WO2011157673A1 - Accelerator solution and process for curing curable resins - Google Patents
Accelerator solution and process for curing curable resins Download PDFInfo
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- WO2011157673A1 WO2011157673A1 PCT/EP2011/059769 EP2011059769W WO2011157673A1 WO 2011157673 A1 WO2011157673 A1 WO 2011157673A1 EP 2011059769 W EP2011059769 W EP 2011059769W WO 2011157673 A1 WO2011157673 A1 WO 2011157673A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/56—Organo-metallic compounds, i.e. organic compounds containing a metal-to-carbon bond
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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
- C08G63/78—Preparation processes
- C08G63/82—Preparation processes characterised by the catalyst used
- C08G63/83—Alkali metals, alkaline earth metals, beryllium, magnesium, copper, silver, gold, zinc, cadmium, mercury, manganese, or compounds thereof
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/10—Metal compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0091—Complexes with metal-heteroatom-bonds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L63/00—Compositions of epoxy resins; Compositions of derivatives of epoxy resins
- C08L63/10—Epoxy resins modified by unsaturated compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/06—Unsaturated polyesters
Definitions
- the present invention relates to a solution suitable for accelerating the cure of a curable resin - such as unsaturated polyester resins, (meth)acrylate resins, and vinyl ester resins - using a peroxide.
- a curable resin - such as unsaturated polyester resins, (meth)acrylate resins, and vinyl ester resins - using a peroxide.
- the invention also relates to the use said solution for curing curable resins.
- the accelerator solution is able to accelerate a free radical cure process, which may optionally be a redox system.
- the accelerator solution is able to increase the activity of the peroxide at lower temperatures and, consequently, to speed up the cure.
- US 4,009,150 discloses iron and copper chelates, the chelates being selected from ⁇ - dicarbonyl compounds having an enol content of at least 4% and a dicarbonyl angle of not greater than 120° and ⁇ -hydroxy nitrogen-heterocyclic fused aromatics in which the hydroxyl group is attached to a carbon beta to the nitrogen in the adjacent ring.
- EP 0 094 160 discloses Cu(dmgH) 2 , Ni(EDTA), Cu(bdm) 2 , Ni(TETA),
- Mn and Fe-containing accelerators are disclosed in WO 2008/003494, WO
- the present invention therefore relates to an accelerator solution comprising:
- the invention further relates to a process for curing a curable resin comprising the step of adding a peroxide and said accelerator solution to a curable resin.
- This process makes use of a non-toxic accelerator that has excellent reactivity. Furthermore, this process results in end products with limited colouring that may be tack-free. In addition, this process has a high peak exotherm and high cure efficiency.
- the accelerator solution according to the present invention comprises a (i) a manganese salt, a copper salt, or a combination thereof, and (ii) an iron complex. In a preferred embodiment, it comprises both a manganese salt and a copper salt.
- Suitable manganese salts are manganese halides, nitrate, sulphate, lactate, 2- ethyl hexanoate, acetate, proprionate, butyrate, oxalate, laurate, oleate, linoleate, palmitate, stearate, acetyl acetonate, octanoate, nonanoate, heptanoate, neodecanoate, and naphthenate.
- the manganese salt is selected from manganese chloride, nitrate, sulphate, lactate, 2-ethyl hexanoate, octanoate, nonanoate, heptanoate, neodecanoate, naphthenate, and acetate. Both Mn(ll) and Mn(lll) salts can be used.
- the manganese salt is preferably present in the accelerator solution in an amount of at least 0.01 wt%, more preferably at least 0.1 wt%, and preferably less than 10 wt%, more preferably less than 5 wt%, and most preferably less than 2 wt%, calculated as manganese salt and based on the total weight of the accelerator solution.
- Suitable copper salts are copper halides, nitrate, sulphate, lactate, 2-ethyl hexanoate, acetate, proprionate, butyrate, oxalate, laurate, oleate, linoleate, palmitate, stearate, acetyl acetonate, octanoate, nonanoate, heptanoate, neodecanoate, and naphthenate.
- the copper salt is selected from copper chloride, nitrate, sulphate, lactate, 2-ethyl hexanoate, octanoate, nonanoate, heptanoate, neodecanoate, naphthenate, and acetate. Both Cu(l) and Cu(ll) salts can be used.
- the copper salt is preferably present in the accelerator solution in an amount of of at least 0.01 wt%, more preferably at least 0.1 wt%, and preferably less than 10 wt%, more preferably less than 5 wt%, and most preferably less than 2 wt%, calculated as copper salt and based on the total weight of the accelerator solution.
