WO1994010221A1 - Acrylic based powder paint - Google Patents

Acrylic based powder paint Download PDF

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Publication number
WO1994010221A1
WO1994010221A1 PCT/NL1993/000212 NL9300212W WO9410221A1 WO 1994010221 A1 WO1994010221 A1 WO 1994010221A1 NL 9300212 W NL9300212 W NL 9300212W WO 9410221 A1 WO9410221 A1 WO 9410221A1
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WO
WIPO (PCT)
Prior art keywords
agent
isocyanate
crosslinking agent
powder paint
glycol
Prior art date
Application number
PCT/NL1993/000212
Other languages
French (fr)
Inventor
Szu-Ping Lu
Han Xieng Xiao
Kurt Charles Frisch
Franciscus Maria Witte
Antonius Franciscus Maria Josephus VAN DE PLOEG
Original Assignee
Dsm N.V.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dsm N.V. filed Critical Dsm N.V.
Priority to AU54345/94A priority Critical patent/AU5434594A/en
Publication of WO1994010221A1 publication Critical patent/WO1994010221A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/67Unsaturated compounds having active hydrogen
    • C08G18/671Unsaturated compounds having only one group containing active hydrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • C08G18/12Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step using two or more compounds having active hydrogen in the first polymerisation step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/4009Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
    • C08G18/4018Mixtures of compounds of group C08G18/42 with compounds of group C08G18/48
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/4804Two or more polyethers of different physical or chemical nature
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/66Compounds of groups C08G18/42, C08G18/48, or C08G18/52
    • C08G18/6666Compounds of group C08G18/48 or C08G18/52
    • C08G18/667Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
    • C08G18/6674Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/66Compounds of groups C08G18/42, C08G18/48, or C08G18/52
    • C08G18/6666Compounds of group C08G18/48 or C08G18/52
    • C08G18/667Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
    • C08G18/6674Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203
    • C08G18/6677Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203 having at least three hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2150/00Compositions for coatings
    • C08G2150/20Compositions for powder coatings

