WO1995006689A1 - Solid powder-coating composition - Google Patents

Solid powder-coating composition Download PDF

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Publication number
WO1995006689A1
WO1995006689A1 PCT/US1994/008800 US9408800W WO9506689A1 WO 1995006689 A1 WO1995006689 A1 WO 1995006689A1 US 9408800 W US9408800 W US 9408800W WO 9506689 A1 WO9506689 A1 WO 9506689A1
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Prior art keywords
epoxy
coating composition
composition
coating
powder
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PCT/US1994/008800
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French (fr)
Inventor
Jacques L. Poincloux
Rajesh Turakhia
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The Dow Chemical Company
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Publication of WO1995006689A1 publication Critical patent/WO1995006689A1/en

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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
    • C09D167/00Coating compositions based on polyesters obtained by reactions forming a carboxylic ester link in the main chain; Coating compositions based on derivatives of such polymers
    • C09D167/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • 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
    • C09D163/00Coating compositions based on epoxy resins; Coating compositions based on derivatives of epoxy resins

Definitions

  • This invention relates to the art of powder-coating resins and processes to use them.
  • epoxy resins in powder-coatings for articles. See, for example, Tess, "Epoxy Resin Coatings,” Epoxy Resins (2d Ed.) at 772-78 (Marcel-Dekker 1988); and 6 Encyclopedia of Poly. Sci. & Eng.. “Epoxy Resins” at 375 (J. Wiley & Sons 1986),.
  • a solid epoxy resin is mixed with a solid curing agent, and optionally pigments, fillers and stabilizers.
  • the composition is solid at room temperatures but has a glass transition temperature. It is applied as a powder to a cold or preheated substrate, which is usually metal, by methods such as electrostatic spraying, fluidized bed or electrostatic fluidized bed. The powder is heated either by heat from the substrate or by an external heat source, to cause it to melt, flow together, fuse and cure to form a coating.
  • the epoxy resin is a solid advanced resin of bisphenol A and either epichlorohydrin or a diglycidyl ether of bisphenol A.
  • the curing agent is typically dicyanodiamide, an aromatic amine, a phenolic resin, a polyanhydride, a novolac or a carboxyl-terminated polyester.
  • Polyester resins are particularly desirable in some applications because of their excellent appearance, resistance to overbake, and mechanical properties. Common polyesters used are relatively low molecular weight (as compared with polyesters used in fabrics) and branched to promote cross-linking. See, for example, Verborgt, U.S. Patent 4,065,438 (December 27, 1977) and Marsiat, U.S. Patent 4,085,159 (April 18, 1978).
  • the viscosity of the epoxy-polyester powder-coating resins presents an area for improvement.
  • the polyester resins have a relatively high viscosity (such as 150 to 200 poise in a polyester designed for use in a mixture containing 70 weight percent polyester) under curing conditions. (Viscosity is measured using an ICI cone and plate viscometer at 175°C.) Resins with a lower melt viscosity are desirable because they flow together and fuse better to provide a smoother and a more even appearance, and they are easier to process into a powder. It would be desirable to find a powder-coating composition with substantially the same or better flow and/or appearance and lower viscosity under ordinary use conditions.
  • One aspect of the present invention is a solid powder-coating composition
  • a solid powder-coating composition comprising: (1) 20 to 80 parts (per hundred parts resins) of an epoxy resin component which contains on average more than 2 epoxy groups per molecule; and (2) 80 to 20 parts (per hundred parts resin) of an acid-terminated polyester resin component which contains on average from 1.8 to 2.2 acid groups per molecule.
  • a second aspect of the present invention is a process to use the solid powder-coating composition comprising the step of contacting the powder-coating composition with a substrate at a temperature high enough to cause the composition to melt and cure.
  • a third aspect of the present invention is a cured polymer resulting from curing the solid powder-coating composition.
  • a fourth aspect of the present invention is a coated article comprising:
  • compositions of the present invention have a substantially lower overall viscosity under use temperature, and so they can provide a smoother and more even surface coating. Nevertheless, they provide good adhesion to the substrate, good mechanical properties, and good protection for the substrate.
  • the present invention uses a multifunctional epoxy resin component.
  • multifunctional we mean that the epoxy resin component contains on average more than two epoxy groups per molecule.
  • the multifunctional epoxy resin component preferably contains on average at least about 2.05 epoxy groups per molecule, highly preferably contains on average at least about 2.2 epoxy groups per molecule, more preferably contains on average at least about 2.3 epoxy groups per molecule, and most preferably contains at least about 2.5 epoxy groups per molecule.
  • the maximum number of epoxy groups is limited primarily by practical considerations, such as the viscosity of the resin and the ease of fabrication.
  • the resin contains no more than about 6 epoxy groups per molecule, and more preferably no more than about 4 epoxy groups per molecule on average.
  • the multifunctional epoxy resin component preferably has an average epoxy equivalent weight (EEW) of at least about 400, more preferably at least about 450, and most preferably at least about 500.
  • the average EEW of the multifunctional epoxy resin component is preferably no more than about 1200, more preferably no more than about 900 and most preferably no more than about 560.
  • the viscosity of the multifunctional epoxy resin component at 175°C is preferably no more than about 50 poise and more preferably no more than about 30 poise. In most cases, the viscosity of the resin at about 175°C will be at least about 5 or 10 poise.