- the iron complex preferably comprises a tetradentate or pentadentate nitrogen donor ligand. More preferably, it is an iron complex of a pentadentate nitrogen donor ligand.
- the iron complexed by the ligand is selected from Fe(ll) and Fe(lll).
- the iron complex has one or more of the forms [Fel_CI 2 ]; [Fel_CI]CI; [FeL(H 2 O)](PF 6 ) 2 ; [Fel_]CI 2 , [Fel_CI]PF 6 and [FeL(H 2 O)](BF 4 ) 2 , wherein L refers to the ligand.
- the iron complex is preferably present in the accelerator solution in an amount of at least 0.01 wt%, more preferably at least 0.1 wt%, and preferably less than 10 wt%, more preferably less than 5 wt%, and most preferably less than 2 wt%, calculated as metallic iron (Fe) and based on the total weight of the accelerator solution.
- Suitable ligands are listed below. If in the below structures it is referred to, for instance, Ci-i 2 -alkyl chains, alkyl chains having a length in the range of 1 to 12 carbon atoms, such methyl, ethyl, etc. are meant. These alkyl chains can be branched or linear and may optionally be substituted by heteroatoms like O, S, P, etc. Preferred aryl groups in these structures are (substituted) phenyl groups, unless denoted otherwise.
- the ligand of formula (I), also called a bispidon ligand, has the following structure:
- each R is independently selected from: hydrogen, F, CI, Br, hydroxyl, Ci-4-alkylO, -NH-CO-H, -NH 2 , -NH-d-12-alkyl, and C1-12- alkyl;
- R1 and R2 are independently selected from: Ci-2 4 -alkyl, C-6-io-aryl, and a group containing a heteroatom capable of coordinating to a transition metal;
- R3 and R4 are independently selected from hydrogen, Ci-12 alkyl, Ci-12-alkyl-O- Ci-12-alkyl, Ci-i2-alkyl-0-C6-io-aryl, C-6-io-aryl, Ci-12-hydroxyalkyl, and - (CH 2 )nC(O)OR5, wherein R5 is independently selected from hydrogen and Ci -4 - alkyl and n ranges from 0 to 4, and
- R1 and R2 are selected from a heteroatom capable of coordinating to a transition metal, -CH 3 , -C2H5, -C3H7, -C 4 H 9 , C6H 13, CsHu, C12H25, and Ci8H 3 7- More preferably, at least one of R1 and R2 is a group containing a heteroatom capable of coordinating to a transition metal and wherein said group is pyridin-2-yl, optionally substituted by -Ci-12-alkyl or benzyl.
- At least one of R1 or R2 is pyridin-2-ylmethyl and the other is selected from -CH 3 , -C2H5, -C3H7, -C 4 H 9 , -C6H13, -CsHi/, -C12H25,
- R3 and R4 are equal and are selected from -C(O)-O-CH 3 , -C(O)-O- CH2CH3, -C(O)-O-CH 2 C 6 H 5 and -CH 2 OH.
- a preferred ligand according to formula (I) is dimethyl 2,4-di-(2-pyridyl)-3- methyl-7-(pyridin-2-ylmethyl)-3,7-diaza-bicyclo[3.3.1 ]nonan-9-one-1 ,5- dicarboxylate (denoted N2py3o-C1 ).
- the iron complex thereof is denoted FeN2py3o-C1 and can be prepared as described in WO 02/48301 .
- Suitable ligands according to formula (I) are ligands that differ from N2py3o-C1 by having alkyl chains other than methyl at the 3- position, namely isobutyl (N2py3o-C4), n-hexyl (N2py3o-C6), n-octyl(N2py3o- C8), n-dodecyl(N2py3o-C12), n-tetradecyl(N2py3o-C14), n-octadecyl(N2py3o- C18), and which can be prepared in an analogous manner.
- suitable tetradentate ligands are also disclosed in WOOO/60045 and examples of suitable pentadentate ligands are disclosed in WO 02/48301 and WO03/104379.
- the ligand according to formula (II) has the following structure
- each R1 and R2 independently represents ⁇ R3 represents hydrogen, optionally substituted alkyl, aryl or arylalkyl, or -R 4 -R 5 , each R 4 independently representing a single bond or optionally substituted alkylene, alkenylene, oxyalkylene, aminoalkylene, alkylene ether, carboxylic ester or carboxylic amide, and
- each R 5 independently representing an optionally N- substituted aminoalkyl group or an optionally substituted heteroaryl group selected from pyridinyl, pyrazinyl, pyrazolyl, pyrrolyl, imidazolyl, benzimidazolyl, pyrimidinyl, triazolyl, and thiazolyl.
