Hydrogenated terpene polyphenol copolymer resin

Abstract

To provide a terpene-based resin which has excellent adhesion to highly polar adherends such as glass, and which has high transparency and good weather resistance; and an adhesive composition using the same.SOLUTION: Provided are: a hydrogenated terpene-polyphenol copolymer resin obtained by hydrogenating a terpene-polyphenol copolymer resin which can be obtained by polymerizing a terpene-based compound and a polyphenol-based compound; and an adhesive composition obtained by mixing the hydrogenated terpene-polyphenol copolymer resin with a base polymer.SELECTED DRAWING: None

Description

[Technical Field]

[0001] The present invention relates to a hydrogenated terpene-polyphenol copolymer resin and an adhesive composition containing the copolymer resin. [Background technology]

[0002] Terpene phenolic resins are liquid or resinous compounds obtained by copolymerizing phenol with terpene, an essential oil extracted from pine trees and citrus peels. Various products with different polarity, softening point, glass transition temperature, etc., are commercially available depending on the raw material monomer composition and degree of polymerization.

[0003] These resins can be blended with polymeric materials such as rubber and thermoplastic elastomers to adjust the viscoelasticity and polarity of the polymeric materials. These properties are utilized in a variety of fields, including pressure sensitive adhesives, rubber products such as tires, polymer modifiers, and dispersibility improvers.

[0004] For example, in the field of pressure-sensitive adhesives, it is known to blend a terpene phenol resin as a tackifying resin into an acrylic pressure-sensitive adhesive containing an acrylic polymer as the main component in order to improve adhesion to low-polarity adherends such as polyolefins (e.g., Patent Documents 1 and 2). However, blending of a terpene phenol resin leads to a decrease in the weather resistance and transparency that are characteristic of acrylic pressure-sensitive adhesives, and therefore, use of the terpene phenol resin in applications requiring optical properties, such as laminating various sheets and films in the electronics field, has sometimes been avoided.

[0005] In view of the above, the present applicant has proposed the use of a hydrogenated terpene phenolic resin, which is a terpene phenolic resin that has been subjected to a hydrogenation treatment, as a tackifying resin for acrylic adhesives (Patent Document 3). According to this document, the use of a hydrogenated terpene phenolic resin can improve the adhesive strength to low-polarity adherends without reducing the weather resistance or transparency of the acrylic adhesive. On the other hand, with respect to high-polarity adherends such as glass, the thickness of the adhesive layer has become thinner in line with the recent trend toward lighter and thinner displays, making it difficult to achieve sufficient adhesive strength. [Prior art documents] [Patent documents]

[0006] [Patent Document 1] Japanese Patent Application Laid-Open No. 2015-42729 [Patent Document 2] Patent Publication No. 2021-70744 [Patent Document 3] Japanese Patent Application Laid-Open No. 2007-224258 Summary of the Invention [Problem to be solved by the invention]

[0007] An object of the present invention is to provide a novel terpene resin that exhibits excellent adhesive properties, particularly adhesive strength to highly polar adherends such as glass, and also exhibits excellent weather resistance and transparency, and a pressure-sensitive adhesive composition using the same. [Means for solving the problem]

[0008] The present inventors have found that a hydrogenated terpene polyhydric phenol copolymer resin obtained by hydrogenating a terpene polyhydric phenol copolymer resin obtained by copolymerizing a terpene compound with a polyhydric phenol compound is useful as a tackifying resin for producing a pressure-sensitive adhesive having significantly improved adhesive strength to highly polar adherends and excellent weather resistance and transparency, and have completed the present invention.

[0009] That is, the present invention comprises the following claims 1 to 11. <Claim 1> A hydrogenated terpene polyhydric phenol copolymer resin is obtained by hydrogenating a terpene polyhydric phenol copolymer resin obtained by copolymerizing a terpene compound with a polyhydric phenol compound. <Claim 2> 2. The hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, wherein the terpene compound is at least one selected from the group consisting of α-pinene, β-pinene, limonene, dipentene, Δ3-carene, alloocimene, ocimene, and myrcene. <Claim 3> 3. The hydrogenated terpene-polyphenol copolymer resin according to claim 1, wherein the polyphenol compound is represented by general formula (1).

