WO2023010997A1 - Low-voc organic solvent-free heat-resistant water-based paint and high-temperature-resistant corrosion-resistant coating prepared therefrom - Google Patents

Low-voc organic solvent-free heat-resistant water-based paint and high-temperature-resistant corrosion-resistant coating prepared therefrom Download PDF

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WO2023010997A1
WO2023010997A1 PCT/CN2022/097613 CN2022097613W WO2023010997A1 WO 2023010997 A1 WO2023010997 A1 WO 2023010997A1 CN 2022097613 W CN2022097613 W CN 2022097613W WO 2023010997 A1 WO2023010997 A1 WO 2023010997A1
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engineering plastic
resistant coating
organic solvent
low
resistant
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French (fr)
Chinese (zh)
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王锡铭
史海兵
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浙江鹏孚隆新材料有限公司
浙江鹏孚隆科技股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D181/00Coating compositions based on macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur, with or without nitrogen, oxygen, or carbon only; Coating compositions based on polysulfones; Coating compositions based on derivatives of such polymers
    • C09D181/06Polysulfones; Polyethersulfones
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/08Anti-corrosive paints
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/18Fireproof paints including high temperature resistant paints
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/20Diluents or solvents
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/60Additives non-macromolecular
    • C09D7/61Additives non-macromolecular inorganic
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/38Boron-containing compounds
    • C08K2003/382Boron-containing compounds and nitrogen
    • C08K2003/385Binary compounds of nitrogen with boron
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/011Nanostructured additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/08Stabilised against heat, light or radiation or oxydation

Definitions

  • the invention relates to a heat-resistant coating, in particular to a low-VOC organic-solvent-free hot water-resistant coating and a high-temperature-resistant and corrosion-resistant coating prepared therefrom, belonging to the technical field of coatings.
  • Heat-resistant coatings have been widely used in industrial protection, cooking utensils, and household appliances. Solvate.
  • Patent CN104974661 discloses a technical scheme of polyethersulfone ultrafine powder and its material application.
  • the polyethersulfone ultrafine powder described in this patent is obtained by grinding, has an irregular structure, and is a solid particle. During the film formation process, It must be supplemented with solvents (see its examples), failing to achieve environmental improvement.
  • Patents CN1302047 and CN1305936 disclose a method for manufacturing water-based polyethersulfone dispersion liquid and redispersible polyarylethersulfone micropowder.
  • the surfactants described in the two patents decompose and volatilize at a high temperature, resulting in polyethersulfone During the baking and film forming process, a large amount of surfactant cracks remain, which seriously affects the compactness and adhesion of the coating film.
  • the degradation products of the surfactant are biohormone compounds, which pose health risks.
  • Patent C08J 3/12 discloses a method for preparing spherical polyarylene ether sulfone or polyarylene ether ketone micropowder. This patent discloses a method for preparing microspheres by spraying polymer solution. This method consumes a large amount of solvent. Moreover, the energy consumption is high, the particle size is large and the distribution is wide, and the applicable surface of the product is limited.
  • the application of coatings for engineering plastics is mainly divided into oil-based coatings, water-based coatings, and powder coatings.
  • Oil-based coatings have been phased out by the state due to high VOC emissions; at present, water-based coatings mainly use high-temperature solvents for water-soluble engineering plastics to facilitate coating.
  • Film binding force although it is still inevitable to add a certain proportion of solvents, compared with oil-based paints, water-based paints greatly reduce VOC emissions; powder coatings are completely solvent-free, and the current mainstream resin powder manufacturing process, pollution Large, high energy consumption, more restrictions on coating construction.
  • the invention can process specified engineering plastics into hollow particles of 0.1-2 ⁇ m through a special surfactant system and a solvent evaporation process, so as to realize the melting and film-forming of engineering plastics in a solvent-free state of water-based coatings.
  • the engineering plastic dispersion of the present invention is completely dried, and the dried engineering plastic particles will also be suitable for powder coatings.
  • the purpose of the present invention is to provide a low-VOC organic-solvent-free hot-water-resistant coating, which does not contain organic solvents, and can still provide excellent paint film performance when the formula structure remains unchanged and only the organic solvent is removed.
  • the film-forming baking temperature is relatively low (the film-forming baking temperature is 280-380° C. for 10 minutes).
  • the invention also provides a preparation method of the heat-resistant and hydrolysis-resistant engineering plastic dispersion.
  • a low-VOC organic solvent-free hot water resistant coating is mainly made of the following raw materials:
  • the engineering plastic particles are added in the form of engineering plastic dispersion liquid, which is obtained by emulsification-solvent evaporation method.
  • the engineering plastic particle diameter in the engineering plastic dispersion liquid is 0.1-2 ⁇ m, and has a hollow spherical shape. Or a spherical structure; the engineering plastic dispersion is composed of 10-75 wt% of engineering plastic particles, 0.5-10 wt% of surfactant, and the balance is water.
  • the low-VOC, organic-solvent-free, hot-water-resistant coating of the present invention does not contain organic solvents, and the film-forming baking temperature is relatively low (the film-forming baking temperature is 280-380°C, 10min), and the main resin of the coating is engineering plastic dispersion .
  • the organic solvent refers to organic solvents such as N-methylpyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide, and benzene.
  • the engineering plastic is selected from one or a combination of polyethersulfone, polyphenylenesulfone, polyetherimide, polysulfone, polyaryletherketone, polyarylethersulfoneketone.
  • the engineering plastic particles in the engineering plastic dispersion are engineering plastics, or contain 0.5-10% of engineering plastics by mass, carbon nanotubes (CNTs), acidified carbon nanotubes, nano-boron nitride, graphene , graphene oxide, nano-mica, nano-bentonite or a mixture of several modified engineering plastics.
  • CNTs carbon nanotubes
  • acidified carbon nanotubes nano-boron nitride
  • graphene graphene oxide
  • nano-mica nano-bentonite or a mixture of several modified engineering plastics.
  • the solvent is one or a mixture of dichloromethane, trichloromethane, dichloroethane, trichloroethane, carbon disulfide, the boiling point is 40 ⁇ 80 °C (0.1MPa, room temperature 25-27 °C),
  • the boiling point ranges from 45 to 75°C;
  • the most preferred boiling point range is 55-65°C.
  • the emulsifying surfactant is an anionic surfactant of A - B + structure, wherein A - is an alkyl carboxylate structure of the molecular formula C n H 2n-1 O 2 - , wherein n is 8-16; B + is selected from NH 4 + , Na + , K + .
  • the value of n is preferably 10-14.
  • the surfactant is intermixed with two materials with different n values, and the ratio of the two is 0.1-0.9:1. Materials with different n values are more effective when used with each other.
  • A is preferably a straight-chain alkanyl carboxylate;
  • B + is preferably Na + .
  • the composition of the engineering plastic dispersion is 25-55 wt% of engineering plastic particles, 0.5-5 wt% of surfactant, and the balance is water. More preferably, the composition of the engineering plastic dispersion is 35-40 wt% of engineering plastic particles, 0.5-3 wt% of surfactant, and the balance is water. More preferably, the composition of the engineering plastic dispersion is 35-40 wt% of engineering plastic particles, 0.5-1 wt% of surfactant, and the balance is water.
  • the engineering plastic particles in the engineering plastic dispersion have a statistical value of particle size D50 ⁇ 1 ⁇ m and D100 ⁇ 2 ⁇ m; the engineering plastic particles in the engineering plastic dispersion have an average hollow ratio of not less than 25%.
  • the pigment is selected from monoazo pigments, disazo pigments, azo lake pigments, naphthol AS pigments, phthalocyanine blue, phthalocyanine green, other metal phthalocyanines, quinacridone pigments , Benzimidazolone pigments, dioxazine pigments, anthrone pigments and other organic pigments or a mixture of several.
  • the pigment may also be one or a mixture of titanium dioxide, zinc sulfide, zinc oxide, cadmium pigments, chromic acid pigments, ultramarine blue pigments, iron blue pigments, and carbon black pigments.
  • the functional filler is selected from quartz, barium sulfate, titanium dioxide, chromium dioxide, zinc oxide, iron oxide, aluminum oxide, silicon oxide, zirconia aluminum silicate, aluminum magnesium silicate, silicon carbide, titanium carbide, Silicon nitride, titanium nitride, cubic boron nitride, barium sulfate whiskers, calcium carbonate whiskers, carbon fiber powder, glass fiber powder, quartz fiber powder, carbon nanotubes, graphene oxide, graphene, basalt fiber, mica, One or a mixture of talcum powder, hexagonal boron nitride or graphite.
  • the functional fillers may be pre-surface-treated with silane coupling agents and organic polymers.
  • Example 10 is a comparative example. The functional fillers have not been surface-treated and exhibit lower salt water resistance.
  • the functional additive may be a combination of common commercially available leveling agents, anti-settling agents, anti-sagging stabilizers, wetting agents, defoamers, rust inhibitors, and thixotropic agents.
  • the functional auxiliary agent can be inorganic, organic-inorganic hybrid, organic, or a combination of several types of auxiliary agents.
  • the inorganic functional additives may be inorganic mineral materials, and/or artificially synthesized mineral materials.
  • the organic-inorganic hybrid and organic functional additives can be silicones, polyoxyethylenes, polyacrylates, celluloses, polyamides, organic fluorides, mineral oils, carboxylates Polymers, polycarbonates.
  • the organic-inorganic hybrid and organic functional additives preferably have a boiling point and/or degradation temperature range of 100-350°C. More preferably, the boiling point and/or degradation temperature range is 150-320°C. Optimally, the boiling point and/or degradation temperature range is 200-280°C.
  • a kind of preparation method of described engineering plastics dispersion liquid comprises the steps:
  • step S2 Add water to the material obtained in step S1 under stirring at 300-800 rpm to obtain an oil-in-water emulsion;
  • the oil-in-water emulsion is evaporated and concentrated to obtain the water-based engineering plastic dispersion.
  • the viscosity of the system is controlled by a solvent to be 100-500 Pa.s, more preferably the viscosity of the system is 150-250 Pa.s.
  • the solvent evaporation process is in the form of flash evaporation, and the oil-in-water emulsion evaporates the solvent quickly by heating with atomized steam or heating with wiped film evaporation.
  • the solvent evaporation process is fast and efficient, and the system does not introduce normal temperature gas.
  • the invention relates to a high-temperature-resistant and corrosion-resistant coating obtained by coating the low-VOC organic-solvent-free hot water-resistant coating.
  • a method for preparing a high-temperature-resistant and corrosion-resistant coating The raw materials of the low-VOC organic-solvent-free hot water-resistant coating are mixed according to the proportion, dispersed uniformly, sprayed on a substrate that has undergone degreasing and roughening treatment, and wet-coated The film is baked twice at a temperature of 145-155°C for 10 ⁇ 2 minutes and at a temperature of 280-380°C for 10 ⁇ 2 minutes to obtain the high-temperature and corrosion-resistant coating.