- R1 in the formula represents pyridin-2-yl
- R2 represents pyridin-2-yl-methyl.
- either of R2 and R1 represents 2-amino-ethyl, 2- (N-(m) ethyl) amino-ethyl, or 2-(N,N-di(m)ethyl)amino-ethyl.
- R5 preferably represents 3-methyl pyridin-2-yl.
- R3 preferably represents hydrogen, benzyl or methyl.
- Preferred ligands according to formula (II) are N,N-bis(pyridin-2-yl-methyl)-bis (pyridin-2-yl) methylamine) which is denoted as N4Py and is disclosed in
- the ligand of formula (III) has the following structure:
- R20 (III) wherein each R20 is selected from alkyl, cycloalkyi, heterocycloalkyi, heteroaryl, aryl, and arylalkyl groups optionally substituted with a substituent selected from hydroxy, alkoxy, phenoxy, carboxylate, carboxamide, carboxylic ester, sulphonate, amine, alkylamine and N + (R 21 ) 3 , wherein R 21 is selected from hydrogen, alkanyl, alkenyl, arylalkanyl, arylalkenyl, oxyalkanyl, oxyalkenyl, aminoalkanyl, aminoalkenyl, alkanyl ether, alkenyl ether, and -CY2-R 22 , in which Y is independently selected from H, CH 3 , C2H 5 , C3H 7 and R 22 is independently selected from optionally substituted pyridinyl, pyrazinyl, pyrazolyl, pyrrolyl, imid
- R 22 is selected from optionally substituted pyridin-2-yl, imidazol-4-yl, pyrazol-1 -yl, and quinolin-2-yl groups. Most preferably, R 22 is either a pyridin-2- yl or a quinolin-2-yl.
- the ligand of formula (IV) has the following structure:
- R is independently selected from hydrogen, Ci-12-alkyl, CH2CH2OH, pyridin-2-ylmethyl, and CH 2 COOH, or one of R is linked to the N of another Q via an ethylene bridge;
- Ri , R2, R3, R4, R5 and R6 are independently selected from H, Ci-12-alkyl, and Ci- 12-alkylhydroxy;
- Preferred ligands according to formula (IV) are 1 ,4,8,1 1 - tetraazacyclotetradecane (cyclam), 1 ,4,8,1 1 -tetramethyl-1 ,4,8,1 1 - tetraazacyclotetradecane (Me4cyclam), 1 ,4,7,10-tetraazacyclododecane (cyclen), 1 ,4,7,10-tetramethyl-1 ,4,7,10-tetraazacyclododecane (Me4cyclen), and 1 ,4,7,10-tetrakis (pyridine-2ylmethyl)-1 ,4,7,10-tetraazacyclododecane (Py4cyclen).
- the ligand of formula (V) has the following structure:
- R 1 is independently selected from H and linear or branched, substituted or unsubstituted Ci-20-alkyl, -alkylaryl, -alkenyl or -alkynyl; and all nitrogen atoms in the macropolycyclic rings are capable of coordinating to transition metals;
- R 1 is methyl, resulting in the ligand 5,12-dimethyl-1 ,5,8,12-tetraaza- bicyclo[6.6.2]hexadecane of which the complex [Mn(Bcyclam)C12] may be synthesised according to WO98/39098.
- Other suitable ligands according to formula (V) are also disclosed in WO98/39098.
- the ligand of formula (VI) having the following structure (R 17 )(R 17 )N-X-N(R 17 )(R 17 ) (VI) wherein X is selected from -CH 2 CH 2 -, -CH2CH2CH2-, and -CH 2 C(OH)HCH 2 -; and each R 17 is independently selected from the group consisting of alkyl, cydoalkyi, heterocydoalkyi, heteroaryl, aryl and arylalkyi groups optionally substituted with a substituent selected from hydroxy, alkoxy, phenoxy, carboxylate, carboxamide, carboxylic ester, sulphonate, amine, alkylamine and N + (R 19 )3 , wherein R 19 is selected from hydrogen, alkanyl, alkenyl, arylalkanyl, arylalkenyl, oxyalkanyl, oxyalkenyl, aminoalkanyl, aminoalkenyl, alkan
- the heteroatom donor group is preferably pyridinyl, optionally substituted by - Ci-12-alkyl.
- heteroatom donor groups are imidazol-2-yl, 1 -methyl-imidazol- 2-yl, 4-methyl-imidazol-2-yl, imidazol-4-yl, 2-methyl-imidazol-4-yl, 1 -methyl- imidazol-4-yl, benzimidazol-2-yl, and l-methyl-benzimidazol-2-yl .
