hydrolyzate salt, sodium alginate, carboxy Methyl cellulose sodium salt, polyhydroxysiloxane compound, etc.
Is mentioned. In addition, gelatin, a copolymer of the above-mentioned anion unit and cation unit, etc. are used as the amphoteric polymer flocculant, and polyacrylamide, polyoxyethylene, water-soluble urea, starch, etc. are appropriately used as the nonionic polymer flocculant. be able to. Among them, the polyhydroxysiloxane compound, which is a hydrolyzed condensate of alkoxysilane, has a relatively large pKa, so it does not cause abrupt aggregation that causes destabilization of the system, but has a relatively large polymer structure. Therefore, it is an excellent water separation accelerator that causes the above-mentioned cross-linking adsorption action more efficiently and causes rapid water separation by uniformly aggregating the entire system.
Examples of basic compounds that can be used as a water separation accelerator include ammonia, methylamine, ethylamine, dimethylamine, diethylamine, trimethylamine, triethylamine, dimethylethanolamine, diethanolamine, diethylaminoethanol, triethanolamine, tetraethylammonium hydroxide, Examples include amines such as propylamine, dipropylamine, tripropylamine, butylamine, dibutylamine and tributylamine, and hydroxides such as sodium hydroxide and potassium hydroxide.
These water separation promoters may be used alone or in combination of two or more.
 水分離促進剤として、有機酸(例えば酢酸、プロピオン酸など)、酸無水物(例えば無水酢酸、無水プロピオン酸など)および高分子凝集剤からなる群から選択される少なくとも1種を用いるのが好ましい。 As the water separation accelerator, it is preferable to use at least one selected from the group consisting of organic acids (eg, acetic acid, propionic acid, etc.), acid anhydrides (eg, acetic anhydride, propionic anhydride, etc.) and polymer flocculants. .
 水分離促進剤として、高分子凝集剤の1種であるアニオン系高分子凝集剤を用いるのがより好ましく、ポリヒドロキシシロキサン化合物を用いるのがさらに好ましい。水分離促進剤としてより好ましく用いられるポリヒドロキシシロキサン化合物の調製は、モノ、ジ、トリ、テトラアルコキシシランの単独あるいは複数から選ばれる原料を、加水分解、縮合することによって得ることが一般的である。
 具体的な製法としては特に限定はされないが、特許3599277号、5048395号等に記載される公知の手段を用いることができる。
As the water separation accelerator, it is more preferable to use an anionic polymer flocculant which is one type of polymer flocculant, and it is more preferable to use a polyhydroxysiloxane compound. Preparation of a polyhydroxysiloxane compound more preferably used as a water separation accelerator is generally obtained by hydrolysis or condensation of a raw material selected from mono-, di-, tri-, and tetraalkoxysilanes alone or from a plurality thereof. .
Although it does not specifically limit as a specific manufacturing method, The well-known means described in patent 3599277, 5048395 grade | etc., Can be used.
 水分離促進剤を水性塗料組成物に加える場合は、塗膜形成樹脂成分の安定性を損なう量を加える。具体的には、水性塗料組成物100質量部に対して、0.01~50質量部となる量で加えるのが好ましく、0.1~20質量部となる量で加えるのがより好ましい。0.01質量部未満であると、水分離促進剤としての効果が十分に発揮されないおそれがある。50質量部を超えると、塗膜の硬化性や耐水性などの各種塗膜物性が低下するおそれがある。水性塗料組成物に水分離促進剤を加える手法として、一般的な混合方法を用いることができる。 When adding a water separation accelerator to the aqueous coating composition, an amount that impairs the stability of the film-forming resin component is added. Specifically, it is preferably added in an amount of 0.01 to 50 parts by mass, more preferably 0.1 to 20 parts by mass with respect to 100 parts by mass of the aqueous coating composition. There exists a possibility that the effect as a water-separation promoter may not fully be exhibited as it is less than 0.01 mass part. If it exceeds 50 parts by mass, various coating film properties such as the curability and water resistance of the coating film may be deteriorated. As a method for adding a water separation accelerator to the aqueous coating composition, a general mixing method can be used.
 本発明の方法においては、上記塗膜分離工程によって得られた、水分を含有する最上層を、乾燥以外の方法によって除去する(水分除去工程)。ここで「水分を含有する最上層を乾燥以外の方法によって除去」するとは、水性塗料組成物から形成された塗膜中に含まれている水分を、塗装後に、乾燥以外の方法によって除去することを意味する。このような方法の具体例として、例えば、塗装によって得られた塗膜を傾けることなどによって、重力により水分を含有する最上層を流し落とす方法、水分吸収剤を含む最上層を、手または空気で除去するまたは必要に応じて任意の器具を用いて除去するなどの除去方法、水分吸収材料に最上層の水分を吸収させて水分を取り除く方法などが挙げられる。 In the method of the present invention, the uppermost layer containing water obtained by the coating film separating step is removed by a method other than drying (moisture removing step). Here, “removing the uppermost layer containing moisture by a method other than drying” means removing moisture contained in the coating film formed from the aqueous coating composition by a method other than drying after coating. Means. Specific examples of such a method include, for example, a method in which the uppermost layer containing moisture is washed away by gravity by tilting a coating film obtained by painting, or the uppermost layer containing a moisture absorbent is removed by hand or air. Examples of the removal method include removal or removal using an optional instrument as necessary, and a method of removing moisture by absorbing moisture in the uppermost layer into the moisture-absorbing material.