  • a method for preparing a high-temperature-resistant and corrosion-resistant coating The raw materials of the low-VOC organic-solvent-free hot-water-resistant coating according to claim 1 are mixed and uniformly dispersed according to the proportion, and the coating is sprayed onto the aluminum substrate that has undergone degreasing and roughening treatment. The material is baked at 145-155°C for 10 ⁇ 2min and then cooled to room temperature naturally.
  • the composite coating film is baked twice at 145-155°C for 10 ⁇ 2 minutes and 280-380°C for 10 ⁇ 2 minutes to obtain a high-temperature and corrosion-resistant coating.
  • the coating has more excellent non-stick, self-cleaning and corrosion-resistant properties.
  • the heat-resistant and hydrolysis-resistant engineering plastic dispersion liquid of the present invention has expandability, and can evenly introduce functional fillers into micron and submicron engineering plastic particles; it has a more uniform and smaller engineering plastic particle size (0.1 ⁇ 2 ⁇ m); easy to melt in use, high bonding strength of substrate;
  • the low-VOC, organic-solvent-free, hot-water-resistant coating of the present invention does not contain organic solvents, and can still provide excellent paint film performance when the formula structure remains basically unchanged and only organic solvents are removed, greatly reducing the development of new formulas workload:
  • the low-VOC organic solvent-free hot water resistant coating of the present invention has a low film-forming baking temperature (film-forming baking temperature is 280-380°C, 10min);
  • the high-temperature and corrosion-resistant coating obtained by coating the low-VOC organic-solvent-free hot water-resistant coating of the present invention has excellent adhesion.
  • Fig. 1 is the particle size detection report that comparative example 1 makes PES dispersion liquid
  • Fig. 2 is the SEM photograph that comparative example 1 makes PES dispersion liquid particle
  • Fig. 3 is the particle size detection report that comparative example 2 makes PES dispersion liquid
  • Fig. 4 is the SEM photograph that comparative example 3 makes PES dispersion liquid particle
  • Fig. 5 is the particle size detection report that embodiment 1 makes PPSU dispersion liquid
  • Fig. 6 is the SEM photograph that embodiment 1 makes PPSU dispersion liquid particle
  • Fig. 7 is the TEM picture of the PPSU dispersion liquid particle that embodiment 1 makes.
  • the particle size analysis of the dispersed particles of engineering plastics is analyzed and measured by Baxter BT-9300S laser particle size analyzer;
  • the TEM photo of the dispersed particles of engineering plastics was measured by Talos F200X transmission electron microscope.
  • PES coarse powder BASF Co., Ltd., grade E 2020 P, D50 ⁇ 2mm;
  • Nano-boron nitride Suzhou Napor Material Technology Co., Ltd., brand NS-BN, D50 ⁇ 500nm.
  • the particle size analysis of resin dispersed particles is measured by Baxter BT-9300S laser particle size analyzer;
  • Adhesion test refer to GB/T9286-1998 to draw 1mm hundred grids, and the test results;
  • Salt water resistance test refer to GB/T32095.3, measured in 5% sodium chloride solution, slightly boiling conditions;
  • a preparation method of an engineering plastic dispersion the specific steps are as follows: configure materials according to the composition listed in Table 1, grind in a constant temperature vertical ball mill at 25°C for 24 hours, and then grind in a horizontal sand mill for 32 hours to obtain PES grinding Dispersions. Detected by a laser particle size analyzer, the particle size D50 of the PES particles in the dispersion is 7 ⁇ m, and the D90 is 17 ⁇ m.
  • the particle size test report of the PES dispersion is shown in Figure 1, and the SEM photo of the PES dispersion particles is shown in Figure 2.
  • a preparation method of an engineering plastic dispersion the specific steps are as follows: the formula is the same as in Example 1, grind in a constant temperature vertical ball mill at 25°C for 36 hours, and then grind in a horizontal sand mill for 72 hours to obtain the PES grinding dispersion. Detected by a laser particle size analyzer, the particle size D50 of the PES particles in the dispersion is 3 ⁇ m, and the D90 is 12 ⁇ m.
  • a kind of preparation method of engineering plastic dispersion liquid, concrete steps are as follows:
  • Step 1 Take 200 parts of chloroform, add 6 parts of methanol and 60 parts of PES coarse powder, and stir for 30 minutes until PES is fully dissolved; at the same time, take 5 parts of sodium dodecylbenzenesulfonate and dissolve it in 260 parts of water.
  • Step 2 Pour the sodium dodecylbenzenesulfonate aqueous solution into the colloid mill, then slowly add the chloroform solution of PES into the colloid mill, and disperse to obtain the emulsified dispersion of the PES solution.
  • Step 3 pour the material obtained in step 2 into a three-necked flask equipped with a stirring and condensing device, heat it in a water bath, control the temperature in multiple stages, and control the temperature not to exceed 65°C until no solvent is evaporated, and then heat up to 85°C , and keep the temperature for 30 minutes to obtain a solvent-free PES aqueous dispersion.
  • the material in the flask was taken out for laser particle size analysis, and SEM analysis was performed after drying. The SEM analysis results are shown in Figure 4.
  • a kind of preparation method of engineering plastic dispersion liquid, concrete steps are as follows:
  • Step 1 Take 200 parts of chloroform, add 4 parts of sodium dodecanoate, 4 parts of sodium myristate, and 60 parts of PES coarse powder, and stir for 30 minutes until PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 200 ⁇ 10Pa.s.
  • Step 2 Stir at a rotational speed of 500 rpm, and at the same time slowly add 300 parts of water, control the addition of water to complete within 5-10 minutes, and obtain an emulsified dispersion of the PES solution.
  • Step 3 Set the spray steam temperature to 120°C, the steam flow rate to 100L/min, and the emulsified dispersion liquid flow rate of the PES solution to 100g/min, and quickly remove the chloroform in the dispersion liquid by spray evaporation to obtain a heat-resistant and hydrolysis-resistant PES dispersion liquid .
  • Figure 5- Figure 7 proves that after the technical treatment of the present invention, the obtained engineering plastic dispersion product has spherical and spherical appearance, small particle size, D50 ⁇ 0.4 ⁇ m, D100 ⁇ 0.8 ⁇ m, and has a hollow structure.
  • Step 1 Take 150 parts of chloroform, add 4 parts of sodium dodecanoate, 4 parts of sodium myristate, and 60 parts of PPSU coarse powder, and stir for 30 minutes until PPSU is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 500 ⁇ 10Pa.s.
  • Steps 2 and 3 refer to Example 1.
  • the obtained PPSU dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.7-10 ⁇ m.
  • Step 1 Take 200 parts of chloroform, add 4 parts of sodium octadecanoate, 4 parts of sodium hexadecanoate, and 60 parts of PES coarse powder, and stir for 30 minutes until the PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 200 ⁇ 10Pa.s.
  • Steps 2 and 3 refer to Example 1.
  • the obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.5-5 ⁇ m.
  • Step 1 Take 150 parts of chloroform, add 6 parts of sodium octadecanoate, 6 parts of sodium hexadecanoate, and 60 parts of coarse PES powder, and stir for 30 minutes until PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 500 ⁇ 10Pa.s.
  • Steps 2 and 3 refer to Example 1.
  • the obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.1-3 ⁇ m.
  • Step 1 Take 200 parts of chloroform, add 6 parts of sodium dodecanoate, 2 parts of sodium myristate, and 60 parts of PES coarse powder, and stir for 30 minutes until PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 200 ⁇ 10Pa.s.
  • Steps 2 and 3 refer to Example 1.
  • the obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.1-1.6 ⁇ m.
  • Step 1 Take 200 parts of chloroform, add 2 parts of sodium dodecanoate, 6 parts of sodium myristate, and 60 parts of coarse PES powder, and stir for 30 minutes until PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 200 ⁇ 10Pa.s.
  • Steps 2 and 3 refer to Example 1.
  • the obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.1-2.2 ⁇ m.
  • a kind of preparation method of engineering plastic dispersion liquid, concrete steps are as follows:
  • Step 1 Take 200 parts of chloroform, add 4 parts of capric acid, 4 parts of dodecanoic acid, 15 parts of concentrated ammonia water (20wt%), and 60 parts of PES coarse powder, and stir for 30 minutes until PES is fully dissolved. Adjust the viscosity of the solution to 200 Pa.s by post-supplementing chloroform.
  • Step 2 step 3, with reference to embodiment 1.
  • the obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.3-1.8 ⁇ m.
  • a kind of preparation method of engineering plastic dispersion liquid, concrete steps are as follows:
  • Step 1 Take 200 parts of chloroform, add 5 parts of nano-boron nitride, 4 parts of sodium octanoate, 4 parts of sodium dodecanoate, stir well, then add 50 parts of PES coarse powder, stir for 30 minutes until PES Fully dissolve. Adjust the viscosity of the solution to 400 Pa.s by post-supplementing chloroform.
  • Step 2 step 3, refer to Example 1;
  • the obtained nano-mica/PES composite particle dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.3-2 ⁇ m.
  • the particle size data of the dispersions of the above comparative examples and examples are shown in Table 2. According to Table 2, it can be known that the grinding process produces engineering plastic dispersions, and the particle size of engineering plastics is on the order of 10 ⁇ m, and it is difficult to further refine them.
  • the selection of surfactant severely limits the size of emulsified particles, and the unreasonable evaporation process also affects the shape of particles after solvent removal.
  • the selected surfactant system of the present invention has obvious advantages in the emulsification effect, the emulsified particle size is smaller, and the particle size distribution is narrow. Among them, under the formula and process combination of Example 1, the particle size of the dispersion liquid of special engineering materials can be achieved. All in the submicron size range.
  • the PES dispersion obtained in Comparative Example 1 and Example 1 is prepared respectively, and the coatings are formulated according to the coating ingredients listed in Table 3, wherein PTFE, Carbon black pigments, talcum powder, and thickeners are all fed in water-dispersed form when preparing coatings, and the PES described in Table 3 is the solid content.
  • the data in table 4 proves that the prepared engineering plastic dispersion of the present invention, because the engineering plastic particles possess special size and structure, in coating application, can realize the coating that water-based coating does not have organic solvent, but is consistent with the coating that contains organic solvent performance.
  • a low VOC organic solvent-free hot water resistant coating is made of the following raw materials: PES particles 15%, PTFE 0%, carbon black 1%, graphene oxide 1%, wetting agent 0.5%, acrylic acid Thickener 2%, water balance, the total weight of the above raw materials is 100%.
  • the PES particles are fed in the form of the engineering plastic dispersion prepared in Example 1.
  • a method for preparing a high-temperature-resistant and corrosion-resistant coating The raw materials of the above-mentioned low-VOC organic-solvent-free hot-water-resistant coating are mixed according to the proportion, dispersed evenly, and sprayed on a substrate that has been degreased and roughened.
  • the high temperature and corrosion resistant coating is obtained by baking twice at 150°C for 10 minutes and at 340°C for 10 minutes.
  • a low VOC organic solvent-free hot water resistant coating is made of the following raw materials: PES particles 15%, PTFE 0%, carbon black 1%, graphene 1%, wetting agent 0.5%, acrylic thickening Agent 2%, water balance, the total weight of the above raw materials is 100%.