- Suitable ligands according to formula (VI) are ⁇ , ⁇ , ⁇ ', ⁇ '- tetra(pyridin-2-yl-methyl)ethylenediamine), N-methyl-tris(pyridin-2- ylmethyl)ethylene-1 ,2-diamine; N-octyl-tris(pyridin-2-ylmethyl)ethylene-1 ,2- diamine; N-octadecyl-tris(pyridin-2-ylmethyl) ethylene-1 ,2-diamine; N-methyl- ⁇ , ⁇ ', ⁇ '-tris (3-methyl-pyridin-2-ylmethyl)ethylene-1 ,2- diamine; N-ethyl-N,N',N'- tris(3-methyl-pyridin-2-ylmethyl)ethylene-1 ,2-diamine; N-methyl-N,N',N'-tris(5- methyl-pyridin-2-ylmethyl)ethylene-1 ,2-diamine; N-ethyl-N,
- ligands of formula (I) are ligands of formula (I) and the following ligands:
- the accelerator solution according to the present invention comprises one or more organic solvents (also called phlegmatizers).
- Suitable solvents include aliphatic hydrocarbon solvents, aromatic hydrocarbon solvents, and solvents that carry an aldehyde, ketone, ether, ester, alcohol, phosphate, or carboxylic acid group.
- Suitable solvents are aliphatic hydrocarbon solvents such as white spirit and odourless mineral spirit (OMS), aromatic hydrocarbon solvents such naphthenes and mixtures of naphthenes and paraffins, glycols such as ethylene glycol, glycerol, diethylene glycol, dipropylene glycol, and polyethylene glycol; isobutanol; pentanol; 1 ,2-dioximes, N-methyl pyrrol idinone, N-ethyl pyrrolidinone; dimethyl formamide (DMF); dimethylsulfoxide (DMSO); 2,2,4-trimethylpentanediol diisobutyrate (TxlB); phosphorus-containing compounds such as diethyl phosphate, dibutyl phosphate, tributyl phosphate, triethyl phosphate (TEP), dibutyl phosphite, and triethyl phosphite; esters such as dibutyl male
- Preferred solvents are triethyl phosphate, dibutyl phosphate, ethylene glycol, diethylene glycol, polyethylene glycol, N-methyl pyrrolidone, ethyl acetate, and butyl acetate. A mixture of two or more of the aforementioned solvents may also be used.
- the accelerator solution preferably comprises at least 50 wt%, more preferably at least 70 wt%, and preferably less than 95 wt%, more preferably less than 90 wt% of solvent, all based on the total weight of the accelerator solution.
- the accelerator solution according to the present invention may optionally contain one or more promoters, water, reducing agents, additives, and/or fillers. Although not essential, the presence of a promoter is preferred, because it allows the iron complex to be used in only very small amounts, thereby making the process of the present invention and the accelerator solution more economically attractive.
- Suitable amines are tertiary amines such as triethyl amine, dimethylaniline, diethylaniline, or N,N-dimethyl-p-toludine (DMPT), polyamines such as 1 ,2-(dimethyl amine)ethane, secondary amines such as diethyl amine, ethoxylated amines such as triethanol amine, dimethylamino ethanol, diethanol amine (DETA), or monoethanol amine.
- DMPT N,N-dimethyl-p-toludine
- polyamines such as 1 ,2-(dimethyl amine)ethane
- secondary amines such as diethyl amine
- ethoxylated amines such as triethanol amine, dimethylamino ethanol, diethanol amine (DETA), or monoethanol amine.
- suitable metal carboxylate salts are the 2-ethyl hexanoates, octanoates, nonanoates, heptanoates, neodecanoates, and naphthenates of the alkali metals Na, K, Li, Ba, and Cs, and of Ce, Mg, Ca, Zn, Cu, Ni, Mn, Sn, Cr, Au, Ag, Pd, and Pt.
- the promoters may be added to the accelerator solution as such, or they may be formed in situ.
- alkali metal 2-ethyl hexanoates can be prepared in situ in the accelerator solution, after addition of the alkali metal hydroxide and 2-ethyl hexanoic acid to the solution.
- one or more stabiliser(s) is/are present in the accelerator solution, their amount preferably is at least 0.01 wt%, more preferably at least 0.1 wt%, and preferably not more than 20 wt%, more preferably not more than 10 wt%, all based on the total weight of the accelerator solution.