[0010] [ka]

[0011] (R1 is a hydrogen atom or an alkyl or alkenyl group having 1 to 10 carbon atoms, R2 is an alkyl or alkenyl group having 1 to 15 carbon atoms, n is an integer of 1 to 3, and m is an integer of 0 to 2, provided that the sum of n and m is 3 or less. When n is 2 or more, two or more R1s may be the same or different. When m is 2 or more, two or more R2s may be the same or different.) <Claim 4> 4. The hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, wherein the polyhydric phenol compound is at least one selected from the group consisting of catechol, resorcinol, pyrogallol, and guaiacol. <Claim 5> 5. The hydrogenated terpene-polyphenol copolymer resin according to claim 1, wherein the copolymerization ratio of the terpene compound is 20 to 99 mol %. <Claim 6> 6. The hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, which has a weight average molecular weight (Mw) of 400 to 5,000 in terms of polystyrene as determined by a GPC (gel permeation chromatography) method. <Claim 7> 7. The hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, which has a softening point of 70 to 180°C. <Claim 8> 8. The hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, having a hydroxyl value of 10 to 300 mgKOH / g. <Claim 9> 9. The hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, wherein the hydrogenation rate is 5 to 100%. <Claim 10> 10. The method for producing a hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, which comprises hydrogenating a terpene polyhydric phenol copolymer resin obtained by copolymerizing a terpene compound and a polyhydric phenol compound. <Claim 11> 10. A pressure-sensitive adhesive composition comprising 100 parts by weight of a base polymer and 1 to 300 parts by weight of the hydrogenated terpene polyhydric phenol copolymer resin according to claim 1. [Effects of the Invention]

[0012] The hydrogenated terpene polyhydric phenol copolymer resin of the present invention has an excellent effect of modifying polymeric materials such as rubber and thermoplastic elastomers. In particular, when blended into an adhesive, the resin exhibits excellent adhesive properties to adherends with high polarity such as glass, and can provide an adhesive having excellent transparency and heat resistance stability. Therefore, the resin can be used in a variety of applications including the electronics field. [Brief explanation of the drawings]

[0013] [Figure 1] 1 is a GPC chart of the terpene-polyhydric phenol copolymer resin of Production Example 1. [Figure 2] 1 is a proton nuclear magnetic resonance ( 1 H-NMR) spectrum of the terpene polyhydric phenol copolymer resin of Production Example 1. [Figure 3] 1 is a GPC chart of a hydrogenated terpene polyhydric phenol copolymer resin of Production Example 4. [Figure 4]1 is a proton nuclear magnetic resonance ( 1 H-NMR) spectrum of the hydrogenated terpene polyhydric phenol copolymer resin of Production Example 4. Best conditions for carrying out the invention

[0014] The present invention will be described below by constituent element. <Hydrogenated terpene polyphenol copolymer resin> The hydrogenated terpene polyhydric phenol copolymer resin of the present invention is a resinous compound obtained by hydrogenating a terpene polyhydric phenol copolymer resin obtained by copolymerizing a terpene compound and a polyhydric phenol compound. First, the terpene-polyhydric phenol copolymer resin will be described.

[0015] The terpene compounds are hydrocarbons and their oxygen-containing derivatives in which multiple isoprene units, represented by the molecular formula C5H8, are bonded together, and are classified into monoterpenes (C5H8)2, sesquiterpenes (C5H8)3, diterpenes (C5H8)4, etc., depending on the number of isoprene units. Of these, monoterpenes and sesquiterpenes are preferred. The terpene compound is preferably an alicyclic terpene having a carbon ring in the molecule, and more preferably a terpene hydrocarbon having no heteroatoms such as hydroxyl groups in the molecule.

[0016] Specific examples of terpene compounds include α-pinene, β-pinene, 3-carene, camphene, tricyclene, limonene, dipentene, α-phellandrene, β-phellandrene, α-terpinene, β-terpinene, γ-terpinene, terpinolene, ocimene, alloocimene, myrcene, 1,8-cineole, 1,4-cineole, α-terpineol, β-terpineol, γ-terpineol, linalool, longifolene, caryophyllene, and farnesene. Among these, α-pinene, β-pinene, 3-carene, limonene, dipentene, ocimene, alloocimene, myrcene, longifolene, and caryophyllene are preferred, and α-pinene, β-pinene, 3-carene, limonene, and dipentene are more preferred. These compounds can be used alone or in combination of two or more.