 必要に応じて、上記塗装工程の前に、水性塗料組成物に水分吸収剤を加える、水分吸収剤混合工程を行ってもよい。この場合は、水分を含有する最上層に、水分吸収剤が含まれることとなる。水分吸収剤として、例えば、吸水量1g/g以上である剤が挙げられる。吸水量は、JIS K 7223-1996の高吸水性樹脂の吸水量試験方法に準拠して測定することができる。 If necessary, a water absorbent mixing step of adding a water absorbent to the aqueous coating composition may be performed before the coating step. In this case, the moisture absorbent is contained in the uppermost layer containing moisture. Examples of the moisture absorbent include an agent having a water absorption of 1 g / g or more. The amount of water absorption can be measured in accordance with the water absorption amount test method for high water absorption resin of JIS K 7223-1996.
 水分吸収剤として、具体的には、高吸水性樹脂、タンパク質、多糖類などが挙げられる。
 水分吸収剤として用いることができる高吸水性樹脂として、例えば、ポリアクリル酸塩(例えばポリアクリル酸ナトリウム、ポリアクリル酸カリウムなど)、ポリビニルアルコール、ポリアクリルアミド、ポリオキシエチレン、ポリスルホン酸塩、ポリグルタミン酸塩などの樹脂が挙げられる。
 水分吸収剤として用いることができるタンパク質として、例えば、ゼラチン、膠、アルブミン、カゼイン、グルテン、セリシンなどが挙げられる。
 水分吸収剤として用いることができる多糖類として、例えば、カルボキシルメチル化デンプン、カルボキシメチル化セルロース、デンプン、セルロース、キチン、キトサン、ヒドロキシエチルセルロース、ヒドロキシメチルセルロース、ヒドロキシプロピルメチルセルロース、ヒドロキシプロピルセルロース、寒天、アガロース、アラビアゴム、アルギン酸塩、カードラン、カラギーナン、キサンタンガム、グアーガム、グルコマンナン、コンドロイチン硫酸、ジェランガム、トラガカントガム、ヒアルロン酸、プルラン、ペクチン、ローカストビーンガムなどが挙げられる。
 これらの水分吸収剤は、1種を単独で用いてもよく、2種以上を併用してもよい。
Specific examples of the water absorbent include a highly water-absorbent resin, protein, polysaccharide and the like.
Examples of superabsorbent resins that can be used as moisture absorbents include polyacrylates (eg, sodium polyacrylate, potassium polyacrylate), polyvinyl alcohol, polyacrylamide, polyoxyethylene, polysulfonate, polyglutamic acid. Resins such as salts are listed.
Examples of the protein that can be used as a moisture absorbent include gelatin, glue, albumin, casein, gluten, and sericin.
Examples of polysaccharides that can be used as a moisture absorbent include carboxymethylated starch, carboxymethylated cellulose, starch, cellulose, chitin, chitosan, hydroxyethylcellulose, hydroxymethylcellulose, hydroxypropylmethylcellulose, hydroxypropylcellulose, agar, agarose, Examples include gum arabic, alginate, curdlan, carrageenan, xanthan gum, guar gum, glucomannan, chondroitin sulfate, gellan gum, tragacanth gum, hyaluronic acid, pullulan, pectin, locust bean gum and the like.
These moisture absorbents may be used alone or in combination of two or more.
 本発明の方法においては、水分離促進剤および水分吸収剤は、共通する材料を用いてもよい。より具体的には、水分離促進剤の一例である高分子凝集剤が挙げられ、水分吸収剤として、同一の材料を用いてもよい。水分離促進剤の一例である高分子凝集剤は、例えば付加した官能基の塩析作用または凝結作用などによって水性樹脂分散体粒子から水の分離をもたらす成分である。そしてこのような作用は、水を固定化し、樹脂成分より分離除去させる点で、水分吸収剤によってもたらされる水分吸収作用と、作用機構的に共通するところがあるためである。 In the method of the present invention, a common material may be used for the water separation accelerator and the water absorbent. More specifically, a polymer flocculant which is an example of a water separation accelerator is used, and the same material may be used as a moisture absorbent. A polymer flocculant, which is an example of a water separation accelerator, is a component that causes separation of water from aqueous resin dispersion particles by, for example, salting out or coagulating action of added functional groups. This is because such an action is common in terms of action mechanism with the moisture absorption effect provided by the moisture absorbent in that water is fixed and separated and removed from the resin component.
 上記水分吸収剤は、粒子状または粉末状であるのが好ましい。粒子状または粉末状の水分吸収剤として、例えば、体積平均粒子径が100nm~1mmである水分吸収剤が挙げられる。水分吸収剤の体積平均粒子径は、レーザー光散乱法などにより測定することができる。具体的には、レーザー回析式粒子径分布測定装置SALD-2200(島津製作所社製)などを使用して測定することができる。水分吸収剤を、乳鉢またはボールミルなどを用いて、粉砕などを行うことによって、上記粒子径の範囲に調節してもよい。 The moisture absorbent is preferably in the form of particles or powder. Examples of the particulate or powder moisture absorber include a moisture absorber having a volume average particle diameter of 100 nm to 1 mm. The volume average particle diameter of the moisture absorbent can be measured by a laser light scattering method or the like. Specifically, it can be measured using a laser diffraction particle size distribution analyzer SALD-2200 (manufactured by Shimadzu Corporation). You may adjust a water | moisture-content absorber to the range of the said particle diameter by grind | pulverizing etc. using a mortar or a ball mill.