- reducing agents are ascorbic acid, sodium formaldehyde sulphoxylate (SFS), reducing sugars like glucose and fructose, oxalic acid, phosphines, phosphites, organic or inorganic nitrites, organic or inorganic sulphites, organic or inorganic sulphides, mercaptanes, amines, and aldehydes, and mixtures thereof.
- Ascorbic acid which term in this specification includes L- ascorbic acid and D-isoascorbic acid, is the preferred reducing agent.
- a reducing agent is present in the accelerator solution, it is preferably present in an amount of more than 0.1 wt%, preferably at least 1 wt%, and most preferably at least 5%. It is preferably present in an amount of less than 30 wt%, more preferably less than 20 wt%, all based on the total weight of the accelerator solution.
- the accelerator solution may optionally comprise water. If present, the water content of the solution preferably is at least 0.01 wt% and more preferably at least 0.1 wt%. The water content is preferably not more than 50 wt%, more preferably not more than 40 wt%, more preferably not more than 20 wt%, even more preferably not more than 10 wt%, and most preferably not more than 5 wt%, all based on the total weight of the accelerator solution.
- the accelerator solution can be prepared by simply mixing the ingredients, optionally with intermediate heating and/or mixing steps. There is no specific order of addition which has to be applied.
- the invention also relates to the use of accelerator solution according to the present invention for curing curable resins using a peroxide.
- suitable curable resins are (meth)acrylate resins, unsaturated polyester (UP) resins, and vinyl resins.
- UP unsaturated polyester
- vinyl resins vinyl resins.
- the curing is generally started by adding the accelerator solution and the peroxide to said mixture. When both the peroxide and the accelerator solution have been added to the curable resin, the resulting mixture is mixed and dispersed.
- the curing process can be carried out at any temperature from -15°C up to 250°C, depending on the initiator system, the accelerator system, the compounds to adapt the curing rate, and the resin composition to be cured.
- the process can be carried out at temperatures up to 180°C, more preferably up to 150°C, most preferably up to 100°C. Preferably, it is carried out at ambient temperatures.
- the curing process is commonly applied in applications such as hand lay-up, spray-up, filament winding, resin transfer moulding, resin infusion, resin injection, coatings (e.g. gel-coat and standard coatings), button production, centrifugal casting, corrugated sheets or flat panels, relining systems, kitchen sinks via pouring compounds, SMC, BMC, pultrusion techniques, and the like.
- the accelerator solution can be added to the resin or a pre-mix of resin and monomer. It may also be pre-mixed with the optional monomer prior to its addition to the resin.
- the peroxide can be added directly to the mixture of resin, accelerator solution, and optional monomer. However, the peroxide may also be first mixed with the monomer or resin before the accelerator solution is added. Care is to be taken that the peroxide and the accelerator solution are not pre- mixed, since this would be hazardous.
- Various types of resins can be cured in this way. These resins include alkyd resins, unsaturated polyester (UP) resins, vinyl ester resins, (meth)acrylate resins, polyurethanes, and epoxy resins. Preferred resins are (meth)acrylate resins, UP resins and vinyl ester resins.
- Suitable UP resins to be cured by the process of the present invention are so- called ortho-resins, iso-resins, iso-npg resins, and dicyclopentadiene (DCPD) resins.
- Examples of such resins are maleic, fumaric, allylic, vinylic, and epoxy- type resins, bisphenol A resins, terephthalic resins, and hybrid resins.
- Vinyl ester resins include acrylate resins, based on, e.g. methacrylate, diacrylate, dimethacrylate, and oligomers thereof.
- the curable resin may be combined with one or more ethylenically unsaturated reactive monomers.
- Preferred ethylenically unsaturated reactive monomers include styrene and styrene derivatives such as a-methyl styrene, vinyl toluene, indene, divinyl benzene, vinyl pyrrolidone, vinyl siloxane, vinyl caprolactam, stilbene, but also diallyl phthalate, dibenzylidene acetone, allyl benzene, methyl methacrylate, methylacrylate, (meth)acrylic acid, diacrylates, dimethacrylates, acrylamides; vinyl acetate, triallyl cyanurate, thallyl isocyanurate, allyl compounds which are used for optical application (such as (di)ethylene glycol diallyl carbonate), and mixtures thereof.
- the amount of ethylenically unsaturated monomer is preferably at least 0.1 wt%, based on the weight of the resin, more preferably at least 1 wt%, and most preferably at least 5 wt%.
- the amount of ethylenically unsaturated monomer is preferably not more than 50 wt%, more preferably not more than 40 wt%, and most preferably not more than 35 wt%.
- the accelerator solution is generally employed in a conventional amount. Amounts of at least 0.01 wt%, preferably at least 0.1 wt%, and not more than 5 wt%, preferably not more than 2 wt% of the accelerator solution, based on the weight of the resin, are typically used.