  • the PES particles are fed in the form of the engineering plastic dispersion prepared in Example 1.
  • a method for preparing a high-temperature-resistant and corrosion-resistant coating The raw materials of the above-mentioned low-VOC organic-solvent-free hot-water-resistant coating are mixed according to the proportion, dispersed evenly, and sprayed on a substrate that has been degreased and roughened.
  • the high temperature and corrosion resistant coating is obtained by baking twice at 150°C for 10 minutes and at 340°C for 10 minutes.
  • a method for preparing a high-temperature-resistant and corrosion-resistant coating the specific steps are as follows:
  • Spray the undercoat material on the degreased and roughened aluminum substrate control the sintering temperature within the range of 150-180°C for 5-10 minutes; after the undercoat is formed, cool it down to room temperature naturally.
  • the specific method for removing the organic solvent from the PES dispersion prepared in Comparative Example 2 Take 1000 g of the PES dispersion prepared by the grinding method in Comparative Example 2, put it into a 5 L 3-necked flask, add 3000 g of pure water, and stir for 30 minutes at 60 ° C. , and then perform suction filtration.
  • the first step controls the temperature within the range of 150-180°C for 5-10 minutes, and the second step controls the temperature at 375-380°C.
  • the time is 8-10 minutes.
  • top coat 100% by total weight: PTFE 42%, acrylic thickener 3%, pearl powder 0.5%, propylene glycol 2%, surfactant 3%, leveling agent 0.35%, catalyst Dry agent 3%, water balance.
  • each embodiment in this specification is described in a progressive manner, each embodiment focuses on the difference from other embodiments, and the same or similar parts of each embodiment can be referred to each other.
  • the description is relatively simple, and for the related information, please refer to the description of the method part.

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Abstract

The present invention relates to the technical field of paint, and particularly to heat-resistant paint, in particular to low-VOC organic solvent-free heat-resistant water-based paint and a high-temperature-resistant corrosion-resistant coating prepared therefrom. The low-VOC organic solvent-free heat-resistant water-based paint is mainly prepared from the following raw materials: 5-30% of engineering plastic particles, 0-15% of PTFE, 0.1-2% of a pigment, 0.5-5% of a functional filler, 0.1-5% of a functional aid, and the balance of water, wherein the entirety of the raw materials is 100% by weight. The engineering plastic particles are added in the form of an engineering plastic dispersion. The low-VOC organic solvent-free heat-resistant water-based paint of the present invention does not contain any organic solvent, and the film-forming baking temperature is low. The matrix resin of the paint is the engineering plastic dispersion. The organic solvent refers to an organic solvent such as N-methylpyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide, and benzene.

Description

低VOC无有机溶剂耐热水性涂料及其制得的耐高温耐腐涂层Low VOC organic solvent-free hot water resistant coating and the high temperature and corrosion resistant coating prepared therefrom 技术领域technical field
本发明涉及一种耐热涂料,特别涉及一种低VOC无有机溶剂耐热水性涂料及其制得的耐高温耐腐涂层,属于涂料技术领域。The invention relates to a heat-resistant coating, in particular to a low-VOC organic-solvent-free hot water-resistant coating and a high-temperature-resistant and corrosion-resistant coating prepared therefrom, belonging to the technical field of coatings.
背景技术Background technique
耐热涂料已广泛应用于工业防护、炊具、家电行业,年用量达数万吨,但目前使用的耐热水性涂料,粘结层涂料均含有大量溶剂,本发明将实现耐热水性涂料的无溶剂化。Heat-resistant coatings have been widely used in industrial protection, cooking utensils, and household appliances. Solvate.
专利CN104974661公布了一种聚醚砜超细微粉及其物料应用的技术方案,该专利所描的聚醚砜超细微粉为研磨获得,结构不规则,且是实心微粒,在成膜过程中,必须辅以溶剂(参见其实施例),未能实现环保性改进。Patent CN104974661 discloses a technical scheme of polyethersulfone ultrafine powder and its material application. The polyethersulfone ultrafine powder described in this patent is obtained by grinding, has an irregular structure, and is a solid particle. During the film formation process, It must be supplemented with solvents (see its examples), failing to achieve environmental improvement.
专利CN1302047、CN1305936公布了一种水基聚醚砜类分散液、可再分散性聚芳醚砜类微粉的制造方法,两个专利所述表面活性剂分解、挥发温度较高,导致聚醚砜烘烤成膜过程中,大量表面活性剂裂解物残留,严重影响料涂膜致密性及附着力,配合表面活性剂的降解物为生物激素类化合物,存在健康风险。Patents CN1302047 and CN1305936 disclose a method for manufacturing water-based polyethersulfone dispersion liquid and redispersible polyarylethersulfone micropowder. The surfactants described in the two patents decompose and volatilize at a high temperature, resulting in polyethersulfone During the baking and film forming process, a large amount of surfactant cracks remain, which seriously affects the compactness and adhesion of the coating film. The degradation products of the surfactant are biohormone compounds, which pose health risks.
专利C08J 3/12公布了一种球形聚亚芳基醚砜或聚亚芳基醚酮微粉末制备方法,该专利公布了一种高分子溶液喷雾法制微球的方法,该方法溶剂用量大,且能耗高,微粒粒径大、分布宽,产品适用面受限。Patent C08J 3/12 discloses a method for preparing spherical polyarylene ether sulfone or polyarylene ether ketone micropowder. This patent discloses a method for preparing microspheres by spraying polymer solution. This method consumes a large amount of solvent. Moreover, the energy consumption is high, the particle size is large and the distribution is wide, and the applicable surface of the product is limited.
工程塑料的涂料应用,主要分为油性涂料、水性涂料、粉末涂料,油性涂料由于高VOC排放,已被国家明确要求逐步淘汰;目前水性涂料主要采取添加水溶型的工程塑料高温溶剂,以促进涂膜结合力,虽然仍不可不免的需要添加一定比例的溶剂,但与油性涂料相比,水性涂料大大的减少了VOC排放;粉末涂料具有完全无溶剂的特点,目前主流的树脂粉末制造工艺,污染大、能耗高,涂料施工受限较多。本发明通过特殊的表面活性剂体系、溶媒蒸发工艺,可将指定工程塑料加工成0.1~2μm的空心微粒,从而实现水性涂料无溶剂状态下的工程塑料熔融成膜。同样的,对本发明的工程塑料分散液进行完全的干燥,干燥的工程塑料微粒也将适用于粉末涂料。The application of coatings for engineering plastics is mainly divided into oil-based coatings, water-based coatings, and powder coatings. Oil-based coatings have been phased out by the state due to high VOC emissions; at present, water-based coatings mainly use high-temperature solvents for water-soluble engineering plastics to facilitate coating. Film binding force, although it is still inevitable to add a certain proportion of solvents, compared with oil-based paints, water-based paints greatly reduce VOC emissions; powder coatings are completely solvent-free, and the current mainstream resin powder manufacturing process, pollution Large, high energy consumption, more restrictions on coating construction. The invention can process specified engineering plastics into hollow particles of 0.1-2 μm through a special surfactant system and a solvent evaporation process, so as to realize the melting and film-forming of engineering plastics in a solvent-free state of water-based coatings. Similarly, the engineering plastic dispersion of the present invention is completely dried, and the dried engineering plastic particles will also be suitable for powder coatings.
发明内容Contents of the invention
本发明的目的在于提供一种低VOC无有机溶剂耐热水性涂料,该涂料不含有机溶剂,不在配方结构基本保持不变,仅去除有机溶剂的情况下,仍能够提供优异的漆膜性 能,成膜烘烤温度较低(成膜烘烤温度为280~380℃、10min)。The purpose of the present invention is to provide a low-VOC organic-solvent-free hot-water-resistant coating, which does not contain organic solvents, and can still provide excellent paint film performance when the formula structure remains unchanged and only the organic solvent is removed. The film-forming baking temperature is relatively low (the film-forming baking temperature is 280-380° C. for 10 minutes).
本发明还提供一种所述耐热耐水解工程塑料分散液的制备方法。The invention also provides a preparation method of the heat-resistant and hydrolysis-resistant engineering plastic dispersion.
本发明解决其技术问题所采用的技术方案是:The technical solution adopted by the present invention to solve its technical problems is:
一种低VOC无有机溶剂耐热水性涂料,所述涂料主要是由以下原料制成:A low-VOC organic solvent-free hot water resistant coating, the coating is mainly made of the following raw materials:
工程塑料颗粒  5~30%,Engineering plastic particles 5-30%,
PTFE  0~15%, PTFE 0~15%,
颜料  0.1~2%,Pigment 0.1~2%,
功能填料  0.5~5%,Functional filler 0.5~5%,
功能助剂  0.1~5%,Functional additives 0.1~5%,
水 余量,上述原料总重量计为100%;Water surplus, the total weight of the above-mentioned raw materials is 100%;
所述工程塑料颗粒以工程塑料分散液的形式投加,所述工程塑料分散液是通过乳化-溶媒蒸发法制得,工程塑料分散液中的工程塑料颗粒粒径为0.1~2μm,具有空心的球形或类球形结构;该工程塑料分散液组成是工程塑料颗粒10~75wt%,表面活性剂0.5~10wt%,余量为水。The engineering plastic particles are added in the form of engineering plastic dispersion liquid, which is obtained by emulsification-solvent evaporation method. The engineering plastic particle diameter in the engineering plastic dispersion liquid is 0.1-2 μm, and has a hollow spherical shape. Or a spherical structure; the engineering plastic dispersion is composed of 10-75 wt% of engineering plastic particles, 0.5-10 wt% of surfactant, and the balance is water.
本发明所述低VOC无有机溶剂耐热水性涂料不含有机溶剂,成膜烘烤温度较低(成膜烘烤温度为280~380℃、10min),该涂料的主体树脂是工程塑料分散液。所述有机溶剂是指N-甲基吡咯烷酮、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、苯类等有机溶剂。The low-VOC, organic-solvent-free, hot-water-resistant coating of the present invention does not contain organic solvents, and the film-forming baking temperature is relatively low (the film-forming baking temperature is 280-380°C, 10min), and the main resin of the coating is engineering plastic dispersion . The organic solvent refers to organic solvents such as N-methylpyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide, and benzene.
作为优选,所述工程塑料选自聚醚砜、聚亚苯基砜、聚醚酰亚胺、聚砜、聚芳醚酮、聚芳醚砜酮中的一种或几种的组合。Preferably, the engineering plastic is selected from one or a combination of polyethersulfone, polyphenylenesulfone, polyetherimide, polysulfone, polyaryletherketone, polyarylethersulfoneketone.