 水分吸収剤として、タンパク質(例えばゼラチンなど)および多糖類(例えばデンプン、ヒドロキシエチルセルロースなど、)からなる群から選択される少なくとも1種などを用いるのが好ましい。 As the water absorbent, it is preferable to use at least one selected from the group consisting of proteins (for example, gelatin) and polysaccharides (for example, starch, hydroxyethyl cellulose, etc.).
 水分吸収剤を水性塗料組成物に加える場合は、水性塗料組成物100質量部に対して、0.1~100質量部となる量で加えるのが好ましく、0.1~30質量部となる量で加えるのがより好ましい。0.1質量部未満であると、水分を十分に吸収できないおそれがある。水性塗料組成物に水分吸収剤を加える手法として、一般的な混合方法を用いることができる。 When the water absorbent is added to the aqueous coating composition, it is preferably added in an amount of 0.1 to 100 parts by mass, and an amount of 0.1 to 30 parts by mass with respect to 100 parts by mass of the aqueous coating composition. It is more preferable to add at. If the amount is less than 0.1 parts by mass, moisture may not be sufficiently absorbed. A general mixing method can be used as a method of adding a water absorbent to the aqueous coating composition.
 上記水分吸収剤は、必要に応じて、水性塗料組成物に加える前に、有機溶媒中に予め浸漬する浸漬処理を行ってもよい。有機溶媒として、例えば、水難溶性の有機溶媒および水不溶性の有機溶媒からなる群から選択される1種またはそれ以上を用いることができる。浸漬処理を行う場合は、例えば、水分吸収剤1質量部に対して、有機溶媒を0.5~10質量部用いて、有機溶媒に対して0.5分~24時間接触させる態様などが挙げられる。 If necessary, the moisture absorbent may be subjected to an immersion treatment in which it is previously immersed in an organic solvent before being added to the aqueous coating composition. As the organic solvent, for example, one or more selected from the group consisting of poorly water-soluble organic solvents and water-insoluble organic solvents can be used. In the case of performing the immersion treatment, for example, an aspect in which 0.5 to 10 parts by mass of the organic solvent is used for 1 part by mass of the moisture absorbent and the organic solvent is brought into contact with the organic solvent for 0.5 minutes to 24 hours. It is done.
 ここで、水難溶性の有機溶媒とは、20℃における溶解度が10mg/L以上10g/L未満である有機溶媒を意味し、水不溶性の有機溶媒とは、20℃における溶解度が10mg/L未満である有機溶媒を意味する。このような浸漬処理を行うことによって、水分吸収剤の水分吸収作用の発現を遅延させたり抑制させたりすることができるという利点がある。例えば、塗装工程の前に、水性塗料組成物に水分吸収剤を加える、水分吸収剤混合工程を行う場合などにおいて、このような浸漬処理は有用であり、好ましく用いることができる。 Here, the poorly water-soluble organic solvent means an organic solvent having a solubility at 20 ° C. of 10 mg / L or more and less than 10 g / L, and the water-insoluble organic solvent has a solubility at 20 ° C. of less than 10 mg / L. It means an organic solvent. By performing such immersion treatment, there is an advantage that the onset of the water absorption action of the water absorbent can be delayed or suppressed. For example, in the case where a water absorbent is added to the aqueous coating composition or a water absorbent mixing step is performed before the coating step, such a dipping treatment is useful and can be preferably used.
 上記方法において、水分離促進剤混合工程および水分吸収剤混合工程の両方が行われる場合は、水分離促進剤混合工程は、水分吸収剤混合工程の前に行われるのがより好ましい。水分離促進剤混合工程を、水分吸収剤混合工程の前に行うことによって、水分離を水分吸収に先立って起こすことができると考えられる。 In the above method, when both the water separation accelerator mixing step and the water absorbent mixing step are performed, the water separation promoter mixing step is more preferably performed before the water absorbent mixing step. By performing the water separation accelerator mixing step before the water absorbent mixing step, it is considered that water separation can occur prior to moisture absorption.
 本発明の塗膜形成方法の他の1態様として、
 水性塗料組成物を塗装する塗装工程、および
 上記塗装によって得られた塗膜から、水分を、水分吸収材料を用いて除去する、水分吸収材料による水分除去工程、
を包含する方法が挙げられる。この態様においては、塗装によって得られた塗膜の上方から、水分吸収材料を接触させることによって、形成された塗膜から、水分を、水分吸収材料へ吸収させて、水分を取り除くことを特徴とする。
As another aspect of the coating film forming method of the present invention,
A water-removing process using a water-absorbing material, wherein a water-absorbing material is used to remove moisture from the coating process obtained by coating the aqueous coating composition;
The method of including is mentioned. In this aspect, the moisture absorbing material is brought into contact with the moisture absorbing material from above the coating film obtained by painting to absorb moisture into the moisture absorbing material, thereby removing moisture. To do.
 図2は、この塗膜形成方法を示す概略説明図である。水分の除去に用いる水分吸収材料は、図2に示される形状のものに限定されず、任意の形状のものを用いることができる。 FIG. 2 is a schematic explanatory view showing this coating film forming method. The moisture-absorbing material used for removing moisture is not limited to the shape shown in FIG. 2, and any shape can be used.
