US20110281972A1 - Powder coating compositions for low temperature curing and high flow - Google Patents
Powder coating compositions for low temperature curing and high flow Download PDFInfo
- Publication number
- US20110281972A1 US20110281972A1 US13/140,338 US200913140338A US2011281972A1 US 20110281972 A1 US20110281972 A1 US 20110281972A1 US 200913140338 A US200913140338 A US 200913140338A US 2011281972 A1 US2011281972 A1 US 2011281972A1
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- weight percent
- powder coating
- coating composition
- acid
- polyester resin
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Classifications
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING 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
- C09D167/00—Coating compositions based on polyesters obtained by reactions forming a carboxylic ester link in the main chain; Coating compositions based on derivatives of such polymers
- C09D167/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
- C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
- C08G63/46—Polyesters chemically modified by esterification
- C08G63/48—Polyesters chemically modified by esterification by unsaturated higher fatty oils or their acids; by resin acids
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING 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
- C09D167/00—Coating compositions based on polyesters obtained by reactions forming a carboxylic ester link in the main chain; Coating compositions based on derivatives of such polymers
- C09D167/08—Polyesters modified with higher fatty oils or their acids, or with natural resins or resin acids
Definitions
- the present invention relates to powder coating compositions and to components and ingredients for incorporation therein, suitable for low temperature curing schedule, with excellent flow of the coating, good flexibility, no blooming phenomenon and resistance to outside aging.
- thermoset powder coating decoration is that the powder coating is formulated by dispersing coloring agents or pigments within a matrix of cross-linkable material, grinding the material to a powder, applying the powder to a surface to be coated and then heating or baking to cause the powder particles to coalesce to form a layer on the surface to be decorated and thereafter causing or allowing curing or crosslinking to take place to form a thermoset layer. Based on these principles the skilled artisan is always searching the best compromise between cure/production cost and appearance of the thermoset coating. Recently, the industry has showed an interest in lower curing temperature for environmental and economical reasons.
- One of the essential requirements of a powder coating is that it should be curable/cross-linkable. In the majority of cases this means the incorporation of a cross-linking agent and the increase of the melt viscosity over the bake period. It is desirable that the baking should be as efficient as possible to minimize energy costs.
- the flow of the coating is determined by the viscosity build-up of the thermosetting composition during the curing, if the increase of viscosity occurs at a too early stage in the baking process, it will have as result that the powder particles will not have fully coalesced and “leveled”. This will result in the production of an article with an unacceptable finish, usually characterized by “orange peel”.
- thermosetting powder coating with outstanding properties for exterior end applications is typically based on a polyester resin.
- Polyester powder coatings are typically formulated with polyepoxide or beta hydroxyalkyl amide type cross-linking compounds.
- the technology surrounding these materials is generally well known and has been discussed and considered in a number of articles and prior patent specifications.
- Patent EP 0 322 834 describes thermosetting powder compositions essentially containing a polyester bearing carboxyl groups and a beta-hydroxyalkylamide, which is applied to a substrate and is then crosslinked at a temperature of 160 to 200° C.
- benzoin as additive in these compositions, which is added as degassing agent, the bubbles of water and air remain trapped in the hardened coating after it has melted and crosslinked, especially if the coating is relatively thick.
- the flow of the powder when it melts is not optimal.
- Patent application WO 91/14745 describes thermosetting powder compositions containing an amorphous polyester containing carboxyl groups, a semi-crystalline polyester containing carboxyl groups and a crosslinking agent. 10 to 40% by weight of the semi-crystalline polyester is preferably used relative to the polyesters as a whole, and the crosslinking agent can be a beta-hydroxyalkylamide.
- the presence of the semi-crystalline polyester in these compositions improves the mechanical properties of the coatings they provide.
- the presence of these semi-crystalline polyesters also increases the rate of hardening of these compositions, which could be a factor which disfavors the satisfactory flowing and degassing of these compositions when they melt, leading to surface defects in the coatings.
- Patent application EP 0 668 895 also describes thermosetting powder compositions containing a polyester bearing carboxyl groups and a beta-hydroxyalkylamide.
