WO2015053289A1 - コアシェルポリマー含有エポキシ樹脂組成物、その硬化物、及びその製造方法 - Google Patents
コアシェルポリマー含有エポキシ樹脂組成物、その硬化物、及びその製造方法 Download PDFInfo
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- WO2015053289A1 WO2015053289A1 PCT/JP2014/076858 JP2014076858W WO2015053289A1 WO 2015053289 A1 WO2015053289 A1 WO 2015053289A1 JP 2014076858 W JP2014076858 W JP 2014076858W WO 2015053289 A1 WO2015053289 A1 WO 2015053289A1
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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
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F265/00—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00
- C08F265/04—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00 on to polymers of esters
- C08F265/06—Polymerisation of acrylate or methacrylate esters on to polymers thereof
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F279/00—Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00
- C08F279/02—Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00 on to polymers of conjugated dienes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F283/00—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
- C08F283/12—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polysiloxanes
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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
- C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L51/04—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to rubbers
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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
- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/53—Core-shell polymer
Definitions
- the present invention relates to a core-shell polymer-containing epoxy resin composition having a low viscosity and easy to handle and having an excellent impact resistance improvement effect, a cured product containing the same, and a method for producing the same.
- a curable resin typified by a phenol resin, an unsaturated polyester resin, or an epoxy resin is excellent in heat resistance, mechanical strength, dimensional accuracy, and the like and is widely used in various fields.
- epoxy resins are excellent in many respects such as mechanical strength, electrical insulation properties, heat resistance, and adhesiveness, so they are widely used in civil engineering and building materials, electrical and electronic materials, adhesives, fiber reinforced composite materials, etc. in use.
- a molded product obtained from an epoxy resin has a problem that it exhibits very brittle properties because of its low fracture toughness.
- a method for strengthening toughness by adding a modifier to an epoxy resin a method of adding a rubber component to the epoxy resin composition is known.
- a method of adding a rubber component a method of adding a reactive liquid rubber (CTBN or the like) or a nitrile rubber, a method of mixing a core-shell polymer with an epoxy resin, or the like is known (for example, Patent Document 1).
- the reactive liquid rubber undergoes a process of once dissolving in the epoxy resin and then phase-separating at the time of curing, the morphology of the cured product changes depending on the type of epoxy resin to be blended and the curing conditions, and the desired In addition to the effect of improving the quality of the resin, the reproducibility of the quality is poor, and part of the rubber component dissolves and remains in the cured epoxy resin phase. It is known that problems such as a decrease in the quality of epoxy resin products occur due to a decrease in the temperature. Further, in the method of adding the core-shell polymer to the epoxy resin, although the glass transition temperature can be suppressed, the primary particle aggregate (aggregate) is, for example, in the form of powder of several tens to several hundreds of microns.
- Patent Document 2 water is brought into contact with a mixture obtained by mixing an aqueous latex of rubber-like polymer particles with an organic solvent having partial solubility in water, and the rubber-like polymer particles Agglomerates are formed, and the aqueous phase is separated from the mixture of the agglomerates and the aqueous phase to obtain aggregates of rubber-like polymer particles with less impurities, and the dispersion obtained by adding an organic solvent to the aggregates
- the shell layer of the core-shell type polymer shown by this method has a glass transition temperature (hereinafter abbreviated as Tg) significantly higher than room temperature, Tg having a poor impact resistance improving effect of the epoxy resin. High resin component is brought into the composition. For this reason, there was room for further improvement.
- Tg glass transition temperature
- Patent Documents 3 and 4 show compositions comprising a core-shell polymer having a shell part Tg of 20 ° C. or lower and a hydroxyl group in the shell part, and a thermosetting resin.
- this type of core-shell polymer tends to increase the viscosity of the composition and is difficult to handle, and may not exhibit impact resistance, leaving room for improvement.
- the present invention contains a core-shell polymer that has good dispersibility in epoxy resin, further dispersibility after curing, excellent mechanical properties, particularly excellent impact resistance improvement effect, and preferably has low viscosity.
- An object of the present invention is to provide an epoxy resin composition that is easy to handle.
- the present inventors have excellent mechanical properties by allowing a specific core-shell polymer (B) having an epoxy group in the shell portion to exist in a specific state in the epoxy resin.
- the inventors have found a core-shell polymer-containing epoxy resin composition having a particularly excellent impact resistance improvement effect.
- the present invention provides a core-shell polymer-containing epoxy resin composition
- a core-shell polymer-containing epoxy resin composition comprising 100 parts by weight of the epoxy resin (A) and 1 to 100 parts by weight of the core-shell polymer (B), wherein the volume average particle size of the core-shell polymer (B) is 0.01-1 ⁇ m, the glass transition temperature (Tg) of the core part of the core-shell polymer (B) is less than 0 ° C., and the glass transition temperature (Tg) of the shell part of the core-shell polymer (B) ) Is less than 25 ° C., and the shell portion of the core-shell polymer (B) relates to a core-shell polymer-containing epoxy resin composition containing a monomer having an epoxy group.
- the core part of the core-shell polymer (B) has at least 50% by weight of at least one monomer selected from the group consisting of a diene monomer and a (meth) acrylate monomer, A rubber elastic body composed of 0% by weight or more and less than 50% by weight of another copolymerizable vinyl monomer; a polysiloxane rubber-based elastic body; or a mixture of these elastic bodies, and the other copolymerizable
- the shell part of the core-shell polymer (B) contains an alkoxy group- or aryloxy group-containing (meth) acrylate unit, an epoxy group-containing (meth) acrylate unit, and optionally contained. It is to make the said core-shell polymer containing epoxy resin composition which contains the other monomer unit in the range from which the glass transition temperature calculated by FOX formula will be less than 25 degreeC.
- the shell part of the core-shell polymer (B) has 5 to 99% by weight of one or more monomers selected from the group consisting of alkoxyalkyl (meth) acrylate, methyl acrylate and ethyl acrylate, glycidyl 1 to 50% by weight of one or more monomers selected from the group consisting of (meth) acrylate, allyl glycidyl ether, and glycidyl alkyl (meth) acrylate, and other vinyl monomers of 0 to 50% by weight
- the core-shell polymer-containing epoxy resin composition is 5 to 99% by weight of one or more monomers selected from the group consisting of alkoxyalkyl (meth) acrylate, methyl acrylate and ethyl acrylate, glycidyl 1 to 50% by weight of one or more monomers selected from the group consisting of (meth) acrylate, allyl glycidyl ether, and glycidyl alkyl (me
- the shell part of the core-shell polymer (B) is composed of 5 to 99% by weight of 2-alkoxyethyl (meth) acrylate, glycidyl (meth) acrylate, allyl glycidyl ether, and glycidyl alkyl (meth) acrylate.
- the core-shell polymer-containing epoxy resin composition comprises 1 to 50% by weight of one or more monomers selected from the group and 0 to 50% by weight of other vinyl monomers.
- the shell part of the core-shell polymer (B) is selected from the group consisting of 5 to 99% by weight of 2-methoxyethyl acrylate, glycidyl (meth) acrylate, allyl glycidyl ether, and glycidyl alkyl (meth) acrylate.
- the core-shell polymer-containing epoxy resin composition is composed of 1 to 50% by weight of one or more monomers and 0 to 50% by weight of other vinyl monomers.
- the core-shell polymer-containing epoxy resin composition has a glass transition temperature of less than 20 ° C. in the shell portion of the core-shell polymer (B).
- the core-shell polymer (B) includes an intermediate layer between the core part and the shell part, and the intermediate layer contains 30 to 100% by weight of a polyfunctional monomer and other vinyl monomers.
- the core-shell polymer-containing epoxy resin composition containing 0 to 70% by weight of the body.
- the present invention is a cured product of the core-shell polymer-containing epoxy resin composition, wherein the core-shell polymer-containing epoxy resin composition is dispersed in the state of primary particles in the cured product.
- the present invention is a method for producing the core-shell polymer-containing epoxy resin composition, wherein an aqueous medium dispersion in which the core-shell polymer (B) is dispersed in an aqueous medium is dissolved in water at 20 ° C. Is mixed with an organic solvent of 5 wt% or more and 40 wt% or less, and further mixed with excess water to obtain a core-shell polymer (B) loose aggregate, and the agglomerated core-shell polymer (B) is a liquid. After separating and recovering from the phase, the organic solvent is again mixed with the organic solvent to obtain the organic solvent dispersion of the core-shell polymer (B), and the organic solvent dispersion is further mixed with the epoxy resin, and then the organic solvent is added.
- the manufacturing method of the core-shell polymer containing epoxy resin composition including the 3rd process distilled off.
- a core-shell polymer-containing epoxy resin composition having excellent dispersibility of the core-shell polymer and excellent impact resistance can be provided. More preferably, it is possible to provide a core-shell polymer-containing epoxy resin composition that has a low viscosity and is easy to handle and has an excellent impact resistance improvement effect as compared with the prior art.
- Epoxy resin (A) The epoxy resin that can be used in the present invention is not particularly limited as long as it is a compound having an epoxy group, but the epkin resin that can be used in the present invention is preferably an epoxy resin also called a polyepoxide.
- the epoxy resin include polyglycidyl ethers such as addition reaction products of polyphenols such as bisphenol A, bisphenol F, biphenol, and phenol novolak and epichlorohydrin, aniline, diaminobenzene, aminophenol, phenylenediamine, and diaminophenyl ether.
- polyepoxides further include those disclosed in US Pat. Nos. 3,804,735, 3,892,819, 3,948,698, 4,147,771, and an epoxy resin handbook (Nikkan Kogyo Shimbun, 1987). Can be mentioned.
- Polyalkylene glycol diglycidyl ether, glycol diglycidyl ether, diglycidyl ester of aliphatic polybasic acid, glycidyl ether of divalent or higher polyhydric aliphatic alcohol, and divinylbenzene dioxide can also be used as component (A).
- the content of these epoxy resins is preferably 0.5 to 20% by weight, more preferably 1 to 10% by weight, and still more preferably 2 to 5% by weight in the component (A).
- examples of the polyalkylene glycol diglycidyl ether include polyethylene glycol diglycidyl ether and polypropylene glycol diglycidyl ether. More specific examples of the glycol diglycidyl ether include fats such as neopentyl glycol diglycidyl ether, 1,4-butanediol diglycidyl ether, 1,6-hexanediol diglycidyl ether, and cyclohexanedimethanol diglycidyl ether. And diglycidyl ethers of group diols.
- the diglycidyl ester of the aliphatic polybasic acid include dimer acid diglycidyl ester, adipic acid diglycidyl ester, sebacic acid diglycidyl ester, and maleic acid diglycidyl ester.
- the glycidyl ether of the dihydric or higher polyhydric aliphatic alcohol is trimethylolpropane triglycidyl ether, trimethylolethane triglycidyl ether, castor oil modified. Examples include polyglycidyl ether, propoxylated glycerin triglycidyl ether, sorbitol polyglycidyl ether, and the like.
- An epoxy compound obtained by addition reaction of a polybasic acid or the like with an epoxy resin as described in WO2010 / 098950 pamphlet can also be used as the component (A).
- an addition reaction product of a dimer of tall oil fatty acid (dimer acid) and a bisphenol A type epoxy resin can be mentioned.
- Chelate-modified epoxy resins, rubber-modified epoxy resins, and urethane-modified epoxy resins can also be used as the component (A).
- the epoxy resin that can be used in the present invention is as described above, but generally, an epoxy resin having an epoxy equivalent of 80 to 2000 is exemplified.
- These polyepoxides can be obtained by a well-known method, and as a commonly used method, for example, a method in which an excess amount of epihalohydrin is reacted with a polyhydric alcohol or polyhydric phenol in the presence of a base can be mentioned.
- a component may be used independently and may be used together 2 or more types.
- epoxy resins bisphenol A type epoxy resins and bisphenol F type epoxy resins are preferable because the obtained cured products have high elastic modulus, excellent heat resistance and adhesion, and are relatively inexpensive. Resins are particularly preferred.
- an epoxy resin having an epoxy equivalent of less than 220 is preferable because the resulting cured product has high elastic modulus and heat resistance, and the epoxy equivalent is more preferably 90 or more and less than 210, and more preferably 150 or more and less than 200. Is more preferable.
- a bisphenol A type epoxy resin or a bisphenol F type epoxy resin having an epoxy equivalent of less than 220 is preferable because it is liquid at normal temperature and the handleability of the resulting resin composition is good.
- a bisphenol A type epoxy resin or a bisphenol F type epoxy resin having an epoxy equivalent of 220 or more and less than 2000 is added to the component (A), preferably in the range of 40% by weight or less, more preferably 20% by weight or less.
- a cured product is preferred because of its excellent impact resistance.
- the chelate-modified epoxy resin is preferably added in the range of 0.1 to 10% by weight, more preferably 0.5 to 3% by weight in the component (A).
- the chelate-modified epoxy resin is a reaction product of an epoxy resin and a compound containing a chelate functional group (chelate ligand), and when added to the resin composition of the present invention and used as a vehicle adhesive, The adhesion to the surface of a metal substrate contaminated with an oily substance can be improved.
- the chelate functional group is a functional group of a compound having in its molecule a plurality of coordination sites capable of coordinating to metal ions.
- a phosphorus-containing acid group for example, —PO (OH) 2
- a carboxylic acid group for example, — CO 2 H
- sulfur-containing acid groups for example, —SO 3 H
- amino groups and hydroxyl groups particularly, hydroxyl groups adjacent to each other in the aromatic ring.
- chelate ligands include ethylenediamine, bipyridine, ethylenediaminetetraacetic acid, phenanthroline, porphyrin, and crown ether.
- Examples of commercially available chelate-modified epoxy resins include Adeka Resin EP-49-10N manufactured by ADEKA.
- the rubber-modified epoxy resin is a reaction product obtained by reacting rubber with an epoxy group-containing compound and having an average of 1.1 or more epoxy groups per molecule.
- rubber examples include acrylonitrile butadiene rubber (NBR), styrene butadiene rubber (SBR), hydrogenated nitrile rubber (HNBR), ethylene propylene rubber (EPDM), acrylic rubber (ACM), butyl rubber (IIR), butadiene rubber, polypropylene oxide, Mention may be made of rubber polymers such as polyoxyalkylenes such as polyethylene oxide and polytetramethylene oxide.
- the rubber polymer is preferably one having a reactive group such as an amino group, a hydroxy group, or a carboxyl group at the terminal.
- the rubber-modified epoxy resin used in the present invention is a product obtained by reacting these rubber-based polymer and epoxy resin at an appropriate blending ratio by a known method.
- acrylonitrile-butadiene rubber-modified epoxy resin and polyoxyalkylene-modified epoxy resin are preferable from the viewpoint of adhesion of the resulting resin composition and impact peel resistance, and acrylonitrile-butadiene rubber-modified epoxy resin is more preferable.
- the acrylonitrile-butadiene rubber-modified epoxy resin can be obtained, for example, by reacting a carboxyl group-terminated NBR (CTBN) with a bisphenol A type epoxy resin.
- CTBN carboxyl group-terminated NBR
- the polyoxyalkylene-modified epoxy resin is obtained, for example, by a reaction between an amino group-terminated polyoxyalkylene and a bisphenol A type epoxy resin.
- the content of the acrylonitrile monomer component in the acrylonitrile-butadiene rubber is preferably 5 to 40% by weight, more preferably 10 to 35% by weight, from the viewpoints of adhesion of the resin composition to be obtained and impact resistance. Preferably, 15 to 30% by weight is more preferable. From the viewpoint of thixotropy of the obtained resin composition, 20 to 30% by weight is particularly preferable.
- the average number of epoxide-reactive end groups per molecule in the rubber-modified epoxy resin is preferably 1.5 to 2.5, and more preferably 1.8 to 2.2.
- the number average molecular weight of the rubber is preferably 2,000 to 10,000, more preferably 3,000 to 8,000, and particularly preferably 4,000 to 6,000 in terms of polystyrene measured by GPC.
- a rubber modified epoxy resin there is no restriction
- the rubber-modified epoxy resin is produced by heating to a temperature of 100 to 250 ° C.
- the epoxy group-containing compound used in producing the rubber-modified epoxy resin is not particularly limited, but bisphenol A type epoxy resin and bisphenol F type epoxy resin are preferable, and bisphenol A type epoxy resin is more preferable.
- the unreacted epoxy group-containing compound remaining after the reaction is included in the rubber-modified epoxy resin of the present invention. , Not included.
- the rubber-modified epoxy resin can be modified by pre-reaction with a bisphenol component.
- the bisphenol component used for modification is preferably 3 to 35 parts by weight, more preferably 5 to 25 parts by weight, based on 100 parts by weight of the rubber component in the rubber-modified epoxy resin.
- a cured product obtained by curing a resin composition containing a modified rubber-modified epoxy resin is excellent in adhesion durability after high-temperature exposure and excellent in impact resistance at low temperatures.
- the glass transition temperature (Tg) of the rubber-modified epoxy resin is not particularly limited, but is preferably ⁇ 25 ° C. or lower, more preferably ⁇ 35 ° C. or lower, still more preferably ⁇ 40 ° C. or lower, and particularly preferably ⁇ 50 ° C. or lower.
- the content of the rubber-modified epoxy resin in the component (A) is preferably 1 to 40% by weight, more preferably 3 to 30% by weight, still more preferably 5 to 25% by weight, and particularly preferably 10 to 20% by weight. If it is less than 1% by weight, the resulting cured product may be brittle and impact resistance adhesiveness may be low, and if it exceeds 40% by weight, the resulting cured product may have low heat resistance and / or elastic modulus (rigidity).
- the rubber-modified epoxy resins can be used alone or in combination of two or more.
- the urethane-modified epoxy resin is obtained by reacting a compound containing a group having reactivity with an isocyanate group and an epoxy group with a urethane prepolymer containing an isocyanate group. Is a reaction product having 1.1 or more.
- a urethane-modified epoxy resin can be obtained by reacting a hydroxy group-containing epoxy compound with a urethane prepolymer.