Definitions

  • the invention relates to a powder paint based on acrylics.
  • Acrylic based powder coatings which are used in practice, are almost exclusively based on epoxy functional acrylic resins cured with long-chain dicarboxylic acids as hardeners.
  • the long aliphatic chain of the crosslinker provides flexibility and impact resistance to the cured film, but still far below the values which are usually obtainable with the other powder coating systems. In most cases the impact resistance of the acrylic powder coatings does not exceed 30 inch- pounds. This is still several times lower compared to the values of polyester and polyurethane based powder coatings.
  • the crosslinker has a melting point higher than 45°C and a molecular weight M n between 100 and 3000, more preferably between 300 and 1500.
  • the mixture of glycols and/or polyglycols contains preferably more than 50% by weight of polytetra- methylene ether glycol as one polyol. More preferably this amount is between 60 and 75% by weight.
  • Suitable other glycols or polyglycols include a great number of diols, triols and polyols, such as for example butanediol, ethanediol, neopentylglycol, 2,2-bis- (l-hydroxy-2-oxyethylphenyl)propane, 1 ⁇ 1-isopropylidene- bis(phenylene-ox )di-2-propanol-2, cyclohexyldimethylol, trimethylolpropane, trimethylolethane, adipate polyols, polycaprolactone glycols and polycarbonate glycols.
  • diols such as for example butanediol, ethanediol, neopentylglycol, 2,2-bis- (l-hydroxy-2-oxyethylphenyl)propane, 1 ⁇ 1-isopropylidene- bis(phenylene-ox
  • the second additional polyglycol is a polyether polyol.
  • a suitable polyether polyol is Voranol 220-530TM (of Dow) .
  • a suitable polytetramethylene ether glycol is
  • Suitable isocyanates include aliphatic (poly)isocyanates such as for example hydrogenated methylene diphenyldiisocyanate (HMDI), isophorone diisocyanate (IPDI), trimer(isocyanate) of isophorone dissocyanate (T1890TM, H ⁇ ls), 1,6-hexamethylene diisocyanate (HDI) and the trimer of 1,6-hexane- diisocyanate (Tolonate HDTTM, Rhone Poulenc), 1,3-bis- (1-isocyanato-l-methylethyl)-benzene (TMXDI; American Cyanamid) or aromatic polyisocyanates, such as for example 2,4 or 2,6-diisocyanatetolueen (TDI) and 4,4 '-di- isocyanatediphenylmethaan.
  • HMDI hydrogenated methylene diphenyldiisocyanate
  • IPDI isophor
  • HMDI is used.
  • the flexible crosslinker can be prepared by first reacting half of the molar equivalents of an isocyanate with the polyglycol mixture and next reacting the remaining isocyanate equivalent with a blocking agent.
  • a blocked isocyanate is an isocyanate which has been reacted with a material which will prevent its reaction at roomtemperature with compounds that conventionally react with isocyanates but will permit that reaction to occur at higher temperature.
  • the blocking agent is a non-volatile agent having a polymerisable double bond and an oxime function.
  • These agents have the general formula (I):
  • R 1 , R 2 , R 3 H or (Ci-Cs.alkyl
  • the amidegroup is steric hindered.
  • the aliphatic group preferably, contains 1-10 carbon atoms.
  • the organic estergroup can be characterized by 0
  • R 6 (C 1 -C 10 )alkyl
  • the agent having a polymerizable double bond and an oxime function is preferably an acrylamide derivative having the formula (II):
  • This suitable blocking agent according to the invention is diacetoneacrylamide oxime (DAAOX).
  • DAAOX diacetoneacrylamide oxime
  • the preparation of DAAOX is disclosed in Macromolecules, Vol. 16, 10, 1983, pages 1561-1563.
  • the use of DAAOX and other blocking agents having a polymerisable double bond and an oxime function is very advantageous, because these blocking agents do not evolve during the cure of a hydroxy-isocyanate powder paint system.
  • the blocking agent can be polymerised during cure of the powder paint, because they consist of a blocking side and a pol merizable double bond.
  • the polymerizable double bond can be polymerized during the cure of the coating by adding a suitable peroxide. Any peroxide having a suitable halflife-time at the curing temperature of the coatings can be used.
  • the peroxide has a halflife-time of less then 10 minutes at the temperature at which the coating is cured.
  • the amount of peroxide can vary between 0.5 and 4 wt.%, preferably between 1 and 2%, based on the weight of the added blocked isocyanate crosslinker.
  • Suitable peroxides include tert.- amyl-peroxybenzoate, tert.-butylperoxybenzoate and tert.- butylperoxy-2-ethylhexyl carbonate.
  • Said non-volatile blocking agents can be obtained from compounds having a ketone or aldehyde group which can be converted into an oxime and having an unsaturated double bond as well.
  • Suitable examples of unsaturated ketones or aldehydegroups include methyl-vinyl-ketone, ethyl-vinyl-ketone, mesityl-oxide, allylacetone, crotonaldehyde, 2-hexanal and citronellal.
  • the blocking agent can be reacted with a (poly)isocyanate in a conventional way.
  • the molar equivalent ratio (poly)isocyanate: blocking agent is substantially 1:1.
  • the main features of the isocyanate-hydroxyl curing reaction are described in the foregoing cited Powder Coatings, Chemistry and Technology at pages 56-58.
  • the use of a non-volatile agent having a polymerizable double bond and an oxime function is not limited to the reaction between a blocked isocyanate and a hydroxyl functional acrylic resin.
  • the hydroxyl functional resin can also be, for example, a polyester or a polyurethane.
  • Suitable volatile blocking agents include for example phenol, cresol, long-aliphatic-chain substituted phenols such as isononylphenol, amides such as ⁇ -caprolactam, active methylene group containing compounds like malonates such as isopropylidene malonate and acetoacetic esters, sodium bisulfite and oximes such as for example methylethylketone oxime and butanone oxime.