- the polyesters of that patent application have a functionality of carboxyl groups of less than 2, obtained by adding monofunctional acids or alcohols during the synthesis of the polyester. By virtue of this reduced functionality, the polyester is less reactive, which makes the powder flow better when it melts and allows the bubbles of air and of water vapor to escape from the coating before it hardens, unlike the compositions in patent applications EP 0 322 834 and WO 91/14745.
- the polyester contains chain ends which do not bear a reactive group, these ends do not participate in the formation of the three-dimensional network during the crosslinking of the powder, thus reducing the resistance to solvents and the flexibility of the coatings thus obtained.
- the EP 1 054 917 claims to solve the above drawbacks of using a beta-hydroxyalkylamide as crosslinker by incorporation of tertiary carboxyl groups as reactive groups in the polyester resins.
- the said compositions provide coatings with excellent surface appearance, good flexibility and good resistance to poor weather conditions due to the lower reactivity and which induces a longer cure schedule.
- thermosetting powder composition which by itself combines all the qualities which it would be desired to find therein, such as good stability in storage, good flowing when melting in order to give it a smooth, and glossy appearance which has no orange-peel skin or bubbles, good flexibility, at the same time as good resistance to solvents, to aggressive weather exposure and all of this at a low temperature curing.
- the present invention seeks to provide powder coating compositions exhibiting low temperature curing but which fulfill the quality requirement of coating such as flow, flexibility and HSE legislations.
- polyester resin composition comprises:
- a polymeric composition suitable for use as a vehicle for a powder coating composition which comprises: a composition in that the acid/alcohol mole ratio is higher than 1 and with an acid value of higher than 15 mg KOH/g.
- a polymeric composition suitable for use as a vehicle for a powder coating composition which comprises: a composition of in that the acid/alcohol mole ratio is lower that 1 and with a hydroxyl value of higher than 25 mg KOH/g.
- polyester resin comprises:
- polyester resin comprises
- composition with the aromatic diacid, cycloalkyl diacid or anhydride selected from the group consisting of isophthalic acid (IPA), terephthalic acid (TPA), phthalic anhydride (PA), trimellitic anhydride (TMA), furandicarboxylic acid (FDCA), cyclohexandicarboxilic acid (CHDA), hexahydrophtalic anhydride (HHPA).
- IPA isophthalic acid
- TPA terephthalic acid
- PA phthalic anhydride
- TMA trimellitic anhydride
- FDCA furandicarboxylic acid
- CHDA cyclohexandicarboxilic acid
- HHPA hexahydrophtalic anhydride
- the melt viscosity (ICI) at 200° C. of the polyester resin is from 1500 to 12000 mPa ⁇ s and a Tg of above 35° C. but lower than 70° C.
- the powder formulation based on the above acid functional polyester resin is then combined with a curative selected from a non-isocyanurate polyepoxide or beta-hydroxyalkylamide or triglycidyl-isocyanurate or epoxy resins (glycidyl ethers of Bisphenol A & F or epoxy novolac resins, glycidyl esters and mixtures thereof) in a weight percent (on total polyester resin and curative) of 2.5 to 50.
- a curative selected from a non-isocyanurate polyepoxide or beta-hydroxyalkylamide or triglycidyl-isocyanurate or epoxy resins (glycidyl ethers of Bisphenol A & F or epoxy novolac resins, glycidyl esters and mixtures thereof) in a weight percent (on total polyester resin and curative) of 2.5 to 50.
- the curative is selected from trimer of isophorone diisocyanate, trimer of hexamethylene diisocyanate, caprolactam-blocked polyisocyanate or self blocked uretdiones in a weight percent (on total polyester resin and curative) of 8 to 65.
- the polymeric vehicle of the invention is formulated to provide a coating binder with desirable hardness, flexibility, solvent resistance, corrosion resistance, weatherability and gloss.
- the enhancement of these properties depends on the optimization and balancing of factors including monomer composition, T g of the resin, type and amount of crosslinking agent, curing conditions, curing catalysts, and type and amount of pigments, fillers and additives.
- the reactivity is increased without sacrificing chemical storage stability or causing poor flow of the film.