- the content of the urethane-modified epoxy resin in the component (A) is preferably 1 to 40% by weight, more preferably 3 to 30% by weight, still more preferably 5 to 25% by weight, and particularly preferably 10 to 20% by weight. If it is less than 1% by weight, the resulting cured product may be brittle and impact resistance adhesiveness may be low, and if it exceeds 40% by weight, the resulting cured product may have low heat resistance and / or elastic modulus (rigidity).
- Urethane-modified epoxy resins can be used alone or in combination of two or more.
- Epoxy resins that can be used in the present invention include monoepoxides as reactive diluents, for example, aliphatic glycidyl ethers such as butyl glycidyl ether, or aromatic glycidyl ethers such as phenyl glycidyl ether and cresyl glycidyl ether, such as 6 to 12 carbon atoms that can be substituted with an ether composed of an alkyl group having 8 to 10 carbon atoms such as 2-ethylhexyl glycidyl ether and a glycidyl group, for example, an alkyl group having 2 to 8 carbon atoms such as p-tertbutylphenylglycidyl ether.
- monoepoxides as reactive diluents for example, aliphatic glycidyl ethers such as butyl glycidyl ether, or aromatic glycidyl ethers
- Ethers consisting of a phenyl group and a glycidyl group, such as neodecanoic acid monoglycidyl ether, ethers consisting of an alkyl group having 12 to 14 carbon atoms and a glycidyl group; for example, glycidyl (meth) acrylate, glycidyl maleate Aliphatic glycidyl esters such as glycidyl esters, glycidyl esters of aliphatic carboxylic acids having 8 to 12 carbon atoms such as versatic acid glycidyl esters and lauric acid glycidyl esters; pt-butyl benzoic acid glycidyl esters and the like .
- the amount used is preferably 0.1 to 20% by weight, more preferably 0.5 to 10% by weight, and particularly preferably 1 to 5% by weight in the component (A). If it is less than 0.1% by weight, the effect of reducing the viscosity may not be sufficient. If it is more than 20% by weight, physical properties such as adhesiveness may be deteriorated.
- the core-shell polymer in the present invention needs to have a volume average particle diameter of 0.01 to 1 ⁇ m, and from the viewpoint of obtaining a core-shell polymer-containing epoxy resin composition having a preferable viscosity and impact resistance improvement effect.
- the thickness is preferably 0.05 to 0.8 ⁇ m. Further, it may be a mixture of core-shell polymers having different volume average particle diameters, and may be a multi-peak type core-shell polymer having a particle frequency peak in the vicinity of each volume average particle diameter.
- a core-shell polymer having a volume average particle diameter of 0 ⁇ m, preferably 0.15 to 0.9 ⁇ m may be mixed.
- the core-shell polymer-containing epoxy resin composition has a reduced viscosity and is easy to handle.
- the core-shell polymer has at least two layers of a core part existing on the inner side and a shell part existing on the outermost side, and the core part is made of a rubber-like polymer having a Tg of less than 0 ° C.
- the core-shell polymer according to the present invention is obtained by graft polymerization of a monomer (shell-forming monomer) that can be graft-copolymerized in the presence of such a rubber-like polymer (corresponding to the core).
- the weight ratio of the core part to the shell part of the present invention is preferably in the range of 50/50 to 99/1 in terms of the value of the core part / shell part (weight ratio of monomers forming each polymer).
- the polymer constituting the rubber-like polymer in the present invention is preferably crosslinked.
- the crosslinked rubbery polymer can swell in a suitable solvent but does not substantially dissolve. Further, the crosslinked rubber-like polymer is insoluble in the epoxy resin.
- the gel content of the rubbery polymer or the crosslinked rubbery polymer is, for example, 60% by weight or more, preferably 80% by weight or more, more preferably 90% by weight or more, and further preferably 95% by weight or more.
- the Tg of the polymer constituting the rubbery polymer or crosslinked rubbery polymer is less than 0 ° C., preferably less than ⁇ 10 ° C., more preferably less than ⁇ 20 ° C., and even more preferably less than ⁇ 40 ° C.
- the polymer constituting the rubber-like polymer is 50 weight percent of one or more monomers selected from the group consisting of diene monomers (conjugated diene monomers) and (meth) acrylate monomers. % Of rubber and other copolymerizable vinyl monomers of 0% by weight or more and less than 50% by weight; a polysiloxane rubber-based elastic body; or a combination of these elastic bodies is preferable.
- (meth) acryl means acryl and / or methacryl.
- Examples of the conjugated diene monomer constituting the rubber-like polymer include alkadiene monomers having about 4 to 8 carbon atoms such as butadiene, isoprene and chloroprene, and butadiene is particularly preferable.
- Examples of the (meth) acrylic acid ester monomers include (meth) acrylic acid C 3-15 alkyl such as butyl acrylate, 2-ethylhexyl acrylate, lauryl methacrylate, and the like. Butyl acrylate and 2-ethylhexyl acrylate Is particularly preferred. These may be used alone or in combination of two or more.
- the amount of at least one monomer selected from the group consisting of a conjugated diene monomer and a (meth) acrylic acid ester monomer is preferably 50% with respect to the total weight of the rubber-like polymer. % Or more, more preferably 60% by weight or more, and particularly preferably 70% by weight or more. When the amount of the monomer used is less than 50% by weight, the impact resistance improving effect of the core-shell polymer of the present invention tends to decrease.
- the rubber-like polymer may be a copolymer of a conjugated diene monomer or a (meth) acrylic acid ester monomer and a vinyl monomer copolymerizable therewith.
- vinyl monomers copolymerizable with conjugated diene monomers or (meth) acrylic acid ester monomers include aromatic vinyl monomers, vinyl cyanide monomers, unsaturated acid derivatives, Examples include monomers selected from (meth) acrylic acid amide derivatives, maleimide derivatives, and vinyl ether monomers.
- the aromatic vinyl monomer include styrene, ⁇ -methylstyrene, and vinyl naphthalene.
- Examples of the vinyl cyanide monomer include (meth) acrylonitrile and substituted acrylonitrile.
- examples of the unsaturated acid derivative include ⁇ , ⁇ -unsaturated acid, ⁇ , ⁇ -unsaturated acid anhydride, itaconic acid, crotonic acid and the like.
- examples of the (meth) acrylic acid amide derivative include (meth) acrylamide (including N-substituted product).
- Examples of maleimide derivatives include maleic anhydride and maleic imide.
- Examples of the vinyl ether monomer include 2-chloroethyl vinyl ether. These may be used alone or in combination of two or more.
- the amount of these copolymerizable vinyl monomers used is preferably less than 50% by weight, more preferably less than 40% by weight, and particularly less than 10% by weight, based on the total weight of the rubber-like polymer. It may be 0% by weight.
- the rubbery polymer may contain a polyfunctional monomer in order to adjust the degree of crosslinking. Examples of the polyfunctional monomer include divinylbenzene, butanediol di (meth) acrylate, triallyl (iso) cyanurate, allyl (meth) acrylate, diallyl itaconate, diallyl phthalate, and the like.
- the amount of the polyfunctional monomer used is not more than 10% by weight, preferably not more than 5% by weight, more preferably not more than 3% by weight, based on the total weight of the rubber-like polymer. When the amount used exceeds 10% by weight, the impact resistance improving effect of the core-shell polymer of the present invention tends to be lowered.
- the usage-amount may be 0.1 weight% or more and 1 weight% or more with respect to the weight of the whole rubber-like polymer.
- a chain transfer agent may be used to adjust the molecular weight and the degree of crosslinking of the polymer constituting the rubbery polymer, and examples thereof include alkyl mercaptans having 5 to 20 carbon atoms.
- the amount of the chain transfer agent used is 5% by weight or less, preferably 3% by weight or less, based on the total weight of the rubber-like polymer. If the amount of chain transfer agent used exceeds 5% by weight, the amount of the uncrosslinked component of the rubbery polymer increases, the viscosity of the epoxy resin composition of the present invention increases, and handling becomes difficult. This is not preferred because it may adversely affect the heat resistance, rigidity, etc. of the cured product obtained from the composition.
- the rubbery polymer it is possible to use a polysiloxane rubber-based elastic body in place of or in combination with the rubbery polymer.
- a polysiloxane rubber-based elastic body a polysiloxane rubber composed of alkyl or aryl disubstituted silyloxy units such as dimethylsilyloxy, methylphenylsilyloxy, diphenylsilyloxy, etc. is used. it can.
- a polyfunctional alkoxysilane compound is partially used in the polymerization, or (meth) acryloyloxypropylmethyldimethoxysilane or (meth) acryloyloxypropyl is used. It is more preferable to introduce a crosslinked structure in advance by radical reaction of a silane compound having a vinyl reactive group such as a (meth) acryloyloxy group-containing alkoxysilane such as trimethoxysilane.
- the shell portion in the present invention is composed of a polymer (shell polymer) obtained by polymerizing a shell-forming monomer, but improves the compatibility between the core-shell polymer according to the present invention and the epoxy resin, and contains the core-shell polymer according to the present invention. It plays the role which enables a core shell polymer to disperse
- Tg of a shell part will not be specifically limited if it is less than 20 degreeC as a homopolymer or a copolymer of 2 or more types of monomers.
- the lower limit of the Tg of the shell portion may be, for example, -80 ° C or -70 ° C.
- the glass transition temperature Tg n of copolymer is can be calculated by the FOX equation shown below (Equation 1).
- Tg 1 , Tg 2 ,. . . , Tg n each component 1, 2, ..., of a homopolymer of n Tg (K), w 1 , w 2,. . . w n each component 1, 2 is the weight fraction of n.
- the Tg of the homopolymer may be, for example, a numerical value described in Polymer Handbook Fourth Edition (edited by J. Brandup et al., 1999 John Wiley & Sons, Inc).
- the peak temperature of loss tangent (tan ⁇ ) in a viscoelasticity measurement method (shear method, measurement frequency: 1 Hz) may be adopted as Tg.
- the shell portion in the present invention is preferably graft-bonded to the rubbery polymer. More precisely, it is preferable that the shell-forming monomer is graft-polymerized to the core part forming the rubber-like polymer, and the shell part and the core part are substantially chemically bonded.
- the ratio of the shell part chemically bonded to the core part is preferably 50 to 100% by weight, more preferably 80 to 100% by weight, and more preferably 90 to 100% by weight with respect to 100% by weight of the shell part. %, More preferably 95 to 100% by weight.
- This polymerization operation can be carried out, for example, by adding a shell-forming monomer to a core polymer latex prepared and present in the form of an aqueous polymer latex.
- a aqueous polymer latex can be prepared by a known method such as emulsion polymerization, miniemulsion polymerization, or microsuspension polymerization.
- the shell part contains a monomer having an epoxy group as its structural unit.
- the monomer having an epoxy group chemically bonds the core-shell polymer and the epoxy resin in order that the core-shell polymer according to the present invention is dispersed in the state of primary particles in the cured product after the epoxy resin composition is cured. From the viewpoint, it is not particularly limited as long as it is a monomer used as a part of the shell-forming monomer and has an ethylenically unsaturated double bond and an epoxy group in the same molecule.
- ether compounds such as allyl glycidyl ether
- ester compounds such as glycidyl (meth) acrylate, allyl glycidyl ether, and glycidyl alkyl (meth) acrylate (particularly, epoxy group-containing (meth) acrylic acid esters).
- the proportion of the monomer having an epoxy group is, for example, 3 to 60% by weight, preferably 5 to 50% by weight, more preferably 10 to 45% by weight, based on the total monomer constituting the shell portion.
- the shell part may contain a monomer other than the monomer having the epoxy group as a structural unit, and the monomers described in the shell part are all monomers having the epoxy group. Can be used in combination. By the way, while the monomer having an epoxy group is useful for improving dispersibility, the homopolymer has a high Tg in some cases. ) Acrylic acid esters are included. Therefore, when a high Tg monomer (such as an epoxy group-containing (meth) acrylic acid ester) is used to improve dispersibility, it is combined with a low Tg monomer in order to keep the Tg of the shell portion below a predetermined value. It is recommended to configure the shell part.
- a high Tg monomer such as an epoxy group-containing (meth) acrylic acid ester
- Examples of the low Tg monomer include alkoxy group or aryloxy group-containing (meth) acrylic acid ester, (meth) acrylic acid C 3-10 alkyl ester (for example, butyl (meth) acrylate), (meth) acrylic acid Hydroxy C 3-10 alkyl ester (for example, 4-hydroxybutyl (meth) acrylate etc.) etc. are mentioned. Use of such a low Tg monomer can improve impact resistance adhesion.
- the aryloxy group-containing (meth) acrylic acid ester includes (meth) acrylic acid aryloxy C 1-4 alkyl ester such as phenoxyethyl (meth) acrylic acid.
- alkoxy group-containing (meth) acrylic acid examples include an alkoxy group or a methacrylic acid alkyl ester in which a linking group (such as an alkoxyalkoxy group) is bonded to an alkyl group.
- a linking group such as an alkoxyalkoxy group
- an alkoxyalkyl (meth) Say acrylate.
- This alkoxyalkyl (meth) acrylate imparts a certain polarity to the shell polymer from the viewpoint of compatibility of the shell polymer with the epoxy resin because the core-shell polymer according to the present invention is dispersed in the state of primary particles in the epoxy resin. Therefore, it is a monomer used as part of the monomer for shell formation.
- alkoxyalkyl (meth) acrylates include C 1-4 alkoxy groups such as 2-methoxyethyl (meth) acrylate, 2-ethoxyethyl (meth) acrylate, 2- (2-ethoxyethoxy) ethyl (meth) acrylate, and the like.
- Examples thereof include esters of C 1-4 alkyl alcohols to which a linking group of 2 to 4 C 1-4 alkoxy groups is bonded and (meth) acrylic acid.
- 2-methoxyethyl acrylate, 2-ethoxyethyl acrylate and 2- (2-ethoxyethoxy) ethyl acrylate are preferred.
- 2-methoxyethyl acrylate is particularly preferable from the viewpoint of availability and economy. These may be used alone or in combination of two or more.
- an alkoxy group or aryloxy group-containing (meth) acrylic acid ester is preferable, and an alkoxy group-containing (meth) acrylic acid ester is particularly preferable.
- alkoxy group-containing (meth) acrylates are advantageous in reducing the viscosity when the core-shell polymer is blended with an epoxy resin, further improving handling properties. Can be improved.
- an alkoxy group or an aryloxy group containing acrylic ester is preferable.
- the alkoxy group- or aryloxy group-containing acrylate ester can further improve the impact resistance adhesion at a low temperature (for example, ⁇ 20 to ⁇ 40 ° C.) as compared with the alkoxy group- or aryloxy group-containing methacrylate ester.
- Particularly preferred low Tg monomers are alkoxy group-containing acrylic esters.
- the ratio of the low Tg monomer can be set in a range where the glass transition temperature of the shell part calculated by the FOX formula is less than 25 ° C., and is, for example, 30 to 97% by weight in the total monomer constituting the shell part. , Preferably 40 to 95% by weight, more preferably 50 to 90% by weight.
- monomers that can be used as a monomer other than the monomer having an epoxy group include, in addition to the low Tg monomer, alkyl (meth) acrylates such as methyl acrylate and ethyl acrylate, and many other monomers. Examples thereof include functional monomers (such as allyl (meth) acrylate) (these are referred to as other vinyl monomers A). Further, it may be a vinyl monomer that is not any of a monomer having an epoxy group, an alkoxyalkyl (meth) acrylate, an alkyl (meth) acrylate, or a polyfunctional monomer (hereinafter referred to as other vinyl monomers).
- Monomer B for example, vinyl aromatic compounds such as styrene, ⁇ -methylstyrene, 1- or 2-vinylnaphthalene, monochlorostyrene, dichlorostyrene, bromostyrene, methyl (meth) acrylate, ethyl (meth) acrylate , Alkyl (meth) acrylates such as butyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, octyl (meth) acrylate, dodecyl (meth) acrylate, stearyl (meth) acrylate, behenyl (meth) acrylate, ethylene, propylene , Butylene, isobutyl Alkenes such as ethylene, vinyl cyanide compounds typified by (meth) acrylonitrile, (meth) acrylamide, alkyl vinyl ethers, and the like. These may be used alone or in combination of two or more.
- the shell part of the core-shell polymer (B) includes an alkoxy group or aryloxy group-containing (meth) acrylate unit, an epoxy group-containing (meth) acrylate unit, and other monomer units contained as necessary. It is preferable to contain in the range from which the glass transition temperature calculated by FOX formula will be less than 25 degreeC.
- the shell portion of the core-shell polymer (B) has at least one monomer selected from the group consisting of alkoxyalkyl (meth) acrylate, methyl acrylate, and ethyl acrylate, a monomer having an epoxy group, and other vinyl monomers. It is preferable to consist of the monomer B.
- the core portion of the core-shell polymer (B) has 5 to 99% by weight of one or more monomers selected from the group consisting of alkoxyalkyl (meth) acrylate, methyl acrylate, and ethyl acrylate, and an epoxy group. It has 1 to 50% by weight of the monomer and 0 to 50% by weight of the other vinyl monomer B. More preferably, the core portion of the core-shell polymer (B) has 10 to 99% by weight of one or more monomers selected from the group consisting of alkoxyalkyl (meth) acrylate, methyl acrylate, and ethyl acrylate, and an epoxy group.
- the shell part of the core-shell polymer (B) has 20 to 99% by weight of one or more monomers selected from the group consisting of alkoxyalkyl (meth) acrylate, methyl acrylate, and ethyl acrylate, and an epoxy group. It has 1 to 50% by weight of the monomer and 0 to 50% by weight of the other vinyl monomer B.
- the shell part of the core-shell polymer (B) has 40 to 99% by weight of one or more monomers selected from the group consisting of alkoxyalkyl (meth) acrylate, methyl acrylate, and ethyl acrylate, and an epoxy group. It consists of 1 to 50% by weight of monomer and 0 to 50% by weight of other vinyl monomers.