作为优选,所述工程塑料分散液中的工程塑料颗粒,是工程塑料,或含工程塑料质量0.5-10%的,碳纳米管(CNT)、酸化处理碳纳米管、纳米氮化硼、石墨烯、氧化石墨烯、纳米云母、纳米膨润土中的一种或几种的混合物的改性工程塑料。As preferably, the engineering plastic particles in the engineering plastic dispersion are engineering plastics, or contain 0.5-10% of engineering plastics by mass, carbon nanotubes (CNTs), acidified carbon nanotubes, nano-boron nitride, graphene , graphene oxide, nano-mica, nano-bentonite or a mixture of several modified engineering plastics.
作为优选,所述溶媒是二氯甲烷、三氯甲烷、二氯乙烷、三氯乙烷、二硫化碳中的一种或几种的混合物,沸点为40~80℃(0.1MPa,室温25-27℃),Preferably, the solvent is one or a mixture of dichloromethane, trichloromethane, dichloroethane, trichloroethane, carbon disulfide, the boiling point is 40 ~ 80 ℃ (0.1MPa, room temperature 25-27 ℃),
更优选沸点45~75℃范围;More preferably, the boiling point ranges from 45 to 75°C;
最优选沸点55~65℃范围。The most preferred boiling point range is 55-65°C.
作为优选,所述乳化用的表面活性剂为A -B +结构的阴离子表面活性剂,其中,A -是C nH 2n-1O 2 -分子式的烷基羧酸根结构,其中n取值为8~16;B +选自NH 4 +、Na +、K +Preferably, the emulsifying surfactant is an anionic surfactant of A - B + structure, wherein A - is an alkyl carboxylate structure of the molecular formula C n H 2n-1 O 2 - , wherein n is 8-16; B + is selected from NH 4 + , Na + , K + .
作为优选,所述表面活性剂的A -结构中,n值优选10~14。 Preferably, in the A - structure of the surfactant, the value of n is preferably 10-14.
作为优选,所述表面活性剂是由两种不同n值的材料互配,两者比例是0.1~0.9:1。不同n值的材料互配使用效果更好。Preferably, the surfactant is intermixed with two materials with different n values, and the ratio of the two is 0.1-0.9:1. Materials with different n values are more effective when used with each other.
作为优选,所述表面活性剂的A -结构中,A优选直链结构烷烃基羧酸根;B +优选Na +As a preference, in the A - structure of the surfactant, A is preferably a straight-chain alkanyl carboxylate; B + is preferably Na + .
更优选的,该工程塑料分散液组成是工程塑料颗粒25~55wt%,表面活性剂0.5~5wt%,余量为水。更优选的,该工程塑料分散液组成是工程塑料颗粒35~40wt%,表面活性剂0.5~3wt%,余量为水。更优选的,该工程塑料分散液组成是工程塑料颗粒35~40wt%,表面活性剂0.5~1wt%,余量为水。More preferably, the composition of the engineering plastic dispersion is 25-55 wt% of engineering plastic particles, 0.5-5 wt% of surfactant, and the balance is water. More preferably, the composition of the engineering plastic dispersion is 35-40 wt% of engineering plastic particles, 0.5-3 wt% of surfactant, and the balance is water. More preferably, the composition of the engineering plastic dispersion is 35-40 wt% of engineering plastic particles, 0.5-1 wt% of surfactant, and the balance is water.
作为优选,该工程塑料分散液中的工程塑料颗粒,粒径统计值D50≤1μm,D100≤2μm;该工程塑料分散液中的工程塑料颗粒,平均空心率不低于25%。Preferably, the engineering plastic particles in the engineering plastic dispersion have a statistical value of particle size D50≤1 μm and D100≤2 μm; the engineering plastic particles in the engineering plastic dispersion have an average hollow ratio of not less than 25%.
作为优选,所述的颜料是选自单偶氮颜料、双偶氮颜料、偶氮色淀颜料、色酚AS颜料,酞菁蓝、酞菁绿、其他金属酞菁,喹吖啶酮类颜料,苯并咪唑酮类颜料,二噁嗪类颜料颜料,蒽酮类颜料等有机颜料中的一种或几种的混合物。所述的颜料也可以是二氧化钛、硫化锌、氧化锌、镉颜料、铬酸颜料、群青颜料、铁蓝颜料、碳黑颜料中的一种或几种的混合物。Preferably, the pigment is selected from monoazo pigments, disazo pigments, azo lake pigments, naphthol AS pigments, phthalocyanine blue, phthalocyanine green, other metal phthalocyanines, quinacridone pigments , Benzimidazolone pigments, dioxazine pigments, anthrone pigments and other organic pigments or a mixture of several. The pigment may also be one or a mixture of titanium dioxide, zinc sulfide, zinc oxide, cadmium pigments, chromic acid pigments, ultramarine blue pigments, iron blue pigments, and carbon black pigments.
作为优选,所述的功能填料选自石英、硫酸钡、二氧化钛、二氧化铬、氧化锌、氧化铁、氧化铝、氧化硅、氧化锆硅酸铝、硅酸铝镁、碳化硅、碳化钛、氮化硅、氮化钛、立方氮化硼,硫酸钡晶须、碳酸钙晶须,碳纤维粉、玻璃纤维粉、石英纤维粉、碳纳米管、氧化石墨烯、石墨烯、玄武岩纤维,云母、滑石粉、六方氮化硼或石墨中的一种或几种的混合物。Preferably, the functional filler is selected from quartz, barium sulfate, titanium dioxide, chromium dioxide, zinc oxide, iron oxide, aluminum oxide, silicon oxide, zirconia aluminum silicate, aluminum magnesium silicate, silicon carbide, titanium carbide, Silicon nitride, titanium nitride, cubic boron nitride, barium sulfate whiskers, calcium carbonate whiskers, carbon fiber powder, glass fiber powder, quartz fiber powder, carbon nanotubes, graphene oxide, graphene, basalt fiber, mica, One or a mixture of talcum powder, hexagonal boron nitride or graphite.
作为优选,所述的功能填料,可以是预先经过硅烷偶联剂、有机高分子进行表面处理,实施例10为对比例,功能填料未经表面处理,表现出了更低的耐盐水性能。As a preference, the functional fillers may be pre-surface-treated with silane coupling agents and organic polymers. Example 10 is a comparative example. The functional fillers have not been surface-treated and exhibit lower salt water resistance.
作为优选,所述的功能助剂,可以是常见的市售流平剂、防沉剂、防流挂稳定剂、润湿剂、消泡剂、防锈剂、触变剂的组合物。As a preference, the functional additive may be a combination of common commercially available leveling agents, anti-settling agents, anti-sagging stabilizers, wetting agents, defoamers, rust inhibitors, and thixotropic agents.
所述的功能助剂,可以是无机的,也可以是有机无机杂合的,也可以是有机物的,也可以是几种类型助剂的组合物。所述的无机功能助剂,可以是无机类矿物材料,和/或人工合成矿物材料。所述的有机无机杂合、有机物的功能助剂,可以是有机硅类、聚 氧乙烯类、聚丙烯酸酯类、纤维素类、聚酰胺类、有机氟化物类、矿物油类、羧酸盐聚合物类、聚碳酸酯类。所述的有机无机杂合、有机物的功能助剂,优选沸点和/或降解温度区间为100~350℃。更优选沸点和/或降解温度区间为150~320℃。最佳为沸点和/或降解温度区间为200~280℃。The functional auxiliary agent can be inorganic, organic-inorganic hybrid, organic, or a combination of several types of auxiliary agents. The inorganic functional additives may be inorganic mineral materials, and/or artificially synthesized mineral materials. The organic-inorganic hybrid and organic functional additives can be silicones, polyoxyethylenes, polyacrylates, celluloses, polyamides, organic fluorides, mineral oils, carboxylates Polymers, polycarbonates. The organic-inorganic hybrid and organic functional additives preferably have a boiling point and/or degradation temperature range of 100-350°C. More preferably, the boiling point and/or degradation temperature range is 150-320°C. Optimally, the boiling point and/or degradation temperature range is 200-280°C.
一种所述的工程塑料分散液的制备方法,该方法包括如下步骤:A kind of preparation method of described engineering plastics dispersion liquid, this method comprises the steps:
S1、将工程塑料颗粒、表面活性剂溶于溶媒,用溶媒控制体系粘度为50~1000Pa.s;S1. Dissolve engineering plastic particles and surfactants in a solvent, and use the solvent to control the viscosity of the system to 50-1000Pa.s;
S2、300~800rpm转速搅拌状态下,向步骤S1得到的物料中加水,得到水包油乳液;S2. Add water to the material obtained in step S1 under stirring at 300-800 rpm to obtain an oil-in-water emulsion;
S3、水包油乳液经溶媒蒸发,浓缩,得到所述水性的工程塑料分散液。S3. The oil-in-water emulsion is evaporated and concentrated to obtain the water-based engineering plastic dispersion.
作为优选,用溶媒控制体系粘度为100~500Pa.s,更优选的是体系粘度为150~250Pa.s。Preferably, the viscosity of the system is controlled by a solvent to be 100-500 Pa.s, more preferably the viscosity of the system is 150-250 Pa.s.
作为优选,溶媒蒸发过程是闪蒸形式的,水包油乳液通过雾化蒸汽加热或刮膜蒸发加热快速蒸发溶媒。溶媒蒸发过程具有快速、高效,体系不引入常温气体的特点。Preferably, the solvent evaporation process is in the form of flash evaporation, and the oil-in-water emulsion evaporates the solvent quickly by heating with atomized steam or heating with wiped film evaporation. The solvent evaporation process is fast and efficient, and the system does not introduce normal temperature gas.
一种由所述的低VOC无有机溶剂耐热水性涂料涂覆后得到的耐高温耐腐涂层。The invention relates to a high-temperature-resistant and corrosion-resistant coating obtained by coating the low-VOC organic-solvent-free hot water-resistant coating.
一种耐高温耐腐涂层的制备方法,所述的低VOC无有机溶剂耐热水性涂料各原料根据配比混合、分散均匀,喷涂到经过除油、粗糙化处理的基材上,湿涂膜经145~155℃温度10±2min、280~380℃温度10±2min两次烘烤,即得所述耐高温耐腐涂层。A method for preparing a high-temperature-resistant and corrosion-resistant coating. The raw materials of the low-VOC organic-solvent-free hot water-resistant coating are mixed according to the proportion, dispersed uniformly, sprayed on a substrate that has undergone degreasing and roughening treatment, and wet-coated The film is baked twice at a temperature of 145-155°C for 10±2 minutes and at a temperature of 280-380°C for 10±2 minutes to obtain the high-temperature and corrosion-resistant coating.
一种耐高温耐腐涂层的制备方法,权利要求1所述的低VOC无有机溶剂耐热水性涂料各原料根据配比混合、分散均匀,涂料喷涂到经过除油、粗糙化处理的铝基材上,经145~155℃温度10±2min烘烤后自然冷却到室温,A method for preparing a high-temperature-resistant and corrosion-resistant coating. The raw materials of the low-VOC organic-solvent-free hot-water-resistant coating according to claim 1 are mixed and uniformly dispersed according to the proportion, and the coating is sprayed onto the aluminum substrate that has undergone degreasing and roughening treatment. The material is baked at 145-155°C for 10±2min and then cooled to room temperature naturally.
