WO2001053006A1 - Method for coating substrate, coated article and coating apparatus - Google Patents
Method for coating substrate, coated article and coating apparatus Download PDFInfo
- Publication number
- WO2001053006A1 WO2001053006A1 PCT/JP2001/000226 JP0100226W WO0153006A1 WO 2001053006 A1 WO2001053006 A1 WO 2001053006A1 JP 0100226 W JP0100226 W JP 0100226W WO 0153006 A1 WO0153006 A1 WO 0153006A1
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- WIPO (PCT)
- Prior art keywords
- coating
- paint
- composition
- coating composition
- liquid
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D1/00—Processes for applying liquids or other fluent materials
- B05D1/30—Processes for applying liquids or other fluent materials performed by gravity only, i.e. flow coating
- B05D1/305—Curtain coating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C—APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C5/00—Apparatus in which liquid or other fluent material is projected, poured or allowed to flow on to the surface of the work
- B05C5/005—Curtain coaters
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D2506/00—Halogenated polymers
- B05D2506/10—Fluorinated polymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D5/00—Processes for applying liquids or other fluent materials to surfaces to obtain special surface effects, finishes or structures
- B05D5/08—Processes for applying liquids or other fluent materials to surfaces to obtain special surface effects, finishes or structures to obtain an anti-friction or anti-adhesive surface
- B05D5/083—Processes for applying liquids or other fluent materials to surfaces to obtain special surface effects, finishes or structures to obtain an anti-friction or anti-adhesive surface involving the use of fluoropolymers
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/582—Recycling of unreacted starting or intermediate materials
Definitions
- the present invention relates to a method for coating a substrate by applying a liquid fluorine-containing coating composition to the substrate using a force flow coater.
- the foaming of the paint composition is small, and even if the curtain flow is continuously operated using the recovered paint composition, a dry coating film with excellent surface smoothness is provided.
- the coating method of the base material that can be applied and the coating material obtained, such as the coating roller, S, etc., can be coated uniformly even at a low flow rate. About the evening.
- the present invention further provides a fluorine-containing polymer system which has good film forming properties and coating film properties, has low bubbling, and is particularly suitable for coating with a tenth-fluoro-coater.
- a typical curtain flow coater includes a head 3 having a slit 4 as shown in FIG. 1 as a schematic flowchart.
- a storage tank 5 for the liquid coating composition 1 a coating supply pump 6 disposed in the storage tank 5 and having a rotating part (impeller) 7, and a base material 2.
- the conveyor 8 and the power to be supplied are supplied, and the liquid coating composition 1 is supplied from the storage tank 5 to the coating supply pump 6 so that the peripheral speed of the outer periphery of the rotating portion 7 of the pump 6 is controlled.
- it is sent to the head section 3 via the transport pipe 20 and the slit 4 force is caused to flow down in a container form, and then sent by the conveyor 8.
- This is a device for applying the material to the surface of the incoming substrate 2.
- the rotating part 7 of the paint supply pump 6 is rotated from the storage tank 5. Then, the coating composition 1 is supplied to the head section 3, and the coating composition 1 is continuously formed into a thin film (forced tenn) from the slit 4 of the head section 3. Let it flow down.
- the object to be coated is passed under the head part 3 by the conveyor 8 in the horizontal direction, and the base material 2 is coated with the coating composition 1 flowing down from the head part 3.
- the coating composition 1 that has not adhered to the base material 2 is again collected in the storage tank 5 via the collection path of the coating composition, and is reused.
- a fluorocarbon resin for aluminum kitchen appliances is to be painted by a continuous airless coating method. Is described. However, the disclosed device forced air out of slit carbon from the slit cap by applying air pressure to the fluorocarbon resin liquid. This is different from the above-described known force-flow mechanism. Further, it is unclear whether the fluorocarbon resin liquid is a solution or a dispersion of fluoropolymer particles in a liquid carrier, and the fluorocarbon resin liquid at the time of use is unknown. The viscosity is as high as 2000 to 800 mPa.s. Also, there is no description of a solution for foaming.
- a coating composition obtained by dispersing fluorine-containing polymer particles in a medium using a curtain flow coater As described above, it has been difficult to apply a coating composition obtained by dispersing fluorine-containing polymer particles in a medium using a curtain flow coater. Therefore, at present, generally, a coating composition in which fluorine-containing polymer particles are dispersed is applied by a spray coating method or a roll coating method.
- the paint spray method has a problem in that the coating efficiency is poor and the coating composition has a large loss, and the paint efficiency is low in the mouth spray method.
- roll eyes (marks) remain on the coating film.
- a curtain coater using a liquid coating composition containing fluorine-containing polymer particles which has a large amount of foaming and is disadvantageous for long-time continuous operation, can be obtained.
- the method of supplying the coating composition from the storage tank to the head and the range of the viscosity of the coating composition during use should be devised.
- the present inventors have found a coating method capable of giving a dry coating film with less foaming and excellent in surface smoothness even if operated continuously, and completed the present invention. It came to be.
- the aqueous dispersion containing the fluorine-containing polymer particles is generally used for so-called emulsion polymerization using a water-soluble polymerization initiator in the presence of an anionic surfactant.
- the average particle size in the aqueous dispersion (latex) is 0.05 to :! It is obtained in the form of a colloid of ⁇ .
- This aqueous dispersion is unstable as it is, and the polymer particles are liable to precipitate due to storage and agglomeration of the polymer particles due to stirring.
- the dispersion stability of the polymer particles is secured by adding a nonionic surfactant such as alkyl phenyl ether. Therefore, bubbles are easily generated by stirring, and the generated bubbles are not easily erased.
- silicone-based compound having excellent defoaming properties As a defoaming agent which suppresses the generation of bubbles or breaks generated bubbles, a silicone-based compound having excellent defoaming properties is generally used. It was. However, silicone-based antifoaming agents are problematic in that the silicone-based antifoaming agent remaining in the coating film has an adverse effect on film forming properties and coating film properties. There was.
- an acetylene-based antifoaming agent is known as an antifoaming agent having excellent antifoaming performance, but there is a problem that its effectiveness is not sustainable. There is a point.