  • the epoxy groups are typically glycidyl ether groups that result from reacting epihalohydrin with a multifunctional amine, thio or phenolic compound. They typically are represented by Formula I: o
  • each R is independently hydrogen or a lower alkyl group (containing 1 to 8 carbon atoms), and X is -0-, -S- or -NR-. Each R is most preferably hydrogen. Each X is preferably oxygen.
  • the mul ifunctional epoxy resin component may contain a single multifunctional resin, or a mixture of resins. If it is a mixture of epoxy resins, then not all epoxy resins in the mixture need to be multi- functional, as long as the average for epoxy resins in the composition meets the previously-described criteria.
  • the multifunctional epoxy resin component may optionally contain, for instance, at least one multifunctional epoxy resin and a difunctional resin, as long as their proportions are selected so that the entire epoxy resin component averages more than 2 epoxy groups per molecule.
  • the multifunctional epoxy resin composition may contain a mixture of bisphenol A epoxy resin and epoxy novolac resins. Preferably, the amount of monofunctional epoxy resins in the epoxy resin component is minimized.
  • Each Ar represents a single aromatic ring or a plurality of fused or unfused aromatic rings.
  • Each Ar is preferably carbocyclic and more preferably hydrocarbyl. It may have substituents that do not interfere with the manufacture or use of the epoxy resin. Substituents are preferably lower (Cl to C8) alkyl groups.
  • Preferred examples of Ar include monovalent and multivalent benzene, toluene, naphthalene, biphenyl and 2,2-bi ⁇ henyl-isopropylidene structures. Ar is most preferably a divalent or trivalent phenylene moiety.
  • Each GE is independently hydrogen or a glycidyl ether moiety of the Formula I, selected so that the resin contains on average more than 2 epoxy groups per molecule.
  • Each A 1 is independently a divalent moiety that does not interfere with the manufacture or use of the resin.
  • A' may be, for instance, a carbonyl group, an oxygen atom, a sulfonyl group, or an alkyl group.
  • A' is preferably an alkyl group.
  • Each m is selected such that the resin contains on average more than 2 epoxy groups per molecule.
  • the resins can be made by contacting a polyphenol (which corresponds to Formula II or III in which all GE are hydroxyl groups) with epichlorohydrin in the presence of a suitable catalyst. Such processes are well-known to persons of ordinary skill.
  • the present invention also uses an essentially linear (unbranched) acid-terminated polyester resin component.
  • essentially linear it is meant that the polyester resin component contains on average about two carboxylic acid groups per molecule or less.
  • the polyester resin component preferably contains on average at least about 1.8 acid groups per molecule and more preferably at least about 1.9 acid groups per molecule. It preferably contains on average no more than about 2.2 acid groups per molecule and more preferably no more than about 2.1 acid groups per molecule.
  • the average number of acid groups per polyester molecule is most preferably as close to 2 as possible.
  • the polyester backbone may contain aromatic moieties, such as result from the reaction of terephthalic acid, isophthalic acid or bisphenol A. It may also contain aliphatic moieties, such as the remnants of lower alkyl (1 to 8 carbon) diacids and diols - for instance: adipic acid, neopentyl glycol, ethylene glycol, and 1,6- hexanediol.
  • the optimum acid number of the polyester depends on the ratio of epoxy resin to polyester resin and the epoxy equivalent weight of the epoxy resin. In most cases, the acid number is preferably at least about 20 and more preferably at least about 25; it is preferably no more than about 150 and more preferably no more than about 110.
  • the hydroxyl number of the polymer is preferably minimized; it is preferably no more than about 15 and more preferably no more than about 5.
  • the number average molecular weight of the linear polyester is preferably at least about 1000 and most preferably at least about 2000.
  • the number average molecular weight of the linear polyester is preferably no more than about 10,000, and more preferably no more than about 4000.
  • the viscosity of the polyester at 175°C is preferably no more than about 125 poise, more preferably no more than about 100 poise, more highly preferably no more than about 75 poise, and most preferably no more than about 50 poise.
  • the viscosity at 175°C is almost always at least about 10 poise, frequently at least about 25 poise and often at least about 40 poise.
  • the polyester preferably has a glass transition temperature of 50°C to 80°C.
  • Suitable linear polyesters can be made by known processes such as by the reaction of one or more dihydroxy compound with one or more diacid (or derivative of the diacid, such as an acid halide or ester).
  • diacids include: isophthalic acid, terephthalic acid, adipic acid.
  • preferred dihydroxy compounds include: ethylene glycol, propylene glycol, neopentyl glycol and hexanediol.
  • the quantity of multifunctional reagents (such as triacids or triols) used in the reaction is preferably minimized, since any branching increases the viscosity of the polyester.
  • the reagents may contain small quantities of multifunctional reagent (such as about 1 weight percent or less) without unduly raising the viscosity of the resin, as long as the level of branching does not exceed the limits previously described.
  • the polyester is usually made using a catalyst such as dibutyl tin oxide.
  • a catalyst such as dibutyl tin oxide. Examples of processes to make polyesters are described in Danick, U.S. Patent 5,006,612 (April 9, 1991); Merck et al., U.S. Patent 4,740,580 (April 26, 1988); and Concise Ency. of Poly. Sci. & Eng.. “Polyesters”, at 793-799 (J. Wiley & Sons 1990).
  • the branched polyesters that are used in ordinary powder- coatings have a high viscosity. The viscosity of the polyester resin can be significantly lowered by using an essentially linear polyester resin. Since the polyester resin is linear, the epoxy resin should be multifunctional to provide suitable cross-linking.