 この態様において用いることができる水分吸収材料として、上述の水分吸収剤が挙げられる。水分吸収材料として、上記水分吸収剤を含んで構成される、シート、フィルム、膜、ストリップ、発泡シートなどの形状の材料を用いることもできる。このような形状の材料として、例えば、市販されるシートなどの材料を用いることができる。また、上述の水分吸収剤を、シートまたは膜などの形状に加工して用いることもできる。 As the moisture absorbing material that can be used in this embodiment, the above-described moisture absorbent can be cited. As the moisture absorbing material, a material having a shape such as a sheet, a film, a membrane, a strip, and a foamed sheet, which is configured to include the moisture absorbent, can be used. As the material having such a shape, for example, a material such as a commercially available sheet can be used. Moreover, the above-mentioned moisture absorbent can also be used after being processed into a shape such as a sheet or a film.
 この態様において、塗装工程の前に、水性塗料組成物に水分離促進剤を加える、水分離促進剤混合工程をさらに包含してもよい。水分離促進剤として、上述した水分離促進剤を用いることができる。 In this aspect, a water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition may be further included before the coating step. As the water separation accelerator, the water separation accelerator described above can be used.
 本発明の塗膜形成方法は、水性塗料組成物中に含まれる水分を、乾燥以外の方法によって除去することを特徴とする。そのため、低温条件および/または高湿度条件などの、水性塗料組成物中に含まれる水媒体の蒸発が困難である塗装環境下であっても、塗膜を形成することが可能となる。本発明の方法によって、塗装環境に左右されることなく、あらゆる環境下において目的とする機能を有する塗膜を形成することが可能となる。 The coating film forming method of the present invention is characterized by removing water contained in the aqueous coating composition by a method other than drying. Therefore, a coating film can be formed even in a coating environment where it is difficult to evaporate the aqueous medium contained in the aqueous coating composition, such as a low temperature condition and / or a high humidity condition. According to the method of the present invention, it is possible to form a coating film having a desired function in any environment without being influenced by the coating environment.
 なお、本発明の塗膜形成方法は、単層塗膜の形成において用いてもよく、複層塗膜の形成において用いてもよい。本発明の塗膜形成方法を、複層塗膜の形成において用いる態様として、例えば、上記水分除去工程を行った塗膜に対して、さらに塗料組成物を塗装する態様などが挙げられる。ここで、さらに塗料組成物を塗装した後、必要に応じて、上記水分除去工程を行ってもよい。本発明の塗膜形成方法を、複層塗膜の形成において用いる場合は、上記利点に加えて、混層などの不具合の発生を防ぐことができるなどのさらなる利点が挙げられる。 The coating film forming method of the present invention may be used for forming a single layer coating film or may be used for forming a multilayer coating film. As an aspect using the coating-film formation method of this invention in formation of a multilayer coating film, the aspect etc. which apply | coat a coating composition further with respect to the coating film which performed the said water removal process are mentioned, for example. Here, after the coating composition is further applied, the water removal step may be performed as necessary. In the case where the coating film forming method of the present invention is used in the formation of a multilayer coating film, in addition to the above-mentioned advantages, there are further advantages such as prevention of problems such as mixed layers.
 以下の実施例により本発明をさらに具体的に説明するが、本発明はこれらに限定されない。実施例中、「部」および「%」は、ことわりのない限り、質量基準による。 The present invention will be described more specifically with reference to the following examples, but the present invention is not limited thereto. In the examples, “parts” and “%” are based on mass unless otherwise specified.
製造例1
 MKCシリケートMS51(三菱化学社製のテトラメトキシシランの縮合物、SiO含有率51%、縮合度は平均値として5) 10.71gに、アルミキレートD(川研ファインケミカル社製のアルミキレート化合物、76%イソプロパノール溶液)0.44g、メタノール 28.70gを加えて溶解させた。40℃に昇温した後、水 40.18gを2時間かけて徐々に加えて撹拌し、40℃で2時間エージングし、濃度9.6%のポリヒドロキシシロキサン溶液を得た。
Production Example 1
MKC silicate MS51 (condensate of tetramethoxysilane manufactured by Mitsubishi Chemical Co., SiO 2 content 51%, degree of condensation is 5 as an average value) 10.71 g of aluminum chelate D (aluminum chelate compound manufactured by Kawaken Fine Chemical Co., Ltd.) (76% isopropanol solution) 0.44 g and methanol 28.70 g were added and dissolved. After the temperature was raised to 40 ° C., 40.18 g of water was gradually added over 2 hours and stirred, followed by aging at 40 ° C. for 2 hours to obtain a polyhydroxysiloxane solution having a concentration of 9.6%.