- the defoaming performance of the coating composition composed of the aqueous dispersion containing the fluorine-containing polymer particles and the surfactant is persistent, and remains in the coating film.
- specific hydrocarbon compounds were specifically superior in defoaming in this system.
- a coating composition suitable for painting by curtain flooring can be obtained, in particular, without leaving any residue on the coating film. This led to the completion of the present invention. Disclosure of the invention
- the present invention relates to a liquid coating composition containing fluorine-containing polymer particles having an average particle diameter of 0.01 to 100 / m and having a viscosity of 0.1 to 500 mPa's when used.
- the present invention relates to a method for coating a substrate, characterized by being applied to the substrate by a ten-time process.
- the present invention provides a head portion having a slit, a reservoir for a liquid coating composition, and a paint supply port disposed in the reservoir and having a rotating portion. And a substrate supply conveyor.
- the liquid paint composition is supplied from a storage tank to the paint supply pump, and the peripheral speed of the outer periphery of the rotating portion of the pump is adjusted. And then flow down from the slit and apply it to the surface of the substrate that is sent by a conveyor. (Hereinafter referred to as “carton flower (1)”) to coat a substrate, wherein the liquid coating composition has an average particle diameter of 0%.
- a base material characterized in that the composition is supplied to the head portion at a peripheral speed of 0.1 to 12. Om / sec at the outer peripheral portion of the rotating portion of the paint supply pump. Regarding the coating method.
- the present invention provides a head portion having a slit, a lower storage tank for a liquid coating composition, an upper storage tank for a liquid coating composition, a pneumatic pump, Material supply conveyor Then, the liquid paint composition is sent from the lower storage tank to the upper storage tank by a pneumatic pump, and is sent from the upper storage tank to the head by natural dropping.
- a new type of curtain-floor which is made to flow down from the lit and is applied to the surface of the base material sent by a conveyor (hereinafter referred to as “curtain floor”).
- a method for coating a base material using a froth referred to as “Fuco-I (II) J)”, wherein the liquid coating composition has a mean particle diameter of 0.01 to 100 / m.
- the present invention relates to a method for coating a substrate, characterized in that the composition is a liquid coating composition containing nitrogen polymer particles and having a viscosity of 0.1 to 500 mPa * s during use.
- the present invention further relates to a coated article obtained by coating a substrate by these coating methods.
- the present invention provides a force-feeding-in-one-coater having a head portion provided with a paint supply mechanism capable of coating a very uniform film thickness even at a low paint flow rate. It also relates to In such a paint supply mechanism, the inlet for supplying paint into the head section is opposed to two side walls that are provided in a direction across the slit. The feature is that the same number is arranged at the specified position.
- the liquid coating composition used in these methods has an antifoaming action with respect to 100 parts by weight (hereinafter referred to as “parts”) of the solid content of the coating composition.
- parts At least one selected from the group consisting of organic liquids, polyether-based polymer surfactants, fatty acid esters, metal stone cans, and silicone-based compounds It is preferable to use a composition added with 0.01 to 20 parts, preferably 0.01 to 15.0 parts.
- additives act as defoamers, but especially carbon Aliphatic saturated hydrocarbons having the number of 6 to 12 and / or aromatic hydrocarbons having the number of carbon atoms of 7 to 11 have a lower defoaming activity, and have a lower film forming property and film forming property. They are excellent.
- the present invention further includes fluoropolymer particles having an average particle diameter of 0.01 to 100 m and a surfactant, and has a viscosity of 0.1 to 100 ⁇ m when used.
- An aqueous dispersion composition having a viscosity of 500 mPa ⁇ s, and an aliphatic saturated carbonized carbon having 6 to 12 carbon atoms as an antifoaming agent for 100 parts of the solid component of the composition.
- the present invention relates to a composition suitable as a coating composition for flow coating. Brief description of the drawing
- Fig. 1 is a schematic flow chart of the curtain floor (I) used in the present invention.
- Fig. 2 is a schematic flowchart of the curtain flow coater (II) used in the present invention.
- FIG. 3 is a schematic cross-sectional view of a paint supply mechanism to a head portion used in a preferred mode of the present invention.
- FIG. 4 is a plan view of a painted plate for explaining the measurement points of the film thickness of the paint film of the painted article in the present invention.
- FIG. 5 is a schematic cross-sectional view of a conventional paint supply mechanism to a head portion.
- BEST MODE FOR CARRYING OUT THE INVENTION The fluorine-containing polymer used in the present invention imparts, for example, non-adhesiveness and lubricity to a coated article as a base material. In order to It is preferably used.
- Preferred fluorine-containing polymers are those in which some or all of the hydrogen atoms have been substituted with fluorine atoms, or fluorine atoms and chlorine atoms. It is a homopolymer or a copolymer of a monoethylene unsaturated hydrocarbon, and a homopolymer and a mixture containing Z or a copolymer can also be used. Specific examples are shown below, but the present invention is not limited to these examples.
- Homopolymers include, for example, polytetrafluoroethylene (PTFE), polycloth trifluoroethylene (PCTFE), and polyvinylene. DMF and PVF are available.
- PTFE polytetrafluoroethylene
- PCTFE polycloth trifluoroethylene
- PVF polyvinylene
- TFE tetrafluoroethylene
- I the general formula (I):
- X is the same as defined above, Y is a hydrogen atom or a fluorine atom, and q is an integer of 1 to 6).
- TFE perfluoro (alkyl vinyl ether) (PAVE) copolymer
- PFA perfluoro (alkyl vinyl ether) copolymer
- HFP hexafluoropropylene copolymer
- TFE Cross mouth trifluoroethylene (CTFE) copolymer
- TFE vinylenefluoride (VdF) copolymer
- TFE Triplefluorene Polyethylene (3FH) copolymer
- TFE-ethylene copolymer ETFE
- VdF-HFP ethylene-CTFE copolymer
- ECTFE Ethylene-one copolymer Fluoropropylene copolymers and TFE-propylene copolymers are available.
- a VdF-TFE-HFP copolymer can be used as the terpolymer.
- homopolymer or copolymer mixture examples include, for example, a mixture of PTFE and PFA, a mixture of PTFE and FEP, a mixture of PTFE, PFA and FEP, and a mixture of PFA and FEP.
