Patent Application
20100012888
The present application is related to and claims the priority benefit of European Patent Application No. EP/08009315.6 filed on May 21, 2008 which is incorporated herein by reference in its entirety.
The invention relates to curing agents (“hardeners”) for expoxy resins. These curing agents are especially useful for low viscosity, high solid, and low VOC coating compositions with low temperature cure, good tack-free time and improved chemical resistance.
Phenalkamines are still a relatively young class of epoxy resin curing agents. They are products of the reaction (condensation products) of cardanol (I), which, chemically, is a C15-alkylphenol and a major constituent of the oil obtainable from cashew nut shells (CNSL, cashew nut shell liquid), with aliphatic (primary or secondary) amines and formaldehyde.
WO 2004/024792 A1 discloses coating compositions comprising a film forming polymer comprising an epoxide polymer, a mixture of crosslinking agents and pigments. The mixture of crosslinking agents comprises (a) at least one polyamide functional compound and (b) at least one phenalkamine compound.
Phenalkamines (b) are recognized by the skilled artisan as Mannich bases, the reaction product of an aldehyde, such as formaldehyde, amine and a phenolic compound (see WO 2004/024792 A1, page 3, lines 16-18). Useful amines include ethylenediamine (EDA) and diethylenetriamine (DETA) (see WO 2004/024792 A1, page 3, lines 18-19). The phenolic compound is a cardanol-containing extract derived from cashew nutshell liquid (see WO 2004/024792 A1, page 3, lines 19-20).
Polyamides (a) are based on the reaction product of dimerized fatty acid with polyamine, preferably difunctional polyamines (see WO 2004/024792 A1, page 4, lines 4-6). Preferably the amides are formed by a condensation reaction. The polyamide may be solid, like a wax, or liquid (see WO 2004/024792 A1, page 4, lines 11-12). The polyamides (b) preferably have an amine value of 159-175 mg KOH/g (see WO 2004/024792 A1, page 4, line 13).
The problem addressed by the present invention was to develop novel curing agents (“hardeners”) for expoxy resins. These curing agents should be useful for low viscosity, high solid, and low VOC coating compositions with low temperature cure, good tack-free time and improved chemical resistance.
The subject matter of the present invention is hardener compositions for epoxy resins (epoxy resin curing agent compositions) comprising a mixture of crosslinking agents comprising
(a) at least one polyamide functional compound, which has at least one amide function and at least one amine function per molecule, with the proviso that the polyamide (a) is obtained by the reaction of a dimer fatty acid or an alkylester of a dimer fatty acid with at least one polyamine, and
(b) at least one phenalkamine compound, which is the condensation product of cardanol, formaldehyde and one or more at least dibasic polyamine, with the proviso that the dimer fatty acid used to obtain the polyamide functional compound (a) comprises monomeric fatty acid in an amount of 20-60% by weight (based on the total amount of the dimer fatty acid).
As the skilled artisan is aware, dimer fatty acids are carboxylic acids obtainable by oligomerization of unsaturated carboxylic acids, generally fatty acids, such as oleic acid, linoleic acid, erucic acid and the like. The oligomerization is normally carried out at elevated temperature in the presence of a catalyst, for example clay.
The substances obtained—technical-quality dimer fatty acids—are mixtures in which the dimerization products predominate. However, the mixtures also contain small amounts of monomers (the sum total of monomers in the crude mixture of the dimer fatty acids is referred to by the expert as “monomer fatty acids”) and higher oligomers, more especially the so-called “trimer fatty acids”. Dimer fatty acids are commercially available products and are available in various compositions and qualities (for example under the name of Empol®, a product of Cognis).
As already mentioned, the monomeric compounds present in the mixture for the production of dimer fatty acids after the reaction has been carried out and obtainable therefrom by distillation-based processes are normally referred to by the expert as monomer fatty acids. The monomer fatty acids are not unreacted starting material of the process for producing dimer fatty acids, but rather products of a secondary reaction containing small amounts of unreacted starting material. The secondary reaction leads to a structural modification of the fatty acids used.
The composition of the monomer fatty acids is subject to certain variations in regard to the nature of the starting materials used in the production of the dimer fatty acids. For example, the content of compounds containing aromatic structural elements in the monomer fatty acids is particularly pronounced when linoleic acid is predominantly used as starting material. Monomer fatty acids obtainable in the production of dimer fatty acids using either oleic acid or linoleic acid or a mixture of oleic and linoleic acid (for example in the form of the so-called tall oil fatty acids) as starting material are particularly preferred for the purposes of the present invention.
Within the present invention the term “dimer fatty acid” is used for mixtures comprising monomer, dimer and trimer fatty acid as explained above. Consequently, if the content of monomer fatty acids in dimer fatty acid is mentioned in the present invention, this means % by weight of the monomeric fatty acids based on the total of the “dimeric fatty acid” (the mixture of the mono-, di- and tri-species, as explained above).
As mentioned above the polyamide functional compound (a) has at least one amide function and at least one primary and/or secondary amine function per molecule, and is obtainable by the reaction of a dimer fatty acid or an alkylester of a dimer fatty acid with at least one polyamine. Furthermore the dimer fatty acid used to obtain this polyamide functional compound (a) comprises monomeric fatty acid in an amount of 20-60% by weight (based on the total amount of the dimer fatty acid).
The amine functions of (a) can be primary (NH2) and/or secondary (NH). Due to the fact that compound (a) contains at least one amine function, these compounds (a) can be characterized by an amine value.
In a preferred embodiment the dimer fatty acid building block used to obtain this polyamide functional compound (a) comprises monomeric fatty acid in an amount of 30-50% by weight (based on the total amount of the dimer fatty acid building block).