  • Suitable hydroxyl-functional acrylate resin include for example resins based on hydroxyethyl
  • the resin may also be b"ased on methacrylic acid and alkyl esters of (meth)acrylic acid such as methyl acrylate, ethyl (meth)acrylate, isopropyl (meth)acrylate, n-butyl (meth)acrylate, n-propyl (meth)acrylate, isobutyl (meth)acrylate, ethylhexyl acrylate and/or cyclohexyl (meth)acrylate and vinyl compounds such as styrene.
  • the hydroxylacrylate resins have a hydroxyl number between 40 and 150 mg KOH/g resin and an acid number lower than 20 mg KOH/g resin.
  • the acrylate resins can be prepared by a (co)polymerization, where solvent is fed to a reactor and then heated until the solvent boils. Monomers, and subsequently monomers, initiator and, optionally, mercaptan are added during a period of, for instance, between 2 and 4 hours, after which the temperature is kept at the reflux temperature for, for instance, two hours. The solvent is distilled off by increasing the temperature followed by a vacuum distillation lasting, for instance, one to two hours. Then the product is drained and cooled. Suitable solvents include for example toluene, xylene and butylacetate.
  • Suitable initiators include azo-bis- isobutyronitrile, dibenzoylperoxide and tert.-amyl- peroxy-2-ethyl-hexanoate.
  • the weight ratio polymer:crosslinker is generally between 90:10 and 50:50.
  • the molar equivalent ratio of polymer:crosslinker is between 1:0,8 and 1:1,5. Very suitable ratios are between 1:1 and 1:1,2.
  • customary additives include pigments, fillers, flow aids, stabilizers and catalysts.
  • Suitable pigments include inorganic pigments, for instance titanium oxide, zinc sulphide, iron oxide and chromium oxide, and organic pigments, for instance azo compounds.
  • Suitable fillers include metal oxides, silicates, carbonates and sulphates. The technology and production of powder coatings is described at pages 224-226 of Powder Coatings, Chemistry and Technology, by Tosko Misev (1991; John Wiley and Sons) .
  • Powder coatings according to the present invention can be applied in general industrial and domestic appliances, metal furnitures, architectural applications, automotive topfinishes, corrosion protective coatings and finishes for wood, plastics and paper.
  • US-A-5097010 relates to the preparation of thermally-reversible isocyanate polymer by reacting a labile hydrogen segment with an isocyanate segment.
  • the obtained compositions are useful as hot-melt adhesives, coatings and mouldings and furthermore in injection reaction moulding applications and composite and laminate manufacturing followed by thermal forming and pulltrusion.
  • poly- tetramethylene ether glycol incorporated in a poly- urethane resin results in a flexible network. Applying polytetramethylene ether glycol as the glycol alone will not result in a superior powder coating resin.
  • the mixture of polytetramethylene ether glycol with at least one other glycol or polyglycol produces the desired properties. One glycol is responsible for the flexibility, the other glycol is responsible for the level of the glass transition temperature.
  • the coatings of the present invention are further illustrated by the following experiments and examples. The examples are included for illustrative purposes and should not be considered to limit the present invention.
  • the monomer mixture was fed to the reactor in 2.5 hours.
  • the reflux temperature was maintained in the reactor for another 2.5 hours.
  • a separator vessel was included in the setup, and the solvent was removed by a gradual increase of the temperature and application of a vacuum.
  • a clear product was obtained with a glass transition temperature (Tg, Mettler TA-3000, system 5°C/min) of 46°C and a viscosity ( ) (measured with Emila rheo eter, 165°C) of 350 dPa.s.
  • the glycol blend was made by mixing two glycols in a ratio as mentioned in Table I.
  • a reactor equipped with a stirrer and under a stream of dry nitrogen the respective glycol blend and the appropriate amount of HMDI (see Table I) were charged.
  • Methylethylketone (MEK) was added to reduce the viscosity.
  • a small amount of dibutyl- tindilaurate was added (see Table I) as a catalyst, the reaction mixture was heated to 70°C. It was kept at that temperature until the NCO percentage (as determined by titration) was reduced to half of the initial value.
  • DAAOX was dissolved in MEK and then added into the reaction mixture. The reaction temperature was kept at 70°C until the NCO peak (2270 cm -1 ) disappeared by checking the infrared spectrum of the product.
  • the powder coating ingredients were weighted (in grammes) in the formulations as showed in Table II.
  • the formulations were dissolved is aceton to prepare a solution of 25-30% solids content.
  • the solutions were added into cold water dropwise under vigorous agitation.
  • the precipitates in powder form were then filtered and dried.
  • the dried powders were ground into a very fine particle size. They were sprayed electrostatically on plates and cured as showed in Table II.
  • the examples show that the isocyanate crosslinker according to the invention results in very flexible acrylic powder coatings with good properties.
  • the claimed invention results in a remarkable increase in impact resistance.
  • DAAOX 10 > 193,2 193,2 14 , 75 14 , 75 14 , 75 14,75 14,75 15 DBTL 1X) 0,0123
  • HMDI 1 Hydrogenated Methylene Diphenyl Diisocyanate
  • Voranol 2 Voranol 220-530 (Dow Chemical); polyether polyol
  • Terat 2000 9 Terathane 2000 (Du Pont): polytetramethylene ether glycol with molecular weight 2000
  • Resin Exp. I 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100