  • the multifunctional epoxy resin has a somewhat higher viscosity than the linear epoxy resin, but the overall viscosity of the composition containing linear polyester and branched epoxy is significantly lower than the viscosity of the composition containing linear epoxy and branched polyester.
  • the epoxy resin and the polyester resin are preferably used in a ratio to provide about equivalent numbers of epoxy groups and acid groups within the composition.
  • the composition preferably contains at least about 0.5 epoxy groups per acid group, more preferably at least about 0.75 epoxy groups and most preferably at least about 0.9 epoxy groups.
  • the composition preferably contains no more than about 1.5 epoxy groups per acid group, more preferably no more than about 1.25 epoxy groups and most preferably no more than about 1.1 epoxy groups.
  • the weight ratio of epoxy resin component to polyester resin component is between 20:80 and 80:20. Compositions that contain more than about 50 phr epoxy resin (50:50 weight ratio) usually require specially tailored epoxy and polyester resins (with special acid number and epoxy equivalent weight) to meet the previously stated equivalency criteria.
  • the preferred weight ratio of the epoxy resin component and the polyester resin component depends upon the composition of the resins and their equivalent weight per functional group. For the most common epoxy resin and polyester, the weight ratio of polyester resin component to epoxy resin component is preferably at least 50:50 and most preferably at least 60:40.
  • the weight ratio of polyester component to epoxy component is preferably no more than 75:25 and most preferably no more than 70:30.
  • the composition preferably contains a catalyst to promote curing between the epoxy and the polyester resins.
  • a catalyst to promote curing between the epoxy and the polyester resins.
  • suitable curing catalysts include: amines and ammonium salts, phosphines and phosphonium salts, and imidazoles.
  • the composition preferably contains 0.01 to 2 part catalyst per 100 parts resin (phr); it more preferably contains about 0.05 to 0.5 phr catalyst.
  • the composition may also contain curing agents for the epoxy resin, such as amines, polyphenols and imidazoles. It preferably contains no curing agent other than the polyester resin.
  • the composition may also contain other additives, such as fillers, stabilizers, pigments, flow-modifiers and anti-cratering agents.
  • the components of the composition are typically premixed before they are used. For instance, they may be extruded together at a temperature below their curing temperature, and then converted to a powder.
  • the powder composition preferably contains particles of a size suitable for powder-coating applications.
  • the average particle size is preferably at least about 5 ⁇ m in diameter and more preferably at least about 10 ⁇ m.
  • the average particle size is preferably no more than about 100 ⁇ m and more preferably no more than about 50 ⁇ m.
  • the powder-coating may be applied in a manner that is usual for powder-coating resins. Powder-coating application and use is described in detail at Tess, "Epoxy Resin Coatings,” Epoxy Resins (2d Ed.) at 772-78 (Marcel-Dekker 1988).
  • the powder may be applied to a preheated substrate, so that heat from the substrate causes the powder to melt, flow and cure; or the powder may be applied to a cool substrate which is subsequently heated to make the powder melt, flow and cure.
  • the curing temperature is preferably between 140°C and 200°C.
  • the substrate is usually metal, such as steel, although it may be any material that can withstand curing temperatures.
  • the powder is applied to the substrate by known methods such as electrostatic spraying, fluidized bed application, or electrostatic fluidized bed. The process is preferably continued until the cured coating has a thickness of at least about 1 mil and most preferably at least about 2 mil. In most cases, the coating is preferably no more than about 4 mil thick.
  • the powder-coating should be heated long enough to cure to meet required properties. It is preferably baked for at least about 5 minutes. The coating is preferably baked for no more than about 20 minutes, although this is not critical.
  • the cured coating of the present invention preferably has additional advantages over cured coatings of the prior art, such as good appearance, good direct/reverse impact resistance, good pencil hardness and good 60° gloss.
  • additional advantages such as good appearance, good direct/reverse impact resistance, good pencil hardness and good 60° gloss.
  • the following examples are for illustrative purposes only. They do not limit either the specification or the claims. Unless otherwise stated, all parts and percentages are by weight.
  • Example 1 A linear polyester was made by the following process.
  • a mixture containing 528 g of neopentyl glycol, 581 g of terephthalic acid, and 50 g of adipic acid was heated to 150°C.
  • a 1.5 g quantity of FASCAT 4202 catalyst and 0.5 g of FASCAT 4100 catalyst were added.
  • the temperature was increased slowly to 250°C.
  • 276 g of isophthalic acid was added.
  • the reaction was continued for 4 hours at 250°C.
  • a phosphonium curing catalyst was added, and the polyester resin was recovered by casting on a foil surface and grinding the cast precipitate.
  • the polyester resin had an acid number of 43, a hydroxyl number of 1, and a viscosity of 50 poise at 175°C (as measured by ICI cone and plate viscosimeter).
  • the polyester resin had a glass transition temperature at 57°C (as measured by differential scanning calorimeter) and a number average molecular weight of 2137 (as measured by gel permeation chromatography).
  • the following powder-coating elements were weighted and
  • R960 titanium dioxide pigment, 8 g of benzoine, 16 g of RESIFLOW P67 flow-modifier The premix was extruded through an extruder with a barrel temperature of about 200°F. The extrudate was crushed and then ground on a BRINKMANN grinder using a 12 tooth wheel and 0.5 screen. The resulting powder was sieved through a number 140 wire mesh sieve. The powder was applied to cold rolled steel panels using a WAGNER G-100 electrostatic spray gun. The panels were baked in an oven at 180°C for 15 minutes to melt and cure the coating.