The polyamine used to obtain the polyamide functional compound (a) can be derived from any linear, branched, cyclic, aromatic or aliphatic polyamine. As defined herein the term polyamine also includes diamines.
In one embodiment the polyamine used to obtain the polyamide functional compound (a) is a diamine or a mixture of diamines. In a preferred embodiment the diamines are chosen from the group ethylenediamine (EDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), m-xylylendiamine (MXDA), and isophorone diamine. In a further preferred embodiment a mixture of TETA and TEPA is used as diamine mixture.
As mentioned above the phenalkamine compound (b) is the condensation product of an alkyl phenol, formaldehyde and one or more at least dibasic polyamines. Preferably the phenolic alkyl group has 3 to 17 carbon atoms (especially 13 to 15 carbon atoms) and can be saturated or unsaturated. Moreover the alkyl phenol may have additional methyl and/or OH-groups. Cardanol is preferred as alkyl phenol. Cardanol is known to the skilled artisan, as defined by the formula (I) above. In one embodiment cardanol is used which is obtained from cashew nut shell liquid (CNSL) extract.
The phenalkamine compound (b) can be derived from any linear, branched, cyclic, aromatic or aliphatic polyamine. As defined herein the term polyamine also includes diamines.
In one embodiment the polyamine used to obtain the phenalkamine compound (b) is a diamine or a mixture of diamines. In a preferred embodiment the diamines are chosen from the group ethylenediamine (EDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), m-xylylendiamine (MXDA), and isophorone diamine. In a further preferred embodiment a mixture of TETA and TEPA is used as diamine mixture.
The advantages achieved with the epoxy hardener composition comprising components (a) and (b) of the present invention are:
The mixture of compounds (a) and (b) of the present invention is a synergistic mixture, which means that the effects of the epoxy hardener comprising (a) and (b) together, are better compared to either (a) alone or (b) alone.
In one embodiment of the invention the mixture of (a) and (b) comprises 5 to 95% of (a), and 95% and 5% of (b). In a preferred embodiment the mixture of (a) and (b) comprises 65 to 75% of (a), and 35% and 25% of (b).
Mixtures of compounds (a) and (b), in which compounds (b) are based on TETA and TEPA mixtures as the diamine building block, show good properties in formulations which also contain epoxy resins and pigments—in so far as sedimentation and cloudness during storage are not observed.
In a 50 liters multipurpose reactor, 40 kg (135.5 moles) of soy methyl esters with a typical soy fatty acid distribution, 3.2 kg of clay, 0.14 kg (3.33 moles) of lithium hydroxide monohydrated were added to the reactor. Nitrogen purge was carried out during 5 minutes, reactor was closed and heated up to 260° C. over 1 hour. After reaching 260-270° C. pressure was kept at 6 bars using a pressure control valve, reactor was held in this condition during 2 hours to complete dimerization reaction. The temperature was lowered to 150° C. and 0.7 kg (6.07 moles) of H3PO4 85% was added over 1 hour to split the lithium soaps Filtration was done using a conventional press filter to remove clay, catalyst and any other solid material. 38.4 kg of methyl dimers having 38% C18 monobasic fatty acid methyl esters, 46.5% of C36 dibasic fatty acid methyl esters, 15.5% of C54 tribasic fatty acid methyl esters, Gardner color=3.0, acid value=15 mgKOH/g, and saponification value=195 mg KOH/g, viscosity at 25° C.=80 cps were obtained at the end of the above described process.
In a 50 liter multipurpose reactor, 26.34 kg (86.86 moles) of dimers fatty acid methyl ester (from example 1), 11.83 kg (81.03 moles) kg of TETA, 1.83 kg (9.68 moles) of TEPA were added. Nitrogen purge was carried out for 5 minutes, then the temperature was set to 100° C. After reaching 100° C., the temperature was increased to 205° C. over 2 hours. Vacuum of 650 mmHg pressure (relative) was applied during 30 minutes and the final product was cooled and discharged. Analysis: Gardner color=6; Amine value=381.9 mg KOH/g; Brookfield Viscosity at 25° C.=3157 cps.
In a 50 liter multi purpose reactor, 11,16 kg (37.2 mols) of C15 alkylphenol produced from Cashew Nut Shell Liquid through Short Path Disitillation technique having 90% of C 15 alkyl phenol isomers (commercially known as Cardanols) and 10% of C15 alkyl di-hydroxy benzene isomers (Cardols), 2.12 kg (70.7 mols) of paraformaldehyde were charged to the reactor.
3.8 kg (63.8 mols) of Ethylenediamine was added slowly during 2 hours cooling the reactor to keep the temperature at 80° C. at the maximum. Temperature was increased to 115° C. and than reacted during 1 hour, reactor was cooled down to 90° C. and water was distilled off using 650 mmHg of pressure. About 1.5 kg of distillate were obtained. 14.1 kg of epoxy curing agent were obtained at the end with Gardner color=16, Amine Value=287 mg KOH/g, viscosity Brookfield F2/10 rpm at 25° C. =3080 cps.
In a 50 liter jacked reactor, 27 kg of liquid polyamide according to example 2 were added and heated to 60° C., under mixing and nitrogen flow. 9 kg of alkyl-phenol formaldehyde amine condensate (according to example 3) were added to the reactive liquid polyamide and mixed for 30 minutes. The resulting final mixture is a liquid resin that was used in application trials. Analytical results: Gardner color=14; Amine Value=357.0 mgKOH/g; Brookfield Viscosity at 25° C.=5920 cps.
1)= Cognis;
2)= Huntsman;
3)= Southern Clay Products Inc.
Mixture ratio By weight: 9 g of Part-A, 1 g of Part-B By volume: 5 parts of Part-A, 1 part of Part-B
| Number | Date | Country | Kind |
|---|---|---|---|
| 08009315.6 | May 2008 | EP | regional |