Abstract

The invention relates to a powder paint based on acrylics. The thermosetting powder paint comprises a hydroxyl functional acrylic resin and an isocyanate crosslinking agent blocked with a blocking agent wherein the isocyanate crosslinking agent is an adduct of an isocyanate and a mixture of polyetramethylene ether glycol and at least one additional, but other glycol, selected from the group consisting of glycols and polyglycols.

Description

ACRYLIC BASED POWDER PAINT
The invention relates to a powder paint based on acrylics.
The mechanical properties of acrylic based powder coatings are worse (pages 162-167 of "Powder Coatings, Chemistry and Technology" by Tos o Misev; John Wiley and Sons, 1991). Acrylic based powder coatings, which are used in practice, are almost exclusively based on epoxy functional acrylic resins cured with long-chain dicarboxylic acids as hardeners. The long aliphatic chain of the crosslinker provides flexibility and impact resistance to the cured film, but still far below the values which are usually obtainable with the other powder coating systems. In most cases the impact resistance of the acrylic powder coatings does not exceed 30 inch- pounds. This is still several times lower compared to the values of polyester and polyurethane based powder coatings.
It is the object of the invention to provide an acrylic powder coating system which shows excellent hardness, gloss, impact resistance, durability, clearness, chemical resistance and good flexibility.
The invention is characterized in that the thermosetting powder paint comprises
- a hydroxyl functional acrylic resin and
- an isocyanate crosslinking agent blocked with a blocking agent, wherein the isocyanate crosslinking agent is an adduct of an isocyanate and a mixture of polytetra- methylene ether glycol and at least one additional, but other glycol, selected from the group consisting of glycols and polyglycols. Preferably the crosslinker has a melting point higher than 45°C and a molecular weight Mn between 100 and 3000, more preferably between 300 and 1500.
The mixture of glycols and/or polyglycols contains preferably more than 50% by weight of polytetra- methylene ether glycol as one polyol. More preferably this amount is between 60 and 75% by weight.
Suitable other glycols or polyglycols include a great number of diols, triols and polyols, such as for example butanediol, ethanediol, neopentylglycol, 2,2-bis- (l-hydroxy-2-oxyethylphenyl)propane, 1^1-isopropylidene- bis(phenylene-ox )di-2-propanol-2, cyclohexyldimethylol, trimethylolpropane, trimethylolethane, adipate polyols, polycaprolactone glycols and polycarbonate glycols.
According to a preferred embodiment of the invention the second additional polyglycol is a polyether polyol. A suitable polyether polyol is Voranol 220-530™ (of Dow) . A suitable polytetramethylene ether glycol is
Terathane 1000™ (of Du Pont).
Suitable isocyanates include aliphatic (poly)isocyanates such as for example hydrogenated methylene diphenyldiisocyanate (HMDI), isophorone diisocyanate (IPDI), trimer(isocyanate) of isophorone dissocyanate (T1890™, Hϋls), 1,6-hexamethylene diisocyanate (HDI) and the trimer of 1,6-hexane- diisocyanate (Tolonate HDT™, Rhone Poulenc), 1,3-bis- (1-isocyanato-l-methylethyl)-benzene (TMXDI; American Cyanamid) or aromatic polyisocyanates, such as for example 2,4 or 2,6-diisocyanatetolueen (TDI) and 4,4 '-di- isocyanatediphenylmethaan.
Preferably HMDI is used.
The flexible crosslinker can be prepared by first reacting half of the molar equivalents of an isocyanate with the polyglycol mixture and next reacting the remaining isocyanate equivalent with a blocking agent.
A blocked isocyanate is an isocyanate which has been reacted with a material which will prevent its reaction at roomtemperature with compounds that conventionally react with isocyanates but will permit that reaction to occur at higher temperature.
Blocked isocyanates are described by Wicks in Progress in Organic Coatings (3, 1975, 73-99).
According to a preferred embodiment of the invention the blocking agent is a non-volatile agent having a polymerisable double bond and an oxime function. These agents have the general formula (I):
R1 R3
^C=C-R4-C-R5 (I)
R2 N
I OH
where
R1, R2, R3= H or (Ci-Cs.alkyl
R4= aliphatic, amidegroup or organic estergroup and R5= (Ci-Cs.alkyl.
Preferably the amidegroup is steric hindered. The aliphatic group, preferably, contains 1-10 carbon atoms.
The organic estergroup can be characterized by 0
A
-C-O-R6 in which R6=(C1-C10)alkyl.
The agent having a polymerizable double bond and an oxime function is preferably an acrylamide derivative having the formula (II):
Figure imgf000005_0001