- compositions of this invention exhibit remarkable storage stability, smooth surface appearance, high gloss, and excellent mechanical properties which are maintained over time. It will be appreciated by skilled people in the powder coating industry, that an excellent balance among stability and the flow of the cured film and weather-ability and mechanical properties imparted by the use of compositions in accordance with the invention are important factors of commercial importance.
- the powder coating compositions of the invention are cured at a temperature lower than 180° C. and higher than 100° C. and preferably between 160° C. and 140° C.
- coating binder is the polymeric portion of a coating film after baking and after crosslinking.
- Polymeric vehicle means all polymeric and resinous components including crosslinking agents in the formulated coating; i.e. before film formation. Pigments and additives may be mixed with the polymeric vehicle to provide a formulated powder coating composition.
- “Diol” is a compound with two hydroxyl groups. “Polyol” is a compound with two or more hydroxyl groups.
- Diacid is a compound with two carboxyl groups.
- Polyacid is a compound with two or more carboxyl groups.
- polymer means a polymer with repeating monomeric units as defined herein.
- a “film” is formed by application of the formulated coating composition to a base or substrate, and crosslinked.
- Acid number or acid value means the number of milligrams of potassium hydroxide required for neutralization of free acids present in 1 g of resin.
- Hydroxyl number of value that is also called acetyl value is a number that indicates the extent to which a substance may be acetylated; it is the number of milligrams of potassium hydroxide required for neutralization of the acetic acid liberated on saponifying 1 g of acetylated sample.
- polyesters useful in the practice of the invention are thermosettable carboxyl terminated polymers, suitable for formulation of thermosetting powder coatings with epoxide bearing compounds or beta-hydroxyalkylamide. This implies that the polyesters have a sufficiently high glass transition temperature to resist sintering when in powder form and subjected to normally encountered field conditions.
- the polyester of the present invention has a glass transition temperature T g greater than or equal to 44° C., when determined by differential scanning calorimetry employing a heat-up rate of 10° C. per minute in a nitrogen atmosphere; the value is taken at the second run.
- the number average molecular weight of the carboxylated polyester and the hydroxyl value of the hydroxyl terminated polyester vary, the number of equivalents of diacid necessary to react with the hydroxyl terminated polyester also will vary.
- the resulting carboxyl terminated polyester has an acid value in the range of from 14 to 60, and a number average molecular weight in the range of from 2000 to 15000.
- the polyester and the curing compound and various auxiliary substances conventionally used for the manufacture of powder paints and varnishes are mixed homogeneously.
- This homogenization is carried out for example by melting the polyester, the polyepoxide compound and the various auxiliary substances at a temperature within the range of from 90 to 100° C., preferably in an extruder, for example a Buss-Ko-Kneader extruder or a twin-screw extruder of the Werner-Pfleiderer or Baker Perkins type.
- the extrudate is then allowed to cool, and is ground and sieved to obtain a powder, having a particle size of 10 to 120 micrometers.
- the auxiliary substances which can be added to the thermosetting compositions according to the invention include ultraviolet light absorbing compounds such as Tinuvin 928 (from CIBA—Specialties Chemicals), light stabilizers based on sterically hindered amines (for example Tinuvin 144 from CIBA—Specialties Chemicals), phenolic antioxidants (for example Irganox 1010 from CIBA—Specialties Chemicals) and stabilizers of the phosphonite or phosphite type (for example Irgafos 168 or P-EPQ from CIBA—Specialties Chemicals) (Tinuvin, Irganox, Irgafos are Trademarks).
- ultraviolet light absorbing compounds such as Tinuvin 928 (from CIBA—Specialties Chemicals), light stabilizers based on sterically hindered amines (for example Tinuvin 144 from CIBA—Specialties Chemicals), phenolic antioxidants (for example Irganox 10
- pigments may also be added to the thermosetting compositions according to the invention.
- pigments that may be employed in the invention are metal oxides such as titanium dioxide, iron oxide, zinc oxide and the like, metal hydroxides, metal powders, sulfides, sulfates, carbonates, silicates such as aluminum silicate, carbon black, talc, china clays, barytes, iron blues, lead blues, organic reds, organic maroons and the like.