実施例1
 コアシェル型アクリル樹脂ディスパージョン(日本ペイント社製、固形分44%、酸価20mg-KOH/g)をガラス瓶に10g秤量し、水分離促進剤として特級無水酢酸(試薬)を0.18g添加後、室温にて往復10回手で振盪することで均質に混合した。その直後、室温でテストピース上に、10ミルのドクターブレードにて塗装した。その15分後、塗膜上に、水分吸収材料として、高吸水性樹脂粒子(商品名;アクアキープ10SH-PF、住友精化社製、吸水量:500g/g、体積平均粒子径:26μm)を2g添加した。5分後に、水分を含有する最上層を指で払落し、目的とする乾燥膜厚100μmの塗膜を得た。
 高吸水性樹脂粒子の吸水量は、JIS K 7223-1996の高吸水性樹脂の吸水量試験方法に準拠して測定した。具体的には、物質0.2gをティーバッグに入れ、脱イオン水中に3時間浸漬し、10分間つるして水切りを行った直後に重量を測定して、浸漬前後の重量変化から吸水量を求めた。
Example 1
10 g of core-shell acrylic resin dispersion (manufactured by Nippon Paint Co., Ltd., solid content 44%, acid value 20 mg-KOH / g) was weighed in a glass bottle, and 0.18 g of special grade acetic anhydride (reagent) was added as a water separation accelerator, Homogenously mixed by shaking 10 times by hand at room temperature. Immediately thereafter, it was painted on a test piece at room temperature with a 10 mil doctor blade. 15 minutes later, a highly water-absorbent resin particle (trade name: Aquakeep 10SH-PF, manufactured by Sumitomo Seika Co., Ltd., water absorption: 500 g / g, volume average particle diameter: 26 μm) as a moisture absorbing material on the coating film 2 g was added. After 5 minutes, the uppermost layer containing moisture was removed with a finger to obtain a desired coating film having a dry film thickness of 100 μm.
The water absorption amount of the highly water-absorbent resin particles was measured in accordance with the water absorption amount test method for the highly water-absorbent resin of JIS K 7223-1996. Specifically, 0.2 g of the substance is put in a tea bag, immersed in deionized water for 3 hours, suspended for 10 minutes and drained immediately, and the weight is measured. It was.
実施例2
 水分吸収剤をゼラチン(商品名;クックゼラチン、森永製菓社製、吸水量:17g/g、体積平均粒子径:697μm)に、水分を含む最上層を除去するタイミングを水分吸収剤の添加から15分後に変更した以外は、実施例1と同様にして、目的とする乾燥膜厚100μmの塗膜を得た。
 なお、ゼラチンは事前に乳鉢で乳棒を用いて2分間粉砕したものを用いた。またゼラチンの吸水量は実施例1と同様にして求めた。
Example 2
The moisture absorbent is gelatin (trade name; Cook Gelatin, manufactured by Morinaga & Co., Ltd., water absorption: 17 g / g, volume average particle size: 697 μm), and the timing of removing the uppermost layer containing moisture is 15 A coating film having a target dry film thickness of 100 μm was obtained in the same manner as in Example 1 except that the change was made after minutes.
The gelatin used was pulverized in advance using a pestle in a mortar for 2 minutes. The water absorption of gelatin was determined in the same manner as in Example 1.
実施例3
 実施例1記載と同一のディスパージョンをガラス瓶に10g秤量し、水分離促進剤として無水酢酸を0.18g添加後、室温にて往復10回手で振盪することで均質に混合した。その直後、室温でテストピース上に、10ミルのドクターブレードにて塗装した。その15分後、テストピースを傾けることで水分を含む最上層を除去し、目的とする乾燥膜厚100μmの塗膜を得た。
Example 3
10 g of the same dispersion as described in Example 1 was weighed into a glass bottle, 0.18 g of acetic anhydride was added as a water separation accelerator, and then the mixture was uniformly mixed by shaking by hand 10 times at room temperature. Immediately thereafter, it was painted on a test piece at room temperature with a 10 mil doctor blade. Fifteen minutes later, the test piece was tilted to remove the uppermost layer containing moisture, and a desired coating film having a dry film thickness of 100 μm was obtained.
実施例4
 実施例1記載と同一のディスパージョンをガラス瓶に10g秤量し、水分離促進剤として無水酢酸を0.18g添加後、室温にて往復10回手で振盪することで均質に混合した。その直後、水分吸収剤としてゼラチンを8g添加し、さらに往復10回手で振盪することで均質に混合した。その直後、室温でテストピース上に均一に流し塗りした。塗装後、室温で1時間静置し、水分を含有し皮膜となった最上層を薬さじで除去して、目的とする乾燥膜厚200μmの塗膜を得た。
 なお、上記に示すゼラチンは、ゼラチンの吸水を遅延させるために、予め、ゼラチン(商品名;クックゼラチン、森永製菓社製、吸水量:17g/g)8gを、トルエン10gに含浸したものを濾過してから用いた。
Example 4
10 g of the same dispersion as described in Example 1 was weighed into a glass bottle, 0.18 g of acetic anhydride was added as a water separation accelerator, and then the mixture was uniformly mixed by shaking by hand 10 times at room temperature. Immediately thereafter, 8 g of gelatin was added as a water absorbent, and the mixture was shaken by reciprocating 10 times and mixed uniformly. Immediately after that, it was uniformly cast on the test piece at room temperature. After coating, the mixture was allowed to stand at room temperature for 1 hour, and the uppermost layer that contained water and became a film was removed with a spoon. Thus, a coating film having a target dry film thickness of 200 μm was obtained.
In order to delay the water absorption of gelatin, the gelatin shown above was filtered by impregnating 10 g of toluene in advance with 8 g of gelatin (trade name: Cook Gelatin, Morinaga & Co., Ltd., water absorption: 17 g / g). And then used.
実施例5
 静置条件を温度5℃、湿度50%に変更した以外は実施例4と同様にして、目的とする乾燥膜厚200μmの塗膜を得た。
Example 5
A target coating film having a dry film thickness of 200 μm was obtained in the same manner as in Example 4 except that the standing conditions were changed to a temperature of 5 ° C. and a humidity of 50%.