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Abstract

Powder-coating compositions that have a low melt viscosity contain: 1) 20 to 80 parts of a multifunctional epoxy resin component; 2) 80 to 20 parts of an essentially linear acid-terminated polyester resin component.

Description

SOLID POWDER-COATING COMPOSITION
This invention relates to the art of powder-coating resins and processes to use them.
It is well-known to use epoxy resins in powder-coatings for articles. See, for example, Tess, "Epoxy Resin Coatings," Epoxy Resins (2d Ed.) at 772-78 (Marcel-Dekker 1988); and 6 Encyclopedia of Poly. Sci. & Eng.. "Epoxy Resins" at 375 (J. Wiley & Sons 1986),. In summary, a solid epoxy resin is mixed with a solid curing agent, and optionally pigments, fillers and stabilizers. The composition is solid at room temperatures but has a glass transition temperature. It is applied as a powder to a cold or preheated substrate, which is usually metal, by methods such as electrostatic spraying, fluidized bed or electrostatic fluidized bed. The powder is heated either by heat from the substrate or by an external heat source, to cause it to melt, flow together, fuse and cure to form a coating.
For most nonweatherable applications, the epoxy resin is a solid advanced resin of bisphenol A and either epichlorohydrin or a diglycidyl ether of bisphenol A. The curing agent is typically dicyanodiamide, an aromatic amine, a phenolic resin, a polyanhydride, a novolac or a carboxyl-terminated polyester. Polyester resins are particularly desirable in some applications because of their excellent appearance, resistance to overbake, and mechanical properties. Common polyesters used are relatively low molecular weight (as compared with polyesters used in fabrics) and branched to promote cross-linking. See, for example, Verborgt, U.S. Patent 4,065,438 (December 27, 1977) and Marsiat, U.S. Patent 4,085,159 (April 18, 1978).
The viscosity of the epoxy-polyester powder-coating resins presents an area for improvement. The polyester resins have a relatively high viscosity (such as 150 to 200 poise in a polyester designed for use in a mixture containing 70 weight percent polyester) under curing conditions. (Viscosity is measured using an ICI cone and plate viscometer at 175°C.) Resins with a lower melt viscosity are desirable because they flow together and fuse better to provide a smoother and a more even appearance, and they are easier to process into a powder. It would be desirable to find a powder-coating composition with substantially the same or better flow and/or appearance and lower viscosity under ordinary use conditions.
One aspect of the present invention is a solid powder-coating composition comprising: (1) 20 to 80 parts (per hundred parts resins) of an epoxy resin component which contains on average more than 2 epoxy groups per molecule; and (2) 80 to 20 parts (per hundred parts resin) of an acid-terminated polyester resin component which contains on average from 1.8 to 2.2 acid groups per molecule.
(Parts per hundred parts resin or "phr" relates the weight of a component to the total weight of epoxy resin component and polyester resin component in the composition - ignoring other components such as catalyst or pigment) A second aspect of the present invention is a process to use the solid powder-coating composition comprising the step of contacting the powder-coating composition with a substrate at a temperature high enough to cause the composition to melt and cure.
A third aspect of the present invention is a cured polymer resulting from curing the solid powder-coating composition.
A fourth aspect of the present invention is a coated article comprising:
(1) a substrate, and (2) a coating that comprises a cured powder-coating composition of the present invention.
The compositions of the present invention have a substantially lower overall viscosity under use temperature, and so they can provide a smoother and more even surface coating. Nevertheless, they provide good adhesion to the substrate, good mechanical properties, and good protection for the substrate.
The present invention uses a multifunctional epoxy resin component. By multifunctional, we mean that the epoxy resin component contains on average more than two epoxy groups per molecule. The multifunctional epoxy resin component preferably contains on average at least about 2.05 epoxy groups per molecule, highly preferably contains on average at least about 2.2 epoxy groups per molecule, more preferably contains on average at least about 2.3 epoxy groups per molecule, and most preferably contains at least about 2.5 epoxy groups per molecule. The maximum number of epoxy groups is limited primarily by practical considerations, such as the viscosity of the resin and the ease of fabrication. Preferably, the resin contains no more than about 6 epoxy groups per molecule, and more preferably no more than about 4 epoxy groups per molecule on average.
The multifunctional epoxy resin component preferably has an average epoxy equivalent weight (EEW) of at least about 400, more preferably at least about 450, and most preferably at least about 500. The average EEW of the multifunctional epoxy resin component is preferably no more than about 1200, more preferably no more than about 900 and most preferably no more than about 560. The viscosity of the multifunctional epoxy resin component at 175°C is preferably no more than about 50 poise and more preferably no more than about 30 poise. In most cases, the viscosity of the resin at about 175°C will be at least about 5 or 10 poise.
The epoxy groups are typically glycidyl ether groups that result from reacting epihalohydrin with a multifunctional amine, thio or phenolic compound. They typically are represented by Formula I: o
' \ I X-CR2-CR CR2
wherein each R is independently hydrogen or a lower alkyl group (containing 1 to 8 carbon atoms), and X is -0-, -S- or -NR-. Each R is most preferably hydrogen. Each X is preferably oxygen.
The mul ifunctional epoxy resin component may contain a single multifunctional resin, or a mixture of resins. If it is a mixture of epoxy resins, then not all epoxy resins in the mixture need to be multi- functional, as long as the average for epoxy resins in the composition meets the previously-described criteria. The multifunctional epoxy resin component may optionally contain, for instance, at least one multifunctional epoxy resin and a difunctional resin, as long as their proportions are selected so that the entire epoxy resin component averages more than 2 epoxy groups per molecule. For instance, the multifunctional epoxy resin composition may contain a mixture of bisphenol A epoxy resin and epoxy novolac resins. Preferably, the amount of monofunctional epoxy resins in the epoxy resin component is minimized.