再在干燥涂层上,喷涂一层面涂层,On top of the dried coating, spray a top coat,
复合涂膜经145~155℃温度10±2min、280~380℃温度10±2min两次烘烤,即得耐高温耐腐涂层。该涂层具有更优异的不粘、自清洁、耐腐蚀性能。The composite coating film is baked twice at 145-155°C for 10±2 minutes and 280-380°C for 10±2 minutes to obtain a high-temperature and corrosion-resistant coating. The coating has more excellent non-stick, self-cleaning and corrosion-resistant properties.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
1、本发明所述的耐热耐水解工程塑料分散液具拓展性,能在微米、亚微米级工程塑料微粒中均匀引入功能填料;具有更均匀、更小的工程塑料颗粒粒径(0.1~2μm);在使用中易于熔融,基材粘结强度高;1. The heat-resistant and hydrolysis-resistant engineering plastic dispersion liquid of the present invention has expandability, and can evenly introduce functional fillers into micron and submicron engineering plastic particles; it has a more uniform and smaller engineering plastic particle size (0.1~ 2μm); easy to melt in use, high bonding strength of substrate;
2、本发明所述低VOC无有机溶剂耐热水性涂料不含有机溶剂,在配方结构基本 保持不变,仅去除有机溶剂的情况下,仍能够提供优异的漆膜性能,大大减少新配方开发工作量:2. The low-VOC, organic-solvent-free, hot-water-resistant coating of the present invention does not contain organic solvents, and can still provide excellent paint film performance when the formula structure remains basically unchanged and only organic solvents are removed, greatly reducing the development of new formulas workload:
3、本发明所述低VOC无有机溶剂耐热水性涂料,成膜烘烤温度较低(成膜烘烤温度为280~380℃、10min);3. The low-VOC organic solvent-free hot water resistant coating of the present invention has a low film-forming baking temperature (film-forming baking temperature is 280-380°C, 10min);
4、由本发明低VOC无有机溶剂耐热水性涂料涂覆后得到的耐高温耐腐涂层具有优异的粘结性。4. The high-temperature and corrosion-resistant coating obtained by coating the low-VOC organic-solvent-free hot water-resistant coating of the present invention has excellent adhesion.
附图说明Description of drawings
图1是对比例1制得PES分散液的粒度检测报告;Fig. 1 is the particle size detection report that comparative example 1 makes PES dispersion liquid;
图2是对比例1制得PES分散液颗粒的SEM照片;Fig. 2 is the SEM photograph that comparative example 1 makes PES dispersion liquid particle;
图3是对比例2制得PES分散液的粒度检测报告;Fig. 3 is the particle size detection report that comparative example 2 makes PES dispersion liquid;
图4是对比例3制得PES分散液颗粒的SEM照片;Fig. 4 is the SEM photograph that comparative example 3 makes PES dispersion liquid particle;
图5是实施例1制得PPSU分散液的粒度检测报告;Fig. 5 is the particle size detection report that embodiment 1 makes PPSU dispersion liquid;
图6是实施例1制得PPSU分散液颗粒的SEM照片;Fig. 6 is the SEM photograph that embodiment 1 makes PPSU dispersion liquid particle;
图7是实施例1制得PPSU分散液颗粒的TEM照片。Fig. 7 is the TEM picture of the PPSU dispersion liquid particle that embodiment 1 makes.
具体实施方式Detailed ways
下面通过具体实施例,对本发明的技术方案作进一步的具体说明。应当理解,本发明的实施并不局限于下面的实施例,对本发明所做的任何形式上的变通和/或改变都将落入本发明保护范围。The technical solution of the present invention will be further specifically described below through specific examples. It should be understood that the implementation of the present invention is not limited to the following examples, and any modifications and/or changes made to the present invention will fall within the protection scope of the present invention.
在本发明中,若非特指,所有的份、百分比均为重量单位,所采用的设备和原料等均可从市场购得或是本领域常用的。下述实施例中的方法,如无特别说明,均为本领域的常规方法。In the present invention, unless otherwise specified, all parts and percentages are in weight units, and the equipment and raw materials used can be purchased from the market or commonly used in the field. The methods in the following examples, unless otherwise specified, are conventional methods in the art.
以下实施例中,In the following examples,
工程塑料分散颗粒的粒度分析,均采用百特BT-9300S激光粒度仪分析测得;The particle size analysis of the dispersed particles of engineering plastics is analyzed and measured by Baxter BT-9300S laser particle size analyzer;
工程塑料分散颗粒的SEM照片,采用Regulus-8230、SU8000扫描电镜分析测得;SEM photos of dispersed particles of engineering plastics, measured by Regulus-8230 and SU8000 scanning electron microscopes;
工程塑料分散颗粒的TEM照片,采用Talos F200X透射电镜分析测得。The TEM photo of the dispersed particles of engineering plastics was measured by Talos F200X transmission electron microscope.
PES粗粉,巴斯夫股份有限公司,牌号E 2020 P,D50≈2mm;PES coarse powder, BASF Co., Ltd., grade E 2020 P, D50≈2mm;
PPSU粗粉,广东优巨先进新材料股份有限公司,牌号F1550P,D50≈1.5mm;PPSU coarse powder, Guangdong Youju Advanced New Materials Co., Ltd., grade F1550P, D50≈1.5mm;
纳米氮化硼,苏州纳朴材料科技有限公司,牌号NS-BN,D50≤500nm。Nano-boron nitride, Suzhou Napor Material Technology Co., Ltd., brand NS-BN, D50≤500nm.
测试方法:Test Methods:
树脂分散颗粒的粒度分析,采用百特BT-9300S激光粒度仪分析测得;The particle size analysis of resin dispersed particles is measured by Baxter BT-9300S laser particle size analyzer;
树脂分散颗粒的TEM照片,采用Talos F200X透射电镜分析测得;TEM photo of resin dispersed particles, measured by Talos F200X transmission electron microscope;
附着力测试,参照GB/T9286-1998划1mm百格,测试所得;Adhesion test, refer to GB/T9286-1998 to draw 1mm hundred grids, and the test results;
硬度测试,参照GB/T6739,采用铅笔硬度计,测试所得;Hardness test, referring to GB/T6739, using a pencil hardness tester, the test results;
耐盐水测试,参照GB/T32095.3,于5%氯化钠溶液、微沸条件下测得;Salt water resistance test, refer to GB/T32095.3, measured in 5% sodium chloride solution, slightly boiling conditions;
不粘性测试,参照GB/T32095.2,采用煎蛋不粘性实验方法,测试所得。For the non-stick test, refer to GB/T32095.2, and use the non-stick test method of fried eggs to test the results.
对比例1Comparative example 1
一种工程塑料分散液的制备方法,具体步骤如下:按表1所列组合物配置物料,于25℃恒温立式球磨机中研磨24h,然后于卧式砂磨机中研磨32h,即得PES研磨分散液。经激光粒度分析仪检测,分散液中PES微粒粒径D50为7μm,D90为17μm。A preparation method of an engineering plastic dispersion, the specific steps are as follows: configure materials according to the composition listed in Table 1, grind in a constant temperature vertical ball mill at 25°C for 24 hours, and then grind in a horizontal sand mill for 32 hours to obtain PES grinding Dispersions. Detected by a laser particle size analyzer, the particle size D50 of the PES particles in the dispersion is 7 μm, and the D90 is 17 μm.
表1Table 1
成份ingredients 重量百分比weight percentage
PES(粗粉)PES (coarse powder) 2525
N-甲基吡咯烷酮N-Methylpyrrolidone 2525
water 5050
合计total 100100
PES分散液的粒度检测报告见图1,PES分散液颗粒的SEM照片见图2。The particle size test report of the PES dispersion is shown in Figure 1, and the SEM photo of the PES dispersion particles is shown in Figure 2.
对比例2Comparative example 2
一种工程塑料分散液的制备方法,具体步骤如下:配方同实施例1,于25℃恒温立式球磨机中研磨36h,然后于卧式砂磨机中研磨72h,即得PES研磨分散液。经激光粒度分析仪检测,分散液中PES微粒粒径D50为3μm,D90为12μm。A preparation method of an engineering plastic dispersion, the specific steps are as follows: the formula is the same as in Example 1, grind in a constant temperature vertical ball mill at 25°C for 36 hours, and then grind in a horizontal sand mill for 72 hours to obtain the PES grinding dispersion. Detected by a laser particle size analyzer, the particle size D50 of the PES particles in the dispersion is 3 μm, and the D90 is 12 μm.
PES分散液的粒度检测报告见图3。See Figure 3 for the particle size test report of the PES dispersion.
对比例3Comparative example 3
一种工程塑料分散液的制备方法,具体步骤如下:A kind of preparation method of engineering plastic dispersion liquid, concrete steps are as follows:
步骤1、取200份的三氯甲烷,加入6份的甲醇、60份的PES粗粉,搅拌30min至PES充分溶解;同时取5份的十二烷基苯磺酸钠,溶于260份的水。 Step 1. Take 200 parts of chloroform, add 6 parts of methanol and 60 parts of PES coarse powder, and stir for 30 minutes until PES is fully dissolved; at the same time, take 5 parts of sodium dodecylbenzenesulfonate and dissolve it in 260 parts of water.
步骤2、将十二烷基苯磺酸钠水溶液倒入胶体磨中,再将PES的三氯甲烷溶液缓慢加入胶体磨中,分散,获得PES溶液的乳化分散液。Step 2. Pour the sodium dodecylbenzenesulfonate aqueous solution into the colloid mill, then slowly add the chloroform solution of PES into the colloid mill, and disperse to obtain the emulsified dispersion of the PES solution.
步骤3、将步骤2制得材料,倒入装有搅拌、冷凝装置的三口烧瓶中,于水浴锅中加热,多段控温,控制温度不超过65℃至无溶剂蒸出,然后升温到85℃,恒温30min,即得无溶剂的PES水性分散液。取出烧瓶内物料进行激光粒径分析,干燥后进行SEM分析,SEM分析结果见图4。Step 3. Pour the material obtained in step 2 into a three-necked flask equipped with a stirring and condensing device, heat it in a water bath, control the temperature in multiple stages, and control the temperature not to exceed 65°C until no solvent is evaporated, and then heat up to 85°C , and keep the temperature for 30 minutes to obtain a solvent-free PES aqueous dispersion. The material in the flask was taken out for laser particle size analysis, and SEM analysis was performed after drying. The SEM analysis results are shown in Figure 4.
实施例1Example 1
一种工程塑料分散液的制备方法,具体步骤如下:A kind of preparation method of engineering plastic dispersion liquid, concrete steps are as follows:
步骤1、取200份的三氯甲烷,加入4份的十二烷酸钠、4份的十四烷酸钠、60份的PES粗粉,搅拌30min至PES充分溶解。向得到的溶液中加入三氯甲烷,调整溶液粘度为200±10Pa.s。 Step 1. Take 200 parts of chloroform, add 4 parts of sodium dodecanoate, 4 parts of sodium myristate, and 60 parts of PES coarse powder, and stir for 30 minutes until PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 200±10Pa.s.