実施例6
 静置条件を温度23℃、湿度83%に変更した以外は実施例4と同様にして、目的とする乾燥膜厚200μmの塗膜を得た。
Example 6
A target coating film having a dry film thickness of 200 μm was obtained in the same manner as in Example 4 except that the standing conditions were changed to a temperature of 23 ° C. and a humidity of 83%.
実施例7
 水分吸収剤をヒドロキシエチルセルロース(商品名;SP-850、ダイセル社製、吸水量20g/g、体積平均粒子径:92μm)2gに変更した以外は実施例4と同様にして、目的とする乾燥膜厚200μmの塗膜を得た。なお、上記に示すヒドロキシエチルセルロースは、ヒドロキシエチルセルロースの吸水を遅延させるために、予め、ヒドロキシエチルセルロース2gを、トルエン4gに含浸したものを濾過してから用いた。また、ヒドロキシエチルセルロースの吸水量は実施例1と同様にして求めた。
Example 7
The target dry film was obtained in the same manner as in Example 4 except that the water absorbent was changed to 2 g of hydroxyethyl cellulose (trade name: SP-850, manufactured by Daicel, water absorption 20 g / g, volume average particle size: 92 μm). A 200 μm thick coating film was obtained. In addition, in order to delay the water absorption of a hydroxyethyl cellulose, the hydroxyethyl cellulose shown above was used after filtering what impregnated 2 g of hydroxyethyl cellulose in 4 g of toluene in advance. Further, the water absorption amount of hydroxyethyl cellulose was determined in the same manner as in Example 1.
実施例8
 水分離促進剤として、製造例1で調製したポリヒドロキシシロキサン溶液 2.29gを用いたこと以外は実施例4と同様にして、目的とする乾燥膜厚200μmの塗膜を得た。
Example 8
A coating film having a target dry film thickness of 200 μm was obtained in the same manner as in Example 4 except that 2.29 g of the polyhydroxysiloxane solution prepared in Production Example 1 was used as the water separation accelerator.
比較例1
 実施例1記載と同一のディスパージョンをガラス瓶に10g秤量し、室温でテストピース上に、10ミルのドクターブレードにて塗装した。塗装後、室温で1時間静置し、乾燥膜厚100μmの塗膜を得た。なお、水分除去工程は行わなかった。
Comparative Example 1
10 g of the same dispersion as described in Example 1 was weighed in a glass bottle and coated on a test piece at room temperature with a 10 mil doctor blade. After coating, it was allowed to stand at room temperature for 1 hour to obtain a coating film having a dry film thickness of 100 μm. In addition, the water removal process was not performed.
比較例2
 静置条件を温度5℃、湿度50%に変更した以外は比較例1と同様にして、乾燥膜厚100μmの塗膜を得た。なお、水分除去工程は行わなかった。
Comparative Example 2
A coating film having a dry film thickness of 100 μm was obtained in the same manner as in Comparative Example 1 except that the standing conditions were changed to a temperature of 5 ° C. and a humidity of 50%. In addition, the water removal process was not performed.
比較例3
 静置時間を5時間に変更した以外は比較例2と同様にして、乾燥膜厚100μmの塗膜を得た。
Comparative Example 3
A coating film having a dry film thickness of 100 μm was obtained in the same manner as in Comparative Example 2 except that the standing time was changed to 5 hours.
比較例4
 静置条件を温度23℃、湿度83%に変更した以外は比較例1と同様にして、乾燥膜厚100μmの塗膜を得た。なお、水分除去工程は行わなかった。
Comparative Example 4
A coating film having a dry film thickness of 100 μm was obtained in the same manner as in Comparative Example 1 except that the standing conditions were changed to a temperature of 23 ° C. and a humidity of 83%. In addition, the water removal process was not performed.
比較例5
 静置時間を5時間に変更した以外は比較例4と同様にして、乾燥膜厚100μmの塗膜を得た。なお、水分除去工程は行わなかった。
Comparative Example 5
A coating film having a dry film thickness of 100 μm was obtained in the same manner as in Comparative Example 4 except that the standing time was changed to 5 hours. In addition, the water removal process was not performed.
 上記実施例および比較例によって得られた塗膜について、下記評価を行った。評価結果を下記表に示す。 The following evaluations were performed on the coating films obtained by the above examples and comparative examples. The evaluation results are shown in the following table.
 実施例1~8および比較例1~5によって得られた塗膜の状態を指触により確認し、以下に示す判断基準で評価を行なった。
○:塗膜に粘着感がない
×:塗膜に粘着感がある
The states of the coating films obtained in Examples 1 to 8 and Comparative Examples 1 to 5 were confirmed by finger touch and evaluated according to the following criteria.