Suitable multifunctional epoxy resins and processes to make them are described in numerous published references such as: Walker, U.S. Patent 4,868,059 (September 19, 1989); Schrader, U.S. Patent
4,474,929 (October 2, 1984); Berman, U.S. Patent 4,604,317 (August 5, 1986); Wang, U.S. Patent 4,672,103 (June 9, 1987). Other multifunctional epoxy resins are commercially available from The Dow Chemical Company under the tradenames D.E.R.® 642U, D.E.R.® 672U and the D.E.N.® series, (trademark of The Dow Chemical Company). The multifunctional resins are usually glycidyl ethers of novolacs, tris- phenols, and triglycidylisocyanurate. Suitable epoxy resins are preferably represented by one of Formulae II or III:
I I
GE Ar- A ' -hn-A ' -Ar — GE
Figure imgf000006_0001
Figure imgf000006_0002
wherein :
Each Ar represents a single aromatic ring or a plurality of fused or unfused aromatic rings. Each Ar is preferably carbocyclic and more preferably hydrocarbyl. It may have substituents that do not interfere with the manufacture or use of the epoxy resin. Substituents are preferably lower (Cl to C8) alkyl groups. Preferred examples of Ar include monovalent and multivalent benzene, toluene, naphthalene, biphenyl and 2,2-biρhenyl-isopropylidene structures. Ar is most preferably a divalent or trivalent phenylene moiety.
Each GE is independently hydrogen or a glycidyl ether moiety of the Formula I, selected so that the resin contains on average more than 2 epoxy groups per molecule. Each A1 is independently a divalent moiety that does not interfere with the manufacture or use of the resin. A' may be, for instance, a carbonyl group, an oxygen atom, a sulfonyl group, or an alkyl group. A' is preferably an alkyl group. Each m is selected such that the resin contains on average more than 2 epoxy groups per molecule. The resins can be made by contacting a polyphenol (which corresponds to Formula II or III in which all GE are hydroxyl groups) with epichlorohydrin in the presence of a suitable catalyst. Such processes are well-known to persons of ordinary skill.
The present invention also uses an essentially linear (unbranched) acid-terminated polyester resin component. By "essentially linear" it is meant that the polyester resin component contains on average about two carboxylic acid groups per molecule or less. The polyester resin component preferably contains on average at least about 1.8 acid groups per molecule and more preferably at least about 1.9 acid groups per molecule. It preferably contains on average no more than about 2.2 acid groups per molecule and more preferably no more than about 2.1 acid groups per molecule. The average number of acid groups per polyester molecule is most preferably as close to 2 as possible.
The polyester backbone may contain aromatic moieties, such as result from the reaction of terephthalic acid, isophthalic acid or bisphenol A. It may also contain aliphatic moieties, such as the remnants of lower alkyl (1 to 8 carbon) diacids and diols - for instance: adipic acid, neopentyl glycol, ethylene glycol, and 1,6- hexanediol.
The optimum acid number of the polyester depends on the ratio of epoxy resin to polyester resin and the epoxy equivalent weight of the epoxy resin. In most cases, the acid number is preferably at least about 20 and more preferably at least about 25; it is preferably no more than about 150 and more preferably no more than about 110. The hydroxyl number of the polymer is preferably minimized; it is preferably no more than about 15 and more preferably no more than about 5. The number average molecular weight of the linear polyester is preferably at least about 1000 and most preferably at least about 2000. The number average molecular weight of the linear polyester is preferably no more than about 10,000, and more preferably no more than about 4000.
The viscosity of the polyester at 175°C is preferably no more than about 125 poise, more preferably no more than about 100 poise, more highly preferably no more than about 75 poise, and most preferably no more than about 50 poise. The viscosity at 175°C is almost always at least about 10 poise, frequently at least about 25 poise and often at least about 40 poise. The polyester preferably has a glass transition temperature of 50°C to 80°C.
Suitable linear polyesters can be made by known processes such as by the reaction of one or more dihydroxy compound with one or more diacid (or derivative of the diacid, such as an acid halide or ester). Examples of preferred diacids include: isophthalic acid, terephthalic acid, adipic acid. Examples of preferred dihydroxy compounds include: ethylene glycol, propylene glycol, neopentyl glycol and hexanediol. The quantity of multifunctional reagents (such as triacids or triols) used in the reaction is preferably minimized, since any branching increases the viscosity of the polyester. However, the reagents may contain small quantities of multifunctional reagent (such as about 1 weight percent or less) without unduly raising the viscosity of the resin, as long as the level of branching does not exceed the limits previously described.
The polyester is usually made using a catalyst such as dibutyl tin oxide. Examples of processes to make polyesters are described in Danick, U.S. Patent 5,006,612 (April 9, 1991); Merck et al., U.S. Patent 4,740,580 (April 26, 1988); and Concise Ency. of Poly. Sci. & Eng.. "Polyesters", at 793-799 (J. Wiley & Sons 1990). The branched polyesters that are used in ordinary powder- coatings have a high viscosity. The viscosity of the polyester resin can be significantly lowered by using an essentially linear polyester resin. Since the polyester resin is linear, the epoxy resin should be multifunctional to provide suitable cross-linking. The multifunctional epoxy resin has a somewhat higher viscosity than the linear epoxy resin, but the overall viscosity of the composition containing linear polyester and branched epoxy is significantly lower than the viscosity of the composition containing linear epoxy and branched polyester. The epoxy resin and the polyester resin are preferably used in a ratio to provide about equivalent numbers of epoxy groups and acid groups within the composition. The composition preferably contains at least about 0.5 epoxy groups per acid group, more preferably at least about 0.75 epoxy groups and most preferably at least about 0.9 epoxy groups. The composition preferably contains no more than about 1.5 epoxy groups per acid group, more preferably no more than about 1.25 epoxy groups and most preferably no more than about 1.1 epoxy groups.