步骤2、500rpm的转速下搅拌,同时缓慢加入300份的水,控制加水在5~10min内完成,获得PES溶液的乳化分散液。Step 2. Stir at a rotational speed of 500 rpm, and at the same time slowly add 300 parts of water, control the addition of water to complete within 5-10 minutes, and obtain an emulsified dispersion of the PES solution.
步骤3、设置喷雾蒸汽温度120℃,蒸汽流量100L/min,PES溶液的乳化分散液流量100g/min,通过喷雾蒸发的方式快速去除分散液中的三氯甲烷,得到耐热耐水解PES分散液。Step 3. Set the spray steam temperature to 120°C, the steam flow rate to 100L/min, and the emulsified dispersion liquid flow rate of the PES solution to 100g/min, and quickly remove the chloroform in the dispersion liquid by spray evaporation to obtain a heat-resistant and hydrolysis-resistant PES dispersion liquid .
取所得PES分散液,采用激光粒度分析仪检测,获得材料粒径分布为0.1~0.8μm,具体如图5;采用扫描电镜(SEM)、透射电镜(TEM),分析110℃干燥PES分散液所得粉末,获得PES微粒为空心、球形或类球形空间结构的照片,图如图6、图7。Take the obtained PES dispersion liquid and use a laser particle size analyzer to detect the material particle size distribution of 0.1-0.8 μm, as shown in Figure 5; use scanning electron microscope (SEM) and transmission electron microscope (TEM) to analyze the obtained PES dispersion liquid dried at 110 °C Powder, obtain photos of PES particles with hollow, spherical or quasi-spherical spatial structure, as shown in Figure 6 and Figure 7.
由图1-图3可知,研磨法制取工程塑料分散液,加工周期长,产品颗粒颗粒尺寸大,粒径分布宽。It can be seen from Fig. 1-Fig. 3 that the engineering plastic dispersion is prepared by the grinding method, the processing cycle is long, the product particle size is large, and the particle size distribution is wide.
由图4可知,表面活性剂组合选择不合理,即便经过剧烈的乳化工艺处理,制得的工程塑料分散液产品,颗粒尺寸仍难细化到D50≤1μm,且粒径分布宽。通过缓慢升温蒸发溶媒的方式,制得的工程塑料分散液,其产品颗粒形貌规则度降低。It can be seen from Figure 4 that the choice of surfactant combination is unreasonable, and even after a severe emulsification process, the particle size of the prepared engineering plastic dispersion product is still difficult to refine to D50≤1μm, and the particle size distribution is wide. By slowly raising the temperature and evaporating the solvent, the prepared engineering plastic dispersion has a reduced particle shape regularity.
图5-图7证明,经过本发明技术处理,制得的工程塑料分散液产品,其产品颗粒外观呈现球形和球形,粒径小,D50<0.4μm,D100≤0.8μm,且具有空心结构。Figure 5-Figure 7 proves that after the technical treatment of the present invention, the obtained engineering plastic dispersion product has spherical and spherical appearance, small particle size, D50<0.4μm, D100≤0.8μm, and has a hollow structure.
实施例2Example 2
步骤1、取150份的三氯甲烷,加入4份的十二烷酸钠、4份的十四烷酸钠、60份的PPSU粗粉,搅拌30min至PPSU充分溶解。向得到的溶液中加入三氯甲烷,调整溶液粘度为500±10Pa.s。 Step 1. Take 150 parts of chloroform, add 4 parts of sodium dodecanoate, 4 parts of sodium myristate, and 60 parts of PPSU coarse powder, and stir for 30 minutes until PPSU is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 500±10Pa.s.
步骤2、3参照实施例1。Steps 2 and 3 refer to Example 1.
取所得PPSU分散液,采用激光粒度分析仪检测,获得材料粒径分布为0.7~10μm。The obtained PPSU dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.7-10 μm.
实施例3Example 3
步骤1、取200份的三氯甲烷,加入4份的八烷酸钠、4份的十六烷酸钠、60份的PES粗粉,搅拌30min至PES充分溶解。向得到的溶液中加入三氯甲烷,调整溶液粘度为200±10Pa.s。 Step 1. Take 200 parts of chloroform, add 4 parts of sodium octadecanoate, 4 parts of sodium hexadecanoate, and 60 parts of PES coarse powder, and stir for 30 minutes until the PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 200±10Pa.s.
步骤2、3参照实施例1。Steps 2 and 3 refer to Example 1.
取所得PES分散液,采用激光粒度分析仪检测,获得材料粒径分布为0.5~5μm。The obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.5-5 μm.
实施例4Example 4
步骤1、取150份的三氯甲烷,加入6份的八烷酸钠、6份的十六烷酸钠、60份的PES粗粉,搅拌30min至PES充分溶解。向得到的溶液中加入三氯甲烷,调整溶液粘度为500±10Pa.s。 Step 1. Take 150 parts of chloroform, add 6 parts of sodium octadecanoate, 6 parts of sodium hexadecanoate, and 60 parts of coarse PES powder, and stir for 30 minutes until PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 500±10Pa.s.
步骤2、3参照实施例1。Steps 2 and 3 refer to Example 1.
取所得PES分散液,采用激光粒度分析仪检测,获得材料粒径分布为0.1~3μm。The obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.1-3 μm.
实施例5Example 5
步骤1、取200份的三氯甲烷,加入6份的十二烷酸钠、2份的十四烷酸钠、60份的PES粗粉,搅拌30min至PES充分溶解。向得到的溶液中加入三氯甲烷,调整溶液粘度为200±10Pa.s。 Step 1. Take 200 parts of chloroform, add 6 parts of sodium dodecanoate, 2 parts of sodium myristate, and 60 parts of PES coarse powder, and stir for 30 minutes until PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 200±10Pa.s.
步骤2、3参照实施例1。Steps 2 and 3 refer to Example 1.
取所得PES分散液,采用激光粒度分析仪检测,获得材料粒径分布为0.1~1.6μm。The obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.1-1.6 μm.
实施例6Example 6
步骤1、取200份的三氯甲烷,加入2份的十二烷酸钠、6份的十四烷酸钠、60份的PES粗粉,搅拌30min至PES充分溶解。向得到的溶液中加入三氯甲烷,调整溶液粘度为200±10Pa.s。 Step 1. Take 200 parts of chloroform, add 2 parts of sodium dodecanoate, 6 parts of sodium myristate, and 60 parts of coarse PES powder, and stir for 30 minutes until PES is fully dissolved. Add chloroform to the obtained solution to adjust the solution viscosity to 200±10Pa.s.
步骤2、3参照实施例1。Steps 2 and 3 refer to Example 1.
取所得PES分散液,采用激光粒度分析仪检测,获得材料粒径分布为0.1~2.2μm。The obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.1-2.2 μm.
实施例7Example 7
一种工程塑料分散液的制备方法,具体步骤如下:A kind of preparation method of engineering plastic dispersion liquid, concrete steps are as follows:
步骤1、取200份的三氯甲烷,加入4份的葵酸、4份的十二烷酸、15份浓氨水(20wt%)、60份的PES粗粉,搅拌30min至PES充分溶解。通过后补三氯甲烷,调整溶液粘度为200Pa.s。 Step 1. Take 200 parts of chloroform, add 4 parts of capric acid, 4 parts of dodecanoic acid, 15 parts of concentrated ammonia water (20wt%), and 60 parts of PES coarse powder, and stir for 30 minutes until PES is fully dissolved. Adjust the viscosity of the solution to 200 Pa.s by post-supplementing chloroform.
步骤2、步骤3,参照实施例1。Step 2, step 3, with reference to embodiment 1.
取所得PES分散液,采用激光粒度分析仪检测,获得材料粒径分布为0.3~1.8μm。The obtained PES dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.3-1.8 μm.
实施例8Example 8
一种工程塑料分散液的制备方法,具体步骤如下:A kind of preparation method of engineering plastic dispersion liquid, concrete steps are as follows:
步骤1、取200份的三氯甲烷,加入5份的纳米氮化硼,4份的辛酸钠、4份十二烷酸钠,搅匀,然后加入50份的PES粗粉,搅拌30min至PES充分溶解。通过后补三氯甲烷,调整溶液粘度为400Pa.s。 Step 1. Take 200 parts of chloroform, add 5 parts of nano-boron nitride, 4 parts of sodium octanoate, 4 parts of sodium dodecanoate, stir well, then add 50 parts of PES coarse powder, stir for 30 minutes until PES Fully dissolve. Adjust the viscosity of the solution to 400 Pa.s by post-supplementing chloroform.
步骤2、步骤3,参考实施例1;Step 2, step 3, refer to Example 1;
取所得纳米云母/PES复合微粒分散液,采用激光粒度分析仪检测,获得材料粒径分布为0.3~2μm。The obtained nano-mica/PES composite particle dispersion liquid is taken and detected by a laser particle size analyzer, and the particle size distribution of the obtained material is 0.3-2 μm.
以上各对比例和实施例分散液粒径的数据见表2,根据表2可知,研磨工艺制造工程塑料分散液,工程塑料颗粒尺寸为10μm量级,且较难进一步细化。表面活性剂选型严重限制乳化颗粒的尺寸,不合理的蒸发工艺,也影响着去除溶媒后颗粒的形态。本发明所选表面活性剂体系,在乳化效果上有这明显的优势,乳化颗粒尺寸更小,粒径分 布窄,其中实施例1配方及工艺组合下,可以实现特种工程物料分散液颗粒尺寸,全部处于亚微米尺寸范围。The particle size data of the dispersions of the above comparative examples and examples are shown in Table 2. According to Table 2, it can be known that the grinding process produces engineering plastic dispersions, and the particle size of engineering plastics is on the order of 10 μm, and it is difficult to further refine them. The selection of surfactant severely limits the size of emulsified particles, and the unreasonable evaporation process also affects the shape of particles after solvent removal. The selected surfactant system of the present invention has obvious advantages in the emulsification effect, the emulsified particle size is smaller, and the particle size distribution is narrow. Among them, under the formula and process combination of Example 1, the particle size of the dispersion liquid of special engineering materials can be achieved. All in the submicron size range.