- the shell portion of the core-shell polymer (B) is selected from the group consisting of 5-alkoxyethyl (meth) acrylate 5 to 99% by weight, glycidyl (meth) acrylate, allyl glycidyl ether, and glycidyl alkyl (meth) acrylate 1 It is also a preferred embodiment that it consists of 1 to 50% by weight of at least one monomer and 0 to 50% by weight of other vinyl monomers, 2 to 99% by weight of 2-methoxyethyl acrylate, 1 to 50% by weight of one or more monomers selected from the group consisting of glycidyl (meth) acrylate, allyl glycidyl ether, and glycidyl alkyl (meth) acrylate, and others It is also a preferred embodiment that the vinyl monomer consists of 0 to 50% by weight.
- the core-shell polymer in the present invention is preferably dispersed in the state of primary particles in the cured product of the epoxy resin composition.
- “dispersed in the state of primary particles” means the core-shell polymer. It means that the particles do not aggregate with each other and are dispersed independently.
- the particle dispersion rate (%) calculated by using the following (Formula 2) by the method described later is 50%. That means that.
- Such a particle dispersion rate is preferably 75% or more, more preferably 90% or more, from the viewpoint of improving the impact-resistant adhesion.
- the sum B 0 of the number of single core-shell polymers in the measurement sample and the number of lumps in contact with two or more core-shell polymers, and the number B of lumps in contact with two or more core-shell polymers. 1 is obtained and calculated according to the above formula (Formula 2).
- a sample whose B 0 is at least 10 or more and an observation region are selected.
- the intermediate layer in the present invention comprises a polymer containing 30 to 100% by weight of a polyfunctional monomer and 0 to 70% by weight of other vinyl monomers, contained between the core part and the shell part.
- polyfunctional monomer examples include divinylbenzene, butanediol di (meth) acrylate, triallyl (iso) cyanurate, allyl (meth) acrylate, diallyl itaconate, diallyl phthalate, and the like.
- the shell polymer is formed on the intermediate polymer layer through one of the double bonds of the polyfunctional monomer.
- the intermediate layer and the shell polymer are chemically bonded to each other and graft polymerized to the rubber-like polymer through the remaining double bonds, so that the intermediate layer and the rubber-like polymer are substantially Chemically bond.
- the graft efficiency of the shell polymer is increased and the gel content of the entire core-shell polymer is increased, so that the above three effects are easily obtained. .
- a curing agent When the core-shell polymer-containing epoxy resin composition of the present invention is thermally cured, a curing agent may be added to the core-shell polymer-containing epoxy resin composition.
- curing agents include amine curing agents such as aliphatic diamines and aromatic diamines; acid anhydrides such as hexahydrophthalic anhydride; novolac-type phenolic resins, imidazole compounds, tertiary amines, triphenylphosphine, aliphatic polyamines.
- Aromatic polyamines polyamides, polymercaptans, dicyandiamides, dibasic acid dihydrazides, N, N-dialkylurea derivatives, N, N-dialkylthiourea derivatives, alkylaminophenol derivatives, melamine, guanamine and the like.
- These curing agents may be used alone or in combination of two or more.
- Preferred curing agents are amine-based curing agents, acid anhydrides, N, N-dialkylurea derivatives, tertiary amines, and imidazole compounds.
- the amount of the curing agent used is preferably 1 to 80 parts by weight, more preferably 2 to 40 parts by weight, still more preferably 3 to 30 parts by weight, and more preferably 5 to 20 parts by weight with respect to 100 parts by weight of the component (A). Particularly preferred. If it is less than 1 part by weight, the curability of the resin composition of the present invention may deteriorate. When it is more than 80 parts by weight, the storage stability of the resin composition of the present invention may be poor and handling may be difficult.
- dicyanandamide is used as a main component of the curing agent, and further, an N, N′-dialkylurea derivative is used. It is preferable to use a small amount of one or more selected from imidazole compounds, tertiary amines, and amine curing agents as a curing accelerator.
- amine curing agent examples include chain aliphatic polyamines such as diethylenetriamine, triethylenetetramine, tetraethylenepentamine, dipropylenediamine, diethylaminopropylamine, hexamethylenediamine; N-aminoethylpiverazine, bis ( 4-amino-3-methylcyclohexyl) methane, mensendiamine, isophoronediamine, 4,4′-diaminodicyclohexylmethane, 3,9-bis (3-aminopropyl) -2,4,8,10-tetraoxa Cyclic aliphatic polyamines such as spiro [5.5] undecane (spiroacetal diamine), norbornane diamine, tricyclodecane diamine, 1,3-bisaminomethylcyclohexane; aliphatic aromatic amines such as meta-xylene diamine; Metafe Aromatic amines such as range amine,
- an amine-terminated polyether containing a polyether main chain and having an average of 1 to 4 (preferably 1.5 to 3) amino groups and / or imino groups per molecule can also be used.
- Commercially available amine-terminated polyethers include Huntsman's Jeffamine D-230, Jeffamine D-400, Jeffamine D-2000, Jeffamine D-4000, Jeffamine T-5000, and the like.
- an amine-terminated rubber containing a conjugated diene-based polymer main chain and having an average of 1 to 4 (more preferably 1.5 to 3) amino groups and / or imino groups per molecule is also an amine.
- the main chain of the rubber is preferably a polybutadiene homopolymer or copolymer, more preferably a polybutadiene / acrylonitrile copolymer, and an acrylonitrile monomer content of 5 to 40% by weight (more preferably 10 to 35% by weight, still more preferably 15 to Polybutadiene / acrylonitrile copolymers that are 30% by weight) are particularly preferred.
- Examples of commercially available amine-terminated rubbers include Hypro 1300X16 ATBN manufactured by CVC.
- the resin composition of the present invention is used as a two-component adhesive that can be cured at a relatively low temperature of about room temperature, among the amine-based curing agents, polyamidoamines, amine-terminated polyethers, and An amine-terminated rubber is more preferred, and it is particularly preferred to use polyamide amines, an amine-terminated polyether and an amine-terminated rubber in combination. Further, by using a tertiary amine or imidazole compound in combination with an amine curing agent, the curing speed, the physical properties of the cured product, the heat resistance, and the like can be improved.
- the acid anhydride examples include polysebacic acid polyanhydride, polyazeline acid polyanhydride, succinic anhydride, citraconic acid anhydride, itaconic acid anhydride, alkenyl-substituted succinic acid anhydride, dodecenyl succinic acid anhydride, maleic acid anhydride, Tricarballylic anhydride, nadic anhydride, methyl nadic anhydride, linoleic acid adduct with maleic anhydride, alkylated terminal alkylene tetrahydrophthalic anhydride, methyl tetrahydrophthalic anhydride, tetrahydrophthalic anhydride, hexahydro Phthalic anhydride, pyromellitic dianhydride, trimellitic anhydride, phthalic anhydride, tetrachlorophthalic anhydride, tetrabromophthalic anhydride, dichloromaleic anhydride
- N, N-dialkylurea derivative examples include p-chlorophenyl-N, N-dimethylurea (Monuron), 3-phenyl-1,1-dimethylurea (Phenuron), and 3,4-dichlorophenyl-N, N. -Dimethylurea (Diuron), N- (3-chloro-4-methylphenyl) -N ', N'-dimethylurea (Chlortoluron) and the like.
- tertiary amine examples include benzyldimethylamine, 2,4,6-tris (dimethylaminomethyl) phenol, 2- (dimethylaminomethyl) phenol, and 2,4,4 incorporated in a poly (p-vinylphenol) matrix.
- examples thereof include 6-tris (dimethylaminomethyl) phenol, triethylenediamine, N, N-dimethylpiperidine and the like.
- imidazole compound examples include C1-C12 alkylene imidazole, N-aryl imidazole, 2-methylimidazole, 2-ethyl-2-methylimidazole, N-butylimidazole, 1-cyanoethyl-2-undecylimidazolium trimellitate, epoxy
- a photopolymerization initiator may be added to the core-shell polymer-containing epoxy resin composition.
- photopolymerization initiators include onium salts such as aromatic sulfonium salts and aromatic iodonium salts with anions such as hexafluoroantimonate, hexafluorophosphate, and tetraphenylborate, and light such as aromatic diazonium salts and metallocene salts.
- Examples include cationic polymerization initiators (photoacid generators). These photopolymerization initiators may be used alone or in combination of two or more.
- a reinforcing agent other than the component (B), rubber-modified epoxy resin, and urethane-modified epoxy resin is required. Can be used according to.
- the reinforcing agent is not particularly limited, but is, for example, an elastomer type, containing a urethane group and / or a urea group, and having a terminal isocyanate group, and all or part of the terminal isocyanate group is Examples include so-called blocked isocyanate capped with various blocking agents having an active hydrogen group. In particular, a compound in which all of the terminal isocyanate groups are capped with a blocking agent is preferable.
- Such a compound can be prepared, for example, by reacting an organic polymer having an active hydrogen-containing group at the terminal with an excess of a polyisocyanate compound to have a urethane group and / or a urea group in the main chain and an isocyanate group at the terminal. It is obtained by capping all or part of the isocyanate group with a blocking agent having an active hydrogen group after or simultaneously with the polymer (urethane prepolymer).
- a polyether polymer As the main chain skeleton constituting the organic polymer having an active hydrogen-containing group at the terminal, a polyether polymer, a polyacrylic polymer, a polyester polymer, a polydiene polymer, a saturated hydrocarbon polymer (polyolefin) ) And polythioether polymers.
- Examples of the active hydrogen-containing group constituting the organic polymer having an active hydrogen-containing group at the terminal include a hydroxyl group, an amino group, an imino group, and a thiol group.
- a hydroxyl group, an amino group, and an imino group are preferable from the viewpoint of availability, and a hydroxyl group is more preferable from the viewpoint of easy handling (viscosity) of the obtained reinforcing agent.
- organic polymer having an active hydrogen-containing group at the terminal examples include a polyether polymer having a hydroxyl group at the terminal (polyether polyol), and a polyether polymer having an amino group and / or an imino group at the terminal (polyether amine). ), Polyacryl polyol, polyester polyol, diene polymer having a hydroxyl group at the terminal (polydiene polyol), saturated hydrocarbon polymer having a hydroxyl group at the terminal (polyolefin polyol), polythiol compound, polyamine compound, and the like.
- polyether polyol, polyether amine, and polyacryl polyol are excellent in compatibility with the component (A), the glass transition temperature of the organic polymer is relatively low, and the resulting cured product is low in temperature. It is preferable because of its excellent impact resistance.
- polyether polyols and polyether amines are more preferred because the resulting organic polymer has a low viscosity and good workability, and polyether polyols are particularly preferred.
- the organic polymer having an active hydrogen-containing group at the terminal used when preparing the urethane prepolymer that is a precursor of the reinforcing agent may be used alone or in combination of two or more.
- the number average molecular weight of the organic polymer having an active hydrogen-containing group at the end is preferably from 800 to 7000, more preferably from 1500 to 5000, and particularly preferably from 2000 to 4000 in terms of polystyrene equivalent molecular weight measured by GPC.
- the polyether polymer essentially has the general formula (1): -R 1 -O- (1) (Wherein R 1 is a linear or branched alkylene group having 1 to 14 carbon atoms), and R 1 in the general formula (1) is a carbon atom. A linear or branched alkylene group having 1 to 14 or 2 to 4 is preferable. Specific examples of the repeating unit represented by the general formula (1) include —CH 2 O—, —CH 2 CH 2 O—, —CH 2 CH (CH 3 ) O—, —CH 2 CH (C 2 H 5 ) O—, —CH 2 C (CH 3 ) 2 O—, —CH 2 CH 2 CH 2 CH 2 O— and the like.
- the main chain skeleton of the polyether polymer may be composed of only one type of repeating unit, or may be composed of two or more types of repeating units.
- a polymer composed mainly of a propylene oxide polymer having a propylene oxide repeating unit of 50% by weight or more is preferred because of its relatively low viscosity.
- Polytetramethylene glycol (PTMG) obtained by ring-opening polymerization of tetrahydrofuran is preferable because it has low Tg and excellent low-temperature characteristics and high heat resistance.
- the polyether polyol is a polyether polymer having a hydroxyl group at the terminal
- the polyether amine is a polyether polymer having an amino group or an imino group at the terminal.
- polyacrylic polyol examples include a polyol having a (meth) acrylic acid alkyl ester (co) polymer as a skeleton and a hydroxyl group in the molecule.
- a polyacryl polyol obtained by copolymerizing a hydroxyl group-containing (meth) acrylic acid alkyl ester monomer such as 2-hydroxyethyl methacrylate is preferred.
- polyester polyol examples include polybasic acids such as maleic acid, fumaric acid, adipic acid, and phthalic acid, and acid anhydrides thereof, ethylene glycol, propylene glycol, 1,4-butanediol, 1,6-hexanediol, Examples thereof include polymers obtained by polycondensation with polyhydric alcohols such as diethylene glycol, dipropylene glycol and neopentyl glycol in the presence of an esterification catalyst in a temperature range of 150 to 270 ° C. Also included are ring-opening polymers such as ⁇ -caprolactone and valerolactone, and active hydrogen compounds having two or more active hydrogens such as polycarbonate diol and castor oil.
- polybasic acids such as maleic acid, fumaric acid, adipic acid, and phthalic acid
- acid anhydrides thereof ethylene glycol, propylene glycol, 1,4-butanediol, 1,6-hexanedi
- polydiene polyol examples include polybutadiene polyol, polyisoprene polyol, polychloroprene polyol and the like, and polybutadiene polyol is particularly preferable.
- Group polyisocyanates can be mentioned. Among these, aliphatic polyisocyanates are preferable from the viewpoint of heat resistance, and isophorone diisocyanate and hexamethylene diisocyanate are more preferable from the viewpoint of availability.
- the blocking agent examples include a primary amine blocking agent, a secondary amine blocking agent, an oxime blocking agent, a lactam blocking agent, an active methylene blocking agent, an alcohol blocking agent, a mercaptan blocking agent, and an amide.
- Blocking agents, imide-based blocking agents, heterocyclic aromatic compound-based blocking agents, hydroxy-functional (meth) acrylate-based blocking agents, and phenol-based blocking agents are preferable, and a hydroxy functional (meth) acrylate block agent and a phenol block agent are more preferable.
- a phenolic blocking agent is more preferable.
- Examples of the primary amine blocking agent include butylamine, isopropylamine, dodecylamine, cyclohexylamine, aniline, benzylamine and the like.
- Examples of the secondary amine blocking agent include dibutylamine, diisopropylamine, dicyclohexylamine, diphenylamine, dibenzylamine, morpholine, and piperidine.
- Examples of the oxime blocking agent include formaldoxime, acetoaldoxime, acetoxime, methyl ethyl ketoxime, diacetyl monooxime, cyclohexane oxime and the like.
- lactam blocking agent examples include ⁇ -caprolactam, ⁇ -valerolactam, ⁇ -butyrolactam, ⁇ -butyrolactam and the like.
- active methylene-based blocking agent examples include ethyl acetoacetate and acetylacetone.
- Examples of the alcohol blocking agent include methanol, ethanol, propanol, isopropanol, butanol, amyl alcohol, cyclohexanol, 1-methoxy-2-propanol, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, propylene glycol monomethyl ether, benzyl alcohol Methyl glycolate, butyl glycolate, diacetone alcohol, methyl lactate, ethyl lactate and the like.
- Examples of the mercaptan-based blocking agent include butyl mercaptan, hexyl mercaptan, decyl mercaptan, t-butyl mercaptan, thiophenol, methylthiophenol, and ethylthiophenol.
- Examples of the amide blocking agent include acetic acid amide and benzamide.
- Examples of the imide-based blocking agent include succinimide and maleic imide.
- Examples of the heterocyclic aromatic compound blocking agent include imidazoles such as imidazole and 2-ethylimidazole, pyrroles such as pyrrole, 2-methylpyrrole, and 3-methylpyrrole, pyridine, 2-methylpyridine, and 4-methyl. Examples thereof include pyridines such as pyridine, and diazabicycloalkenes such as diazabicycloundecene and diazabicyclononene.
- the hydroxy functional (meth) acrylate blocking agent may be a (meth) acrylate having one or more hydroxyl groups.
- Specific examples of hydroxy functional (meth) acrylate blocking agents include 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, 4-hydroxybutyl (meth) acrylate, 2-hydroxybutyl (meth) An acrylate etc. are mentioned.
- the phenolic blocking agent contains at least one phenolic hydroxyl group, that is, a hydroxyl group directly bonded to a carbon atom of an aromatic ring.
- the phenolic compound may have two or more phenolic hydroxyl groups, but preferably contains only one phenolic hydroxyl group.
- the phenolic compound may contain other substituents, but these substituents are preferably those that do not react with isocyanate groups under the conditions of the capping reaction, and are preferably alkenyl groups and allyl groups.
- substituents include linear, branched, or cycloalkyl alkyl groups; aromatic groups (eg, phenyl, alkyl-substituted phenyl, alkenyl-substituted phenyl, etc.); aryl-substituted alkyl groups; phenol-substituted alkyl groups Can be mentioned.
- phenolic blocking agent examples include phenol, cresol, xylenol, chlorophenol, ethylphenol, allylphenol (especially o-allylphenol), resorcinol, catechol, hydroquinone, bisphenol, bisphenol A, bisphenol AP (1,1- Bis (4-hydroxylphenyl) -1-phenylethane), bisphenol F, bisphenol K, bisphenol M, tetramethylbiphenol and 2,2′-diallyl-bisphenol A.
- the blocking agent is preferably bonded to the end of the polymer chain of the urethane prepolymer in such a manner that the terminal to which it is bonded no longer has a reactive group.
- the blocking agent may be used alone or in combination of two or more.
- the toughening agent may contain residues of crosslinkers, residues of chain extenders, or both.
- the molecular weight of the crosslinking agent is preferably 750 or less, more preferably 50 to 500, and a polyol or polyamine compound having at least three hydroxyl groups, amino groups and / or imino groups per molecule.
- Crosslinkers are useful for imparting branching to the toughener and increasing the functionality of the toughener (ie, the number of capped isocyanate groups per molecule).
- the molecular weight of the chain extender is preferably 750 or less, more preferably 50 to 500, and a polyol or polyamine compound having two hydroxyl groups, amino groups and / or imino groups per molecule. Chain extenders are useful for increasing the molecular weight of the toughening agent without increasing functionality.
- crosslinking agent and chain extender include trimethylolpropane, glycerin, trimethylolethane, ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, sucrose, sorbitol, pentaerythritol, ethylenediamine, triethanolamine, monoethanol.