○: There is no sticky feeling in the coating film ×: There is a sticking feeling in the coating film
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
 比較例1の結果は、塗装後、室温で1時間静置して得られた塗膜の評価結果である。比較例1の結果から、たとえ室温条件下であっても、水分除去工程を行わない場合においては、1時間の静置のみでは、良好な塗膜が得られないことが分かる。
 実施例1~8の結果は、いずれも、上記実施例によって形成された直後の塗膜の評価結果である。本発明の実施例では、比較例1と同じ塗料を用いた場合であってもいずれも、乾燥以外の方法で水分を除去したことにより、良好な塗膜を形成することができることが確認された。
 比較例2の結果は、低温条件下であって、水媒体の蒸発が困難である塗装環境下において、1時間静置して得られた塗膜の評価結果である。また比較例4の結果は、高湿度条件下であって、水媒体の蒸発が困難である塗装環境下において、1時間静置して得られた塗膜の評価結果である。これら比較例2そして4の塗装環境下においては、水の揮発を促進するべくさらに4時間静置した場合であっても(比較例3、比較例5)、塗膜に粘着感が残っていた。これらの低温条件下および/または高湿度条件下においては、水性塗料組成物の塗装による塗膜形成が困難であることが確認できる。
 他方、比較例2そして4の塗装環境下においても、本発明の塗装方法を行った場合には、良好な塗膜が得られることが、実施例5および6により確認することができた。ここで、比較例1~5はいずれも、ドクターブレード塗装を行っている。ドクターブレード塗装は、塗装膜厚が薄く、塗装膜厚中の総水分量が少ないため、より良好な塗膜を得やすい条件である。一方で、実施例5および6は、比較例2そして4の塗装環境下であることに加えて、流し塗り塗装という、塗装膜厚が厚く塗膜中の総水分量が多いため、ドクターブレード塗装に対して、成膜上において、より不利な条件となる塗装方法で塗膜形成を行っている。そして実施例5および6においては、成膜上においてもよりハードルの高い塗装方法を用いて塗膜を形成したにもかかわらず、粘着感の無い良好な塗膜が得られることが、確認できた。
The result of the comparative example 1 is an evaluation result of the coating film obtained by leaving it at room temperature for 1 hour after coating. From the results of Comparative Example 1, it can be seen that even when the room temperature condition is not used, when the water removal step is not performed, a good coating film cannot be obtained only by standing for 1 hour.
The results of Examples 1 to 8 are all evaluation results of the coating film immediately after being formed according to the above examples. In the examples of the present invention, it was confirmed that even when the same paint as in Comparative Example 1 was used, a good coating film could be formed by removing moisture by a method other than drying. .
The result of the comparative example 2 is an evaluation result of the coating film obtained by being allowed to stand for 1 hour in a coating environment where the evaporation of the aqueous medium is difficult under low temperature conditions. Moreover, the result of the comparative example 4 is an evaluation result of the coating film obtained by leaving still for 1 hour in the coating environment where the evaporation of the aqueous medium is difficult under high humidity conditions. In the coating environment of these comparative examples 2 and 4, even when it was allowed to stand for another 4 hours to promote the volatilization of water (Comparative Example 3 and Comparative Example 5), the coating film remained sticky. . Under these low-temperature conditions and / or high-humidity conditions, it can be confirmed that it is difficult to form a coating film by applying the aqueous coating composition.
On the other hand, even in the coating environments of Comparative Examples 2 and 4, it was confirmed from Examples 5 and 6 that a good coating film was obtained when the coating method of the present invention was performed. Here, in each of Comparative Examples 1 to 5, doctor blade coating is performed. The doctor blade coating is a condition that makes it easier to obtain a better coating film because the coating film thickness is thin and the total water content in the coating film thickness is small. On the other hand, in Examples 5 and 6, in addition to being in the coating environment of Comparative Examples 2 and 4, since the coating film thickness is thick and the total water content in the coating film is large, doctor blade coating On the other hand, the coating film is formed by a coating method that is more disadvantageous in film formation. In Examples 5 and 6, it was confirmed that a good coating film without sticky feeling could be obtained even though the coating film was formed using a coating method with higher hurdles on film formation. .
 本願発明の方法によって、低温条件および/または高湿度条件などの、水性塗料組成物中に含まれる水媒体の蒸発が困難である塗装環境下であっても、目的の機能を有する塗膜を形成することが可能となるという利点がある。 By the method of the present invention, a coating film having a desired function is formed even in a coating environment where it is difficult to evaporate an aqueous medium contained in an aqueous coating composition such as a low temperature condition and / or a high humidity condition. There is an advantage that it becomes possible to do.

Claims (13)

  1.  水性塗料組成物を塗装する塗装工程、
     前記塗装によって得られた塗膜を、水分を含有する最上層および塗膜形成層に分離する、塗膜分離工程、および
     前記水分を含有する最上層を、乾燥以外の方法によって除去する、水分除去工程、
    を包含する、塗膜形成方法。
    A painting process for painting a water-based paint composition;
    The coating film obtained by the coating is separated into the uppermost layer containing moisture and the coating film forming layer, and the coating layer separating step, and the uppermost layer containing moisture is removed by a method other than drying. Process,
    A method for forming a coating film.
  2.  前記水分を含有する最上層は、さらに水分吸収剤を含む、請求項1記載の塗膜形成方法。 The coating film forming method according to claim 1, wherein the uppermost layer containing moisture further contains a moisture absorbent.
  3.  前記塗装工程の前に、水性塗料組成物に水分吸収剤を加える、水分吸収剤混合工程をさらに包含する、請求項2記載の塗膜形成方法。 The coating film forming method according to claim 2, further comprising a moisture absorbent mixing step of adding a moisture absorbent to the aqueous coating composition before the coating step.
  4.  前記塗装工程の前に、水性塗料組成物に水分離促進剤を加える、水分離促進剤混合工程をさらに包含し、
     前記塗膜分離工程は、前記水分離促進剤によってもたらされる、
    請求項1~3いずれかに記載の塗膜形成方法。
    A water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition before the coating step;
    The coating film separation step is brought about by the water separation accelerator.