[0017] The polyhydric phenol compound is a compound in which two or more hydrogen atoms of an aromatic hydrocarbon are substituted with hydroxyl groups or alkoxy groups, and is represented by the general formula (1).

[0018] [ka]

[0019] (R1 is a hydrogen atom or an alkyl or alkenyl group having 1 to 10 carbon atoms, R2 is an alkyl or alkenyl group having 1 to 15 carbon atoms, n is an integer of 1 to 3, and m is an integer of 0 to 2, provided that the sum of n and m is 3 or less. When n is 2 or more, two or more R1s may be the same or different. When m is 2 or more, two or more R2s may be the same or different.)

[0020] Specific examples of polyhydric phenol compounds include catechol, resorcinol, hydroquinone, guaiacol, p-methoxyphenol, m-methoxyphenol, pyrogallol, phloroglucinol, eugenol, propylcatechol, etc. These can be used alone or in combination of two or more.

[0021] It is known that catechol, guaiacol, pyrogallol, etc. are extracted or derived from renewable natural resources. In recent years, there have been concerns about global warming due to the depletion of petroleum resources and increased carbon dioxide emissions, so it is preferable to use such plant-derived polyhydric phenol compounds. In the terpene-polyhydric phenol copolymer resin of the present invention, the terpene compound as a copolymerization component is usually an essential oil component derived from a plant. Therefore, by using the terpene-polyhydric phenol compound in combination with a plant-derived polyhydric phenol compound, a material with a high biomass content and low environmental impact can be provided. For example, pyrogallol can be produced by decarboxylation of gallic acid, which is found in a variety of plants, such as Chinese gallnut (a gall from the Chinese oak tree), gallnut (a gall from beech and oak trees in the Middle East), witch hazel (a plant of the Hamamelidaceae family), tea leaves, and oak bark. It is also known that catechol can be produced by microbial fermentation using plant-derived sugars.

[0022] The terpene polyhydric phenol copolymer resin may contain at least one other monomer selected from the group consisting of monohydric phenol compounds and vinyl compounds as a copolymerization component other than the terpene compound and polyhydric phenol compound, in an amount of approximately 50 mol% or less as an overall copolymerization ratio, as long as the effects of the present invention are not impaired.

[0023] The monohydric phenol compound is a compound in which one hydrogen atom of an aromatic hydrocarbon is substituted with a hydroxyl group or an alkoxy group, and specific examples thereof include phenol, cresol, xylenol, ethylphenol, propylphenol, butylphenol, octylphenol, nonylphenol, decylphenol, thymol, carvacrol, etc. These can be used alone or in combination of two or more.

[0024] Examples of vinyl compounds include ethylene, propylene, butylene, butadiene, isoprene, piperylene, cyclopentadiene, hexene, vinyl acetate, vinyl chloride, styrene, α-methylstyrene, coumarone, indene, vinyltoluene, isopropenyltoluene, divinylbenzene, divinyltoluene, 2-phenyl-2-butene, vinylnaphthalene, etc. Preferred are styrene, α-methylstyrene, etc., and these can be used alone or in combination of two or more.

[0025] The synthesis method of the terpene-polyhydric phenol copolymer resin is not particularly limited, and can be based on a known synthesis method for terpene-phenol resins, except that phenol is replaced with a polyhydric phenol compound. For example, the terpene-polyhydric phenol copolymer resin can be produced by adding a terpene compound, a polyhydric phenol compound, and optionally other monomers, individually or as a mixture, dropwise to an organic solvent in the presence of a Friedel-Crafts catalyst, reacting them at a predetermined temperature for a predetermined time, and then removing the catalyst, unreacted monomers, solvent, etc., by methods such as water washing or distillation, as necessary.

[0026] The ratio of the terpene compound to the polyhydric phenol compound used in the synthesis of the terpene-polyhydric phenol copolymer resin is not particularly limited, but the ratio of the terpene compound to the total amount of the terpene compound and the polyhydric phenol compound is preferably 20 to 99 mol%, more preferably 40 to 95 mol%, and even more preferably 50 to 90 mol%. If it is less than 20 mol%, the resin yield may be too low, and if it exceeds 99 mol%, the polyhydric phenol structure in the resin may be too small to exhibit the desired properties, which is not preferred.