This suitable blocking agent according to the invention is diacetoneacrylamide oxime (DAAOX). The preparation of DAAOX is disclosed in Macromolecules, Vol. 16, 10, 1983, pages 1561-1563. The use of DAAOX and other blocking agents having a polymerisable double bond and an oxime function is very advantageous, because these blocking agents do not evolve during the cure of a hydroxy-isocyanate powder paint system. The blocking agent can be polymerised during cure of the powder paint, because they consist of a blocking side and a pol merizable double bond. The polymerizable double bond can be polymerized during the cure of the coating by adding a suitable peroxide. Any peroxide having a suitable halflife-time at the curing temperature of the coatings can be used. Preferably the peroxide has a halflife-time of less then 10 minutes at the temperature at which the coating is cured. The amount of peroxide can vary between 0.5 and 4 wt.%, preferably between 1 and 2%, based on the weight of the added blocked isocyanate crosslinker. Suitable peroxides include tert.- amyl-peroxybenzoate, tert.-butylperoxybenzoate and tert.- butylperoxy-2-ethylhexyl carbonate. Said non-volatile blocking agents can be obtained from compounds having a ketone or aldehyde group which can be converted into an oxime and having an unsaturated double bond as well. Suitable examples of unsaturated ketones or aldehydegroups include methyl-vinyl-ketone, ethyl-vinyl-ketone, mesityl-oxide, allylacetone, crotonaldehyde, 2-hexanal and citronellal. The blocking agent can be reacted with a (poly)isocyanate in a conventional way. Preferably the molar equivalent ratio (poly)isocyanate: blocking agent is substantially 1:1.
The main features of the isocyanate-hydroxyl curing reaction are described in the foregoing cited Powder Coatings, Chemistry and Technology at pages 56-58. The use of a non-volatile agent having a polymerizable double bond and an oxime function is not limited to the reaction between a blocked isocyanate and a hydroxyl functional acrylic resin. The hydroxyl functional resin can also be, for example, a polyester or a polyurethane. Suitable volatile blocking agents include for example phenol, cresol, long-aliphatic-chain substituted phenols such as isononylphenol, amides such as ε-caprolactam, active methylene group containing compounds like malonates such as isopropylidene malonate and acetoacetic esters, sodium bisulfite and oximes such as for example methylethylketone oxime and butanone oxime. Suitable hydroxyl-functional acrylate resin include for example resins based on hydroxyethyl
(meth)acrylate, hydroxypropyl (meth)acrylate and methyl (meth)acrylate. The resin may also be b"ased on methacrylic acid and alkyl esters of (meth)acrylic acid such as methyl acrylate, ethyl (meth)acrylate, isopropyl (meth)acrylate, n-butyl (meth)acrylate, n-propyl (meth)acrylate, isobutyl (meth)acrylate, ethylhexyl acrylate and/or cyclohexyl (meth)acrylate and vinyl compounds such as styrene.
Preferably, the hydroxylacrylate resins have a hydroxyl number between 40 and 150 mg KOH/g resin and an acid number lower than 20 mg KOH/g resin.
The acrylate resins can be prepared by a (co)polymerization, where solvent is fed to a reactor and then heated until the solvent boils. Monomers, and subsequently monomers, initiator and, optionally, mercaptan are added during a period of, for instance, between 2 and 4 hours, after which the temperature is kept at the reflux temperature for, for instance, two hours. The solvent is distilled off by increasing the temperature followed by a vacuum distillation lasting, for instance, one to two hours. Then the product is drained and cooled. Suitable solvents include for example toluene, xylene and butylacetate. Suitable initiators include azo-bis- isobutyronitrile, dibenzoylperoxide and tert.-amyl- peroxy-2-ethyl-hexanoate. The weight ratio polymer:crosslinker is generally between 90:10 and 50:50.
Preferably the molar equivalent ratio of polymer:crosslinker is between 1:0,8 and 1:1,5. Very suitable ratios are between 1:1 and 1:1,2. Obviously, all customary additives may be included in the composition. Examples of customary additives include pigments, fillers, flow aids, stabilizers and catalysts. Suitable pigments include inorganic pigments, for instance titanium oxide, zinc sulphide, iron oxide and chromium oxide, and organic pigments, for instance azo compounds. Suitable fillers include metal oxides, silicates, carbonates and sulphates. The technology and production of powder coatings is described at pages 224-226 of Powder Coatings, Chemistry and Technology, by Tosko Misev (1991; John Wiley and Sons) .