表2 工程塑料分散液粒径数据统计表Table 2 Statistical table of engineering plastic dispersion particle size data
实验编码experimental coding 粒径范围Particle size range 实验编码experimental coding 粒径范围Particle size range 实验编码experimental coding 粒径范围Particle size range
对比例1Comparative example 1 D90=28.8μmD90=28.8μm 对比例2Comparative example 2 D90=21.4μmD90=21.4μm 对比例3Comparative example 3 D90=8.0D90=8.0
实施例1Example 1 0.1~0.8μm0.1~0.8μm 实施例2Example 2 0.7~10μm0.7~10μm 实施例3Example 3 0.5~5μm0.5~5μm
实施例4Example 4 0.1~3μm0.1~3μm 实施例5Example 5 0.1~1.6μm0.1~1.6μm 实施例6Example 6 0.1~2.2μm0.1~2.2μm
实施例7Example 7 0.3~1.8μm0.3~1.8μm 实施例8Example 8 0.3~2μm0.3~2μm  the  the
应用例1-2Application example 1-2
为比较含有机溶剂和不含有机溶剂的涂料涂覆后形成的涂层性能,分别取对比例1和实施例1所得PES分散液进行配制,按表3所列涂料成份配制涂料,其中PTFE、碳黑颜料、滑石粉、增稠剂在配制涂料时均以水分散形态投料,表3中所述PES为固含量。In order to compare the coating properties formed after the coatings containing organic solvents and coatings without organic solvents, the PES dispersion obtained in Comparative Example 1 and Example 1 is prepared respectively, and the coatings are formulated according to the coating ingredients listed in Table 3, wherein PTFE, Carbon black pigments, talcum powder, and thickeners are all fed in water-dispersed form when preparing coatings, and the PES described in Table 3 is the solid content.
表3 涂料成份(单位kg)Table 3 Coating composition (unit: kg)
应用例Application example 11 22
PES(对比例1研磨方法制得的分散液)PES (the dispersion that comparative example 1 grinding method makes) 11.511.5 //
PES(实施例1制得的分散液)PES (the dispersion that embodiment 1 makes) // 11.511.5
NMP(N-甲基吡咯烷酮)NMP(N-Methylpyrrolidone) 11.511.5 //
PTFE(聚四氟乙烯)PTFE (polytetrafluoroethylene) 1515 1515
碳黑颜料carbon black pigment 1.51.5 1.51.5
滑石粉(<5μm)Talc powder (<5μm) 33 33
流平剂 leveling agent 11 11
增稠剂thickener 0.50.5 0.50.5
water 余量margin 余量margin
合计total 100100 100100
将表3所列配方制得的涂料喷涂到经过除油、粗糙化处理的铝基材上,经150℃-10min、380℃-10min烘烤,即得PES耐高温、耐腐涂层;经涡流测厚仪测得,涂层厚 度为20μm。涂层性能检测结果如表4。Spray the paint prepared from the formula listed in Table 3 onto the degreasing and roughened aluminum substrate, and bake it at 150°C-10min and 380°C-10min to obtain a PES high-temperature-resistant and corrosion-resistant coating; The thickness of the coating was measured by an eddy current thickness gauge to be 20 μm. The coating performance test results are shown in Table 4.
表4 涂层性能对比数据Table 4 Coating performance comparison data
Figure PCTCN2022097613-appb-000001
Figure PCTCN2022097613-appb-000001
表4的数据证明,本发明所制得工程塑料分散液,由于工程塑料颗粒具备特殊的尺寸及结构,在涂料应用中,可以实现水性涂料无有机溶剂,但与含有机溶剂涂料一致的涂层性能。The data in table 4 proves that the prepared engineering plastic dispersion of the present invention, because the engineering plastic particles possess special size and structure, in coating application, can realize the coating that water-based coating does not have organic solvent, but is consistent with the coating that contains organic solvent performance.
实施例9Example 9
一种低VOC无有机溶剂耐热水性涂料,所述涂料是由以下原料制成:PES颗粒 15%,PTFE 0%,碳黑 1%,氧化石墨烯 1%,润湿剂 0.5%,丙烯酸增稠剂 2%,水 余量,上述原料总重量计为100%。PES颗粒以实施例1制得的工程塑料分散液形式进行投料。A low VOC organic solvent-free hot water resistant coating, the coating is made of the following raw materials: PES particles 15%, PTFE 0%, carbon black 1%, graphene oxide 1%, wetting agent 0.5%, acrylic acid Thickener 2%, water balance, the total weight of the above raw materials is 100%. The PES particles are fed in the form of the engineering plastic dispersion prepared in Example 1.
一种耐高温耐腐涂层的制备方法,将上述低VOC无有机溶剂耐热水性涂料各原料根据配比混合、分散均匀,喷涂到经过除油、粗糙化处理的基材上,湿涂膜经150℃温度10min、340℃温度10min两次烘烤,即得所述耐高温耐腐涂层。A method for preparing a high-temperature-resistant and corrosion-resistant coating. The raw materials of the above-mentioned low-VOC organic-solvent-free hot-water-resistant coating are mixed according to the proportion, dispersed evenly, and sprayed on a substrate that has been degreased and roughened. The high temperature and corrosion resistant coating is obtained by baking twice at 150°C for 10 minutes and at 340°C for 10 minutes.
实施例10Example 10
一种低VOC无有机溶剂耐热水性涂料,所述涂料是由以下原料制成:PES颗粒 15%,PTFE 0%,碳黑 1%,石墨烯 1%,润湿剂 0.5%,丙烯酸增稠剂 2%,水 余量,上述原料总重量计为100%。PES颗粒以实施例1制得的工程塑料分散液形式进行投料。A low VOC organic solvent-free hot water resistant coating, the coating is made of the following raw materials: PES particles 15%, PTFE 0%, carbon black 1%, graphene 1%, wetting agent 0.5%, acrylic thickening Agent 2%, water balance, the total weight of the above raw materials is 100%. The PES particles are fed in the form of the engineering plastic dispersion prepared in Example 1.
一种耐高温耐腐涂层的制备方法,将上述低VOC无有机溶剂耐热水性涂料各原料根据配比混合、分散均匀,喷涂到经过除油、粗糙化处理的基材上,湿涂膜经150℃温度10min、340℃温度10min两次烘烤,即得所述耐高温耐腐涂层。A method for preparing a high-temperature-resistant and corrosion-resistant coating. The raw materials of the above-mentioned low-VOC organic-solvent-free hot-water-resistant coating are mixed according to the proportion, dispersed evenly, and sprayed on a substrate that has been degreased and roughened. The high temperature and corrosion resistant coating is obtained by baking twice at 150°C for 10 minutes and at 340°C for 10 minutes.
对实施例9和10的涂层进行性能检测,结果见表5。The coatings of Examples 9 and 10 were tested for performance, and the results are shown in Table 5.
表5table 5
项目project 厚度/umThickness/um 附着力Adhesion 水附着力Water Adhesion 耐盐水salt water resistant
实施例9Example 9 2020 1级 Level 1 1级 Level 1 28h28 hours
实施例10Example 10 2020 1级 Level 1 1级 Level 1 21h21h
对比例11~16及实施例11~16Comparative Examples 11-16 and Examples 11-16
一种耐高温耐腐涂层的制备方法,具体步骤如下:A method for preparing a high-temperature-resistant and corrosion-resistant coating, the specific steps are as follows:
1、将表6各原料根据配比混合、分散均匀得到底涂层材料,1. Mix and disperse the raw materials in Table 6 according to the ratio to obtain the primer coating material,
将底涂层材料喷涂到经过除油、粗糙化处理的铝基材上,烧结温度控制在150~180℃范围内,时间5~10min;底涂层形成后,自然冷却至室温。Spray the undercoat material on the degreased and roughened aluminum substrate, control the sintering temperature within the range of 150-180°C for 5-10 minutes; after the undercoat is formed, cool it down to room temperature naturally.
取对比例2(脱除有机溶剂)和实施例1所得PES分散液进行配制,按表5所列涂料成份配制涂料,其中PTFE、碳黑颜料、碳化硅、丙烯酸增稠剂在配制涂料时均以水分散形态投料,表5中所述PES为固含量。在保证PES含量相同的情况下进行对比试验。对比例11~16考察添加不同含量的有机溶剂的底涂层性能,实施例11~16考察以本发明实施例1所得PES分散液在额外添加不同含量的有机溶剂的底涂层性能。Get comparative example 2 (remove organic solvent) and embodiment 1 gained PES dispersion liquid and prepare, prepare coating by the coating composition listed in table 5, wherein PTFE, carbon black pigment, silicon carbide, acrylic acid thickener are all when preparing coating. Feed in the form of water dispersion, the PES mentioned in Table 5 is the solid content. Under the condition that the content of PES is guaranteed to be the same, a comparative test is carried out. Comparative Examples 11-16 investigated the performance of the primer layer with different contents of organic solvents, and Examples 11-16 investigated the performance of the primer layer with the PES dispersion obtained in Example 1 of the present invention with additional addition of different contents of organic solvents.
对比例2制得的PES分散液脱除有机溶剂的具体方法:取对比例2研磨法制得的PES分散液1000g,装入5L的3口烧瓶中,加入纯水3000g,60℃条件下搅拌30min,然后进行抽滤。取滤饼投入5L的3口烧瓶中,倒入纯水3000g,60℃条件下搅拌30min,然后进行抽滤,循环洗料3次后,检测滤液中N-甲基吡咯烷酮含量,如含量超过100ppm,则重复洗料至滤液中N-甲基吡咯烷酮含量低于100ppm。The specific method for removing the organic solvent from the PES dispersion prepared in Comparative Example 2: Take 1000 g of the PES dispersion prepared by the grinding method in Comparative Example 2, put it into a 5 L 3-necked flask, add 3000 g of pure water, and stir for 30 minutes at 60 ° C. , and then perform suction filtration. Take the filter cake and put it into a 5L 3-neck flask, pour 3000g of pure water into it, stir at 60°C for 30min, then carry out suction filtration, and wash the material 3 times, then check the content of N-methylpyrrolidone in the filtrate, if the content exceeds 100ppm , then repeat the washing until the N-methylpyrrolidone content in the filtrate is lower than 100ppm.
2、再将面涂层材料喷涂在底涂层之上,分两步烧结,第一步控制温度在150~180℃范围内,时间5~10min,第二步控制温度为375~380℃,时间为8~10min。2. Then spray the surface coating material on the bottom coating, and sinter in two steps. The first step controls the temperature within the range of 150-180°C for 5-10 minutes, and the second step controls the temperature at 375-380°C. The time is 8-10 minutes.
面涂层的组分及配比(总重量合计100%):PTFE 42%,丙烯酸增稠剂 3%,珠光粉 0.5%,丙二醇 2%,表面活性剂 3%,流平剂 0.35%,催干剂 3%,水 余量。Components and ratio of top coat (100% by total weight): PTFE 42%, acrylic thickener 3%, pearl powder 0.5%, propylene glycol 2%, surfactant 3%, leveling agent 0.35%, catalyst Dry agent 3%, water balance.
表6 底涂层的组分及配比(单位kg)Table 6 Components and ratio of primer (unit: kg)
Figure PCTCN2022097613-appb-000002
Figure PCTCN2022097613-appb-000002
表6 (续表)底涂层的组分及配比(单位kg)Table 6 (Continued table) Components and proportions of primer (unit: kg)
Figure PCTCN2022097613-appb-000003
Figure PCTCN2022097613-appb-000003
对对比例11~16及实施例11~16得到的涂层进行测试试验,经检测其性能见表7。The coatings obtained in Comparative Examples 11-16 and Examples 11-16 were tested, and their performances are shown in Table 7 after testing.