The weight ratio of epoxy resin component to polyester resin component is between 20:80 and 80:20. Compositions that contain more than about 50 phr epoxy resin (50:50 weight ratio) usually require specially tailored epoxy and polyester resins (with special acid number and epoxy equivalent weight) to meet the previously stated equivalency criteria. The preferred weight ratio of the epoxy resin component and the polyester resin component depends upon the composition of the resins and their equivalent weight per functional group. For the most common epoxy resin and polyester, the weight ratio of polyester resin component to epoxy resin component is preferably at least 50:50 and most preferably at least 60:40. The weight ratio of polyester component to epoxy component is preferably no more than 75:25 and most preferably no more than 70:30.
The composition preferably contains a catalyst to promote curing between the epoxy and the polyester resins. Such catalysts and their use are well known in the art. Examples of suitable curing catalysts include: amines and ammonium salts, phosphines and phosphonium salts, and imidazoles. The use of catalysts such as
1-methylimidazole is also described in: McLafferty et al., U.S. Patent 4,910,287 (March 20, 1990). The composition preferably contains 0.01 to 2 part catalyst per 100 parts resin (phr); it more preferably contains about 0.05 to 0.5 phr catalyst. The composition may also contain curing agents for the epoxy resin, such as amines, polyphenols and imidazoles. It preferably contains no curing agent other than the polyester resin. The composition may also contain other additives, such as fillers, stabilizers, pigments, flow-modifiers and anti-cratering agents.
The components of the composition are typically premixed before they are used. For instance, they may be extruded together at a temperature below their curing temperature, and then converted to a powder. The powder composition preferably contains particles of a size suitable for powder-coating applications. The average particle size is preferably at least about 5 μm in diameter and more preferably at least about 10 μm. The average particle size is preferably no more than about 100 μm and more preferably no more than about 50 μm.
The powder-coating may be applied in a manner that is usual for powder-coating resins. Powder-coating application and use is described in detail at Tess, "Epoxy Resin Coatings," Epoxy Resins (2d Ed.) at 772-78 (Marcel-Dekker 1988). In summary, the powder may be applied to a preheated substrate, so that heat from the substrate causes the powder to melt, flow and cure; or the powder may be applied to a cool substrate which is subsequently heated to make the powder melt, flow and cure. The curing temperature is preferably between 140°C and 200°C.
The substrate is usually metal, such as steel, although it may be any material that can withstand curing temperatures. The powder is applied to the substrate by known methods such as electrostatic spraying, fluidized bed application, or electrostatic fluidized bed. The process is preferably continued until the cured coating has a thickness of at least about 1 mil and most preferably at least about 2 mil. In most cases, the coating is preferably no more than about 4 mil thick. The powder-coating should be heated long enough to cure to meet required properties. It is preferably baked for at least about 5 minutes. The coating is preferably baked for no more than about 20 minutes, although this is not critical.
The cured coating of the present invention preferably has additional advantages over cured coatings of the prior art, such as good appearance, good direct/reverse impact resistance, good pencil hardness and good 60° gloss. The following examples are for illustrative purposes only. They do not limit either the specification or the claims. Unless otherwise stated, all parts and percentages are by weight. Example 1 A linear polyester was made by the following process.
A mixture containing 528 g of neopentyl glycol, 581 g of terephthalic acid, and 50 g of adipic acid was heated to 150°C. A 1.5 g quantity of FASCAT 4202 catalyst and 0.5 g of FASCAT 4100 catalyst were added. The temperature was increased slowly to 250°C. After 130 g of water had been collected from the reaction mixture, 276 g of isophthalic acid was added. The reaction was continued for 4 hours at 250°C. A phosphonium curing catalyst was added, and the polyester resin was recovered by casting on a foil surface and grinding the cast precipitate. It had an acid number of 43, a hydroxyl number of 1, and a viscosity of 50 poise at 175°C (as measured by ICI cone and plate viscosimeter). The polyester resin had a glass transition temperature at 57°C (as measured by differential scanning calorimeter) and a number average molecular weight of 2137 (as measured by gel permeation chromatography). The following powder-coating elements were weighted and
® premixed: 910 g polyester resin, 390 g of D.E.R. 642U epoxy resin commercially available from The Dow Chemical Company, 676 g of TI PURE
R960 titanium dioxide pigment, 8 g of benzoine, 16 g of RESIFLOW P67 flow-modifier. The premix was extruded through an extruder with a barrel temperature of about 200°F. The extrudate was crushed and then ground on a BRINKMANN grinder using a 12 tooth wheel and 0.5 screen. The resulting powder was sieved through a number 140 wire mesh sieve. The powder was applied to cold rolled steel panels using a WAGNER G-100 electrostatic spray gun. The panels were baked in an oven at 180°C for 15 minutes to melt and cure the coating.
The cured coating had the following characteristics:
(a) film thickness: 2 mil ± 0.2 (measured as per ASTM 1186-87);
(b) direct impact resistance: 160/160 in-lbs (as measured as per the Gardner impact test ASTM D 2794-90); (c) pencil hardness: H (measured as per ASTM D 3363-74);
(d) 60 percent gloss: 95 percent (measured as per ASTM D 523-89. Visual inspection shows no pinholes, craters or "orange peel" texture.