- the mixture etc. will be exfoliated.
- esters containing (per) fluoroalkyl groups of (meth) acrylic acid for example,
- R f CH ? CHCH, OCOCR 3 CH 9 , (Wherein, Rf is A Ruki the path one full O b
- R 1 is hydrogen or is A alkyl group having 1-10 carbon atoms
- R 2 is 1 to 10 carbon atoms of 4 to 20 carbon atoms
- a ren group R 3 is hydrogen or a methyl group
- R 4 is an alkyl group having 1 to 17 carbon atoms
- r represents an integer of 1 to 10
- a Vinyl esters of carboxylic acids containing fluoroalkyl groups for example
- Rf is the same as described above, and s represents an integer of 0 to: 10
- s represents an integer of 0 to: 10
- Ruestel for example
- Rf and r are the same as those described above), such as a homopolymer or a copolymer, or other monomer which can be copolymerized with these monomers.
- a copolymer consisting of monomers is obtained.
- Examples of other copolymerizable monomers include (meth) acrylic acid alkylester (alkyl having 1 to 20 carbon atoms) and (meth) acrylic acid. Cyclohexyl acid or benzyl ester, polyethylene glycol di (meth) acrylate, N-methylpropane alcohol Lil amide, ethylene, vinyl chloride, bifluoride, (meth) acrylamide, styrene, dimethyl styrene, p-methyl styrene Tylene, vinyl alkyl ether (alkyl carbon number 1 to 20) Halogenated alkyl vinyl ether (alkyl carbon number 1 to 20), vinyl alkyl ketone (alkyl carbon number 1 to 20) ), Maleic anhydride, butadiene, isoprene, chloroprene Do etc. but that Ki out and the Oh gel this, in even Ru limited to this are these flowers Les.
- the fluorine-containing polymer particles usually have a surfactant in an aqueous medium.
- the monomer is produced by so-called emulsion polymerization of the monomer in the presence of a surfactant, and has an average particle diameter in an aqueous dispersion (latex).
- This aqueous dispersion is left as it is or is appropriately coagulated and redispersed to obtain an aqueous dispersion in which particles having an average particle diameter of 0.01 to 100 ⁇ m are dispersed.
- the fluorine-containing polymer particles in the aqueous dispersion preferably have a particle size in the range of 0.1 to 10 ⁇ from the viewpoint of good dispersion stability.
- the surfactant may be unstable in this state, and the surfactant is added because the polymer particles are likely to settle due to storage and agglomeration of the polymer particles due to stirring. As a result, the dispersion stability of the polymer particles is ensured.
- Surfactants as such dispersion stabilizers include, for example, nonionics such as polyoxyalkylene alkyl phenyl ether and polyoxyethylene alkyl ether. Surfactants are mainly used, as well as non-fluorinated anionic surfactants such as sodium rauryl sulfate, perfluorooctane Fluorine-containing anionic surfactants such as ammonium phosphate are used in combination.
- the fluorine-containing aqueous dispersion containing defoamer according to the present invention basically has an average particle diameter of 0.01 to: ⁇ 00 ⁇ , preferably 0.05 to 50. ⁇ , more preferably 0.1 ⁇ : ⁇ makes the fluorine-containing polymer particles stable to an aqueous liquid carrier such as water by the action of the surfactant. They are dispersed.
- fluoropolymer as resin particles in the coating composition used in the present invention, it is included for the purpose of improving coating properties such as film-forming properties and corrosion resistance. It is also possible to add resins other than fluorine-based resins. Specifically, polyamide resin, polyimide resin, polyimide resin, polyethersulfone tree Resin, polyphenylene sulfide resin, phenolic resin, urea resin, epoxy resin, urethane resin, melamine resin, polyester resin, polyester resin Examples of acrylate resins, acryl resins, acryl silicone resins, silicone resins, silicone polyester resins, etc. can be given. However, the present invention is not limited to these. The average particle size of these other resins is preferably in the same range as that of the fluorine-containing polymer in the range of 0.01 to 100 mm. The compounding amount is appropriately selected depending on the purpose, application, required characteristics, and the like.
- the liquid medium of the liquid coating composition used in the present invention may be water or a mixed liquid containing water as a main component and an organic liquid (hereinafter, collectively referred to as “aqueous medium”), or It is one type of organic liquid or a mixed liquid of two or more types (hereinafter referred to as “organic medium”).
- Organic liquids include, for example, nitrogen-containing solvents such as N-methyl-2-pyrrolidone and dimethyl acetamide; and lactones with a lip mouth.
- Oxygenated solvents Aromatic hydrocarbons such as xylene and toluene; Mineral spirit (Nihon Kogyo Standard, Kogyo Gasolin No. 4) and Solvent Hydrocarbons such as petroleum-based mixed solvents represented by Sox (manufactured by Xeon Chemical Co.); Esters such as butyl acetate; ketones such as methylisobutyl ketone Selected from alcohols, such as butyric alcohol, such as butyl alcohol, etc., and at least one alcohol can be used. However, it is not limited to these.
- the organic solvent to be added to water is added as a hydrocarbon solvent, particularly as an antifoaming agent described later.
- Fats with 6 to 12 carbon atoms Aromatic saturated hydrocarbons and aromatic hydrocarbon solvents having 7 to 11 carbon atoms act not as solvents but as antifoaming agents.
- an antifoaming agent in order to eliminate bubbles which may be generated when mixing, transporting, painting and collecting paints.
- the defoaming agent may be one or more of an organic liquid, a polyether-based polymer surfactant, a fatty acid ester, a metal stone gen or a silicone-based compound. Two or more species are extinct.
- the organic liquid as an antifoaming agent is used when the liquid carrier is an aqueous medium, and the following can be exemplified, but not limited thereto.
- Nitrogen-containing solvents such as mine and triethanolamine
- ⁇ - oxygen-containing solvents such as lactone, lactone
- fragrances such as xylene and toluene Petroleum-based hydrocarbons represented by mineral spirits (Japanese Industrial Standards, Industrial Gasoline No.
- Solbesso manufactured by Eksonyi Gakusha
- Hydrocarbons such as mixed solvents; esters such as butyl acetate; ketones such as methylisobutylketone and acetate; ethylene glycol and diethylene Multi-valent alcohol such as glycol, tri-cylinder alcohol, glycerin, etc.