- Peroxides suitable for the curable resins include inorganic peroxides and organic peroxides, such as conventionally used ketone peroxides, peroxyesters, diaryl peroxides, dialkyl peroxides, and peroxydicarbonates, but also peroxycarbonates, peroxyketals, hydroperoxides, diacyl peroxides, and hydrogen peroxide.
- organic peroxides such as conventionally used ketone peroxides, peroxyesters, diaryl peroxides, dialkyl peroxides, and peroxydicarbonates, but also peroxycarbonates, peroxyketals, hydroperoxides, diacyl peroxides, and hydrogen peroxide.
- phlegmatisers such as hydrophilic esters and hydrocarbon solvents.
- the amount of peroxide to be used in the curing process is preferably at least 0.1 wt%, more preferably at least 0.5 wt%, and most preferably at least 1 wt%.
- the amount of peroxide is preferably not more than 8 wt%, more preferably not more than 5 wt%, most preferably not more than 2 wt%, all based on the weight of the resin.
- the promoter used was potassium 2-ethyl hexanoate.
- the accelerator solutions - 0.5 phr (per hundred resin) solution - were used to cure an ortho phthalic acid-based unsaturated polyester resin (Palatal® P6 ex DSM resin) at 20°C with 2 phr methyl ethyl ketone peroxide (Butanox® M50, ex-AkzoNobel).
- the curing was analysed by the method of the Society of Plastic Institute (SPI method F/77.1 ; available from Akzo Nobel Polymer Chemicals). This method involves measuring of the peak exotherm, the time to peak, and the gel time. According to this method, 25 g of a mixture comprising 100 parts of resin, 2 parts of peroxide, and accelerator solution were poured into a test tube and a thermocouple was placed through the enclosure at the centre of the tube. The glass tube was then placed in the oil bath maintained at 20°C and the time- temperature curve was measured. From the curve the following parameters were calculated:
- Time to peak (TTP) time elapsed between the start of the experiment and the moment that the peak temperature is reached.
- Peak exotherm (PE) the maximum temperature that is reached.
- Example 4 and Comparative Example B were repeated, except that 0.25 and 1 .0 phr of the accelerator solution were used. The results are shown in Table 2 below. Table 2
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Priority Applications (17)
Application Number | Priority Date | Filing Date | Title |
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MX2012014475A MX2012014475A (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins. |
DK11725083.7T DK2582744T3 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and method of curing curable resins |
SI201130166T SI2582744T1 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins |
AU2011267128A AU2011267128B2 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins |
KR1020127033492A KR101860460B1 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins |
PL11725083T PL2582744T3 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins |
JP2013514669A JP5654123B2 (en) | 2010-06-16 | 2011-06-14 | Curing acceleration solution and method for curing curable resin |
US13/704,855 US9034785B2 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins |
CN201180027877.4A CN102947375B (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and method of curing a curable resin |
ES11725083.7T ES2469168T3 (en) | 2010-06-16 | 2011-06-14 | Accelerator dissolution and process to cure curable resins |
RU2012158109/05A RU2572965C2 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and method of curing curable resins |
EP11725083.7A EP2582744B1 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins |
CA2801821A CA2801821C (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins |
BR112012031416-5A BR112012031416B1 (en) | 2010-06-16 | 2011-06-14 | accelerator solution and use of an accelerator solution |
IL222995A IL222995A (en) | 2010-06-16 | 2012-11-12 | Accelerator solution and process for curing curable resins |
ZA2012/09046A ZA201209046B (en) | 2010-06-16 | 2012-11-29 | Accelerator solution and process for curing curable resins |