[0027] Examples of the catalyst include, but are not limited to, hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, hydrofluoric acid, p-toluenesulfonic acid, methanesulfonic acid, trifluoroacetic acid, trifluoromethanesulfonic acid, aluminum chloride, iron chloride, zinc chloride, copper chloride, boron trifluoride, boron trifluoride ether complex, boron trifluoride phenol complex, solid phosphoric acid, activated clay, zeolite, and cation exchange resin.

[0028] When the reaction is carried out in a batch system, the amount of catalyst used is 0.01 to 20% by weight, preferably 1 to 10% by weight, based on the raw material monomer. If the amount of catalyst is less than 0.01% by weight, the reaction yield will be significantly reduced, while if it exceeds 20% by weight, the catalytic effect will not increase, which is not preferable.

[0029] Furthermore, a reaction solvent does not necessarily have to be used, but a solvent may be used for the purpose of suppressing heat generation accompanying the polymerization reaction, allowing the reaction to proceed gently, etc. The solvent is not particularly limited as long as it does not inhibit the polymerization, and examples thereof include saturated hydrocarbons such as pentane, hexane, heptane, octane, nonane, decane, cyclopentane, cyclohexane, methylcyclohexane, cyclooctane, and paramenthane, aromatic hydrocarbons such as benzene, toluene, xylene, cumene, and cymene, and ethers such as diethyl ether, diisopropyl ether, tetrahydrofuran, and dioxane.

[0030] The amount of solvent used is preferably 500% by weight or less, more preferably 300% by weight or less, based on the total amount of the terpene compound and polyhydric phenol compound as raw materials. If the amount of solvent exceeds 500% by weight, batch efficiency decreases and production costs increase, which is not preferable.

[0031] The reaction temperature is appropriately selected taking into consideration the activity of the catalyst used, the boiling point of the solvent, etc., but is usually -20 to 150°C, preferably 0 to 100°C. If the temperature is below -20°C, the reaction slows down significantly, while if the temperature exceeds 150°C, the reaction becomes unstable and is not preferred. In particular, when aluminum chloride or boron trifluoride is used as the catalyst, the reaction temperature is preferably 0 to 80°C, more preferably 10 to 60°C.

[0032] The weight-average molecular weight (Mw) of the terpene-polyhydric phenol copolymer resin obtained in this manner is usually 400 to 5,000, preferably 500 to 4,000, and more preferably 600 to 3,000. If Mw is less than 400, the resin itself becomes difficult to handle, and there is a concern that it may bleed out after being compounded. On the other hand, if Mw exceeds 5,000, it may become extremely difficult to dissolve the resin in rubber or thermoplastic elastomer, which is undesirable. The average molecular weight in this specification is a value measured by gel permeation chromatography (GPC) using standard polystyrene as a standard substance.

[0033] The softening point of the terpene polyhydric phenol copolymer resin is not particularly limited, but is preferably 70 to 180°C, more preferably 80 to 160°C, and even more preferably 100 to 140°C. If the softening point is less than 70°C, there is a concern that the resin may bleed out after being blended. On the other hand, if the softening point exceeds 180°C, it may become extremely difficult to dissolve the resin in rubber or a thermoplastic elastomer, which is undesirable. The softening point in this specification is the softening point measured by the ring and ball method according to JIS K2207.

[0034] The hydroxyl value of the terpene polyhydric phenol copolymer resin is usually in the range of 10 to 300 mgKOH / g, preferably 20 to 250 mgKOH / g. If the hydroxyl value is less than 10 mgKOH / g, sufficient modification effect of rubber or thermoplastic elastomer may not be obtained. On the other hand, if the hydroxyl value exceeds 300 mgKOH / g, compatibility will be deteriorated. The hydroxyl value in this specification is the hydroxyl value measured in accordance with JIS K0070, 7.1, neutralization titration method.

[0035] Next, the hydrogenation of the terpene-polyhydric phenol copolymer resin obtained by the above method will be described. The hydrogenation method is not particularly limited, and can be carried out by a known method. For example, the terpene polyhydric phenol copolymer resin is heated in the presence of a hydrogenation catalyst, usually under a hydrogen pressure of 1 to 25 MPa, preferably 3 to 20 MPa, for 0.5 to 24 hours, preferably 1 to 10 hours.