- Ethers such as tetrahydrofuran; glycol ethers such as butyl alcohol; 1-butanol, methyl alcohol, ethyl alcohol Monovalent alcohols such as alcohol, isopropropyl alcohol; 2, 4, 7, 9—tetramethylethyl 15—decinyl 4, 7 —Examples of acetylenes such as diols, 3,5 dimethyls and 11-hexyls At least one species selected from these can be used.
- At least one selected from tetramethyl-5-decyne-4,7-diol is preferably used.
- aliphatic saturated hydrocarbons having 6 to 12 carbon atoms and Z or aromatic hydrocarbons having 7 to 11 carbon atoms exert a remarkable defoaming effect, and It is preferable from the viewpoint of imparting the film-forming properties and film-forming properties of the composition. The details will be described later.
- Polyether polymer surfactants as antifoaming agents include, for example, monoester, sorbitan laurate and sodium sorbitan laurate. Acid triester, polyethylene glycol fatty acid ester, oxyethylene-oxypropylene random copolymer, oxyshelen-oxo Use of at least one nonionic surfactant with a low HLB value (hydrophilicity) selected from propylene block copolymers, etc.
- HLB value hydrophilicity
- the fatty acid ester as an antifoaming agent is, for example, triglyceride ester of fatty acid and glycerin (so-called triglyceride). It is also possible to use esters (so-called raw or plex) of fatty acids with higher monohydric alcohols or dihydric alcohols. However, it is not limited to these.
- a metal salt other than an alkali metal such as a fatty acid, a resin acid, and a naphthenic acid
- silicone-based compound as an antifoaming agent examples include dimethylsilicone, methylsilicone silicone, and organically modified silicone. It is possible to use at least one species from which to choose, but it is not limited to these. It can also be used in the form of a solution in which a silicone compound is dissolved in an organic solvent, or in the form of an emulsion in which the silicone compound is emulsified and dispersed in water. .
- the coating composition used in the present invention includes an organic liquid as a defoaming agent, a polyether-based polymer surfactant, and a silicone-based compound, which are blended as necessary. Is the solid content of the coating composition
- the viscosity of the coating composition when used is 0.1 to 50 OmPa '. s, preferably l-300 mPa * s, more preferably 5-130 mPa * s.
- the temperature of the paint at the time of use is usually from 0 to 25 ° C, and more preferably from 10 to 25 ° C.
- the paint viscosity is too high, it is difficult for the foam to break, so many traces of foam remain in the coating film even after drying and firing, and when the curtain floor is operated for a long period of time, The solid content adheres to the storage tank, and the traces of bubbles in the coating film further increase. If the viscosity of the paint is too low, the paint adhering to the substrate tends to flow. If the temperature at the time of coating is too low, the liquid carrier of the coating composition freezes when it is water, or the coating material needs to be diluted with the liquid carrier due to the lack of fluidity of the coating material. The thickness of the coating film after coating and drying becomes thin. Also, the temperature at the time of painting At 25 ° C. or higher, the fluorine-containing polymer particles tend to agglomerate.
- the measurement of viscosity in the present invention is carried out with a single cylinder rotational viscometer (SB type viscometer) described in JISK540-4.5.3.
- the present invention also relates to the use of a specific hydrocarbon compound as an anti-foaming agent, as described above, especially for a curtain floor coating. It relates to a suitable aqueous dispersion composition, and also to a coating composition.
- aqueous dispersion compositions and the specific hydrocarbon compounds used therein will be described in detail, but the parts already described, such as surfactants, will be described. Omitted to avoid duplication.
- Particular hydrocarbons that are particularly preferred as antifoaming agents are aliphatic saturated hydrocarbons having 6 to 12 carbon atoms and / or aromatic hydrocarbons having 7 to 11 carbon atoms. It is. The fact that these hydrocarbon compounds have a remarkable defoaming effect on the aqueous fluoropolymer-containing dispersion is a fact found for the first time in the present invention.
- Aliphatic saturated hydrocarbons having 5 or less carbon atoms have low boiling points and poor defoaming performance.
- aliphatic saturated hydrocarbons having 13 or more carbon atoms and aromatic hydrocarbons having 12 or more carbon atoms have a weak defoaming performance, and further have a high boiling point, so that the It delays drying and easily remains on the coating film.
- the aliphatic saturated hydrocarbon having 6 to 12 carbon atoms that can be used in the present invention is preferably one or a mixture of two or more compounds represented by the following general formulas. It is not limited to these. It also includes cyclic compounds such as ethylcyclohexane. CH 3 (CH 2 ) JCH 3
- aromatic hydrocarbons of to 11 include, for example, toluene, xylene, trimethylbenzen, methethylbenzene, propylbenzen, butylbenzene and the like. To It can be illustrated, but not limited to. Also, a mixture of two or more aromatic hydrocarbons selected from these may be used.
- Commercially available products include Solvesso 100, Solbesso 150, and Solbesso 200 (manufactured by Eksonyi Daigaku Co., Ltd.).
- At least one kind of aliphatic saturated hydrocarbon having 6 to 12 carbon atoms and at least one kind of aromatic hydrocarbon having 7 to 11 carbon atoms may be used in combination.
- No. As a commercially available product of this mixture, it is possible to exemplify a mineral spirit (Japanese Industrial Standard, Industrial Gasoline No. 4), and it is very inexpensive to obtain. This is advantageous in that
- the amount of the hydrocarbon compound added as an antifoaming agent is, as described above, 100% of the solid content of the aqueous fluoropolymer-containing dispersion.
- the above-mentioned other known antifoaming agents may be used in combination.
- the viscosity of the aqueous dispersion composition of the present invention is 0.1 to 500 mPa * s for curtain flow coating, preferably:! Preferably, it is adjusted to ⁇ 300 mPa-s.
- the viscosity is not particularly limited when applied to other uses or coating methods, and may be 0.1 to 10,000 mPa-s, depending on the application. Niha :! The viscosity may be adjusted in the range of ⁇ 100mPa.s. From the viewpoint of the solid content concentration, it is 10 to 80% by weight, usually 20 to 70% by weight.