- Auxiliary substances may also include flow control agents such as Fluidep F 630 (from COMIEL) Resiflow PV88 (from WORLEE), Modaflow (from Cytec), Acronal 4F (from BASF) (Fluidep, Resiflow, Modaflow, Acronal are trademarks) plasticizers such as dicyclohexyl phthalate, triphenyl phosphate, grinding aids, degassing agents such as benzoin and fillers.
- flow control agents such as Fluidep F 630 (from COMIEL) Resiflow PV88 (from WORLEE), Modaflow (from Cytec), Acronal 4F (from BASF) (Fluidep, Resiflow, Modaflow, Acronal are trademarks) plasticizers such as dicyclohexyl phthalate, triphenyl phosphate, grinding aids, degassing agents such as benzoin and fillers.
- plasticizers such as dicyclohexyl phthalate, triphenyl
- the ground powder paint composition may be applied to the substrate by any of the known means of application. After coating, the deposited layer is cured by heating in an oven. While typically curing is effected at a temperature of 180° C. in order to obtain sufficient crosslinking to provide the required coating properties, the compositions of the invention may be cured at lower temperature, for example by maintaining a temperature 160° C. or even 140° C. The decrease of curing temperature is economically and technically advantageous since it permits to save energy costs and it offers the possibility to work with substrate that are less thermal resistant than steel.
- Another advantage of the invention is that the coatings prepared from the compositions containing the polyesters according to the invention have a combination of outstanding properties. Improving the appearance of coatings applied as powders to be equivalent to the quality liquid coating finishes is an important consideration, and the present invention provides coatings with excellent appearance. While conventional coatings can be applied as relatively low viscosity liquids to give smooth films after removal of water and/or solvents, applied powder particles must melt, flow, wet the substrate, and coalesce and level to form a continuous film.
- the polymeric vehicle of the present invention is effective for providing a stable melt viscosity and flow.
- T g of a coating powder resin must be above 45° C. in order to possess acceptable non sintering characteristics. If the T g of the coating is high enough, sintering can be avoided. However, coalescing and leveling at the lowest possible temperature are promoted by reducing T g . If the stability of the formulated composition is to be maintained in storage without partial curing, then the T g must be maintained at a sufficient level, i.e. greater than 44° C. The present invention optimizes T g in combination with other factors to provide good coalescence and leveling of the coating prior to cure, whilst not sacrificing storage stability of the formulated powder coating.
- Example a Composition According to the Invention
- Second stage 27.0 parts of D-Isosorbide are placed in a flask under nitrogen and with stirring with 11.4 parts of neopentilglycol 90%, 7.3 parts of terephthalic acid, 30.9 parts of isophtalic acid, 3.4 parts of adipic acid, 19.9 parts of satured 80/20 dimer/trimer fatty acid and 0.1 part of MBTO as catalyst and heated to 245° C.
- the reaction is continued at 245° C. until the distillation under atmospheric pressure stops then the content of the flask is placed under vacuum (residual pressure 50 mmHg) until the polyester obtained has the following characteristics: Acid number 34.2 mg KOH/g, ICI viscosity at 200° C. 3280 mPa ⁇ s, Tg (DSC; 10° C./min) 53° C., Mw 11348 and Gardner Holdt color as a 50 wt. % solution in N-methyl-2-pyrrolidone is 3.
- the polyesters of examples b, c, d, e, f, g and h are prepared (compositions and properties are given in Tables 1 and 2).
- First stage 36.6 parts of neopentilglycol 90% are placed in a flask under nitrogen and with stirring with 1.9 parts of Trimethylolpropane, 42.6 parts of terephthalic acid, 5.4 parts of isophtalic acid, 0.1 part of MBTO as catalyst and heated to 245° C.
- the reaction is continued at atmospheric pressure until a prepolymer containing hydroxyl groups is thus obtained which has the following characteristics: acid number mg KOH/g, ICI viscosity at 200° C. 605 mPa ⁇ s.
- Second stage 4.8 parts of adipic acid, 8.4 parts of isophthalic and 0.2 parts of trimethylolpropane are added at 220° C. to the prepolymer obtained in the first stage.