[0036] Examples of the hydrogenation catalyst include metal catalysts such as palladium, ruthenium, rhodium, platinum, and nickel, and supported catalysts in which these are supported on carriers such as activated carbon, activated alumina, and diatomaceous earth. In this case, the reaction can be carried out in a batch system in which a powdered catalyst is suspended and stirred while the reaction is carried out, or in a continuous system using a reaction tower filled with a molded catalyst, and there are no particular limitations on the reaction system.

[0037] When the reaction is carried out in a batch system, the amount of the hydrogenation catalyst used is 0.1 to 30% by weight, preferably 1 to 20% by weight, based on the raw material (terpene polyhydric phenol copolymer resin). If the amount of catalyst is less than 0.1% by weight, the reaction rate is significantly slow, while if the amount exceeds 30% by weight, the catalytic effect is not increased, which is not preferable.

[0038] During hydrogenation, a reaction solvent does not need to be used, but alcohols, ethers, esters, and saturated hydrocarbons are usually used. The amount of the reaction solvent used is usually 10 to 500% by weight, preferably about 50 to 300% by weight, based on the raw materials.

[0039] The reaction temperature during hydrogenation is not particularly limited, but is usually 0 to 300° C., and preferably 50 to 250° C. If the reaction temperature is below 0° C., the reaction rate will be significantly slow, while if it exceeds 300° C., decomposition of the hydrogenated product will increase, which may result in a decrease in the yield of the target resin.

[0040] In the hydrogenation reaction, hydrogen is added to the double bonds in the terpene-polyhydric phenol copolymer resin to form carbon-carbon single bonds. The double bonds include those of aromatic rings derived from polyhydric phenols, etc. The hydrogenation rate of the double bonds is 5% or more, preferably 10% or more, and more preferably 20% or more. The hydrogenation rate of the aromatic rings is 0.5% or more, preferably 1% or more. The higher the hydrogenation rate of the double bonds, the higher the transparency and oxidation stability of the resulting resin, making it suitable for use in applications requiring transparency, such as optical materials. On the other hand, if the hydrogenation rate of the double bonds is less than 5%, the resin will have poor color or insufficient oxidation stability.

[0041] Here, the hydrogenation rate of the double bond (hydrogenation rate) is 1 It is a value calculated from the integral values ​​of the peaks derived from double bonds in H-NMR (proton NMR) using the following formula. Hydrogenation rate (%)={(AB) / A}×100 A: Integrated value of the double bond peak before hydrogenation B: Integrated value of the double bond peak after hydrogenation

[0042] The weight-average molecular weight (Mw) of the hydrogenated terpene polyhydric phenol copolymer resin is usually 400 to 5,000, preferably 500 to 4,000, and more preferably 600 to 3,000. If Mw is less than 400, the resin itself becomes difficult to handle, and there is a concern that it may bleed out after being compounded. On the other hand, if Mw exceeds 5,000, it may become extremely difficult to dissolve the resin in rubber or thermoplastic elastomer, which is undesirable.

[0043] The softening point of the hydrogenated terpene polyhydric phenol copolymer resin is not particularly limited, but is preferably 70 to 180°C, more preferably 80 to 160°C, and even more preferably 100 to 140°C. If the softening point is below 70°C, the resin itself becomes difficult to handle, and there is a concern that the resin may bleed out after being compounded. On the other hand, if the softening point exceeds 180°C, it may become extremely difficult to dissolve the resin in rubber or a thermoplastic elastomer, which is undesirable.

[0044] The hydroxyl value of the hydrogenated terpene polyphenol copolymer resin varies depending on the type of elastomer to be mixed, but is typically in the range of 10 to 300 mgKOH / g, preferably 20 to 250 mgKOH / g, and more preferably 40 to 210 mgKOH / g. A hydroxyl value of less than 10 mgKOH / g is undesirable because it may not exhibit sufficient adhesive properties to highly polar substrates such as metals and glass. On the other hand, a hydroxyl value of more than 300 mgKOH / g may make it extremely difficult to dissolve the resin in low-polarity elastomers such as rubber.

[0045] To the hydrogenated terpene polyhydric phenol copolymer resin of the present invention, various additives such as known phenol-based antioxidants, phosphorus-based antioxidants, and sulfur-based antioxidants can be added.

[0046] <Adhesive composition> The hydrogenated terpene polyhydric phenol copolymer resin can be blended with a base polymer such as natural rubber or a thermoplastic elastomer to form a pressure-sensitive adhesive composition.