- the coating composition used in the present invention may further contain various additives depending on the intended use of the coating film or for the purpose of improving paintability and coating film. And can be done.
- Additives include, for example, solid lubricants, pigments, fillers, pigment dispersants, anti-settling agents, moisture absorbers, surface conditioners, thixotropic agents, viscosity modifiers, gels
- the base material to be coated by the coating method of the present invention includes, for example, metals such as iron, aluminum, copper, and alloys thereof; Inorganic materials such as glass and ceramics can be exemplified, but are not limited to these.
- metals such as iron, aluminum, copper, and alloys thereof
- Inorganic materials such as glass and ceramics can be exemplified, but are not limited to these.
- curtain floor coater (I) which can be used in the present invention
- a well-known curtain floor coater (I) can be used for fluorine-containing polymer particles.
- a particularly improved force-to-tempo mouth-to-coater (II) may be used.
- the curtain flow coater (I) will be described according to the schematic flowchart shown in FIG. Basically, the curtain flower (I) is composed of a head section 3 having a slit 4, a storage tank 5 for the liquid coating composition 1, and a storage tank 5 for storing the liquid coating composition 1. 5, a paint supply pump 6 having a rotating part (impeller) 7 and a base material supply conveyor 8 and a liquid paint composition.
- the material 1 is transferred from the storage tank 5 at the lower part to the paint supply pump 6 so that the peripheral speed of the outer periphery of the rotating part 7 of the pump is adjusted via the transport pipe 20.
- This is a device that sends the substrate 2 to the head section 3, flows down from the slit 4, and coats the surface of the base material 2 sent by the conveyor 8.
- the paint supply pump 6 there are several types of paints depending on the viscosity of the paint composition 1, but the paint viscosity during use is 0.1 to 500 mPa * s.
- the impeller rotor blade
- a centrifugal pump that uses the centrifugal force to suck up the coating composition is preferred.
- the peripheral speed of the outer periphery of the rotating part (impeller 1) 7 needs to be 0.1 to 12.0 m / sec, preferably 1.0 to 8.0 Om / sec. More preferably, 3.0 to 7.0 ms is more preferable.
- the peripheral velocity of the outer periphery of the rotating part (impeller 1) can be obtained by the following equation.
- a flow control valve 16 and foreign substances are removed from a transport pipe 20 for feeding the coating composition from the pump 6 to the head section 3.
- a filter chamber 17 is provided for this purpose.
- a diagonal pump As the paint supply pump 6, besides the centrifugal pump described above, a diagonal pump, an axial pump, a gear pump, a vane pump, a screw pump, and a pump can be used.
- a diagonal pump As the paint supply pump 6, besides the centrifugal pump described above, a diagonal pump, an axial pump, a gear pump, a vane pump, a screw pump, and a pump can be used.
- Mump pump, screw pump, vortex Pumps with rotating parts, such as pumps, can also be used.
- the coating composition of the fluorine-containing polymer can be continuously applied to the base material.
- Other operating conditions are selected as appropriate.
- the curtain flow coater (II) includes a head portion 3 having a slit 4, a lower storage tank 5a of the liquid paint composition 1, and a liquid paint composition.
- the upper reservoir 5b, the pneumatic pump 9 and the base material supply conveyor 8 and the liquid paint composition 1 is transferred from the lower reservoir 5a to the pneumatic pump 9.
- This is a device for applying to the surface of the base material 2 sent in (8).
- This curtain floor overnight ( ⁇ ) is new in that the lower storage tank 5a, the upper storage tank 5b, and the pneumatic pump 9 are used to transport and supply the coating composition. It is. As described above, if a shear force is applied to the coating composition containing the fluorine-containing polymer particles, agglomeration and fiberization tend to occur. Therefore, in the curtain floor coater (II), the use of the pneumatic pump 9 minimizes the shear force of the sensor.
- the pneumatic pump 9 is disposed on the chamber 10, the connecting valve 11, the compressed air valve 12, the discharge valve 13, the transport pipe 14, and the transport pipe 14. It is basically composed of a check valve 15 and a valve. First, open the connecting valve 11 and open the lower storage tank 5a. The coating composition is introduced into the chamber 10.
- the coating composition raised in the upper storage tank 5b naturally falls due to its static pressure, flows down to the head section 3, and flows from the slit 4 to the curtain. It is applied to the base material 2 in the form of a film.
- a flow adjusting knob 16 may be provided to adjust the amount of water flowing down to the head section 3. The pumping operation of the paint composition by the pneumatic pump 9 is repeated in a cycle that allows the flow from the slit 4 to flow down in a steady state.
- Examples of the pneumatic pump 9 include a piston pump, a pranja pump, and a diaphragm pump, in addition to the above-described type of pump for supplying compressed air. Can be used.
- the air pressure applied to the chamber 10 may be appropriately selected according to the viscosity of the coating composition, the type of the fluorine-containing polymer, the effective width of the slit 4, and the like. Preferably, it is about 0.01 to 1. OMPa. Brief description of other favorable conditions common to (1) and (2).
- the gap of slit 4 in head 3 is adjusted so that the curtain-shaped film of the coating composition does not break in the viscosity and flow rate of the coating composition to be used. You Usually, it is in the range of 0.1 to 1.0 mm.
- the coating amount increases when the speed is slow, and the coating amount decreases when the speed is fast.
- the conveyor speed is determined to achieve the desired application rate, but is typically in the range of 20 to 150 meters per minute.
- the supply of the paint to the head 3 is performed by setting a flow control valve 16 in the middle of a single transport pipe 20, and is a schematic sectional view of the head 3.
- the inlet 22a is provided on one of the side walls 21a provided on the side wall 21a and 21b provided in the direction crossing the slit 4. It is doing better.
- the head section is naturally used.
- the amount of paint supplied to the head 3 is reduced, and the amount of the paint 1 in the head 3 is reduced.
- the amount of water flowing downstream from the inlet 22a decreases, and the amount of paint flowing down from the slit 4 becomes flat in the longitudinal direction of the slit 4. .
- the thickness of the coating film applied to the base material 2 becomes thinner at a portion farther from the inlet 22a.