EG2012122028A EG26959A (en) | 2010-06-16 | 2012-12-09 | Accelerator solution and process for curing curable resins |
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EP10166163.5 | 2010-06-16 | ||
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PCT/EP2011/059769 WO2011157673A1 (en) | 2010-06-16 | 2011-06-14 | Accelerator solution and process for curing curable resins |
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US (1) | US9034785B2 (en) |
EP (1) | EP2582744B1 (en) |
JP (1) | JP5654123B2 (en) |
KR (1) | KR101860460B1 (en) |
CN (1) | CN102947375B (en) |
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BR (1) | BR112012031416B1 (en) |
CA (1) | CA2801821C (en) |
DK (1) | DK2582744T3 (en) |
EG (1) | EG26959A (en) |
ES (1) | ES2469168T3 (en) |
IL (1) | IL222995A (en) |
MX (1) | MX2012014475A (en) |
MY (1) | MY160959A (en) |
PL (1) | PL2582744T3 (en) |
RU (1) | RU2572965C2 (en) |
SI (1) | SI2582744T1 (en) |
TW (1) | TWI506046B (en) |
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WO2013083630A1 (en) * | 2011-12-06 | 2013-06-13 | Dsm Ip Assets B.V. | Resin composition |
WO2014032710A1 (en) * | 2012-08-29 | 2014-03-06 | Akzo Nobel Chemicals International B.V. | Iron-based accelerator for curing resins |
WO2014070661A1 (en) * | 2012-10-29 | 2014-05-08 | Ashland Licensing And Intellectual Property Llc | Resin compositions |
EP2688947B1 (en) * | 2011-03-24 | 2015-05-06 | Akzo Nobel Chemicals International B.V. | Accelerator for curing resins |
WO2015086546A1 (en) * | 2013-12-12 | 2015-06-18 | Akzo Nobel Chemicals International B.V. | Method for curing a radically curable resin |
US9068045B2 (en) | 2013-04-05 | 2015-06-30 | Reichhold, Inc. | Curing of liquid thermosetting resins |
WO2015121178A1 (en) * | 2014-02-11 | 2015-08-20 | Akzo Nobel Chemicals International B.V. | Process for curing (meth)acrylate-containing up or ve resin |
US9255196B2 (en) | 2011-03-24 | 2016-02-09 | Akzo Nobel Chemicals International B.V. | Accelerator for curing resins |
EP3296372A1 (en) * | 2016-09-19 | 2018-03-21 | Daw Se | Solvent-containing coating composition |
US10000602B2 (en) | 2014-10-02 | 2018-06-19 | Reichhold Llc 2 | Curable compositions |
RU2665570C2 (en) * | 2013-02-11 | 2018-08-31 | Чемсенти Лимитед | Oxidatively curable coating composition |
US11193038B2 (en) | 2016-07-19 | 2021-12-07 | Allnex Austria Gmbh | Drier compositions for alkyd resins |
WO2022089879A1 (en) * | 2020-10-28 | 2022-05-05 | Evonik Operations Gmbh | Composite resins comprising unsaturated phosphate compounds |
EP3077467B1 (en) | 2013-12-03 | 2022-11-02 | PPG Europe B.V. | Drier composition and use thereof |
US11518834B2 (en) | 2019-01-02 | 2022-12-06 | Polynt Composites USA, Inc. | Radically polymerizable compositions |
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EP2343336A1 (en) * | 2010-01-06 | 2011-07-13 | Unilever Plc, A Company Registered In England And Wales under company no. 41424 of Unilever House | Curing liquids |
AR107070A1 (en) * | 2015-12-18 | 2018-03-14 | Catexel Ltd | OXIDATIVELY CURABLE COATING COMPOSITION |
BR112019012077A2 (en) | 2016-12-14 | 2019-11-12 | Arkema France | airflow control composition for polymerization of carbonyl-containing monomers |
KR20200016208A (en) * | 2017-06-08 | 2020-02-14 | 디아이씨 가부시끼가이샤 | Curing accelerator, printing ink and paint for oxidative polymerization type unsaturated resin |
US11873381B2 (en) | 2018-02-19 | 2024-01-16 | Arkema Inc. | Accelerated peroxide-cured resin compositions having extended open times |
AU2019297083B2 (en) * | 2018-07-05 | 2022-07-21 | Borchers Catalyst (UK) Limited | Liquids |
CN114249864B (en) * | 2022-01-25 | 2023-09-05 | 广东美亨新材料科技有限公司 | Unsaturated polyester resin accelerator, and preparation method and application thereof |
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- 2011-06-14 RU RU2012158109/05A patent/RU2572965C2/en active
- 2011-06-14 KR KR1020127033492A patent/KR101860460B1/en active IP Right Grant
- 2011-06-14 AU AU2011267128A patent/AU2011267128B2/en active Active