- the polyesters of examples L, M, 1, 2, 3, 4 and 5 are prepared (compositions and properties are given in Tables 3 and 4).
- the examples I, L, M are compositions according the prior art and the examples 1 to 5 are compositions according to the invention.
- thermosetting powder compositions in according with the invention have advantageous characteristics compared to those obtained from compositions of the prior art (Comparative examples I, L and M).
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- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
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- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Paints Or Removers (AREA)
- Polyesters Or Polycarbonates (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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EP08075956.6 | 2008-12-19 | ||
EP08075956A EP2199314A1 (fr) | 2008-12-19 | 2008-12-19 | Compositions de revêtement de poudre pour le durcissement à basse température et haut débit |
PCT/EP2009/008928 WO2010069531A1 (fr) | 2008-12-19 | 2009-12-14 | Compositions de revêtement en poudre pour durcissement à basse température et fluidité élevée |
Publications (1)
Publication Number | Publication Date |
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US20110281972A1 true US20110281972A1 (en) | 2011-11-17 |
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Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
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US13/140,338 Abandoned US20110281972A1 (en) | 2008-12-19 | 2009-12-14 | Powder coating compositions for low temperature curing and high flow |
US13/967,001 Active 2031-12-15 US9475956B2 (en) | 2008-12-19 | 2013-08-14 | Powder coating compositions for low temperature curing and high flow |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US13/967,001 Active 2031-12-15 US9475956B2 (en) | 2008-12-19 | 2013-08-14 | Powder coating compositions for low temperature curing and high flow |
Country Status (6)
Country | Link |
---|---|
US (2) | US20110281972A1 (fr) |
EP (2) | EP2199314A1 (fr) |
CN (1) | CN102257030B (fr) |
ES (1) | ES2572161T3 (fr) |
PL (1) | PL2370493T3 (fr) |
WO (1) | WO2010069531A1 (fr) |
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EP2623538A1 (fr) | 2012-02-02 | 2013-08-07 | A Et A Mader | Résine alkyde biosourcée et procédé de fabrication d'une telle résine alkyde |
EP2835390A1 (fr) | 2013-08-05 | 2015-02-11 | A Et A Mader | Résine alkyde biosourcée et procédé de fabrication d'une telle résine alkyde |
CN104927593A (zh) * | 2015-06-02 | 2015-09-23 | 广西柳州高昭贸易有限公司 | 一种汽车轮毂翻新用涂料的调制工艺 |
CN104927594A (zh) * | 2015-06-02 | 2015-09-23 | 广西柳州高昭贸易有限公司 | 一种汽车轮毂翻新用涂料的加工工艺 |
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US20170037182A1 (en) * | 2014-04-25 | 2017-02-09 | Mitsubishi Rayon Co., Ltd. | Polyester resin, method for manufacturing polyester resin, and coating composition containing polyester resin |
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WO2012005645A1 (fr) | 2010-07-07 | 2012-01-12 | Perstorp Ab | Résine alkyde |
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- 2009-12-14 PL PL09775113T patent/PL2370493T3/pl unknown
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- 2009-12-14 WO PCT/EP2009/008928 patent/WO2010069531A1/fr active Application Filing
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- 2009-12-14 EP EP09775113.5A patent/EP2370493B1/fr active Active
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- 2013-08-14 US US13/967,001 patent/US9475956B2/en active Active
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WO2013114052A1 (fr) | 2012-02-02 | 2013-08-08 | A Et A Mader | Résine alkyde biosourcée et procédé de fabrication d'une telle résine alkyde |
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Also Published As
Publication number | Publication date |
---|---|
WO2010069531A1 (fr) | 2010-06-24 |
EP2199314A1 (fr) | 2010-06-23 |
US20130331513A1 (en) | 2013-12-12 |
EP2370493A1 (fr) | 2011-10-05 |
ES2572161T3 (es) | 2016-05-30 |
US9475956B2 (en) | 2016-10-25 |
CN102257030A (zh) | 2011-11-23 |
EP2370493B1 (fr) | 2016-03-23 |
PL2370493T3 (pl) | 2016-08-31 |
CN102257030B (zh) | 2014-04-02 |
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