Claims

Cl aims
1. A solid powder-coating composition comprising:
(1) 20 to 80 phr of an epoxy resin component which contains on average more than 2 epoxy groups per molecule;
(2) 80 to 20 phr of an acid-terminated polyester resin component which contains on average from 1.8 to 2.2 acid groups per molecule.
2. A solid powder-coating composition as described in Claim 1 wherein the epoxy resin component contains on average at least 2.05 epoxy groups per molecule.
3. A solid powder-coating composition as described in any of the preceding Claims wherein the epoxy resin component has an epoxy equivalent weight of from 450 to 900.
4. A solid powder-coating composition as described in any of the preceding claims wherein the polyester resin contains on average no more than about 2 acid groups per molecule.
5. A solid powder-coating composition as described in any of the preceding claims wherein the polyester resin has an acid number between 20 and 110.
6. A solid powder-coating composition as described in any of the preceding claims wherein the polyester resin has a viscosity of no more than 75 poise at 175°C.
7. A solid powder-coating composition as described in any of the preceding claims wherein the composition contains 50 to 70 phr polyester and 50 to 30 phr epoxy resin.
8. A process to apply a coating to an article, containing the step of contacting a substrate with a powder-coating composition at a temperature high enough to cause the composition to melt and cure, characterized in that the composition is a solid powder-coating composition as described in any of Claims 1-7.
9. A coated article that contains a substrate and a coating on the substrate, characterized in that the coating contains a cured composition as described in any of Claims 1-7.
PCT/US1994/008800 1993-09-02 1994-08-03 Solid powder-coating composition WO1995006689A1 (en)

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Cited By (7)

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Publication number Priority date Publication date Assignee Title
WO1996036674A1 (en) * 1995-05-18 1996-11-21 Dsm N.V. Thick-layer coil coatings and composition and process for preparing the same
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US6270855B1 (en) 1996-05-17 2001-08-07 The Valspar Corporation Powder coating compositions and methods
US6458439B1 (en) 1996-05-17 2002-10-01 The Valspar Corporation Extrusion coating compositions and method
US6472472B2 (en) 1996-05-17 2002-10-29 The Valspar Corporation Powder coating compositions and method
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ES2210701T3 (en) 1997-02-07 2004-07-01 Vantico Ag POWDER PAINT.
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US6850995B1 (en) * 1999-01-25 2005-02-01 Canon Kabushiki Kaisha Control unit selectively connected with a first bus and a second bus for controlling a displaying process in parallel with a scanning process
US6294610B1 (en) 1999-11-29 2001-09-25 Rohm And Haas Company Coating powders for heat-sensitive substrates
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0136263A2 (en) * 1983-08-25 1985-04-03 Vernicolor AG Lack- und Farbenfabrik Duroplastic powder lacquer, metallic container with a welded joint coated with a duroplast and method of coating the surface of a metallic container welded joint
US4910287A (en) * 1989-01-06 1990-03-20 Ruco Polymer Corporation 1-methyl imidazole catalyzed carboxyl terminated polyester
EP0365428A2 (en) * 1988-10-18 1990-04-25 Daicel Chemical Industries, Ltd. A powder coating composition
US5006612A (en) * 1989-10-18 1991-04-09 Cargill, Incorporated Polyesters for powder coating resins using an intermediate having low process viscosity
US5043401A (en) * 1988-10-07 1991-08-27 Somar Corporation Powder coating composition based on mixed bisphenol epoxy resins, polyester resin and curing agent