Powder coatings according to the present invention can be applied in general industrial and domestic appliances, metal furnitures, architectural applications, automotive topfinishes, corrosion protective coatings and finishes for wood, plastics and paper. US-A-5097010 relates to the preparation of thermally-reversible isocyanate polymer by reacting a labile hydrogen segment with an isocyanate segment. The obtained compositions are useful as hot-melt adhesives, coatings and mouldings and furthermore in injection reaction moulding applications and composite and laminate manufacturing followed by thermal forming and pulltrusion. In contrast to the present invention, it is the object of US-A-5097010 to provide a thermally-reversible system. Futhermore in contrast to the present invention, which relates to thermosetting coatings, said US-patent discloses a thermoplastic system with polymer networks which are insoluble strong solids at room temperature but become soluble free flowing melts at high temperature. Of course the polyurethanes are based on diisocyanates and polyols and a man skilled in the art also knows that long flexible polyols result in flexible polymers. The present invention, however, relates to a flexible network and does not relate only to a flexible resin. It is for a man skilled in the art not obvious that a flexible part in a resin will also result in a flexible network. It is the essential feature of the present invention that the poly- tetramethylene ether glycol incorporated in a poly- urethane resin (together with other diols and diiso- cyanates) in combination with an acrylate resin results in a flexible network. Applying polytetramethylene ether glycol as the glycol alone will not result in a superior powder coating resin. The mixture of polytetramethylene ether glycol with at least one other glycol or polyglycol produces the desired properties. One glycol is responsible for the flexibility, the other glycol is responsible for the level of the glass transition temperature.
The coatings of the present invention are further illustrated by the following experiments and examples. The examples are included for illustrative purposes and should not be considered to limit the present invention.
Experiment I Synthesis of an hydroxyl functional acrylic resin A 2 L reactor vessel, equipped with a thermometer, a stirrer and a reflux cooler, was charged with 500 g toluene. The reactor was stirred, a nitrogen flow passed through the reactor and the temperature was increased to reflux temperature. A monomer mixture consisting of 417 g methyl methacrylate (MMA), 175 g hydroxyethyl methacrylate (HEMA), 200 g cyclohexylmeth- acrylate (CHMA), 200 g n-butylacrylate (BA) and 8 g methacrylic acid (MA) was added. In this monomer mixture 29,4 g 2,2-azo-bis-isobutyronitrile (AIBN) was dissolved. The monomer mixture was fed to the reactor in 2.5 hours. The reflux temperature was maintained in the reactor for another 2.5 hours. Then a separator vessel was included in the setup, and the solvent was removed by a gradual increase of the temperature and application of a vacuum. A clear product was obtained with a glass transition temperature (Tg, Mettler TA-3000, system 5°C/min) of 46°C and a viscosity ( ) (measured with Emila rheo eter, 165°C) of 350 dPa.s.
Experiment II
Synthesis of diacetone acrylamide oxime (DAAOX)
100 g diacetone acrylamide was dissolved in 375 ml of distilled water and 45.75 g hydroxylamine hydro- chloride was added with stirring. A solution of 43.75 g potassium carbonate in 62.5 ml of distilled water was added at room temperature over a period of 20 min. After the addition was completed, most of the oxime product precipitated. The reaction was continued for an additional hour and the precipitate was filtered and washed with 50 ml of ice water twice. The wet crude product was dissolved in ethylacetate (500 ml), the organic layer was separated and crystallized in the refrigerator. The crystallized product was filtered and washed with 100 ml hexane twice. The final product was dried at 40°C in a vacuum oven to yield 77 g of the DAAOX product. The melting point (112°C) of DAAOX was measured by using a DSC.
Experiment III
The blocking of IPDI with DAAOX (BIPDI)
40.48 g (10% excess) DAAOX obtained according to Experiment I was dissolved in 50 g methylethyl ketone and 22.2 g IPDI was added. The reaction was carried out at room temperature under dry nitrogen. The NCO content was less then 0.1% (by titration) after one hour reaction. The solvent was removed by destination at 40°C in a vacuum oven overnight. The final blocked IPDI (BIPDI) can be pulverized into fine powder with a melting point of 55- 60°C. The blocked NCO content of BIPDI is 13.5% by calculation.
Experiment IV The blocking of H1?MDI with DAAOX (BHMDI)