- examples include amine, diethanolamine, piperazine, and aminoethylpiperazine.
- Resorcinol catechol, hydroquinone, bisphenol, bisphenol A, bisphenol AP (1,1-bis (4-hydroxylphenyl) -1-phenylethane), bisphenol F, bisphenol K, bisphenol M, tetramethylbiphenol, 2,2 Also included are compounds having two or more phenolic hydroxyl groups, such as' -diallyl-bisphenol A.
- the reinforcing agent is, for example, general formula (2): A- (NR 2 —C ( ⁇ O) —X) a (2) (Wherein, a R 2 s are each independently a hydrocarbon group having 1 to 20 carbon atoms. A represents the average number of capped isocyanate groups per molecule, 1.1 or more. It is preferably 1.5 to 8, more preferably 1.7 to 6, and particularly preferably 2 to 4.
- X is a residue obtained by removing an active hydrogen atom from the blocking agent. Is a residue obtained by removing a terminal isocyanate group from an isocyanate-terminated prepolymer.
- the number average molecular weight of the reinforcing agent is preferably 2000 to 40000, more preferably 3000 to 30000, and particularly preferably 4000 to 20000 in terms of polystyrene-converted molecular weight measured by GPC.
- the molecular weight distribution (ratio of weight average molecular weight to number average molecular weight) is preferably 1 to 4, more preferably 1.2 to 3, and particularly preferably 1.5 to 2.5.
- the amount used is preferably 1 to 50 parts by weight, more preferably 5 to 30 parts by weight, and particularly preferably 10 to 20 parts by weight with respect to 100 parts by weight of component (A). If it is less than 1 part by weight, there are cases where the modifying effects such as toughness, impact resistance and adhesion are not sufficient, and if it exceeds 50 parts by weight, the elastic modulus of the resulting cured product may be low.
- a reinforcing agent may be used independently and may be used together 2 or more types.
- numerator can be used as needed.
- a low molecular compound having a molecular weight of less than 300 and having at least one double bond in the molecule can be added.
- the low molecular weight compound has a function of adjusting viscosity, physical properties of a cured product, and curing speed by using in combination with the radical curable resin, and functions as a so-called reactive diluent for the radical curable resin.
- a radical polymerization initiator can be added to the resin composition of the present invention.
- the radical polymerization initiator is preferably a potential type that is activated when the temperature is increased (preferably, about 50 ° C. to about 150 ° C.).
- radical curable resins examples include unsaturated polyester resins, polyester (meth) acrylates, epoxy (meth) acrylates, urethane (meth) acrylates, polyether (meth) acrylates, and acrylated (meth) acrylates. These may be used alone or in combination.
- Specific examples of the radical curable resin include compounds described in the pamphlet of WO2014 / 115778.
- specific examples of the low molecular weight compound and the radical polymerization initiator include compounds described in WO2014 / 115778 pamphlet.
- the resin composition can be partially cured by selective polymerization of the radical curable resin. Become. This partial curing can increase the viscosity of the composition after coating and improve the wash-off resistance.
- the uncured adhesive composition is partially dissolved, scattered, or deformed by the shower water pressure during the washing shower process. The corrosion resistance of the coated steel sheet may be adversely affected, and the rigidity of the steel sheet may be reduced.
- the “hardness to be washed off” means resistance to this problem.
- this partial curing can provide a function of temporarily fixing (temporarily adhering) the substrates to each other until the composition is completely cured.
- the free radical initiator is preferably activated by heating to 80 ° C. to 130 ° C., more preferably 100 ° C. to 120 ° C.
- a filler in the present invention, can be used as necessary.
- the filler include reinforcing silica fillers such as dry silica such as hydrophobic fumed silica surface-treated with polydimethylsiloxane, wet silica, aluminum silicate, magnesium silicate, calcium silicate, dolomite and carbon black.
- Plate-like fillers such as talc and wollastonite; colloidal calcium carbonate, heavy calcium carbonate, calcium oxide, magnesium carbonate, titanium oxide, ferric oxide, aluminum fine powder, zinc oxide, activated zinc white and the like.
- a microballoon having an average particle size of up to 200 ⁇ m and a density of up to 0.2 g / cc can also be used.
- the particle size is preferably about 25 to 150 ⁇ m and the density is preferably about 0.05 to about 0.15 g / cc.
- Examples of commercially available microballoons include Dualite manufactured by Dualite Corporation, Expandel manufactured by Akzo Nobel, and Microsphere manufactured by Matsumoto Yushi Seiyaku.
- an organic peroxide in using the core-shell polymer-containing epoxy resin composition of the present invention, an organic peroxide, a dehydrating agent such as calcium oxide, an expanding agent such as an azo type chemical blowing agent or a thermally expandable microballoon, or a fiber such as an aramid pulp Pulp, antioxidant, leveling agent, antifoaming agent, silane coupling agent, antistatic agent, flame retardant, lubricant, low shrinkage agent, thermoplastic resin, drying agent, dispersant, curing accelerator, chain transfer agent, light Sensitizer, reducing agent, plasticizer, flexibilizer, liquid rubber (reactive / non-reactive), adhesion-imparting agent (including primer), dye, pigment, stabilizer, UV absorber, Diluents (reactive / non-reactive), organic solvents and the like can be mixed in various production stages.
- a dehydrating agent such as calcium oxide
- an expanding agent such as an azo type chemical blowing agent or a thermally expandable microballoon
- the core-shell polymer-containing epoxy resin composition of the present invention can be prepared by the method described in International Publication No. 2005/28546 pamphlet. Specifically, an aqueous medium dispersion in which the core-shell polymer (B) is dispersed in an aqueous medium (an aqueous latex containing the core-shell polymer (specifically, a reaction mixture after producing the core-shell polymer by emulsion polymerization)) ) Is mixed with an organic solvent having a solubility in water at 20 ° C.
- the first step includes an operation of mixing an aqueous latex with an organic solvent having a solubility in water at 20 ° C. of preferably 5% by weight or more and 40% by weight or less (particularly 30% by weight or less).
- an organic solvent having a solubility in water at 20 ° C. of preferably 5% by weight or more and 40% by weight or less (particularly 30% by weight or less).
- solubility of the organic solvent When the solubility of the organic solvent is less than 5% by weight, mixing with the aqueous medium dispersion containing the core-shell polymer may be somewhat difficult. When the solubility exceeds 40% by weight, it may be difficult to separate and recover the core-shell polymer (described later) from the liquid phase (mainly the aqueous phase) in the second step.
- Examples of the organic solvent having a solubility in water at 20 ° C. of 5 wt% to 40 wt% include ketones such as methyl ethyl ketone, esters such as methyl formate, methyl acetate, and ethyl acetate, diethyl ether, ethylene glycol diethyl ether, Examples include ethers such as tetrahydropyran, acetals such as methylal, alcohols such as n-butyl alcohol, isobutyl alcohol, and sec-butyl alcohol. These organic solvents may be used alone or in combination of two or more.
- the organic solvent used in the first step may be a mixed organic solvent as long as the solubility in water at 20 ° C. is 5 wt% or more and 40 wt% or less as a whole.
- ketones such as methyl propyl ketone, diethyl ketone, methyl isobutyl ketone and ethyl butyl ketone
- esters such as diethyl carbonate, butyl formate, propyl acetate and butyl acetate
- ethers such as diisopropyl ether and dibutyl ether, pentane and hexane
- Aliphatic hydrocarbons such as heptane and octane
- aromatic hydrocarbons such as benzene, toluene and xylene
- halogenated hydrocarbons such as methylene chloride and chloroform, and acetone, cyclohexanone, etc.
- the organic solvent used in the first step is preferably one having a specific gravity lighter than water from the viewpoint of facilitating removal of the liquid phase (mainly the aqueous phase) in the second step described later.
- the amount of the organic solvent mixed with the aqueous latex is preferably 50 parts by weight or more (particularly 60 parts by weight or more) and 250 parts by weight or less (particularly 150 parts by weight or less) with respect to 100 parts by weight of the aqueous latex.
- the mixing amount of the organic solvent is less than 50 parts by weight, it may be difficult to form an aggregate of the core-shell polymer contained in the aqueous latex.
- the amount of the organic solvent mixed exceeds 300 parts by weight, the amount of water required for obtaining the core-shell polymer loose aggregate thereafter increases, and the production efficiency may decrease.
- a well-known thing can be used for mixing operation of the said aqueous latex and an organic solvent.
- a general apparatus such as a stirring tank with a stirring blade may be used, or a static mixer (static mixer), a line mixer (a system in which a stirring apparatus is incorporated in a part of piping), or the like may be used.
- the first step includes an operation of adding and mixing excess water after the operation of mixing the aqueous latex and the organic solvent. As a result, phase separation occurs, and an agglomerated state of the core-shell polymer can be obtained.
- electrolyte such as the water-soluble emulsifier or dispersant, the water-soluble polymerization initiator, or the reducing agent used in the preparation of the aqueous latex can be eluted into the aqueous phase.
- the amount of water mixed is 40 parts by weight or more (particularly 60 parts by weight or more) and 1000 parts by weight or less (particularly 700 parts by weight or less) with respect to 100 parts by weight of the organic solvent used when mixing with the aqueous latex. preferable. If the amount of water mixed is less than 40 parts by weight, it may be difficult to obtain the core-shell polymer as a loose aggregate. When the amount of water exceeds 1000 parts by weight, the concentration of the organic solvent in the agglomerated core-shell polymer becomes low, so the time required to redisperse the agglomerated core-shell polymer in the second step described later is long. In some cases, the dispersibility of the core-shell polymer may decrease.
- the second step includes an operation of separating and recovering the slowly aggregated core-shell polymer from the liquid phase to obtain a core-shell polymer dope.
- water-soluble impurities such as an emulsifier can be separated and removed from the core-shell polymer.
- a method for separating and recovering the agglomerated core-shell polymer from the liquid phase for example, since the agglomerated core-shell polymer is generally floatable with respect to the liquid phase, when the agitation tank is used in the first step, Examples of the method include discharging a liquid phase (mainly an aqueous phase) from the bottom, and filtering using a filter paper, a filter cloth, or a metal screen having a relatively wide opening.
- a liquid phase mainly an aqueous phase
- the amount of the organic solvent contained in the core-shell polymer loose agglomerates is preferably 30% by weight or more (particularly 35% by weight or more), preferably 95% by weight or less (particularly 90% by weight) based on the total weight of the slow agglomerates. Or less).
- the content of the organic solvent is less than 30% by weight, the time required for re-dispersing the core-shell polymer dope in the organic solvent (described later) is prolonged, and irreversible aggregates are likely to remain. May occur.
- the content of the organic solvent exceeds 95% by weight, a large amount of water dissolves and remains in the organic solvent, which may cause the core-shell polymer to aggregate in the third step. .
- the amount of the organic solvent contained in the core-shell polymer aggregate is determined by drying the core-shell polymer aggregate at 120 ° C. for 15 minutes after precise weighing, and then reducing the organic solvent contained in the aggregate. It is calculated
- the second step includes an operation of mixing the core-shell polymer aggregate with an organic solvent. Since the core-shell polymer is aggregated in a loose state, the core-shell polymer can be easily redispersed in the state of primary particles in the organic solvent by mixing with the organic solvent.
- Examples of the organic solvent used in the second step include those exemplified as those that can be used in the first step. By using such an organic solvent, water contained in the core-shell polymer can be removed by azeotroping with water when the organic solvent is distilled off in the third step described later. Further, the organic solvent used in the second step may be the same as or different from the organic solvent used in the first step.
- the mixing amount of the organic solvent used in the second step is 40 parts by weight or more (more preferably 200 parts by weight or more), 1400 parts by weight or less (more preferably 1000 parts by weight or less) with respect to 100 parts by weight of the core-shell polymer aggregate. ).
- the mixing amount of the organic solvent is less than 40 parts by weight, the core-shell polymer is difficult to uniformly disperse in the organic solvent, and the agglomerated core-shell polymer may remain as a lump, or the viscosity may increase and handling may be difficult. .
- the agglomerated core-shell polymer is separated and recovered from the liquid phase, and again an organic solvent having a solubility in water at 20 ° C. of 5 wt% to 40 wt% After mixing, it is preferable to perform one or more operations of further mixing with excess water to obtain a core-shell polymer loose aggregate. In addition, this makes it possible to lower the remaining amount of water-soluble impurities such as emulsifiers contained in the core-shell polymer dope.
- the third step includes an operation for replacing the organic solvent in the organic solvent solution of the core-shell polymer obtained in the second step with the epoxy resin.
- a core-shell polymer-containing epoxy resin composition in which the core-shell polymer is dispersed in the form of primary particles can be obtained.
- water remaining in the core-shell polymer aggregate can be distilled off azeotropically.
- a well-known method is applicable as a method of distilling off the organic solvent. For example, a method of charging a mixture of an organic solvent solution and the epoxy resin into a tank and distilling under reduced pressure by heating, a method of countercurrently contacting the mixture with a dry gas in the tank, a continuous type using a thin film evaporator And a method using an extruder equipped with a devolatilization mechanism or a continuous stirring tank.
- Conditions such as temperature and time required for distilling off the organic solvent can be appropriately selected within a range that does not impair the quality of the obtained core-shell polymer-containing epoxy resin composition.
- the amount of volatile matter remaining in the core-shell polymer-containing epoxy resin composition can be appropriately selected within a range where there is no problem depending on the purpose of use of the core-shell polymer-containing epoxy resin composition.
- the resin composition of the present invention can be used as a one-component resin composition in which all compounding components are preliminarily blended and stored and cured by heating or light irradiation after coating.
- it is prepared as a two-component or multi-component resin composition comprising a component A containing the component (A) as a main component and a separately prepared component B containing a curing agent.
- B liquid can also be mixed and used before use.
- the resin composition contains 100 parts by weight of the epoxy resin (A) and 1 to 100 parts by weight of the core-shell polymer (B), preferably 100 parts by weight of the epoxy resin (A) and 10 to 70 parts by weight of the core-shell polymer (B). More preferably, it contains 100 parts by weight of the epoxy resin (A) and 20 to 50 parts by weight of the core-shell polymer (B).
- the present invention includes a cured product obtained by curing the resin composition.
- a resin composition in which polymer fine particles are dispersed in the form of primary particles a cured product in which polymer fine particles are uniformly dispersed can be easily obtained by curing the resin composition.
- the polymer fine particles hardly swell and the viscosity of the resin composition is low, a cured product can be obtained with good workability.
- the resin composition of the present invention can be applied by any method. It can be applied at a low temperature of about room temperature, and can be applied by heating as necessary.
- the resin composition of the present invention is extruded onto a substrate in a bead shape, a monofilament shape or a swirl shape using a coating robot, or a mechanical coating method such as a caulking gun or other manual coating means is used. You can also.
- the composition can also be applied to the substrate using a jet spray method or a streaming method.
- the resin composition of this invention is apply
- the resin composition of the present invention When used as an adhesive for vehicles, it is effective to increase the viscosity of the composition in order to improve the “hardness to be washed off”. It is preferable because of its high thixotropy and high viscosity.
- a highly viscous composition can be adjusted to a viscosity that can be applied by heating.
- a polymer compound having a crystalline melting point near the coating temperature of the composition is used as the curable composition of the present invention. It is preferable to blend in.
- the composition has a low viscosity at the coating temperature (easy to apply), and a high viscosity at the temperature in the washing shower step, thus improving the “hardness to be washed off”.
- the polymer compound having a crystalline melting point near the coating temperature include various polyester resins such as crystalline or semicrystalline polyester polyols.
- the resin composition is made into a two-component type, and a curing agent to be used is an amino group or Examples include a method in which a small amount of a curing agent capable of being cured at room temperature such as an amine curing agent having an imino group is used, and a latent curing agent such as dicyandiamide that exhibits activity at high temperatures is used in combination.
- a curing agent capable of being cured at room temperature such as an amine curing agent having an imino group
- a latent curing agent such as dicyandiamide that exhibits activity at high temperatures
- Adhesive substrate When various substrates are bonded using the resin composition of the present invention, for example, wood, metal, plastic, glass or the like can be bonded. It is preferable to join automobile parts, more preferably joining of automobile frames or joining of an automobile frame and other automobile parts.
- the substrate include various plastic substrates such as steel materials such as cold-rolled steel and hot-dip galvanized steel, aluminum materials such as aluminum and coated aluminum, general-purpose plastics, engineering plastics, and composite materials such as CFRP and GFRP. . Since the resin composition of the present invention is excellent in toughness, it is suitable for joining different kinds of substrates having different linear expansion coefficients.
- the resin composition of the present invention can also be used for joining aerospace components, particularly exterior metal components.
- the curing temperature of the resin composition of the present invention is not particularly limited, but when used as a one-pack type resin composition, it is preferably 50 ° C to 250 ° C, more preferably 80 ° C to 220 ° C, and more preferably 100 ° C to 200 ° C. is more preferable, and 130 ° C. to 180 ° C. is particularly preferable.
- it is not particularly limited, but is preferably 0 ° C to 150 ° C, more preferably 10 ° C to 100 ° C, further preferably 15 ° C to 80 ° C, and more preferably 20 ° C to 60 ° C. Is particularly preferred.
- the resin composition of the present invention is used as an automobile adhesive, after the adhesive is applied to an automobile member, the coating is then applied, and the adhesive is cured at the same time as the coating is baked and cured. It is preferable from the viewpoint of process shortening and simplification.
- the core-shell polymer-containing epoxy resin composition of the present invention comprises a molding material, an adhesive, a structural adhesive (preferably a structural adhesive for vehicles and aircraft, a structural adhesive for wind power generation), a fiber or filler reinforced composite material, Sealing materials such as liquid crystal panels, OLED lighting, OLED displays, and other display devices and lighting device sealing materials, casting materials, printed wiring board materials, solder resists, interlayer insulating films, build-up materials, adhesion for FPC Electrical insulation materials such as encapsulants, sealing materials for electronic components such as semiconductors and LEDs, die bonding materials, underfills, semiconductor mounting materials such as ACF, ACP, NCF, NCP, coating materials, fillers, photomolding materials, optical components, It is suitably used as ink and toner.