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3397254A (en) * 1964-09-21 1968-08-13 Union Carbide Corp Carboxy terminated polyesters prepared from tribasic acid anhydrides and hydroxy terminated polyesters
US4147737A (en) * 1970-12-23 1979-04-03 Internationale Octrooi Maatschappij Octropa B.V. Powder coating composition employing mixture of polyepoxide resin with modified polyester resin
GB1509043A (en) * 1975-04-29 1978-04-26 Ucb Sa Powdered epoxy resin and polyester coating compositions
GB1588230A (en) * 1976-09-27 1981-04-15 British Industrial Plastics Artificial resin powder coating compositions
NL164082C (en) * 1978-10-31 1980-11-17 Unilever Nv POWDER COAT.
JPS5829342B2 (en) * 1979-11-02 1983-06-22 東洋紡績株式会社 Resin composition for powder coating
JPS5783564A (en) * 1980-11-12 1982-05-25 Dainippon Ink & Chem Inc Resin composition for powder coating
US4365046A (en) * 1981-01-12 1982-12-21 The Goodyear Tire & Rubber Company Process to control the curing reaction between a copolyester resin and an epoxide compound, and a composition formed for that process
US4370452A (en) * 1981-01-12 1983-01-25 The Goodyear Tire & Rubber Company Process to induce rapid curing of a copolyester resin with epoxide compounds and a composition formed for that process
US4568606A (en) * 1984-12-14 1986-02-04 Morton Thiokol, Inc. Powder coatable epoxy/polyester composition and electrical conductors coated therewith
GB8609034D0 (en) * 1986-04-14 1986-05-21 Ucb Sa Preparation of polyesters
DE3936973A1 (en) * 1989-03-11 1991-05-08 Hoechst Ag HAERTBARE, POWDERFUL MIXTURES
US4933429A (en) * 1989-03-13 1990-06-12 General Electric Company Method for preparing polyester-polyepoxide compositions of high melt viscosity
JP2810500B2 (en) * 1990-07-03 1998-10-15 日本ペイント株式会社 Powder paint

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0136263A2 (en) * 1983-08-25 1985-04-03 Vernicolor AG Lack- und Farbenfabrik Duroplastic powder lacquer, metallic container with a welded joint coated with a duroplast and method of coating the surface of a metallic container welded joint
US5043401A (en) * 1988-10-07 1991-08-27 Somar Corporation Powder coating composition based on mixed bisphenol epoxy resins, polyester resin and curing agent
EP0365428A2 (en) * 1988-10-18 1990-04-25 Daicel Chemical Industries, Ltd. A powder coating composition
US4910287A (en) * 1989-01-06 1990-03-20 Ruco Polymer Corporation 1-methyl imidazole catalyzed carboxyl terminated polyester
US5006612A (en) * 1989-10-18 1991-04-09 Cargill, Incorporated Polyesters for powder coating resins using an intermediate having low process viscosity

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
CHEMICAL ABSTRACTS, vol. 85, no. 12, 20 September 1976, Columbus, Ohio, US; abstract no. 79827m, YOSHIHARA M.: "Epoxy resin polyester coating compositions" page 111; *

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996036674A1 (en) * 1995-05-18 1996-11-21 Dsm N.V. Thick-layer coil coatings and composition and process for preparing the same
NL1000387C2 (en) * 1995-05-18 1997-01-21 Dsm Nv Thick layer of coil coatings.
US6551662B1 (en) 1996-05-17 2003-04-22 The Valspar Corporation Extrusion coating compositions and method
CN1111187C (en) * 1996-05-17 2003-06-11 德克斯特公司 Polyester compositions and use thereof in extrusion coating
US6153264A (en) * 1996-05-17 2000-11-28 The Dexter Corporation Polyester compositions and use thereof in extrusion coating
US6270855B1 (en) 1996-05-17 2001-08-07 The Valspar Corporation Powder coating compositions and methods
US6458439B1 (en) 1996-05-17 2002-10-01 The Valspar Corporation Extrusion coating compositions and method
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US5942285A (en) * 1996-05-17 1999-08-24 The Dexter Corporation Extrusion coating compositions and method
US6827980B2 (en) 1996-05-17 2004-12-07 Valspar Corporation Extrusion coating compositions and method
US7101590B2 (en) 1996-05-17 2006-09-05 Valspar Corporation Extrusion coating compositions and method
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US9737906B2 (en) 2012-08-28 2017-08-22 Nippon Paint Automotive Coatings Co., Ltd. Method for forming excellent multi-layer coating film
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EP3030615A4 (en) * 2013-08-09 2017-05-03 SABIC Global Technologies B.V. Poly(phenylene ether) /epoxy homogeneous solid and powder coating composition incorporating same

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