147.5 g DAAOX (5% excess) obtained according to Experiment I was dissolved in methylethyl ketone (330 g) and 100 g H12MDI was then added. The reaction was carried out at 50°C under dry nitrogen. The NCO content was less then 0.1% (by titration) after one hour of reaction. The solvent was removed at 40°C in a vacuum oven. The final blocked product BHMDI was pulverized to a fine powder and had a melting point (by DSC) of appr. 54°C. In order to examine the polymerization of BHMDI, the intiator (tert.-amylperbenzoate) was added into BHMDI to initiate polymerization. An exothermic peak was found in the analysis of DSC.
Examples I-VII
Preparation of modified crosslinkers
The glycol blend was made by mixing two glycols in a ratio as mentioned in Table I. In a reactor, equipped with a stirrer and under a stream of dry nitrogen the respective glycol blend and the appropriate amount of HMDI (see Table I) were charged. Methylethylketone (MEK) was added to reduce the viscosity. A small amount of dibutyl- tindilaurate was added (see Table I) as a catalyst, the reaction mixture was heated to 70°C. It was kept at that temperature until the NCO percentage (as determined by titration) was reduced to half of the initial value. DAAOX was dissolved in MEK and then added into the reaction mixture. The reaction temperature was kept at 70°C until the NCO peak (2270 cm-1) disappeared by checking the infrared spectrum of the product.
After the products in MEK were further diluted with acetone to 25-30% solids content. The dilute solutions were then added dropwise into cold water under vigorous agitation (> 1500 RPM). The precipitates in the powdered form were then filtered and dried. Glass transition temperature and equivalent weights of NCO are given in Table I.
Examples VIII-XIV
Preparation of a powder coating
The powder coating ingredients were weighted (in grammes) in the formulations as showed in Table II. The formulations were dissolved is aceton to prepare a solution of 25-30% solids content. The solutions were added into cold water dropwise under vigorous agitation. The precipitates in powder form were then filtered and dried. The dried powders were ground into a very fine particle size. They were sprayed electrostatically on plates and cured as showed in Table II.
The present tests are described at pages 296-303 of Powder Coatings by Misev.
Comparative Example A
0.942 g of BHMDI according to Experiment IV was mixed with 2.058 g acrylic resin according to Example I, and the powder mixture was dissolved in 7.5 g of cellosolve acetate. 0.0015 g dibutyltin diacetate was added as a deblocking catalyst. 0.0188 t-amyl-perbenzoate was added as initiator for the polymerization of DAAOX after deblocking reaction. 0.0585 g of E-25™ was added as flow control agent. The solution of this mixture was coated on stell panels, and the panels were baked at 160°C for 30 in. The coatings were well cured, which was proved by the pencil hardness of 2H and more then 200 aceton rubs. However, the impact resistance (ASTM-D-2794) was less than 30 inchpound.
This shows that the coating made with a non- modified crosslinker has poor properties.
The examples show that the isocyanate crosslinker according to the invention results in very flexible acrylic powder coatings with good properties. The claimed invention results in a remarkable increase in impact resistance.
Figure imgf000013_0001
TABLE I ( grammes )
II III IV V VI VII
5 HMDI1 ' 20 20 20 20
Voranol2 '
CHDM3 )
Figure imgf000013_0002
Dianol -224 ) 6,94
Dianol-33S ) 7,28 10 1 , 4-BD6 ) 2,84
NPG7 > 3,20
Terat 10008> 165,0 9,6 16,2 17,0 6,63 7,46
Terat 20009) 148,5
DAAOX10> 193,2 193,2 14 , 75 14 , 75 14 , 75 14,75 14,75 15 DBTL1X) 0,0123
MEK12> 50
Tg ( "C)13) 45
NCO equivalent weight
Figure imgf000013_0003
586
20
HMDI1> Hydrogenated Methylene Diphenyl Diisocyanate
Voranol2) Voranol 220-530 (Dow Chemical); polyether polyol
CHDM3) Cyclohexyldimethanol
Dianol-224) 2,2-bis(l-hydroxy-2-oxy-ethylphenyl)propane
25 Dianol-335) 1,1-isopropylidene-bis(p-phenyleneoxy)-di-2- propanol-2
1,4-BD6> 1,4-butanediol
NPG7) Neopentylglycol
Terat 1000β) Terathane 1000 (Du Pont): polytetramethylene
30 ether glycol with molecular weight 1000
Terat 20009) Terathane 2000 (Du Pont): polytetramethylene ether glycol with molecular weight 2000
DAAOX10> See Experiment II
DBTL11' Dibutyltindilaurate
35 MEK12)' Methylethylketone
Tg (*C)13) Glass transition point; n.m.= not measured
TABLE II
VIII IX X XI XII XIII XIV
Resin Exp. I 100 100 100 100 100 100 100
Crosslinker I 105,3
Crosslinker II 105,8
Crosslinker III 96,85
10 Crosslinker IV 111,0
Crosslinker V 113,1
Crosslinker VI 80,61
Crosslinker VII TID
15 TAP2'
E25 3)
Cure conditions
20 Hardness4' Aceton res.5' Impact res.6'
- direct
- reverse
Figure imgf000014_0001
25
TID Dibutyltin diacetate
TAp2) Tert. amyl perbenzoate E25 3) Flow control agent (DSM)
30 Hardness4' Pencil hardness (ASTM-D-3363) Aceton res.5' Acetone resistance (solvent cure test method) Impact res.6> Impact resistance (ASTM-D-2794)