表7Table 7
Figure PCTCN2022097613-appb-000004
Figure PCTCN2022097613-appb-000004
结论:表7的数据证明,研磨法制得细化的PES的分散材料,在树脂良溶剂含量逐渐减少的过程中,由其所制备的水性涂料表现出同步减弱的涂层粘结强度,而本发明制得的工程塑料分散液,因其分散颗粒的特殊结构,在树脂良溶剂含量逐渐减少,直至不含树脂良溶剂、其他有机溶剂的情况下,仍能提供优异的粘结强度。Conclusion: The data in Table 7 proves that the fine PES dispersion material prepared by the grinding method, in the process of gradually reducing the resin good solvent content, the water-based coating prepared by it shows synchronously weakened coating bond strength, while this The engineering plastic dispersion prepared by the invention, because of the special structure of dispersed particles, can still provide excellent bonding strength when the content of resin good solvent is gradually reduced until it does not contain resin good solvent or other organic solvents.
本说明书中各个实施例采用递进的方式描述,每个实施例重点说明的都是与其它实施例的不同之处,各个实施例之间相同或相似部分互相参见即可。对于实施例公开的装置而言,由于其与实施例公开的方法相对应,所以描述的比较简单,相关之处参见方法部分说明即可。Each embodiment in this specification is described in a progressive manner, each embodiment focuses on the difference from other embodiments, and the same or similar parts of each embodiment can be referred to each other. As for the device disclosed in the embodiment, since it corresponds to the method disclosed in the embodiment, the description is relatively simple, and for the related information, please refer to the description of the method part.
以上对本发明所提供的一种耐热耐水解工程塑料分散液及其制备方法进行了详细介绍。本文中应用了具体个例对本发明的原理及实施方式进行了阐述,以上实施例的说明只是用于帮助理解本发明的方法及其核心思想。应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以对本发明进行若干改进和修饰,这些改进和修饰也落入本发明权利要求的保护范围内。The heat-resistant and hydrolysis-resistant engineering plastic dispersion provided by the present invention and its preparation method have been introduced in detail above. In this paper, specific examples are used to illustrate the principle and implementation of the present invention, and the descriptions of the above embodiments are only used to help understand the method and core idea of the present invention. It should be pointed out that for those skilled in the art, without departing from the principle of the present invention, some improvements and modifications can be made to the present invention, and these improvements and modifications also fall within the protection scope of the claims of the present invention.

Claims (10)

  1. 一种低VOC无有机溶剂耐热水性涂料,其特征在于所述涂料主要是由以下原料制成:A low-VOC organic solvent-free hot water resistant coating is characterized in that the coating is mainly made of the following raw materials:
    工程塑料颗粒  5~30%,Engineering plastic particles 5-30%,
    PTFE  0~15%,PTFE 0~15%,
    颜料  0.1~2%,Pigment 0.1~2%,
    功能填料  0.5~5%,Functional filler 0.5~5%,
    功能助剂  0.1~5%,Functional additives 0.1~5%,
    水  余量,上述原料总重量计为100%;Water surplus, the total weight of the above-mentioned raw materials is 100%;
    所述工程塑料颗粒以工程塑料分散液的形式投加,所述工程塑料分散液是通过乳化-溶媒蒸发法制得,工程塑料分散液中的工程塑料颗粒粒径为0.1~2μm,具有空心的球形或类球形结构;该工程塑料分散液组成是工程塑料颗粒10~75wt%,表面活性剂0.5~10wt%,余量为水。The engineering plastic particles are added in the form of engineering plastic dispersion liquid, which is obtained by emulsification-solvent evaporation method. The engineering plastic particle diameter in the engineering plastic dispersion liquid is 0.1-2 μm, and has a hollow spherical shape. Or a spherical structure; the engineering plastic dispersion is composed of 10-75 wt% of engineering plastic particles, 0.5-10 wt% of surfactant, and the balance is water.
  2. 根据权利要求1所述的低VOC无有机溶剂耐热水性涂料,其特征在于:所述工程塑料选自聚醚砜、聚亚苯基砜、聚醚酰亚胺、聚砜、聚芳醚酮、聚芳醚砜酮中的一种或几种的组合;所述溶媒是二氯甲烷、三氯甲烷、二氯乙烷、三氯乙烷、二硫化碳中的一种或几种的混合物,沸点为40~80℃。The low VOC organic solvent-free hot water resistant coating according to claim 1, characterized in that: said engineering plastic is selected from polyethersulfone, polyphenylenesulfone, polyetherimide, polysulfone, polyaryletherketone , polyaryl ether sulfone ketone or a combination of several; the solvent is a mixture of one or more of dichloromethane, chloroform, dichloroethane, trichloroethane, carbon disulfide, boiling point It is 40-80°C.
  3. 根据权利要求1所述的低VOC无有机溶剂耐热水性涂料,其特征在于:所述工程塑料分散液中的工程塑料颗粒,是工程塑料,The low-VOC organic solvent-free hot water resistant coating according to claim 1, characterized in that: the engineering plastic particles in the engineering plastic dispersion are engineering plastics,
    或含工程塑料质量0.5-10%的,碳纳米管(CNT)、酸化处理碳纳米管、纳米氮化硼、石墨烯、氧化石墨烯、纳米云母、纳米膨润土中的一种或几种的混合物的改性工程塑料。Or containing 0.5-10% of the mass of engineering plastics, one or more of carbon nanotubes (CNT), acidified carbon nanotubes, nano-boron nitride, graphene, graphene oxide, nano-mica, and nano-bentonite modified engineering plastics.
  4. 根据权利要求1所述的低VOC无有机溶剂耐热水性涂料,其特征在于:所述乳化用的表面活性剂为A -B +结构的阴离子表面活性剂,其中, The low-VOC organic solvent-free hot water resistant coating according to claim 1, characterized in that: the emulsifying surfactant is an anionic surfactant of A - B + structure, wherein,
    A -是C nH 2n-1O 2 -分子式的烷基羧酸根结构,其中n取值为8~16; A - is an alkyl carboxylate structure with the molecular formula of C n H 2n-1 O 2 - , wherein the value of n is 8-16;
    B +选自NH 4 +、Na +、K +B + is selected from NH 4 + , Na + , K + .
  5. 根据权利要求1所述的低VOC无有机溶剂耐热水性涂料,其特征在于:该工程塑料分散液中的工程塑料颗粒,粒径统计值D50≤1μm,D100≤2μm;该工程塑料分散液中的工程塑料颗粒,平均空心率不低于25%。The low-VOC organic solvent-free hot water resistant coating according to claim 1, characterized in that: the engineering plastic particles in the engineering plastic dispersion have a statistical value of particle size D50≤1μm, D100≤2μm; in the engineering plastic dispersion Engineering plastic particles, the average hollow rate is not less than 25%.
  6. 根据权利要求1所述的低VOC无有机溶剂耐热水性涂料,其特征在于:所述的功 能填料选自石英、硫酸钡、二氧化钛、二氧化铬、氧化锌、氧化铁、氧化铝、氧化硅、氧化锆硅酸铝、硅酸铝镁、碳化硅、碳化钛、氮化硅、氮化钛、立方氮化硼,硫酸钡晶须、碳酸钙晶须,碳纤维粉、玻璃纤维粉、石英纤维粉、碳纳米管、氧化石墨烯、石墨烯、玄武岩纤维,云母、滑石粉、六方氮化硼或石墨中的一种或几种的混合物。The low VOC organic solvent-free hot water resistant coating according to claim 1, characterized in that: the functional filler is selected from quartz, barium sulfate, titanium dioxide, chromium dioxide, zinc oxide, iron oxide, aluminum oxide, silicon oxide , zirconia aluminum silicate, aluminum magnesium silicate, silicon carbide, titanium carbide, silicon nitride, titanium nitride, cubic boron nitride, barium sulfate whisker, calcium carbonate whisker, carbon fiber powder, glass fiber powder, quartz fiber Powder, carbon nanotubes, graphene oxide, graphene, basalt fiber, mica, talcum powder, hexagonal boron nitride or graphite or one or a mixture of several.
  7. 一种权利要求1所述的低VOC无有机溶剂耐热水性涂料的工程塑料分散液的制备方法,其特征在于该方法包括如下步骤:A preparation method of the engineering plastic dispersion liquid of the low-VOC organic solvent-free hot water resistant coating according to claim 1, characterized in that the method comprises the steps:
    S1、将工程塑料颗粒、表面活性剂溶于溶媒,用溶媒控制体系粘度为50~1000Pa.s;S1. Dissolve engineering plastic particles and surfactants in a solvent, and use the solvent to control the viscosity of the system to 50-1000Pa.s;
    S2、300~800rpm转速搅拌状态下,向步骤S1得到的物料中加水,得到水包油乳液;S2. Add water to the material obtained in step S1 under stirring at 300-800 rpm to obtain an oil-in-water emulsion;
    S3、水包油乳液经溶媒蒸发,浓缩,得到所述水性的工程塑料分散液。S3. The oil-in-water emulsion is evaporated and concentrated to obtain the water-based engineering plastic dispersion.
  8. 一种由权利要求1所述的低VOC无有机溶剂耐热水性涂料涂覆后得到的耐高温耐腐涂层。A high temperature and corrosion resistant coating obtained by coating the low VOC organic solvent-free hot water resistant coating according to claim 1.
  9. 一种耐高温耐腐涂层的制备方法,其特征在于:权利要求1所述的低VOC无有机溶剂耐热水性涂料各原料根据配比混合、分散均匀,喷涂到经过除油、粗糙化处理的基材上,湿涂膜经145~155℃温度10±2min、280~380℃温度10±2min两次烘烤,即得所述耐高温耐腐涂层。A method for preparing a high-temperature-resistant and corrosion-resistant coating, characterized in that: the raw materials of the low-VOC organic-solvent-free hot-water-resistant coating according to claim 1 are mixed and uniformly dispersed according to the proportion, and sprayed until after degreasing and roughening treatment On the substrate, the wet coating film is baked twice at 145-155°C for 10±2 minutes and 280-380°C for 10±2 minutes to obtain the high-temperature and corrosion-resistant coating.
  10. 一种耐高温耐腐涂层的制备方法,其特征在于:权利要求1所述的低VOC无有机溶剂耐热水性涂料各原料根据配比混合、分散均匀,涂料喷涂到经过除油、粗糙化处理的铝基材上,经145~155℃温度10±2min烘烤后自然冷却到室温,A method for preparing a high-temperature and corrosion-resistant coating, characterized in that: the raw materials of the low-VOC organic-solvent-free hot water-resistant coating according to claim 1 are mixed and uniformly dispersed according to the proportion, and the coating is sprayed until after degreasing and roughening On the treated aluminum substrate, it is baked at 145-155°C for 10±2min and then cooled to room temperature naturally.
    再在干燥涂层上,喷涂一层面涂层,On top of the dry coating, spray a top coat,
    复合涂膜经145~155℃温度10±2min、280~380℃温度10±2min两次烘烤,即得耐高温耐腐涂层。The composite coating film is baked twice at 145-155°C for 10±2 minutes and 280-380°C for 10±2 minutes to obtain a high-temperature and corrosion-resistant coating.
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