- a structural adhesive preferably a structural adhesive for vehicles and aircraft, a structural adhesive for wind power generation
- Sealing materials such as liquid crystal panels, OLED lighting, OLED displays, and other display devices and lighting device sealing materials, casting materials, printed wiring board materials,
- the cured product was split in liquid nitrogen, and the frozen fracture surface was scanned with a scanning electron microscope (JSM-6300F, manufactured by JEOL Ltd.). Observation was performed at a magnification of 20,000 times, and the dispersion state was determined using the particle dispersion rate (%) by the following method as an index.
- particle dispersion rate In the obtained scanning electron micrograph at a magnification of 20,000 times, four 5 cm square areas were selected at random, and the particle dispersion rate (%) was calculated using Equation 2 according to the above method, and the average value was calculated. Was used.
- the evaluation criteria for the particle dispersion rate are as follows. Good: Particle dispersion is 70% or more. Poor: The particle dispersion rate is less than 70%.
- volume average particle diameter of rubber particles and core-shell polymer The volume average particle size was measured with a particle size measuring device (Microtrac UPA manufactured by Nikkiso Co., Ltd.). An aqueous latex diluted with deionized water was used as a measurement sample. The measurement is performed by inputting the refractive index of water and the refractive index of each rubber particle or core-shell polymer, and measuring the sample concentration so that the measurement time is 600 seconds and the Signal Level is in the range of 0.6 to 0.8. Adjusted.
- Viscosity of core-shell polymer-containing epoxy resin composition The viscosity of the core-shell polymer-containing epoxy resin composition was measured by using a viscosity measuring epoxy resin composition obtained by the method described below using a digital viscometer DV-II + Pro type manufactured by BROOKFIELD. Depending on the viscosity region, spindle CPE-41 or CPE-52 was used separately, and the viscosity at a measurement temperature of 50 ° C. and a shear rate of 10 / s was measured.
- Tg of core part Using the Tg value of the following homopolymer, the calculation was performed according to the above-mentioned formula 1. Butadiene -85 °C Dimethylsiloxane -123 ° C ⁇ -Methacryloyloxypropylmethyldimethoxysilane 43 ° C n-Butyl acrylate -54 ° C
- Tg of shell part Using the Tg value of the following homopolymer, the calculation was performed according to the above-mentioned formula 1.
- Styrene 100 ° C Methyl methacrylate 105 ° C Acrylonitrile 97 ° C
- 2-Methoxyethyl acrylate -50 °C 4-hydroxybutyl acrylate -40 ° C
- PPP paramentane hydroperoxide
- SSS sodium formaldehyde sulfoxylate
- EDTA 0.003 parts by weight of ferrous sulfate heptahydrate
- the residual monomer was removed by devolatilization under reduced pressure to complete the polymerization, and a polybutadiene rubber latex (R-1) containing polybutadiene rubber as a main component was obtained.
- the volume average particle diameter of the polybutadiene rubber particles contained in the obtained latex was 0.08 ⁇ m.
- Polymerization was started by adding 0.02 part by weight of PHP and subsequently 0.10 part by weight of SFS. 0.025 parts by weight of PHP, 0.0006 parts by weight of EDTA, and 0.003 parts by weight of ferrous sulfate heptahydrate were added every 3 hours from the start of polymerization to 24 hours. At 30 hours after polymerization, the residual monomer was removed by devolatilization under reduced pressure to complete the polymerization, and a polybutadiene rubber latex (R-2) containing polybutadiene rubber as a main component was obtained. The volume average particle diameter of the polybutadiene rubber particles contained in the obtained latex was 0.20 ⁇ m.
- This emulsion was immediately charged all at once into a glass reactor having a thermometer, a stirrer, a reflux condenser, a nitrogen inlet, and an auxiliary material addition device such as a monomer and an emulsifier.
- the reaction was started at 30 ° C. while stirring the system. After 6 hours, the mixture was cooled to 23 ° C. and allowed to stand for 20 hours, the pH of the system was returned to 6.8 with sodium bicarbonate to complete the polymerization, and latex (R-3) containing polyorganosiloxane rubber particles was obtained. .
- the volume average particle diameter of the polyorganosiloxane rubber particles contained in the obtained latex was 0.28 ⁇ m.
- aqueous latex (L-4) containing a core-shell polymer After adding 0.004 parts by weight of EDTA, 0.001 part by weight of ferrous sulfate heptahydrate, and 0.2 parts by weight of SFS, a mixture of 10 parts by weight of MEA, 3 parts by weight of GMA, and 0.04 parts by weight of CHP was added. Added continuously over 85 minutes. After the addition was completed, 0.065 part by weight of CHP was added, and stirring was further continued for 1 hour to complete the polymerization, thereby obtaining an aqueous latex (L-4) containing a core-shell polymer. The polymerization conversion rate of the monomer component was 99% or more. The volume average particle size of the core-shell polymer contained in the obtained aqueous latex was 0.19 ⁇ m.
- TAIC triallyl isocyanurate
- CHP0 0.07 part by weight 2 parts by weight of triallyl isocyanurate (TAIC) and CHP0 0.07 part by weight was added and stirred for 60 minutes.
- TAIC triallyl isocyanurate
- MEA 11.5 parts by weight, BA 0.5 parts by weight, GMA 1 part by weight, and CHP 0.04 parts by weight was continuously added as a shell part component over 85 minutes.
- 0.065 parts by weight of CHP was added, and stirring was further continued for 1 hour to complete the polymerization, thereby obtaining an aqueous latex (L-10) containing a core-shell polymer.
- the polymerization conversion rate of the monomer component was 99% or more.
- the volume average particle size of the core-shell polymer contained in the obtained aqueous latex was 0.19 ⁇ m.
- Production Example 16 Polymerization of core-shell polymer (L-12)
- an aqueous latex containing a core-shell polymer (L) was used in the same manner as in Production Example 15 except that StA 7 parts by weight, AN 4 parts by weight, and GMA 6 parts by weight were used instead of MEA 11 parts by weight and GMA 6 parts by weight. -12) was obtained.
- the polymerization conversion rate of the monomer component was 99% or more.
- the volume average particle diameter of the core-shell polymer contained in the obtained aqueous latex was 0.30 ⁇ m.
- aqueous latex (L-13) containing a core-shell polymer was obtained.
- the polymerization conversion rate of the monomer component was 99% or more.
- the volume average particle size of the core-shell polymer contained in the obtained aqueous latex was 0.11 ⁇ m.
- Production Example 18 Polymerization of core-shell polymer (L-14)
- an aqueous latex (L) containing a core-shell polymer was used in the same manner as in Production Example 17 except that StA 7 parts by weight, AN 4 parts by weight, and GMA 6 parts by weight were used instead of MEA 11 parts by weight and GMA 6 parts by weight. -14) was obtained.
- the polymerization conversion rate of the monomer component was 99% or more.
- the volume average particle size of the core-shell polymer contained in the obtained aqueous latex was 0.11 ⁇ m.
- Example 1 As a reactive diluent (glycidyl ester compound), 120 parts by weight of the epoxy resin composition (A-1) obtained in Production Example 19 (including 30 parts by weight of the core-shell polymer), 10 parts by weight of the above jER (registered trademark) 828EL 10 parts by weight of “Cardura (registered trademark) E10P” (trade name, manufactured by Momentive), 7 parts by weight of dicyandiamide “jER Cure (registered trademark) DICY7” (trade name, manufactured by Mitsubishi Chemical Corporation) as a curing agent, curing accelerator 1 part by weight of aromatic dimethylurea “Dyhard (registered trademark) UR300” (trade name, manufactured by AlzChem GmbH), 3 parts by weight of silica “CAB-O-SIL (registered trademark) TS720” (trade name, manufactured by CABOT) Carbon Black “Monarch® 280” (trade name, CABOT ) 0.3 parts by weight, calcium carbonate “Whiteon SB” (trade name,
- Example 2 (Examples 2 to 6) In Example 1, instead of the epoxy resin composition (A-1), the epoxy resin compositions (A-4), (A-5), (A-10), (A-11), (A-13) ) was used in the same manner as in Example 1, except that each core-shell polymer-containing adhesive composition (B-4), (B-5), (B-10), (B-11), (B-13) was used. ) To obtain a symmetrical wedge impact test piece. These were designated as Examples 2 to 6, respectively.
- Example 1 In Example 1, instead of the epoxy resin composition (A-1), the epoxy resin compositions (A-2), (A-3), (A-6), (A-7), (A-8) ), (A-9), (A-12), and (A-14), respectively, and in the same manner as in Example 1, the core-shell polymer-containing adhesive composition (B-2), (B-3) ), (B-6), (B-7), (B-8), (B-9), (B-12), and (B-14) were obtained, respectively, and symmetrical wedge impact test pieces were prepared. These were designated as Comparative Examples 1 to 8, respectively. Table 2 summarizes the results of various physical property evaluations of Examples 1 to 6 and Comparative Examples 1 to 8.
- Example 1 (In case of polybutadiene rubber core 1; Example 1, Comparative Examples 1 and 2) As shown in Table 2, it was found that in Comparative Example 1, the viscosity of the epoxy resin composition was higher than that in Example 1, and the impact resistance adhesion at 23 ° C. and ⁇ 40 ° C. was low. In Comparative Example 2, the viscosity of the epoxy resin composition was almost the same as in Example 1, but the impact resistance adhesion at 23 ° C. and ⁇ 40 ° C. was low, and it was found that no strength was obtained at ⁇ 40 ° C. It was. It was also found that the core-shell polymer does not disperse in the primary particles during curing because no epoxy group-containing monomer is used in the shell portion of the core-shell polymer. In contrast, Example 1 was found to have a lower viscosity of the epoxy resin composition and higher impact resistance adhesion at both 23 ° C. and ⁇ 40 ° C. than Comparative Examples 1 and 2.
- Comparative Example 5 the viscosity of the epoxy resin composition is substantially the same as in Examples 2 to 4, but the impact resistance adhesion at 23 ° C. is somewhat low, and the impact resistance strength at ⁇ 40 ° C. is not at all. It was also found that since the epoxy group-containing monomer is not used in the shell part of the core-shell polymer, the core-shell polymer is not dispersed in the primary particles during curing. Comparative Example 6 was found to have a higher epoxy resin viscosity than Examples 2 to 4 and low impact adhesion at 23 ° C. and ⁇ 40 ° C. On the other hand, in Examples 2 to 4, it was found that the viscosity of the epoxy resin composition was lower and the impact resistance adhesion at 23 ° C. and ⁇ 40 ° C. was higher than those of Comparative Examples 3 to 6.
- Example 5 Comparative Example 7
- Table 2 it was found that in Comparative Example 7, the viscosity of the epoxy resin composition was higher than that in Example 5, and the impact resistance strength at 23 ° C. did not appear at all.
- Example 5 was found to have a lower viscosity of the epoxy resin composition and higher impact resistance adhesion at 23 ° C. than Comparative Example 7.
- Example 6 Comparative Example 8
- Table 2 it was found that in Comparative Example 8, the viscosity of the epoxy resin composition was higher than that in Example 6, and the impact resistance strength at 23 ° C. was not exhibited at all.
- Example 6 was found to have a lower viscosity of the epoxy resin composition and higher impact resistance adhesion at 23 ° C. than Comparative Example 8.
- aqueous latex L-15
- the polymerization conversion rate of the monomer component was 99% or more.
- the volume average particle size of the core-shell polymer contained in the obtained aqueous latex was 0.19 ⁇ m.
- Example 7 In Example 1, instead of 120 parts by weight of the epoxy resin composition (A-1) (including 30 parts by weight of the core-shell polymer) and 10 parts by weight of the above jER (registered trademark) 828EL, the epoxy resin composition (A-15) To (A-19) 75 parts by weight (including 30 parts by weight of the core-shell polymer) and 55 parts by weight of the above jER (registered trademark) 828EL were used in the same manner as in Example 1 to obtain the core-shell polymer-containing adhesive composition (B -15 to 19) were obtained, and symmetrical wedge impact test pieces were prepared. These were designated as Examples 7 to 11, respectively.
- Example 9 In Example 1, in place of 120 parts by weight of the epoxy resin composition (A-1) (including 30 parts by weight of the core-shell polymer) and 10 parts by weight of the jER (registered trademark) 828EL, the epoxy resin composition (A-20) A core-shell polymer-containing adhesive composition (B-20) was obtained in the same manner as in Example 1 except that 75 parts by weight (including 30 parts by weight of the core-shell polymer) and 55 parts by weight of the above jER (registered trademark) 828EL were used. Symmetric wedge impact specimens were prepared. These were designated as Comparative Example 9, respectively. The results of impact resistance adhesion at 23 ° C. in Examples 7 to 11 and Comparative Example 9 are summarized in Table 4.
- Example 7 the impact resistance adhesion at ⁇ 30 ° C. was 21.1 kN / m, and the viscosity at 50 ° C. was 9200 mPa ⁇ s.
- Example 8 the impact resistance adhesion at ⁇ 30 ° C. was 19.9 kN / m, and the viscosity at 50 ° C. was 9800 mPa ⁇ s.
- Example 9 the viscosity at 50 ° C. was 13300 mPa ⁇ s.
- Example 11 the impact resistance adhesion at ⁇ 30 ° C. was 24.4 kN / m.
- Comparative Example 9 had lower impact resistance adhesion at 23 ° C. than Examples 7-11. In contrast, Examples 7 to 11 show higher impact resistance adhesion at 23 ° C. than Comparative Example 9.
- the examples of the present invention particularly examples in which an acrylate ester is used in the shell portion
- the examples of the present invention show excellent impact resistance at ⁇ 30 ° C.
- the examples of the present invention exhibit excellent low viscosity characteristics.