- the supply of the paint to the head part 3 was reduced to the side wall 21a as shown in FIG. And the side wall 21b, the inlets 22a and 22b respectively provided at the same time, so that the paint supply amount is reduced and the inside of the head section 3 is reduced.
- the amount of paint 1 has decreased
- the transport pipe 20 is branched into two near the head 3 of the filter 117, and two pipes are used.
- the transport pipes 23a and 23b there is a method in which flow control valves 24a and 24b are provided in the respective transport pipes 23a and 23b and connected to the inlets 22a and 22b.
- two supply pumps shown in Fig. 1
- the amount of paint flowing into the head portion 3 from the opposed inlets 22a and 22b is adjusted by the flow control valves 24a and 24b so that they are substantially the same.
- the number of inlets provided on each side wall 21a or 21b may be one or more, but it is preferable that the number is the same.
- the coating composition is applied with a ten-flow coater, the coating composition is applied at 10 to 420 ° C for 10 to 45 minutes depending on the type of the coating composition. Dry and bake. After the coating film has been dried, if necessary, the coating can be performed using a curtain floor coater, and the process can be repeated. It is also possible to apply two or more coating layers.
- the coating film thus obtained is superior in surface smoothness and gloss as compared with a coating film applied by a conventional spray coating method.
- the use of the painted product is not particularly limited, but when the non-stickiness of the coating film is used, it can be used for flypans, pots, grill pots, rice cookers, ovens, and electric appliances. Pots, ice trays, hotplates, bakers, kitchen knives, gastables and other metal cooking utensils; rolls, range hoods, General industrial uses such as molds; and when utilizing the lubricity of coatings, tools such as saws and files; irons, bearings, valves, Examples include electric wires and metal foil (for sliding members).
- PTFE aqueous dispersion (Aqueous dispersion of PTFE particles with an average particle size of 60% by weight solid content)
- Polyether-based nonionic surfactant as dispersion stabilizer for PTFE
- Aqueous dispersion of polyamidoimid (contains 6% by weight), polyamidoimid varnish (solid content 29% by weight of polyamidoimid varnish (N-methyl-1--2)
- This coating composition was applied to a curtain flow coater (I) shown in Fig. 1 (peripheral speed of the rotating part (impeller) of the centrifugal pump) at a peripheral speed of 5 mZ sec. 0.5mm gap, effective conveyor width 300mm, conveyor length 1010mm (two installations.) Conveyor speed was adjusted to 80-100mZ). 18 to 22 ° C so that the film thickness after drying on a pre-degreased and sand-blasted aluminum plate is 12 to 15 ⁇ . After performing the Brammer coating, the coating was dried at 80 to 100 ° C for 15 minutes to prepare a dry coating film. The viscosity (20 ° C) at the time of use (painting) was 116 mPa * s, and painting was started 30 minutes after the start of operation of the tenth floor coater. No baking was done because it is a primer layer.
- the viscosity was measured at 20 ° C by rotating the rotor at 60 rpm for 2 minutes using a No. 2 porter, B-type viscometer (BM type) manufactured by Tokyo Keiki Co., Ltd. .
- a liquid coating composition was prepared by mixing the following components in the proportions (mass parts) shown in Table 1 and a layer of primer coated in the primer prepared in Example 1 was coated with a curtain flow coater. The paint was applied repeatedly using the tar (I).
- Polyether polymer surfactant 2 is a polyether polymer surfactant
- Oxyethylene propylene propylene random copolymer with average molecular weight of 25,000 (Polyether type high molecular surfactant as antifoaming agent)
- Toluene an anti-foaming agent as an organic liquid
- the curtain flower (I) has the same specifications as in Example 1, and the conveyor speed is 45 to 90 m / m depending on the target film thickness. Adjusted in minutes.
- Examples 2 to 7 were placed on the primer layer prepared in Example 1.
- the coating composition after drying under the coating conditions (peripheral speed of the pump impeller) shown in Table 1 was 17 to 22 / m (Table 2).
- the object to be coated obtained 30 minutes after the start of coating is dried at 80 to 100 ° C for 10 minutes, baked at 380 ° C for 20 minutes, cooled to room temperature, and then cooled as described above. A special coating test was performed. Table 1 shows the results.
- the average value (Ra value) of the surface roughness of the coating film is determined using a surface roughness meter (trade name: Surf Com) manufactured by Tokyo Seimitsu Co., Ltd. (Glossy)
- a liquid coating composition having the composition shown in Table 1 was prepared, and the primer layer prepared in Example 1 was prepared using the ten-floor coater (II) having the following specifications. At 20 ° C. Painting was performed about 30 minutes after the start of operation.
- II ten-floor coater
- the object to be coated 30 minutes after the start of coating was dried at 80 to 100 minutes for 10 minutes, baked at 380 ° C for 20 minutes, cooled to room temperature, and treated in the same manner as in Example 2.
- the coating film appearance and coating film test were performed. Table 1 shows the results.
- the gap of slit 4 is 0.5mm, the effective conveyor width is 300mm, and the conveyor length is 1010mm (two installations).
- Con Bear speed was adjusted to 45-90m / min.
- the maximum air pressure of the chamber 10 is set to 0. IMPa.
- Liquid coating compositions having the compositions shown in Table 1 were prepared. This coating composition was applied to a gravity spray nozzle with a spray gun with a diameter of 1.0 mm (RG-2 type, manufactured by Anest Iwata Co., Ltd.). / m spray spray pressure was applied under the condition of 0.2 MPa.
- the particles contained fluorine-containing polymer particles having an average particle diameter of 0.01 to 100 ⁇ and were used (0%).
- the paint composition containing fluoropolymer particles is used. It is possible to use a curtain flow coater, which was difficult to apply, has low surface roughness, excellent gloss, and shows traces of bubbles even when observed under a microscope. A coating film in which no or little is present is obtained.
- the peripheral speed of the rotating part of the paint supply pump should be set to 0.
- the peripheral speed of the rotating part of the paint supply pump should be set to 0.
- the curtain flow coater ( ⁇ ) using a pneumatic pump also has a small surface roughness, excellent gloss, and traces of bubbles even when observed under a microscope. An unacceptable coating film is obtained.