Claims

1. A powder paint based on acrylics, characterized in that, the thermosetting powder paint comprises - a hydroxyl functional acrylic resin and
- an isocyanate crosslinking agent blocked with a blocking agent, wherein the isocyanate crosslinking agent is an adduct of an isocyanate and a mixture of polytetramethylene ether glycol and at least one additional, but other glycol, selected from the group consisting of glycols and polyglycols.
2. Powder paint according to claim 1, characterized in that the additional polyglycol is a polyether polyol.
3. Powder paint according to any one of claims 1-2, characterized in that the blocking agent is an agent having a polymerisable double bond and an oxime- function.
4. Powder paint according to claim 3, characterized in that the agent is diacetone acrylamide oxime.
5. Use of an adduct of an isocyanate and a mixture of polytetramethylene ether glycol and at least one additional but other glycol selected from the group consisting of glycols and polyglycols as crosslinking agent in the preparation of powder coatings.
6. A method for preparing a powder paint composition comprising a hydroxyl functional acrylic resin and an isocyanate crosslinking agent which is blocked, characterized in that the isocyanate crosslinking agent comprises an adduct of an isocyanate and a mixture of polytetramethylene ether glycol and at least one additional, but other glycol selected from the group consisting of glycols and polyglycols and the weight ratio of polymer:crosslinking agent is between 90:10 and 50:50.
7. Method according to claim 6, characterized in that the blocking agent is an agent having a polymerisable double bond and an oxime-function.
8. Method according to claim 7, characterized in that the agent is diacetone acrylamide oxime.
9. Binder composition comprising a resin and a crosslinking agent characterized in that the resin is a hydroxyl' functional acrylic resin and the crosslinking agent an isocyanate crosslinking agent blocked with a blocking agent, wherein the isocyanate crosslinking agent is an adduct of an isocyanate and a mixture of polytetramethylene ether glycol and at least one additional, but other glycol, selected from the group consisting of glycols and polyglycols.
10. Binder composition comprising a hydroxyl group containing polymer and an isocyanate crosslinking agent blocked with a blocking agent, characterized in that the blocking agent is an agent having a polymerizable double bond and an oxime-function.
11. Powder paint composition comprising a hydroxyl group containing polymer and an isocyanate crosslinking agent blocked with a blocking agent, characterized in that the blocking agent is an agent having a polymerizable double bond and an oxime-function.
12. An article coated with a composition according to any one of claims 1-4 or an article coated with a composition obtained according to any one of claims 6-8.
PCT/NL1993/000212 1992-10-27 1993-10-21 Acrylic based powder paint WO1994010221A1 (en)

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EP0987283A1 (en) * 1998-09-18 2000-03-22 Dsm N.V. Block polymer and powder-paint binder composition
EP1178080A2 (en) * 2000-07-19 2002-02-06 Nippon Shokubai Co., Ltd. Curable resin coating composition
EP1559751A2 (en) 2004-01-28 2005-08-03 Xerox Corporation Emulsion aggregation process for forming curable powder coating compositions, curable powder coating compositions and method for using the same
US7112394B2 (en) 2004-03-01 2006-09-26 Xerox Corporation Thermosetting toner compositions, thermosetting developer compositions and methods for making and using the same
US7247415B2 (en) 2004-08-31 2007-07-24 Xerox Corporation Process for preparing toner particles and toner particles
US7501150B2 (en) 2004-01-28 2009-03-10 Xerox Corporation Emulsion aggregation process for forming powder coating compositions, powder coating compositions and method for using the same
US9469768B1 (en) * 2012-05-30 2016-10-18 Pison Stream Solutions Powder coating composition useful as a finish
CN110167985A (en) * 2017-01-12 2019-08-23 巴斯夫欧洲公司 The physical property of polyurethane is improved

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EP0327031A2 (en) * 1988-02-01 1989-08-09 Asahi Kasei Kogyo Kabushiki Kaisha A urethane prepolymer composition and a polyurethane coating composition system

Cited By (12)

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EP0987283A1 (en) * 1998-09-18 2000-03-22 Dsm N.V. Block polymer and powder-paint binder composition
EP1178080A2 (en) * 2000-07-19 2002-02-06 Nippon Shokubai Co., Ltd. Curable resin coating composition
EP1178080A3 (en) * 2000-07-19 2003-07-09 Nippon Shokubai Co., Ltd. Curable resin coating composition
US6713551B2 (en) 2000-07-19 2004-03-30 Nippon Shokubai Co., Ltd. Resin composition for coating and coating composition for curing
KR100563420B1 (en) * 2000-07-19 2006-03-22 가부시키가이샤 닛폰 쇼쿠바이 Resin composition for coating and coating composition for curing
EP1559751A2 (en) 2004-01-28 2005-08-03 Xerox Corporation Emulsion aggregation process for forming curable powder coating compositions, curable powder coating compositions and method for using the same
US7501150B2 (en) 2004-01-28 2009-03-10 Xerox Corporation Emulsion aggregation process for forming powder coating compositions, powder coating compositions and method for using the same
US7985524B2 (en) 2004-01-28 2011-07-26 Xerox Corporation Emulsion aggregation process for forming curable powder coating compositions, curable powder coating compositions and method for using the same
US7112394B2 (en) 2004-03-01 2006-09-26 Xerox Corporation Thermosetting toner compositions, thermosetting developer compositions and methods for making and using the same
US7247415B2 (en) 2004-08-31 2007-07-24 Xerox Corporation Process for preparing toner particles and toner particles
US9469768B1 (en) * 2012-05-30 2016-10-18 Pison Stream Solutions Powder coating composition useful as a finish
CN110167985A (en) * 2017-01-12 2019-08-23 巴斯夫欧洲公司 The physical property of polyurethane is improved

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