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Abstract
Description
本発明に用いられ得るエポキシ樹脂は、エポキシ基を有する化合物であれば特に制限されないが、本発明に用いられ得るエポキン樹脂はポリエポキシドとも言われるエポキシ樹脂であることが好ましい。前記のエポキシ樹脂としては、ビスフェノールA、ビスフェノールF、ビフェノール、フェノール類ノボラック等の多価フェノールとエピクロルヒドリンの付加反応生成物などのポリグリシジルエーテル、アニリン、ジアミノベンゼン、アミノフェノール、フェニレンジアミン、ジアミノフェニルエーテル等のモノアミンおよび多価アミンより誘導される多価グリシジルアミン化合物、シクロヘキシルエポキシ等の脂環式エポキシ構造を有する脂環式エポキシ樹脂、多価アルコール類とエピクロルヒドリンとの付加反応生成物、これらの一部の水素を臭素等のハロゲン元素で置換したハロゲン化エポキシ樹脂、アリルグリシジルエーテル等の不飽和モノエポキシドを含む単量体を重合して得られるホモポリマーもしくはコポリマーなどが例示される。これらは1種または2種以上の混合物であっても良い。多価フェノールより合成される多くのポリエポキシドは、例えば米国特許第4431782号に開示されている。ポリエポキシドの例としては更に、米国特許第3804735号、同第3892819号、同第3948698号、同第4014771号、及び、エポキシ樹脂ハンドブック(日刊工業新聞社、昭和62年)に開示されているものが挙げられる。
前記のエポキシ樹脂の中でも、ビスフェノールA型エポキシ樹脂やビスフェノールF型エポキシ樹脂は、得られる硬化物の弾性率が高く、耐熱性および接着性に優れ、比較的安価である為好ましく、ビスフェノールA型エポキシ樹脂が特に好ましい。
前記ゴム変性エポキシ樹脂は、ゴムとエポキシ基含有化合物とを反応させて得た、1分子当り平均して、エポキシ基を1.1個以上有する反応生成物である。ゴムとしては、アクリロニトリルブタジエンゴム(NBR)、スチレンブタジエンゴム(SBR)、水素添加ニトリルゴム(HNBR)、エチレンプロピレンゴム(EPDM)、アクリルゴム(ACM)、ブチルゴム(IIR)、ブタジエンゴム、ポリプロピレンオキシドやポリエチレンオキシドやポリテトラメチレンオキシド等のポリオキシアルキレンなどのゴム系重合体を挙げることができる。該ゴム系重合体は、アミノ基、ヒドロキシ基、またはカルボキシル基等の反応性基を末端に有するものが好ましい。これらのゴム系重合体とエポキシ樹脂とを公知の方法により適宜の配合比にて反応させた生成物が本発明に使用されるゴム変性エポキシ樹脂である。これらの中でも、アクリロニトリル-ブタジエンゴム変性エポキシ樹脂や、ポリオキシアルキレン変性エポキシ樹脂が、得られる樹脂組成物の接着性や耐衝撃剥離接着性の観点から好ましく、アクリロニトリル-ブタジエンゴム変性エポキシ樹脂がより好ましい。なお、アクリロニトリル-ブタジエンゴム変性エポキシ樹脂は、例えば、カルボキシル基末端NBR(CTBN)とビスフェノールA型エポキシ樹脂との反応により得られる。また、ポリオキシアルキレン変性エポキシ樹脂は、例えば、アミノ基末端ポリオキシアルキレンとビスフェノールA型エポキシ樹脂との反応により得られる。
ゴム変性エポキシ樹脂は、単独でまたは2種以上を組み合わせて使用することができる。
ウレタン変性エポキシ樹脂は、単独でまたは2種以上を組み合わせて使用することができる。
本発明におけるコアシェルポリマーは、その体積平均粒子径が、0.01~1μmであることを要し、好ましい粘度、及び、耐衝撃接着性改良効果を有するコアシェルポリマー含有エポキシ樹脂組成物を得る観点から、好ましくは0.05~0.8μmであることである。また異なる体積平均粒子径のコアシェルポリマーの混合物であってもよく、それぞれの体積平均粒子径付近に粒子頻度のピークを有するマルチピーク型のコアシェルポリマーであってもよい。異なる体積平均粒子径のコアシェルポリマーの混合物を用いる場合、例えば、0.01~0.20μm、好ましくは0.05~0.15μmに体積平均粒子径を有するコアシェルポリマーと、0.10~1.0μm、好ましくは0.15~0.9μmに体積平均粒子径を有するコアシェルポリマーとを混合してもよい。こうした混合型又はマルチピーク型(例えば、2ピーク型)のコアシェルポリマーによれば、コアシェルポリマー含有エポキシ樹脂組成物が低粘度化し、取り扱い易くなる。
本発明におけるゴム状重合体を構成するポリマーは、架橋されているのが好ましい。架橋ゴム状重合体は、適切な溶媒に対して膨潤しうるけれども実質的には溶解しない。また、架橋ゴム状重合体はエポキシ樹脂に不溶である。ゴム状重合体又は架橋ゴム状重合体のゲル分は例えば60重量%以上、好ましくは80重量%以上であり、より好ましくは90重量%以上で、さらに好ましくは95重量%以上である。ゴム状重合体又は架橋ゴム状重合体を構成するポリマーのTgは0℃未満であり、好ましくは-10℃未満、より好ましくは-20℃未満、さらに好ましくは-40℃未満である。
また、前記ゴム状重合体は、架橋度を調節するために、多官能性単量体を含んでいても良い。多官能性単量体としては、ジビニルベンゼン、ブタンジオールジ(メタ)アクリレート、(イソ)シアヌル酸トリアリル、(メタ)アクリル酸アリル、イタコン酸ジアリル、フタル酸ジアリル等が例示できる。多官能性単量体の使用量はゴム状重合体全体の重量に対して10重量%以下、好ましくは5重量%以下、更に好ましくは3重量%以下である。使用量が10重量%を超えると、本発明のコアシェルポリマーが有する耐衝撃接着性改良効果が低下する傾向がある。なお多官能性単量体を使用する場合、その使用量は、ゴム状重合体全体の重量に対して0.1重量%以上、1重量%以上であってもよい。
本発明におけるシェル部は、シェル形成用単量体を重合した重合体(シェルポリマー)からなるが、本発明に係るコアシェルポリマーとエポキシ樹脂との相溶性を向上させ、本発明に係るコアシェルポリマー含有エポキシ樹脂組成物、又は、その硬化物中においてコアシェルポリマーが一次粒子の状態で分散することを可能にする役割を担う。
さらに、本発明におけるコアシェルポリマー含有エポキシ樹脂組成物に良好な耐衝撃接着性改良効果を付与するために本発明に係るシェル部のTgは、25℃未満であり、20℃未満とすることが好ましく、より好ましくは0℃未満、さらに好ましくは-20℃未満、特に好ましくは-40℃未満である。また、シェル部のTgは、単独重合体、又は、2種以上の単量体の共重合物として20℃未満で有れば特に限定されるものではない。シェル部のTgの下限は、例えば-80℃又は-70℃であってもよい。共重合物のガラス転移温度Tgnは以下に示すFOX式(数式1)で算出することが可能である。
前記シェル部は、エポキシ基を持つ単量体をその構成単位として含有する。このエポキシ基をもつ単量体は、本発明に係るコアシェルポリマーがエポキシ樹脂組成物の硬化後もその硬化物中で一次粒子の状態で分散するために、コアシェルポリマーとエポキシ樹脂とを化学結合させる観点からシェル形成用単量体の一部として使用される単量体であり、同一分子内にエチレン性不飽和二重結合とエポキシ基を有する単量体であれば、特に限定されない。例えばアリルグリシジルエーテルなどのエーテル系化合物;グリシジル(メタ)アクリレート、アリルグリシジルエーテル、グリシジルアルキル(メタ)アクリレートなどのエステル系化合物(特にエポキシ基含有(メタ)アクリル酸エステル)等があげられる。これらは単独で用いても、2種以上を組み合わせて用いてもよい。
エポキシ基を持つ単量体の割合は、シェル部を構成する全単量体中、例えば、3~60重量%、好ましくは5~50重量%、より好ましくは10~45重量%である。
また前記低Tg単量体としては、アルコキシ基又はアリールオキシ基含有アクリル酸エステルが好ましい。アルコキシ基又はアリールオキシ基含有アクリル酸エステルは、アルコキシ基又はアリールオキシ基含有メタクリル酸エステルに比べると、低温(例えば、-20~-40℃)での耐衝撃接着性をさらに向上できる。
特に好ましい低Tg単量体は、アルコキシ基含有アクリル酸エステルである。
シェル部において、エポキシ基を持つ単量体以外の単量体として使用可能な単量体としては、上記低Tg単量体の他、メチルアクリレート、エチルアクリレートなどのアルキル(メタ)アクリレート、及び多官能性単量体(アリル(メタ)アクリレートなど)が挙げられる(これらをその他のビニル単量体Aという)。またエポキシ基を持つ単量体、アルコキシアルキル(メタ)アクリレート、アルキル(メタ)アクリレート、多官能性単量体のいずれでもでないビニル単量体であってもよく(以下、これらをその他のビニル単量体Bという)、例えば、スチレン、α-メチルスチレン、1-又は2-ビニルナフタレン、モノクロロスチレン、ジクロロスチレン、ブロモスチレン等のビニル芳香族化合物類、メチル(メタ)クリレート、エチル(メタ)クリレート、ブチル(メタ)アクリレート、2-エチルヘキシル(メタ)アクリレート、オクチル(メタ)アクリレート、ドデシル(メタ)アクリレート、ステアリル(メタ)アクリレート、ベヘニル(メタ)アクリレート等のアルキル(メタ)アクリレート類、エチレン、プロピレン、ブチレン、イソブチレン等のアルケン類、(メタ)アクリロニトリルに代表されるシアン化ビニル化合物、(メタ)アクリルアミド、アルキルビニルエーテル等が挙げられ、これらは、単独で用いても、2種以上を組み合わせて用いてもよい。
前記コアシェルポリマー(B)のシェル部は、アルコキシ基又はアリールオキシ基含有(メタ)アクリル酸エステル単位と、エポキシ基含有(メタ)アクリル酸エステル単位と、必要に応じて含有される他のモノマー単位とを、FOX式で計算されるガラス転移温度が25℃未満となる範囲で含有することが好ましい。
前記コアシェルポリマー(B)のシェル部は、アルコキシアルキル(メタ)アクリレート、メチルアクリレート、及びエチルアクリレートからなる群より選ばれる1種以上の単量体、エポキシ基を持つ単量体、並びにその他ビニル単量体Bからなることが好ましい。
より好ましくは、前記コアシェルポリマー(B)のシェル部が、アルコキシアルキル(メタ)アクリレート、メチルアクリレート、及びエチルアクリレートからなる群より選ばれる1種以上の単量体5~99重量%、エポキシ基を持つ単量体1~50重量%、並びにその他ビニル単量体B0~50重量%からなる。より好ましくは、前記コアシェルポリマー(B)のシェル部が、アルコキシアルキル(メタ)アクリレート、メチルアクリレート、及びエチルアクリレートからなる群より選ばれる1種以上の単量体10~99重量%、エポキシ基を持つ単量体1~50重量%、並びにその他ビニル単量体B0~50重量%からなる。さらに好ましくは、前記コアシェルポリマー(B)のシェル部が、アルコキシアルキル(メタ)アクリレート、メチルアクリレート、及びエチルアクリレートからなる群より選ばれる1種以上の単量体20~99重量%、エポキシ基を持つ単量体1~50重量%、並びにその他ビニル単量体B0~50重量%からなる。特に好ましくは、前記コアシェルポリマー(B)のシェル部が、アルコキシアルキル(メタ)アクリレート、メチルアクリレート、及びエチルアクリレートからなる群より選ばれる1種以上の単量体40~99重量%、エポキシ基を持つ単量体1~50重量%、並びにその他ビニル単量体0~50重量%からなる。
さらに前記コアシェルポリマー(B)のシェル部が、2-アルコキシエチル(メタ)アクリレート5~99重量%、グリシジル(メタ)アクリレート、アリルグリシジルエーテル、及びグリシジルアルキル(メタ)アクリレートからなる群から選ばれる1種以上の単量体1~50重量%、並びに、その他のビニル単量体0~50重量%からなることも好ましい態様であり、
2-メトキシエチルアクリレート5~99重量%、グリシジル(メタ)アクリレート、アリルグリシジルエーテル、及びグリシジルアルキル(メタ)アクリレートからなる群から選ばれる1種以上の単量体1~50重量%、並びに、その他のビニル単量体0~50重量%からなることも好ましい態様である。
本発明におけるコアシェルポリマーは、エポキシ樹脂組成物の硬化物中で一次粒子の状態で分散していることが好ましいが、本明細書において「一次粒子の状態で分散している」とは、コアシェルポリマー同士が互いに凝集せず、それぞれ独立して分散していることを意味し、具体的には、後述の方法で以下の(数式2)を用いて算出した粒子分散率(%)が、50%以上であることを意味する。このような粒子分散率は、前記耐衝撃接着性改良の観点から、75%以上であることが好ましく、より好ましくは90%以上である。
本発明における中間層は、コア部とシェル部の間に含み、多官能性単量体30~100重量%、及びその他のビニル単量体0~70重量%の重合体からなり、本発明のコアシェルポリマー含有エポキシ樹脂組成物の粘度を低下させる効果、前記シェルポリマーをコアシェルポリマー外壁面へ均一に存在せしめる効果、コアシェルポリマーのエポキシ樹脂への分散性を向上させる効果、の内何れかの効果を奏するものであれば、特に限定されない。多官能性単量体としては、ジビニルベンゼン、ブタンジオールジ(メタ)アクリレート、(イソ)シアヌル酸トリアリル、(メタ)アクリル酸アリル、イタコン酸ジアリル、フタル酸ジアリル等が例示できる。
本発明のコアシェルポリマー含有エポキシ樹脂組成物を熱硬化する場合には、コアシェルポリマー含有エポキシ樹脂組成物に硬化剤を添加してもよい。かかる硬化剤としては、脂肪族ジアミンや芳香族ジアミンなどのアミン系硬化剤;無水ヘキサヒドロ無水フタル酸などの酸無水物;ノボラック型フェノール樹脂、イミダゾール化合物、3級アミン、トリフェニルホスフィン、脂肪族ポリアミン、芳香族ポリアミン、ポリアミド、ポリメルカプタン、ジシアンジアミド、二塩基酸ジヒドラジド、N,N-ジアルキル尿素誘導体、N,N-ジアルキルチオ尿素誘導体、アルキルアミノフェノール誘導体、メラミン、グアナミンなどが挙げられる。これらの硬化剤は単独で用いても、2種以上を組み合わせて用いてもよい。好ましい硬化剤は、アミン系硬化剤、酸無水物、N,N-ジアルキル尿素誘導体、3級アミン、イミダゾール化合物である。
本発明の樹脂組成物を、加熱により硬化しうる一液型の接着剤として使用する場合には、ジシアアンジアミドを硬化剤の主成分として使用し、更に、N,N’-ジアルキル尿素誘導体、イミダゾール化合物、3級アミン、及び、アミン系硬化剤から選択される1種以上を、硬化促進剤として少量併用することが好ましい。
本発明では、靭性、耐衝撃性、せん断接着性、及び、剥離接着性などの性能を更に向上させる目的で、(B)成分やゴム変性エポキシ樹脂やウレタン変性エポキシ樹脂以外の強化剤を、必要に応じて使用することができる。
末端に活性水素含有基を有する有機重合体の数平均分子量は、GPCで測定したポリスチレン換算分子量にて、800~7000が好ましく、1500~5000がより好ましく、2000~4000が特に好ましい。
-R1-O- (1)
(式中、R1は、炭素原子数1から14の直鎖状もしくは分岐アルキレン基である。)で示される繰り返し単位を有する重合体であり、一般式(1)におけるR1は、炭素原子数1から14の、さらには2から4の、直鎖状もしくは分岐状アルキレン基が好ましい。一般式(1)で示される繰り返し単位の具体例としては、-CH2O-、-CH2CH2O-、-CH2CH(CH3)O-、-CH2CH(C2H5)O-、-CH2C(CH3)2O-、-CH2CH2CH2CH2O-等が挙げられる。ポリエーテル系重合体の主鎖骨格は、1種類だけの繰り返し単位からなってもよいし、2種類以上の繰り返し単位からなってもよい。特に、プロピレンオキシドの繰り返し単位を50重量%以上有するプロピレンオキシド重合体を主成分とする重合体から成るものは、比較的低粘度である点から好ましい。また、テトラヒドロフランを開環重合して得られるポリテトラメチレングリコール(PTMG)は、Tgが低い為に低温特性に優れ、かつ、耐熱性が高いことから好ましい。
前記ポリイソシアネート化合物の具体例としては、トルエン(トリレン)ジイソシアネート、ジフェニルメタンジイソシアネート、キシリレンジイソシアネート等の芳香族系ポリイソシアネート;イソフォロンジイソシアネート、ヘキサメチレンジイソシアネート、水素化トルエンジイソシアネート、水素化ジフェニルメタンジイソシアネート等の脂肪族系ポリイソシアネートなどを挙げることができる。これらの中でも、耐熱性の点から、脂肪族系ポリイソシアネートが好ましく、更に入手性の点から、イソフォロンジイソシアネートやヘキサメチレンジイソシアネートがより好ましい。
前記ブロック剤は、単独で用いても良く2種以上併用しても良い。
前記強化剤は、架橋剤の残基、鎖延長剤の残基、または、その両方を含有していてもよい。
A-(NR2-C(=O)-X)a (2)
(式中、a個のR2は、それぞれ独立に、炭素原子数1~20の炭化水素基である。aはキャップされたイソシアネート基の1分子当たりの平均数を表し、1.1個以上が好ましく、1.5~8個がより好ましく、1.7~6個が更に好ましく、2~4個が特に好ましい。Xは、前記ブロック剤から活性水素原子を除いた残基である。Aは、イソシアネート末端化プレポリマーから末端イソシアネート基を除いた残基である。)で表される。
強化剤の数平均分子量は、GPCで測定したポリスチレン換算分子量にて、2000~40000が好ましく、3000~30000がより好ましく、4000~20000が特に好ましい。分子量分布(重量平均分子量と数平均分子量との比)は、1~4が好ましく、1.2~3がより好ましく、1.5~2.5が特に好ましい。
強化剤は単独で用いても良く2種以上併用しても良い。
本発明では、分子内に2個以上の二重結合を有するラジカル硬化性樹脂を、必要に応じて使用することができる。また、必要により、分子内に少なくとも1個の二重結合を有する分子量300未満の低分子化合物を添加することができる。前記低分子化合物は、前記ラジカル硬化性樹脂との併用により、粘度や硬化物の物性や硬化速度を調整する機能を有し、ラジカル硬化性樹脂の所謂反応性希釈剤として機能するものである。更に、本発明の樹脂組成物には、ラジカル重合開始剤を添加することができる。ここで、ラジカル重合開始剤は、温度を上げる(好ましくは、約50℃~約150℃)と活性化される潜在的なタイプであることが好ましい。
本発明では、充填剤を、必要に応じて使用することができる。充填剤の具体例としては、ポリジメチルシロキサンで表面処理した疎水性ヒュームドシリカなどの乾式シリカ、湿式シリカ、ケイ酸アルミニウム、ケイ酸マグネシウム、ケイ酸カルシウム、ドロマイトおよびカーボンブラックの如き補強性充填材;タルクやウォラストナイト等の板状フィラー;膠質炭酸カルシウム、重質炭酸カルシウム、酸化カルシウム、炭酸マグネシウム、酸化チタン、酸化第二鉄、アルミニウム微粉末、酸化亜鉛、活性亜鉛華等が挙げられる。また、200μmまでの平均粒子径と0.2g/ccまでの密度を有するマイクロバルーンも使用できる。粒子径は好ましくは約25~150μmであり、密度は好ましくは約0.05~約0.15g/ccである。市販されているマイクロバルーンとしては、Dualite Corporation製Dualite、アクゾノーベル社製Expancel、松本油脂製薬製マイクロスフェアーなどが挙げられる。