    The coating film forming method according to any one of claims 1 to 3.
  5.  前記塗膜形成方法において、前記塗装工程の前に、水性塗料組成物に水分離促進剤を加える水分離促進剤混合工程、および、水性塗料組成物に水分吸収剤を加える水分吸収剤混合工程が行われ、
    ここで、前記水分離促進剤混合工程は、前記水分吸収剤混合工程の前に行われる、
    請求項4記載の塗膜形成方法。
    In the coating film forming method, before the coating step, a water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition, and a moisture absorbent mixing step of adding a moisture absorber to the aqueous coating composition Done,
    Here, the water separation accelerator mixing step is performed before the moisture absorbent mixing step.
    The coating film forming method according to claim 4.
  6.  前記水分吸収剤は、吸水量1g/g以上である、請求項2、3、または5に記載の塗膜形成方法。 The coating film forming method according to claim 2, 3 or 5, wherein the moisture absorbent has a water absorption of 1 g / g or more.
  7.  前記水分吸収剤は、高吸水性樹脂、タンパク質および多糖類からなる群から選択される1種またはそれ以上である、請求項2、3、または5に記載の塗膜形成方法。 The coating film forming method according to claim 2, 3 or 5, wherein the moisture absorbent is one or more selected from the group consisting of a superabsorbent resin, protein and polysaccharide.
  8.  前記水分離促進剤は、有機酸、無機酸、酸無水物、pH緩衝液、金属塩、塩基性化合物および高分子凝集剤からなる群から選択される1種またはそれ以上である、請求項4または5に記載の塗膜形成方法。 The water separation accelerator is one or more selected from the group consisting of organic acids, inorganic acids, acid anhydrides, pH buffer solutions, metal salts, basic compounds, and polymer flocculants. Or the coating-film formation method of 5.
  9.  前記水分離促進剤が高分子凝集剤である、請求項8に記載の塗膜形成方法。 The method for forming a coating film according to claim 8, wherein the water separation accelerator is a polymer flocculant.
  10.  前記高分子凝集剤が、ポリヒドロキシシロキサン化合物である、請求項9に記載の塗膜形成方法。 The coating film forming method according to claim 9, wherein the polymer flocculant is a polyhydroxysiloxane compound.
  11.  水性塗料組成物を塗装する塗装工程、および
     前記塗装によって得られた塗膜から、水分を、水分吸収材料を用いて除去する、水分吸収材料による水分除去工程、
    を包含する、塗膜形成方法。
    A water-removing step using a water-absorbing material, wherein a water-absorbing material is used to remove water from the coating process obtained by coating the water-based paint composition;
    A method for forming a coating film.
  12.  前記塗装工程の前に、水性塗料組成物に水分離促進剤を加える、水分離促進剤混合工程をさらに包含する、
    請求項11記載の塗膜形成方法。
    A water separation accelerator mixing step of adding a water separation accelerator to the aqueous coating composition before the coating step;
    The coating film forming method according to claim 11.
  13.  前記水分吸収材料は、高吸水性樹脂、タンパク質および多糖類からなる群から選択される1種またはそれ以上の水分吸収剤、または前記水分吸収剤を含んで構成される、シート、フィルム、膜、ストリップまたは発泡シートである、請求項11または12記載の塗膜形成方法。 The moisture absorbing material is one or more moisture absorbents selected from the group consisting of a superabsorbent resin, protein and polysaccharide, or a sheet, film, membrane, comprising the moisture absorbent, The coating film forming method according to claim 11 or 12, which is a strip or a foam sheet.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57130575A (en) * 1981-02-03 1982-08-13 Grace W R & Co Method of removing moisture from aqueous can end section lining compound
JPS61243866A (en) * 1985-04-17 1986-10-30 アクゾ・ナ−ムロ−ゼ・フエンノ−トシヤツプ Application of road marking composition
JPH08500405A (en) * 1993-06-10 1996-01-16 プラスティルート ソシエテ アノニム Method and apparatus for applying horizontal markings to roads or other traffic areas
JPH09235489A (en) * 1996-02-26 1997-09-09 Rohm & Haas Co Water-based traffic marking material
JP2001214409A (en) * 1999-12-03 2001-08-07 Rohm & Haas Co Method to shorten drying time of exterior coating
JP2004148133A (en) * 2002-09-05 2004-05-27 Sk Kaken Co Ltd Method of forming decorated surface

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57130575A (en) * 1981-02-03 1982-08-13 Grace W R & Co Method of removing moisture from aqueous can end section lining compound
JPS61243866A (en) * 1985-04-17 1986-10-30 アクゾ・ナ−ムロ−ゼ・フエンノ−トシヤツプ Application of road marking composition
JPH08500405A (en) * 1993-06-10 1996-01-16 プラスティルート ソシエテ アノニム Method and apparatus for applying horizontal markings to roads or other traffic areas
JPH09235489A (en) * 1996-02-26 1997-09-09 Rohm & Haas Co Water-based traffic marking material
JP2001214409A (en) * 1999-12-03 2001-08-07 Rohm & Haas Co Method to shorten drying time of exterior coating
JP2004148133A (en) * 2002-09-05 2004-05-27 Sk Kaken Co Ltd Method of forming decorated surface

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