- this transport pipe 20 is branched into two at the upper part of the filter chamber 17. Then, the two transport pipes 23a and 23b were connected to the inlets 22a and 22b provided in the head section 3 as shown in FIG. 3, respectively.
- the peripheral speed of the outer periphery of the rotating part (impeller) of the centrifugal pump was 4.7 mZ seconds, and the gap of slit 4 was 0. 5mm, Conveyor effective width 300miri, Conveyor length 1010mm (2 pieces installed).
- the conveyor speed was adjusted to 85 m / min.) Under the coating conditions, an aluminum plate (200 mm x 200 mm) that had been previously degreased and sandblasted was used.
- the coating was started 30 minutes after the start of the operation of Riki-Ten-Flo-Ko overnight so that the film thickness after drying was 20 / z m.
- the object to be coated obtained 30 minutes after the start of coating is 80 ⁇ : dried at 100 ° C for 10 minutes, baked at 380 ° C for 20 minutes, cooled to room temperature, and then coated with the properties of m.
- the appearance of the coating film was examined, and the thickness of the coating film on each part of the article to be tested was measured in the following manner. Table 2 shows the results.
- the film thickness was also measured for the coated product obtained in Example 2 (in the case of one inlet).
- Example 10 the peripheral speed of the outer periphery of the rotating part (in-buff) of the centrifugal pump was reduced to 4.0 m / sec.
- the coated article was examined for coating film properties, appearance and film thickness. Table 2 shows the results. Table 2
- the coating composition was prepared by mixing the following components in the proportions (parts by weight) shown in Table 3.
- PTFE average particle size 0.28 i mPTFE particles
- Polyester-terminated resin emulsion An emulsion of polyether-based resin particles with a solid content of 30% by weight and a molecular weight of about 2,000.
- Nonionic surfactant Polyoxyethylene alkylphenyl ether (molecular weight 640)
- Fluorine-containing anionic surfactant perfluorooctanoic acid ammonium
- Anionic surfactant sodium rauryl sulfate
- Polyester-based film-forming agent oxyshylene oxy propylene block copolymer having an average molecular weight of 25,000
- Millbase 6.75 parts by weight of deionized water, 0.72 parts by weight of a polyether nonionic surfactant, ammonium perfluoromonate A mixture obtained by mixing a mixture of 0.18 parts by weight of a rubber, 0.90 parts by weight of carbon, and 0.45 parts by weight of bengala (a ferric oxide) with a pole mill (filler)
- Titanium dioxide coated mica Mica coated with titanium dioxide having a specific gravity of about 3 and an average particle size
- the measurement of the amount of foaming was performed as follows.
- the paint (aqueous dispersion) composition shown in Example 18 in Table 3 was preliminarily degreased and applied to an aluminum plate as shown in FIG.
- the painting was performed about 30 minutes after the start of operation of the container flow coater under the condition that the conveyor speed was 85 m / min in seconds.
- the coating is dried at 80-100 ° C for 10 minutes, baked at 380 ° C for 20 minutes (film thickness after firing: 22 m), cooled to room temperature, and examined for the properties of the coating film in the following manner. I thought it.
- aqueous dispersion composition was applied to the curtain floor overnight as shown in Fig. 1 (peripheral speed of the rotating part (impeller) of the centrifugal pump: 4.7 mZ sec. 0.5mm gap, effective conveyor width 300mm, conveyor length 1010mm (2 pieces installed). The conveyor speed was adjusted to 80-100m. Then, the pre-degreased aluminum plate was painted at 18 to 22 ° C. 80 to after coating: L After drying at 00 ° C for 10 minutes, baking at 380 ° C for 20 minutes, cooling to room temperature, and observing the appearance of the coating film. The film thickness after firing was 22 ⁇ m. The viscosity (20 ° C) at the time of use (painting) was 106 mPa * s, and painting was started 30 minutes after the start of operation of the power and tenter port.
- Viscosity was measured at 20 ° C by rotating the mouth at 60 rpm for 2 minutes using a No. 2 rotor with a B-type viscometer (BM type) manufactured by Tokyo Keiki Co., Ltd. was
- Coating was carried out using a tenth-flow coater under the same conditions as in Example 18 except that the composition shown in Comparative Example 4 in Table 3 was used as the aqueous dispersion composition. became . Visual observation of the fired coating film showed traces of bubbles, and no smooth coating film was formed.
- the present invention it is possible to apply a ten-thousand-one-hour system which has been difficult to use for coating a coating composition containing a fluorine-containing polymer.
- a large amount of paint can be continuously applied, and the paint can be reused, so that an economical and environmentally friendly coating method can be provided.
- the resulting coating film of the coated article has low surface roughness, excellent gloss, and no or little traces of bubbles even when observed under a microscope.
- the fluorine-containing polymer aqueous dispersion composition to which the specific hydrocarbon compound of the present invention has been added as an antifoaming agent has little foaming, and has a reduced flow rate.
- the coating film obtained by applying the aqueous dispersion composition of the present invention on a curtain floor is suitable for painting by a microscope. Observed at, there is no trace of bubbles and it is smooth.