本発明のコアシェルポリマー含有エポキシ樹脂組成物の使用に際しては、有機過酸化物や、酸化カルシウムなどの脱水剤、アゾタイプ化学的発泡剤や熱膨張性マイクロバルーンなどの膨張剤、アラミド系パルプなどの繊維パルプ、酸化防止剤、レベリング剤、消泡剤、シランカップリング剤、帯電防止剤、難燃剤、滑剤、低収縮剤、熱可塑性樹脂、乾燥剤、分散剤、硬化促進剤、連鎖移動剤、光増感剤、還元剤、可塑剤、可撓化剤(flexibilizer)、液状ゴム(反応性/非反応性)、接着性付与剤(プライマーを含む)、染料、顔料、安定剤、紫外線吸収剤、希釈剤(反応性/非反応性)、有機溶剤などを各種製造の段階で混合することができる。
本発明のコアシェルポリマー含有エポキシ樹脂組成物は、国際公開第2005/28546号パンフレットに記載の方法により調製することができる。具体的には、前記コアシェルポリマー(B)が水媒体中に分散されてなる水媒体分散液(コアシェルポリマーを含有する水性ラテックス(詳細には、乳化重合によってコアシェルポリマーを製造した後の反応混合物))を、20℃における水に対する溶解度が5重量%以上40重量%以下の有機溶媒と混合した後、さらに過剰の水と混合して、コアシェルポリマー緩凝集体を得る第1工程と、緩凝集したコアシェルポリマーを液相から分離して回収した後、再度有機溶媒と混合して、コアシェルポリマーの有機溶媒分散液を得る第2工程と、この有機溶媒分散液をさらにエポキシ樹脂と混合した後、前記有機溶媒を留去する第3工程を含んで調製されるものである。
第1工程は、20℃における水に対する溶解度が好ましくは5重量%以上で、40重量%以下(特に30重量%以下)の有機溶媒と、水性ラテックスとを混合する操作を含む。かかる有機溶媒を用いることによって、上記混合操作の後、さらに水を添加すると(後述する)相分離することとなって、再分散が可能な程度の緩やかな状態のコアシェルポリマー緩凝集体を得ることができる。
水性ラテックスと混合する有機溶媒の混合量は、水性ラテックス100重量部に対して50重量部以上(特に60重量部以上)、250重量部以下(特に150重量部以下)であることが好ましい。有機溶媒の混合量が50重量部未満の場合には、水性ラテックスに含有されるコアシェルポリマーの凝集体が生成し難くなる場合がある。また、有機溶媒の混合量が300重量部を超える場合には、その後コアシェルポリマー緩凝集体を得るために要する水量が増大して、製造効率が低下する場合がある。
第1工程は、上記水性ラテックスと有機溶媒とを混合する操作の後、さらに過剰の水を添加して混合する操作を含む。これにより、相分離することとなって、緩やかな状態コアシェルポリマーの凝集体を得ることができる。また、あわせて、水性ラテックスの調製に際して使用した水溶性の乳化剤もしくは分散剤、水溶性を有する重合開始剤、あるいは還元剤等の電解質の大半を水相に溶出させることができる。
第2工程は、緩凝集したコアシェルポリマーを液相から分離・回収して、コアシェルポリマードープを得る操作を含む。かかる操作によって、コアシェルポリマーから乳化剤等の水溶性の夾雑物を分離・除去することができる。
本発明においては、第1工程と第2工程との間に、凝集したコアシェルポリマーを液相から分離・回収し、再度20℃における水に対する溶解度が5重量%以上40重量%以下の有機溶媒と混合した後、さらに過剰の水と混合してコアシェルポリマーの緩凝集体を得る操作を1回以上行うことが好ましい。また、これによりコアシェルポリマードープ中に含まれる乳化剤等の水溶性の夾雑物の残存量をより低くすることができる。
第3工程は、第2工程で得たコアシェルポリマーの有機溶媒溶液中の有機溶媒を前記エポキシ樹脂に置換する操作を含む。かかる操作によって、コアシェルポリマーが一次粒子の状態で分散したコアシェルポリマー含有エポキシ樹脂組成物を得ることができる。また、コアシェルポリマーの凝集体に残存する水分を共沸留去することができる。
また、有機溶媒を留去する方法としては、公知の方法が適用できる。例えば、槽内に有機溶媒溶液と前記エポキシ樹脂との混合物を仕込み、加熱減圧留去する方法、槽内で乾燥ガスと上記混合物を向流接触させる方法、薄膜式蒸発機を用いるような連続式の方法、脱揮機構を備えた押出機あるいは連続式撹拌槽を用いる方法等が挙げられる。有機溶媒を留去する際の温度や所要時間等の条件は、得られるコアシェルポリマー含有エポキシ樹脂組成物の品質を損なわない範囲で適宜選択することができる。また、コアシェルポリマー含有エポキシ樹脂組成物に残存する揮発分の量は、コアシェルポリマー含有エポキシ樹脂組成物の使用目的に応じて問題のない範囲で適宜選択できる。
本発明の樹脂組成物は、すべての配合成分を予め配合密封保存し、塗布後加熱や光照射により硬化する一液型樹脂組成物として使用することができる。また、(A)成分を主成分とするA液と、硬化剤を含有する別途調整したB液からなる、二液型または多液型の樹脂組成物として調製しておき、該A液と該B液を使用前に混合して、使用することもできる。
本発明には、上記樹脂組成物を硬化して得られる硬化物が含まれる。ポリマー微粒子が一次粒子の状態で分散している樹脂組成物の場合には、これを硬化することによって、ポリマー微粒子が均一に分散した硬化物を容易に得ることができる。また、ポリマー微粒子が膨潤し難く、樹脂組成物の粘性が低いことから、硬化物を作業性よく得ることができる。
本発明の樹脂組成物は、任意の方法によって塗布可能である。室温程度の低温で塗布可能であり、必要に応じて加温して塗布することも可能である。
本発明の樹脂組成物は、塗布ロボットを使用してビード状またはモノフィラメント状またはスワール(swirl)状に基板上へ押出したり、コーキングガン等の機械的な塗布方法や他の手動塗布手段を用いることもできる。また、ジェットスプレー法またはストリーミング法を用いて組成物を基板へ塗布することもできる。本発明の樹脂組成物を、一方または両方の基板へ塗布し、接合しようとする基板間に組成物が配置されるよう基板同士を接触させ、硬化させることにより接合する。
本発明の樹脂組成物を使用して、様々な基板同士を接着させる場合、例えば、木材、金属、プラスチック、ガラス等を接合することができる。自動車部品を接合することが好ましく、自動車フレーム同士の接合または自動車フレームと他の自動車部品との接合がより好ましい。基板としては、冷間圧延鋼や溶融亜鉛メッキ鋼などの鋼材、アルミニウムや被覆アルミニウムなどのアルミニウム材、汎用プラスチック、エンジニアリングプラスチック、CFRPやGFRP等の複合材料、等の各種のプラスチック系基板が挙げられる。
本発明の樹脂組成物は、靭性に優れる為に、線膨張係数の異なる異種基材間の接合に適している。
また、本発明の樹脂組成物は、航空宇宙用の構成材、特に、外装金属構成材の接合にも使用できる。
本発明の樹脂組成物の硬化温度は、特に限定はないが、一液型樹脂組成物として使用する場合には、50℃~250℃が好ましく、80℃~220℃がより好ましく、100℃~200℃が更に好ましく、130℃~180℃が特に好ましい。二液型樹脂組成物として使用する場合には、特に限定はないが、0℃~150℃が好ましく、10℃~100℃がより好ましく、15℃~80℃が更に好ましく、20℃~60℃が特に好ましい。
本発明の樹脂組成物を自動車用接着剤として使用する場合、該接着剤を自動車部材へ施工した後、次いでコーティングを塗布し、該コーティングを焼付け・硬化するのと同時に接着剤を硬化させるのが工程短縮・簡便化の観点から好ましい。
本発明のコアシェルポリマー含有エポキシ樹脂組成物は、成形材料、接着剤、構造接着剤(好ましくは、車両や航空機向けの構造用接着剤、風力発電用構造接着剤)、繊維あるいはフィラー強化複合材料、液晶パネル、OLED照明、OLEDディスプレイ等の表示機器・照明機器用封止材等の封止材料、注型材料、およびプリント配線基板用材料、ソルダーレジスト、層間絶縁膜、ビルドアップ材料、FPC用接着剤、半導体・LED等電子部品用封止材等の電気絶縁材料、ダイボンド材料、アンダーフィル、ACF、ACP、NCF、NCP等の半導体実装材料、コーティング材料、充填材、光造型材料、光学部品、インキ、トナーとして好適に使用される。
本製造例、実施例、比較例における評価方法は以下の通りである。
後述するコアシェルポリマー含有エポキシ樹脂組成物(A-1~A-14)それぞれ20重量部にそれぞれ液状ビスフェノールA型エポキシ樹脂「jER(登録商標)828EL」(商品名、三菱化学株式会社製)を80重量部、及び、ジシアンジアミド「jERキュア(登録商標)DICY7」(商品名、三菱化学株式会社製)7重量部、芳香族ジメチルウレア「Dyhard(登録商標) UR300」(商品名、AlzChem GmbH社製)1重量部を混合し、170℃で1時間硬化させた後、その硬化物を液体窒素中で割裂させ、その凍結破断面を、走査型電子顕微鏡(日本電子株式会社製、JSM-6300F)を用いて倍率2万倍にて観察を行い、以下の方法による粒子分散率(%)を指標として分散状態を判定した。
得られた2万倍の走査型電子顕微鏡写真において、5cm四方のエリアを無作為に4カ所選択して、上述の方法で数式2を用いて粒子分散率(%)を算出し、その平均値を用いた。粒子分散率の評価基準は以下の通りである。
良好:粒子分散率が70%以上である。
不良:粒子分散率が70%未満である。
体積平均粒子径は、粒子径測定装置(日機装(株)製Microtrac UPA)で測定した。水性ラテックスを脱イオン水で希釈したものを測定試料として用いた。測定は、水の屈折率、及びそれぞれのゴム粒子、又は、コアシェルポリマーの屈折率を入力し、計測時間600秒、Signal Levelが0.6~0.8の範囲内になるように試料濃度を調整して行った。
コアシェルポリマー含有エポキシ樹脂組成物の粘度は、後述の方法で得た粘度測定用のエポキシ樹脂組成物をBROOKFIELD社製デジタル粘度計DV-II+Pro型を用いて測定した。粘度領域によってスピンドルCPE-41またはCPE-52を使い分け、測定温度50℃、Shear Rate10「1/s」時の粘度を測定した。
JIS K 6865に準拠して、対称くさび試験片を作製し、衝撃速度2m/秒、衝撃エネルギー50Jの条件で、23℃、及び/又は、-30℃、及び/又は、-40℃で試験を実施した。
以下の単独重合体のTg値を用い、上述の数式1に従い算出した。
ブタジエン -85℃
ジメチルシロキサン -123℃
γ-メタクリロイルオキシプロピルメチルジメトキシシラン 43℃
n-ブチルアクリレート -54℃
以下の単独重合体のTg値を用い、上述の数式1に従い算出した。
スチレン 100℃
メチルメタクリレート 105℃
アクリロニトリル 97℃
グリシジルメタクリレート 46℃
2-メトキシエチルアクリレート -50℃
4-ヒドロキシブチルアクリレート -40℃
n-ブチルアクリレート -54℃
2-(2-エトキシエトキシ)エチルアクリレート -54℃
2-メトキシエチルメタクリレート 16℃
2-エトキシエチルメタクリレート -31℃
フェノキシエチルアクリレート -22℃
耐圧重合機中に、脱イオン水200重量部、リン酸三カリウム0.03重量部、エチレンジアミン四酢酸二ナトリウム(EDTA)0.002重量部、硫酸第一鉄・7水和塩0.001重量部、及び、ドデシルベンゼンスルホン酸ナトリウム(SDBS)1.55重量部を投入し、撹拌しつつ十分に窒素置換を行なって酸素を除いた後、ブタジエン(Bd)100重量部を系中に投入し、45℃に昇温した。パラメンタンハイドロパーオキサイド(PHP)0.03重量部、続いてナトリウムホルムアルデヒドスルホキシレート(SFS)0.10重量部を投入し重合を開始した。重合開始から3、5、7時間目それぞれに、パラメンタンハイドロパーオキサイド(PHP)0.025重量部を投入した。また、重合開始4、6、8時間目それぞれに、EDTA0.0006重量部、及び硫酸第一鉄・7水和塩0.003重量部を投入した。重合15時間目に減圧下残存モノマーを脱揮除去して重合を終了し、ポリブタジエンゴムを主成分とするポリブタジエンゴムラテックス(R-1)を得た。得られたラテックスに含まれるポリブタジエンゴム粒子の体積平均粒子径は0.08μmであった。
耐圧重合機中に、製造例1で得たポリブタジエンゴムラテックス(R-1)を21重量部(ポリブタジエンゴム7重量部を含む)、脱イオン水185重量部、リン酸三カリウム0.03重量部、EDTA0.002重量部、及び硫酸第一鉄・7水和塩0.001重量部を投入し、撹拌しつつ十分に窒素置換を行なって酸素を除いた後、Bd93重量部を系中に投入し、45℃に昇温した。PHP0.02重量部、続いてSFS0.10重量部を投入し重合を開始した。重合開始から24時間目まで3時間おきに、それぞれ、PHP0.025重量部、及びEDTA0.0006重量部、及び硫酸第一鉄・7水和塩0.003重量部を投入した。重合30時間目に減圧下残存モノマーを脱揮除去して重合を終了し、ポリブタジエンゴムを主成分とするポリブタジエンゴムラテックス(R-2)を得た。得られたラテックスに含まれるポリブタジエンゴム粒子の体積平均粒子径は0.20μmであった。
脱イオン水200重量部、SDBS1.0重量部、ドデシルベンゼンスルホン酸1.0重量部、平均分子量2000の末端ヒドロキシポリジメチルシロキサン97.5重量部およびγ-メタクリロイルオキシプロピルメチルジメトキシシラン2.5重量部の混合物をホモミキサーにより10000rpmで5分間撹拌後、高圧ホモジナイザーに500barの圧力下で3回通過させてシロキサンエマルジョンを調製した。このエマルジョンを速やかに温度計、撹拌器、還流冷却器、窒素流入口、モノマーと乳化剤などの副原料の添加装置を有するガラス反応器に一括して投入した。系を撹拌しながら、30℃で反応を開始させた。6時間後、23℃に冷却して20時間放置後、系のpHを炭酸水素ナトリウムで6.8に戻して重合を終了し、ポリオルガノシロキサンゴム粒子を含むラテックス(R-3)を得た。得られたラテックスに含まれるポリオルガノシロキサンゴム粒子の体積平均粒子径は0.28μmであった。
温度計、撹拌機、還流冷却器、窒素流入口、モノマーと乳化剤の添加装置を有するガラス反応器に、脱イオン水180重量部、EDTA0.002重量部、Fe0.001重量部、SFS0.04重量部およびSDBS0.5重量部を仕込み、窒素気流中で撹拌しながら45℃に昇温した。次にn-ブチルアクリレート(BA)98重量部、アリルメタクリレート(ALMA)2重量部およびクメンハイドロパーオキサイド(CHP)0.02重量部の混合物を3時間要して滴下した。また、前記のモノマー混合物の添加とともに、1重量部のSDSを5重量%濃度の水溶液にしたものを3時間にわたり連続的に追加した。モノマー混合物添加終了から1時間撹拌を続けて重合を完結し、アクリルゴム粒子を含むラテックス(R-4)を得た。得られたラテックスに含まれるアクリルゴム粒子の体積平均粒子径は0.09μmであった。
温度計、撹拌機、還流冷却器、窒素流入口、及びモノマーの添加装置を有するガラス反応器に、製造例1で調製したポリブタジエンゴムラテックス(R-1)250重量部(ポリブタジエンゴム粒子83重量部を含む)、及び、脱イオン水65重量部を仕込み、窒素置換を行いながら60℃で撹拌した。EDTA0.004重量部、硫酸第一鉄・7水和塩0.001重量部、及びSFS0.2重量部を加えた後、2-メトキシエチルアクリレート(MEA)10重量部、グリシジルメタクリレート(GMA)7重量部、及び、CHP0.08重量部の混合物を110分間かけて連続的に添加した。添加終了後、CHP0.04重量部を添加し、さらに1時間撹拌を続けて重合を完結させ、コアシェルポリマーを含む水性ラテックス(L-1)を得た。モノマー成分の重合転化率は99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は0.10μmであった。
製造例5において、MEA10重量部、GMA7重量部に代えて、スチレン(St)6重量部、アクリロニトリル(AN)3重量部、メチルメタクリレート(MMA)1重量部、GMA7重量部、又は、MEA16.2重量部、アリルメタクリレート(ALMA)0.8重量部を用いたこと以外は、製造例5と同様にして、コアシェルポリマーを含む水性ラテックス(L-2)、(L-3)をそれぞれ得た。モノマー成分の重合転化率はいずれも99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径はいずれも0.10μmであった。
温度計、撹拌機、還流冷却器、窒素流入口、及びモノマーの添加装置を有するガラス反応器に、製造例1で得たポリブタジエンゴムラテックス(R-1)183重量部(ポリブタジエンゴム粒子61重量部を含む)、製造例2で得たポリブタジエンゴムラテックス(R-2)78重量部(ポリブタジエンゴム粒子26重量部を含む)、及び脱イオン水54重量部を仕込み、窒素置換を行いながら60℃で撹拌した。EDTA0.004重量部、硫酸第一鉄・7水和塩0.001重量部、及びSFS0.2重量部を加えた後、MEA10重量部、GMA3重量部、及び、CHP0.04重量部の混合物を85分間かけて連続的に添加した。添加終了後、CHP0.065重量部を添加し、さらに1時間撹拌を続けて重合を完結させ、コアシェルポリマーを含む水性ラテックス(L-4)を得た。モノマー成分の重合転化率は99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は0.19μmであった。
製造例8において、MEA10重量部、GMA3重量部に代えて、MEA9重量部、MMA2重量部、GMA2重量部、又は、St7重量部、AN3重量部、GMA3重量部、又は、MMA13重量部、又は、MEA13重量部、又は、MEA12重量部、4-ヒドロキシブチルアクリレート(4HBA)1重量部を用いたこと以外は、製造例8と同様にして、コアシェルポリマーを含む水性ラテックス(L-5)~(L-9)それぞれを得た。モノマー成分の重合転化率は全て99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は全て0.19μmであった。
温度計、撹拌機、還流冷却器、窒素流入口、及びモノマーの添加装置を有するガラス反応器に、製造例1で得たポリブタジエンゴムラテックス(R-1)183重量部(ポリブタジエンゴム粒子61重量部を含む)、製造例2で得たポリブタジエンゴムラテックス(R-2)78重量部(ポリブタジエンゴム粒子26重量部を含む)、及び脱イオン水54重量部を仕込み、窒素置換を行いながら60℃で撹拌した。EDTA0.004重量部、硫酸第一鉄・7水和塩0.001重量部、及びSFS0.2重量部を加えた後、中間部成分として、イソシアヌル酸トリアリル(TAIC)2重量部、及び、CHP0.07重量部を添加し60分間攪拌した。その後、シェル部成分として、MEA11.5重量部、BA0.5重量部、GMA1重量部、及び、CHP0.04重量部の混合物を85分間かけて連続的に添加した。添加終了後、CHP0.065重量部を添加し、さらに1時間撹拌を続けて重合を完結させ、コアシェルポリマーを含む水性ラテックス(L-10)を得た。モノマー成分の重合転化率は99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は0.19μmであった。