- 2011-06-14 DK DK11725083.7T patent/DK2582744T3/en active
- 2011-06-14 WO PCT/EP2011/059769 patent/WO2011157673A1/en active Application Filing
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Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2688947B1 (en) * | 2011-03-24 | 2015-05-06 | Akzo Nobel Chemicals International B.V. | Accelerator for curing resins |
US9255196B2 (en) | 2011-03-24 | 2016-02-09 | Akzo Nobel Chemicals International B.V. | Accelerator for curing resins |
US9206302B2 (en) | 2011-03-24 | 2015-12-08 | Akzo Nobel Chemicals International B.V. | Accelerator for curing resins |
WO2013083630A1 (en) * | 2011-12-06 | 2013-06-13 | Dsm Ip Assets B.V. | Resin composition |
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CN104583291A (en) * | 2012-08-29 | 2015-04-29 | 阿克佐诺贝尔化学国际公司 | Iron-based accelerator for curing resins |
WO2014032710A1 (en) * | 2012-08-29 | 2014-03-06 | Akzo Nobel Chemicals International B.V. | Iron-based accelerator for curing resins |
AU2012388409B2 (en) * | 2012-08-29 | 2016-06-16 | Akzo Nobel Chemicals International B.V. | Iron-based accelerator for curing resins |
US9428631B2 (en) | 2012-08-29 | 2016-08-30 | Akzo Nobel Chemicals International B.V. | Iron-based accelerator for curing resins |
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WO2014070661A1 (en) * | 2012-10-29 | 2014-05-08 | Ashland Licensing And Intellectual Property Llc | Resin compositions |
RU2665570C2 (en) * | 2013-02-11 | 2018-08-31 | Чемсенти Лимитед | Oxidatively curable coating composition |
US9068045B2 (en) | 2013-04-05 | 2015-06-30 | Reichhold, Inc. | Curing of liquid thermosetting resins |
EP3077467B1 (en) | 2013-12-03 | 2022-11-02 | PPG Europe B.V. | Drier composition and use thereof |
WO2015086546A1 (en) * | 2013-12-12 | 2015-06-18 | Akzo Nobel Chemicals International B.V. | Method for curing a radically curable resin |
US9751994B2 (en) | 2013-12-12 | 2017-09-05 | Akzo Nobel Chemicals International B.V. | Method for curing a radically curable resin |
AU2015217844B2 (en) * | 2014-02-11 | 2018-02-01 | Akzo Nobel Chemicals International B.V. | Process for curing (meth)acrylate-containing UP or VE resin |
WO2015121178A1 (en) * | 2014-02-11 | 2015-08-20 | Akzo Nobel Chemicals International B.V. | Process for curing (meth)acrylate-containing up or ve resin |
US10000602B2 (en) | 2014-10-02 | 2018-06-19 | Reichhold Llc 2 | Curable compositions |
US11193038B2 (en) | 2016-07-19 | 2021-12-07 | Allnex Austria Gmbh | Drier compositions for alkyd resins |
EP3296372A1 (en) * | 2016-09-19 | 2018-03-21 | Daw Se | Solvent-containing coating composition |
US11518834B2 (en) | 2019-01-02 | 2022-12-06 | Polynt Composites USA, Inc. | Radically polymerizable compositions |
US12071498B2 (en) | 2019-01-02 | 2024-08-27 | Polynt Composites USA, Inc. | Radically polymerizable compositions |
WO2022089879A1 (en) * | 2020-10-28 | 2022-05-05 | Evonik Operations Gmbh | Composite resins comprising unsaturated phosphate compounds |
Also Published As
Publication number | Publication date |
---|---|
MY160959A (en) | 2017-03-31 |
EG26959A (en) | 2015-02-01 |
BR112012031416A2 (en) | 2016-11-08 |
TW201213362A (en) | 2012-04-01 |
IL222995A0 (en) | 2013-02-03 |
US9034785B2 (en) | 2015-05-19 |
MX2012014475A (en) | 2013-02-21 |
BR112012031416B1 (en) | 2020-10-20 |
RU2572965C2 (en) | 2016-01-20 |
KR101860460B1 (en) | 2018-05-23 |
IL222995A (en) | 2016-02-29 |
JP5654123B2 (en) | 2015-01-14 |
EP2582744A1 (en) | 2013-04-24 |
TWI506046B (en) | 2015-11-01 |
KR20130087403A (en) | 2013-08-06 |
AU2011267128B2 (en) | 2015-05-07 |
CN102947375B (en) | 2014-02-26 |
US20130211013A1 (en) | 2013-08-15 |
CA2801821C (en) | 2018-05-15 |
ES2469168T3 (en) | 2014-06-17 |
DK2582744T3 (en) | 2014-06-30 |
CN102947375A (en) | 2013-02-27 |
SI2582744T1 (en) | 2014-06-30 |
CA2801821A1 (en) | 2011-12-22 |
PL2582744T3 (en) | 2014-08-29 |
JP2013531715A (en) | 2013-08-08 |
RU2012158109A (en) | 2014-07-27 |
EP2582744B1 (en) | 2014-03-26 |
ZA201209046B (en) | 2013-08-28 |
AU2011267128A1 (en) | 2012-12-06 |
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