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
- Paints Or Removers (AREA)
- Coating Apparatus (AREA)
Description
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020027009367A KR20020074482A (ko) | 2000-01-24 | 2001-01-16 | 기재의 피복방법, 피복물품 및 피복장치 |
| EP01900787A EP1252937A4 (en) | 2000-01-24 | 2001-01-16 | METHOD OF SUBSTRATE TREATMENT, COATED ARTICLE AND COATING DEVICE |
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000015011 | 2000-01-24 | ||
| JP2000-15011 | 2000-01-24 | ||
| JP2000-82764 | 2000-03-23 | ||
| JP2000082764A JP2001261908A (ja) | 2000-03-23 | 2000-03-23 | 含フッ素重合体系水性分散液組成物および塗料組成物 |
| JP2000158790A JP2001276705A (ja) | 2000-01-24 | 2000-05-29 | 基材の被覆方法、被覆物品および被覆装置 |
| JP2000-158790 | 2000-05-29 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2001053006A1 true WO2001053006A1 (en) | 2001-07-26 |
Family
ID=27342119
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2001/000226 Ceased WO2001053006A1 (en) | 2000-01-24 | 2001-01-16 | Method for coating substrate, coated article and coating apparatus |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US20030054110A1 (ja) |
| EP (1) | EP1252937A4 (ja) |
| KR (1) | KR20020074482A (ja) |
| CN (1) | CN1199737C (ja) |
| TW (1) | TW500639B (ja) |
| WO (1) | WO2001053006A1 (ja) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111495681A (zh) * | 2020-04-18 | 2020-08-07 | 宋翔 | 一种汽车配件模具着色剂覆盖装置 |
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| CN1261195C (zh) * | 2003-10-24 | 2006-06-28 | 深圳奥特迅电气设备有限公司 | 一种油气分离膜、其制造方法以及用其制成的气体传感器 |
| EP1550703A1 (de) * | 2004-01-05 | 2005-07-06 | Sika Technology AG | Schutzfolie aus Schmelzklebstoff sowie Verfahren und Vorrichtung zum Applizieren derselben |
| GB0416900D0 (en) * | 2004-07-29 | 2004-09-01 | Arjo Wiggins Fine Papers Ltd | Curtain coating process using a high solids content composition |
| CN101197209B (zh) * | 2006-12-05 | 2010-06-09 | 泉州市火炬电子元件厂 | 利用幕式淋涂制造多层陶瓷元件的方法和装置 |
| DE102008026199B3 (de) * | 2008-05-30 | 2009-10-08 | Rena Gmbh | Vorrichtung und Verfahren zur elektrischen Kontaktierung von ebenem Gut in Durchlaufanlagen |
| DE102010000449A1 (de) * | 2010-02-17 | 2011-08-18 | Hydro Aluminium Deutschland GmbH, 53117 | Verfahren zur Herstellung eines Architekturblechelements |
| US8783273B2 (en) * | 2011-04-07 | 2014-07-22 | Intermolecular, Inc. | No-contact wet processing tool with site isolation |
| RU2585187C2 (ru) | 2011-10-13 | 2016-05-27 | Кроноплюс Текникаль АГ | Устройство и способ нанесения покрытия на листовые элементы наливом |
| UA111997C2 (uk) | 2012-04-02 | 2016-07-11 | Кроноплюс Текнікал Аг | Панель з покриттям, нанесеним методом прямого друку |
| WO2013185814A1 (de) | 2012-06-13 | 2013-12-19 | Kronoplus Technical Ag | Paneel mit dekorschicht sowie verfahren zum bedrucken von platten |
| CN102847670A (zh) * | 2012-08-16 | 2013-01-02 | 青岛华美木业有限公司 | 一种表面人造板淋涂表面漆工艺 |
| UA111803C2 (uk) | 2012-10-05 | 2016-06-10 | Кроноплюс Текнікал Аг | Підлогова панель для зовнішнього застосування |
| JP5680604B2 (ja) * | 2012-10-29 | 2015-03-04 | 株式会社川熱 | 防食被膜付き鉄筋棒の製造装置 |
| CN103640219B (zh) * | 2013-12-06 | 2016-01-20 | 中国科学院化学研究所 | 一种三维制造方法及其在柔版制备中的应用 |
| CN113097457A (zh) * | 2021-03-26 | 2021-07-09 | 中国电子科技集团公司第十八研究所 | 一种高稳定性氟化碳水系浆料及其制备方法 |
| US11660631B2 (en) * | 2021-05-05 | 2023-05-30 | Oav Equipment And Tools, Inc. | Glue applying mechanism of edge banding machine with glue quantity regulator |
| US11541415B2 (en) * | 2021-05-26 | 2023-01-03 | Oav Equipment And Tools, Inc. | Glue applying mechanism of edge banding machine for applying glue to workpiece having oblique surface and edge banding machine using the glue applying mechanism |
| IT202100018653A1 (it) | 2021-07-15 | 2023-01-15 | Durst Group Ag | "Metodo per rivestire almeno un supporto di stampa con un fluido liquido" |
| CN115672662B (zh) * | 2022-11-10 | 2025-07-04 | 德安县塑丽龙纺织有限公司 | 一种用于纺织纤维的表面上处理剂装置及方法 |
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| KR100417357B1 (ko) * | 1995-02-02 | 2004-05-03 | 미네소타 마이닝 앤드 매뉴팩춰링 캄파니 | 유체 박막 코팅방법 및 그 장치 |
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2001
- 2001-01-16 KR KR1020027009367A patent/KR20020074482A/ko not_active Withdrawn
- 2001-01-16 CN CNB018040292A patent/CN1199737C/zh not_active Expired - Fee Related
- 2001-01-16 US US10/181,714 patent/US20030054110A1/en not_active Abandoned
- 2001-01-16 TW TW090100898A patent/TW500639B/zh not_active IP Right Cessation
- 2001-01-16 WO PCT/JP2001/000226 patent/WO2001053006A1/ja not_active Ceased
- 2001-01-16 EP EP01900787A patent/EP1252937A4/en not_active Withdrawn
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| JPS57147473A (en) * | 1981-03-09 | 1982-09-11 | Shigeharu Nagane | Method and apparatus for curtain flow coating |
| JPS6238272A (ja) * | 1985-08-12 | 1987-02-19 | Kawakami Toryo Kk | カ−テンフロ−コ−タ−による凹凸面を有する板状素材の塗装方法 |
| JPH01289896A (ja) * | 1988-05-16 | 1989-11-21 | Central Glass Co Ltd | 含フッ素樹脂分散体 |
| JPH0657893A (ja) * | 1992-08-05 | 1994-03-01 | Nisshin Kogyo Kk | 屋根下葺材 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111495681A (zh) * | 2020-04-18 | 2020-08-07 | 宋翔 | 一种汽车配件模具着色剂覆盖装置 |
| CN111495681B (zh) * | 2020-04-18 | 2021-08-20 | 义乌市旻具五金工具有限公司 | 一种汽车配件模具着色剂覆盖装置 |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1252937A1 (en) | 2002-10-30 |
| TW500639B (en) | 2002-09-01 |
| CN1199737C (zh) | 2005-05-04 |
| CN1395510A (zh) | 2003-02-05 |
| US20030054110A1 (en) | 2003-03-20 |
| EP1252937A4 (en) | 2007-10-24 |
| KR20020074482A (ko) | 2002-09-30 |
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