温度計、撹拌機、還流冷却器、窒素流入口、及びモノマーの添加装置を有するガラス反応器に、製造例3で得たポリオルガノシロキサンゴムラテックス(R-3)250重量部(ポリオルガノシロキサンゴム粒子83重量部を含む)、及び、脱イオン水65重量部を仕込み、窒素置換を行いながら60℃で撹拌した。EDTA0.004重量部、硫酸第一鉄・7水和塩0.001重量部、及びSFS0.2重量部を加えた後、TAIC2重量部、及び、CHP0.07重量部を添加し60分間攪拌した。その後、MEA11重量部、GMA6重量部、及び、CHP0.05重量部の混合物を110分間かけて連続的に添加した。添加終了後、CHP0.065重量部を添加し、さらに1時間撹拌を続けて重合を完結させ、コアシェルポリマーを含む水性ラテックス(L-11)を得た。モノマー成分の重合転化率は99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は0.30μmであった。
製造例15において、MEA11重量部、GMA6重量部に代えて、St7重量部、AN4重量部、GMA6重量部を用いたこと以外は、製造例15と同様にして、コアシェルポリマーを含む水性ラテックス(L-12)を得た。モノマー成分の重合転化率は99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は0.30μmであった。
温度計、撹拌機、還流冷却器、窒素流入口、及びモノマーの添加装置を有するガラス反応器に、製造例4で調製したアクリルゴムラテックス(R-4)250重量部(アクリルゴム粒子83重量部を含む)、及び、脱イオン水65重量部を仕込み、窒素置換を行いながら60℃で撹拌した。EDTA0.004重量部、硫酸第一鉄・7水和塩0.001重量部、及びSFS0.2重量部を加えた後、MEA11重量部、GMA6重量部、及び、CHP0.08重量部の混合物を110分間かけて連続的に添加した。添加終了後、CHP0.04重量部を添加し、さらに1時間撹拌を続けて重合を完結させ、コアシェルポリマーを含む水性ラテックス(L-13)を得た。モノマー成分の重合転化率は99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は0.11μmであった。
製造例17において、MEA11重量部、GMA6重量部に代えて、St7重量部、AN4重量部、GMA6重量部を用いたこと以外は、製造例17と同様にして、コアシェルポリマーを含む水性ラテックス(L-14)を得た。モノマー成分の重合転化率は99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は0.11μmであった。
30℃の1L混合槽にメチルエチルケトン(MEK)126重量部を仕込み、撹拌しながら、製造例5で得られたコアシェルポリマーの水性ラテックス(L-1)を126重量部投入した。均一に混合後、水200重量部を80重量部/分の供給速度で投入した。供給終了後、速やかに撹拌を停止し、浮上性の凝集体を含むスラリー液を得た。次に、凝集体を残し、液相350重量部を槽下部の払い出し口より排出させた。得られた凝集体にMEK150重量部を追加して混合し、コアシェルポリマーが分散した分散液を得た。この分散液に液状ビスフェノールA型エポキシ樹脂「jER(登録商標)828EL」(商品名、三菱化学株式会社製、エポキシ当量184~194)をコアシェルポリマー/エポキシ樹脂が25/75となるように添加、混合後、有機溶媒を減圧留去し、エポキシ樹脂組成物(A-1)として得た。また、同様に製造例6~18で得られたコアシェルポリマーの水性ラテックス(L-2~L-14)をそれぞれ用いることで、エポキシ樹脂組成物(A-2~A-14)をそれぞれ得た。
製造例5~18で得られたコアシェルポリマーの水性ラテックス(L-1~L-14)それぞれ126重量部を、撹拌しながら、MEK126重量部を仕込んだ30℃の1L混合槽にそれぞれ投入した。均一に混合後、水200重量部を80重量部/分の供給速度で投入した。供給終了後、速やかに撹拌を停止し、浮上性の凝集体を含むスラリー液を得た。次に、凝集体を残し、液相350重量部を槽下部の払い出し口より排出させた。得られた凝集体にMEK150重量部を追加して混合し、コアシェルポリマーが分散した分散液をそれぞれ得た。この分散液に上記jER(登録商標)828ELをコアシェルポリマー/エポキシ樹脂が25/75、又は、45/55となるように添加、混合後、有機溶媒を減圧留去し、粘度測定用のエポキシ樹脂組成物をそれぞれ得た。
製造例19で得られた、エポキシ樹脂組成物(A-1~A-14)の成分を、表1にまとめて示す。
製造例19で得られたエポキシ樹脂組成物(A-1)120重量部(コアシェルポリマー30重量部を含む)に上記jER(登録商標)828EL 10重量部、反応性希釈剤(グリシジルエステル化合物)として「Cardura(登録商標) E10P」(商品名、Momentive社製)10重量部、硬化剤としてジシアンジアミド「jERキュア(登録商標)DICY7」(商品名、三菱化学株式会社製)7重量部、硬化促進剤として芳香族ジメチルウレア「Dyhard(登録商標) UR300」(商品名、AlzChem GmbH社製)1重量部、シリカ「CAB-O-SIL(登録商標) TS720」(商品名、CABOT社製)3重量部、カーボンブラック「Monarch(登録商標)280」(商品名、CABOT社製)0.3重量部、炭酸カルシウム「ホワイトンSB」(商品名、白石カルシウム株式会社製)15重量部、酸化カルシウム「CML#31」(商品名、近江化学工業株式会社製)5重量部を添加し、自動公転ミキサー(シンキー社製、AR-250)で混合した後、3本ロールミルで3回混合撹拌しコアシェルポリマー含有接着組成物(B-1)を得た。
実施例1において、エポキシ樹脂組成物(A-1)に代えて、エポキシ樹脂組成物(A-4)、(A-5)、(A-10)、(A-11)、(A-13)をそれぞれ用いたこと以外は実施例1と同様にして、コアシェルポリマー含有接着組成物(B-4)、(B-5)、(B-10)、(B-11)、(B-13)をそれぞれ得、対称くさび衝撃試験片を作製した。これらをそれぞれ実施例2~6とした。
実施例1において、エポキシ樹脂組成物(A-1)に代えて、エポキシ樹脂組成物(A-2)、(A-3)、(A-6)、(A-7)、(A-8)、(A-9)、(A-12)、(A-14)をそれぞれ用いたこと以外は実施例1と同様にして、コアシェルポリマー含有接着組成物(B-2)、(B-3)、(B-6)、(B-7)、(B-8)、(B-9)、(B-12)、(B-14)をそれぞれ得、対称くさび衝撃試験片を作製した。これらをそれぞれ比較例1~8とした。
実施例1~6、比較例1~8の各種物性評価の結果を表2にまとめて示す。
表2に示す通り、比較例1は、実施例1と比較してエポキシ樹脂組成物の粘度が高く、また、23℃、-40℃いずれの耐衝撃接着性も低いことが分かった。比較例2は実施例1と比較してエポキシ樹脂組成物の粘度はほぼ同等ながら、23℃、-40℃いずれの耐衝撃接着性も低く、特に-40℃では全く強度が出ないことが分かった。また、コアシェルポリマーのシェル部にエポキシ基含有モノマーを使用しないため硬化時にコアシェルポリマーが一次粒子分散しないことも分かった。これに対し、実施例1は、比較例1、2と比較して、エポキシ樹脂組成物の粘度が低く、23℃、-40℃いずれの耐衝撃接着性も高いことが分かった。
表2に示す通り、比較例3は、実施例2~4と比較してエポキシ樹脂組成物の粘度が高く、また、23℃、-40℃いずれの耐衝撃接着性も低いことが分かった。比較例4は、実施例2~4と比較してエポキシ樹脂組成物の粘度が高く、また、23℃、-40℃いずれの耐衝撃接着性も低く、特に、-40℃では全く強度が出ないこと、及び、コアシェルポリマーのシェル部にエポキシ基含有モノマーを使用しないため硬化時にコアシェルポリマーが一次粒子分散しないことも分かった。比較例5は実施例2~4と比較してエポキシ樹脂組成物の粘度はほぼ同等ながら、23℃での耐衝撃接着性がやや低く、-40℃での耐衝撃接着強度は全くでないこと、及び、コアシェルポリマーのシェル部にエポキシ基含有モノマーを使用しないため硬化時にコアシェルポリマーが一次粒子分散しないことも分かった。比較例6は実施例2~4と比較してエポキシ樹脂粘度が高く、また、23℃、-40℃いずれの耐衝撃接着性も低いことが分かった。これに対し、実施例2~4は、比較例3~6と比較して、エポキシ樹脂組成物の粘度が低く、23℃、-40℃いずれの耐衝撃接着性も高いことが分かった。
表2に示す通り、比較例7は、実施例5と比較してエポキシ樹脂組成物の粘度が高く、また、23℃の耐衝撃接着強度が全く出ないことが分かった。これに対し、実施例5は、比較例7と比較して、エポキシ樹脂組成物の粘度が低く、23℃の耐衝撃接着性が高いことが分かった。
表2に示す通り、比較例8は、実施例6と比較してエポキシ樹脂組成物の粘度が高く、また、23℃の耐衝撃接着強度が全く出ないことが分かった。これに対し、実施例6は、比較例8と比較して、エポキシ樹脂組成物の粘度が低く、23℃の耐衝撃接着性が高いことが分かった。
温度計、撹拌機、還流冷却器、窒素流入口、及びモノマーの添加装置を有するガラス反応器に、製造例1で調製したポリブタジエンゴムラテックス(R-1)90重量部(ポリブタジエンゴム粒子30重量部を含む)、製造例2で調製したポリブタジエンゴムラテックス(R-2)180重量部(ポリブタジエンゴム粒子60重量部を含む)、及び、脱イオン水65重量部を仕込み、窒素置換を行いながら60℃で撹拌した。EDTA0.004重量部、硫酸第一鉄・7水和塩0.001重量部、及びSFS0.2重量部を加えた後、MEA8.5重量部、GMA1.5重量部、及び、CHP0.05重量部の混合物を60分間かけて連続的に添加した。添加終了後、CHP0.04重量部を添加し、さらに1時間撹拌を続けて重合を完結させ、コアシェルポリマーを含む水性ラテックス(L-15)を得た。モノマー成分の重合転化率は99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径は0.19μmであった。
製造例21において、MEA8.5重量部に代えて、2-(2-エトキシエトキシ)エチルアクリレート(EEEA)8.5重量部、又は2-メトキシエチルメタクリレート(MEMA)8.5重量部、又は2-エトキシエチルメタクリレート(EEMA)8.5重量部、又はフェノキシエチルアクリレート(PEA)8.5重量部、又はMMA8.5重量部を用いたこと以外は、製造例21と同様にして、コアシェルポリマーを含む水性ラテックス(L-16)~(L-20)をそれぞれ得た。モノマー成分の重合転化率はいずれも99%以上であった。得られた水性ラテックスに含まれるコアシェルポリマーの体積平均粒子径はいずれも0.19μmであった。
30℃の1L混合槽にメチルエチルケトン(MEK)126重量部を仕込み、撹拌しながら、製造例21で得られたコアシェルポリマーの水性ラテックス(L-15)を126重量部投入した。均一に混合後、水200重量部を80重量部/分の供給速度で投入した。供給終了後、速やかに撹拌を停止し、浮上性の凝集体を含むスラリー液を得た。次に、凝集体を残し、液相350重量部を槽下部の払い出し口より排出させた。得られた凝集体にMEK150重量部を追加して混合し、コアシェルポリマーが分散した分散液を得た。この分散液に上記液状ビスフェノールA型エポキシ樹脂「jER(登録商標)828EL」をコアシェルポリマー/エポキシ樹脂が40/60となるように添加、混合後、有機溶媒を減圧留去し、エポキシ樹脂組成物(A-15)を得た。また、同様に製造例22~26で得られたコアシェルポリマーの水性ラテックス(L-16~L-20)をそれぞれ用いることで、エポキシ樹脂組成物(A-16~A-20)をそれぞれ得た。
製造例27で得られた、エポキシ樹脂組成物(A-16~A-20)の成分を表3にまとめて示す。
実施例1において、エポキシ樹脂組成物(A-1)120重量部(コアシェルポリマー30重量部を含む)、上記jER(登録商標)828EL 10重量部に代えて、エポキシ樹脂組成物(A-15)~(A-19)75重量部(コアシェルポリマー30重量部を含む)、上記jER(登録商標)828EL 55重量部用いたこと以外は実施例1と同様にして、コアシェルポリマー含有接着組成物(B-15~19)をそれぞれ得、対称くさび衝撃試験片を作製した。これらをそれぞれ実施例7~11とした。
実施例1において、エポキシ樹脂組成物(A-1)120重量部(コアシェルポリマー30重量部を含む)、上記jER(登録商標)828EL 10重量部に代えて、エポキシ樹脂組成物(A-20)75重量部(コアシェルポリマー30重量部を含む)、上記jER(登録商標)828EL 55重量部用いたこと以外は実施例1と同様にして、コアシェルポリマー含有接着組成物(B-20)を得、対称くさび衝撃試験片を作製した。これらをそれぞれ比較例9とした。
実施例7~11、比較例9の23℃での耐衝撃接着性の結果を表4にまとめて示す。
これに対し、実施例7~11は、比較例9と比較して、23℃での耐衝撃接着性が高いことが分かる。また実施例7、8、11などの結果によれば、本発明例(特にアクリル酸エステルをシェル部に用いた例)は、優れた-30℃での耐衝撃接着性を示すことも分かる。さらに実施例7、8などによれば、本発明例(特にアルコキシ基含有アクリル酸エステルをシェル部に用いた例)は、優れた低粘度特性を示すことも分かる。
Claims (10)
- エポキシ樹脂(A)100重量部、コアシェルポリマー(B)1~100重量部を含む
コアシェルポリマー含有エポキシ樹脂組成物であって、
前記コアシェルポリマー(B)の体積平均粒子径が0.01~1μmであり、かつ、
前記コアシェルポリマー(B)のコア部のガラス転移温度が0℃未満であり、かつ、
前記コアシェルポリマー(B)のシェル部のガラス転移温度が25℃未満であり、かつ、
前記コアシェルポリマー(B)のシェル部が、エポキシ基をもつ単量体を含む、コアシェルポリマー含有エポキシ樹脂組成物。 - 前記コアシェルポリマー(B)のコア部が、ジエン系単量体及び(メタ)アクリル酸エステル単量体からなる群より選ばれる1種以上の単量体50重量%以上と、他の共重合可能なビニル単量体0重量%以上50重量%未満とから構成されるゴム弾性体;ポリシロキサンゴム系弾性体;またはそれら弾性体の混合物からなり、
前記他の共重合可能なビニル単量体が、芳香族ビニル化合物、シアン化ビニル化合物、不飽和酸誘導体、(メタ)アクリル酸アミド誘導体、マレイミド誘導体、及びビニルエーテル系単量体から選ばれる1種以上からなる、請求項1に記載のコアシェルポリマー含有エポキシ樹脂組成物。 - 前記コアシェルポリマー(B)のシェル部が、
アルコキシ基又はアリールオキシ基含有(メタ)アクリル酸エステル単位と、エポキシ基含有(メタ)アクリル酸エステル単位と、必要に応じて含有される他のモノマー単位とを、FOX式で計算されるガラス転移温度が25℃未満となる範囲で含有する請求項1または2に記載のコアシェル含有エポキシ樹脂組成物。 - 前記コアシェルポリマー(B)のシェル部が、
アルコキシアルキル(メタ)アクリレート、メチルアクリレート、及びエチルアクリレートからなる群から選ばれる1種以上の単量体5~99重量%、グリシジル(メタ)アクリレート、アリルグリシジルエーテル、及びグリシジルアルキル(メタ)アクリレートからなる群から選ばれる1種以上の単量体1~50重量%、並びに、その他のビニル単量体0~50重量%からなる、請求項1~3のいずれかに記載のコアシェルポリマー含有エポキシ樹脂組成物。 - 前記コアシェルポリマー(B)のシェル部が、
2-アルコキシエチル(メタ)アクリレート5~99重量%、グリシジル(メタ)アクリレート、アリルグリシジルエーテル、及びグリシジルアルキル(メタ)アクリレートからなる群から選ばれる1種以上の単量体1~50重量%、並びに、その他のビニル単量体0~50重量%からなる、請求項1~4のいずれかに記載のコアシェルポリマー含有エポキシ樹脂組成物。 - 前記コアシェルポリマー(B)のシェル部が、
2-メトキシエチルアクリレート5~99重量%、グリシジル(メタ)アクリレート、アリルグリシジルエーテル、及びグリシジルアルキル(メタ)アクリレートからなる群から選ばれる1種以上の単量体1~50重量%、並びに、その他のビニル単量体0~50重量%からなる、請求項1~5のいずれかに記載のコアシェルポリマー含有エポキシ樹脂組成物。 - 前記コアシェルポリマー(B)のシェル部のガラス転移温度が20℃未満である請求項1~6のいずれかに記載のコアシェルポリマー含有エポキシ樹脂組成物。
- 前記コアシェルポリマー(B)が、
コア部とシェル部の間に中間層を含み、
その中間層が、多官能性単量体30~100重量%、及びその他のビニル単量体0~70重量%を含む請求項1~7のいずれかに記載のコアシェルポリマー含有エポキシ樹脂組成物。 - 請求項1~8のいずれかに記載のコアシェルポリマー含有エポキシ樹脂組成物の硬化物であって、前記コアシェルポリマー(B)が硬化物中に一次粒子の状態で分散しているコアシェルポリマー含有エポキシ樹脂組成物の硬化物。
- 請求項1~8のいずれかに記載のコアシェルポリマー含有エポキシ樹脂組成物の製造方法であって、順に、
前記コアシェルポリマー(B)が水媒体中に分散されてなる水媒体分散液を、20℃における水に対する溶解度が5重量%以上40重量%以下の有機溶媒と混合した後、さらに過剰の水と混合して、コアシェルポリマー(B)緩凝集体を得る第1工程と、
凝集したコアシェルポリマー(B)を液相から分離・回収した後、再度有機溶媒と混合して、コアシェルポリマー(B)の有機溶媒分散液を得る第2工程と、
前記有機溶媒分散液をさらにエポキシ樹脂と混合した後、有機溶媒を留去する第3工程とを含む、コアシェルポリマー含有エポキシ樹脂組成物の製造方法。
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EP3056540A1 (en) | 2016-08-17 |
JPWO2015053289A1 (ja) | 2017-03-09 |
TW201529699A (zh) | 2015-08-01 |
CN105612215B (zh) | 2018-01-19 |
US20160251510A1 (en) | 2016-09-01 |
ES2778199T3 (es) | 2020-08-10 |
US10370531B2 (en) | 2019-08-06 |
JP6463271B2 (ja) | 2019-01-30 |
EP3056540B1 (en) | 2020-02-19 |
EP3056540A4 (en) | 2017-06-28 |
CN105612215A (zh) | 2016-05-25 |
TWI652303B (zh) | 2019-03-01 |
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