[0047] Thermoplastic elastomers that can be used as the base polymer are not particularly limited, and examples thereof include styrene-based block copolymers such as styrene-isoprene-styrene block copolymer, styrene-butadiene-styrene block copolymer, styrene-ethylene-butylene-styrene block copolymer, and styrene-ethylene-propylene-styrene block copolymer, ethylene-vinyl acetate copolymer, (meth)acrylic copolymer, etc. Among these, (meth)acrylic polymers are particularly preferred from the viewpoint of compatibility.

[0048] The (meth)acrylic polymer is a polymer obtained by polymerizing a polymerizable monomer containing at least an alkyl (meth)acrylate. The type of alkyl (meth)acrylate is not particularly limited, and examples thereof include methyl (meth)acrylate, ethyl (meth)acrylate, n-propyl (meth)acrylate, isopropyl (meth)acrylate, n-butyl (meth)acrylate, isobutyl (meth)acrylate, t-butyl (meth)acrylate, pentyl (amyl) (meth)acrylate, hexyl (meth)acrylate, heptyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, n-octyl (meth)acrylate, isooctyl (meth)acrylate, nonyl (meth)acrylate, decyl (meth)acrylate, undecyl (meth)acrylate, lauryl (dodecyl) (meth)acrylate, tridecyl (meth)acrylate, and tetradecyl (meth)acrylate. In this specification, the term "(meth)acrylate" means "acrylate" or "methacrylate." The alkyl (meth)acrylates may be used alone or in combination of two or more.

[0049] Furthermore, a copolymerizable polar group-containing vinyl monomer may be further contained as a polymerizable monomer other than the alkyl(meth)acrylate. As will be described later, this polar group-containing vinyl monomer is used to effectively form a crosslinked structure with a crosslinking agent having a specific functional group, such as an isocyanate-based crosslinking agent, an epoxy-based crosslinking agent, or an aziridine-based crosslinking agent, thereby achieving both cohesive strength and resilience, and further, to adjust the Tg, adhesiveness, etc. of the copolymer, as necessary.

[0050] Specific examples of polar group-containing vinyl monomers include styrene-based monomers such as styrene, α-methylstyrene, o-methylstyrene, and p-methylstyrene; carboxylic acid vinyl esters such as vinyl acetate; carboxylic acids containing a vinyl group such as (meth)acrylic acid and itaconic acid; anhydrides of the carboxylic acids having the vinyl group; vinyl monomers having a hydroxyl group such as 2-hydroxyethyl (meth)acrylate, 2-hydroxypropyl (meth)acrylate, 4-hydroxybutyl (meth)acrylate, caprolactone-modified (meth)acrylate, polyoxyethylene (meth)acrylate, and polyoxypropylene (meth)acrylate; and nitrogen-containing vinyl monomers such as (meth)acrylonitrile, N-vinylpyrrolidone, N-vinylcaprolactam, N-vinyllaurolactam, (meth)acryloylmorpholine, (meth)acrylamide, dimethyl(meth)acrylamide, N-methylol(meth)acrylamide, N-butoxymethyl(meth)acrylamide, and dimethylaminomethyl (meth)acrylate. The polar group-containing vinyl monomers may be used alone or in combination of two or more kinds.

[0051] Furthermore, in the present invention, by blending a small amount of a polyfunctional (meth)acrylate into the base polymer, crosslinking can be carried out simultaneously with the polymerization of the acrylic copolymer. Examples of such polyfunctional (meth)acrylates include 1,4-butanediol di(meth)acrylate, 1,6-hexanediol di(meth)acrylate, 1,9-nonanediol di(meth)acrylate, (poly)ethylene glycol di(meth)acrylate, (poly)propylene glycol di(meth)acrylate, neopentyl glycol di(meth)acrylate, pentaerythritol di(meth)acrylate, glycerin methacrylate acrylate, pentaerythritol tri(meth)acrylate, trimethylolpropane trimethacrylate, allyl (meth)acrylate, vinyl (meth)acrylate, divinylbenzene, epoxy (meth)acrylate, polyester (meth)acrylate, and urethane (meth)acrylate. These may be used alone or in combination of two or more. The amount of the polyfunctional (meth)acrylate blended is usually 0 to 5 parts by weight based on 100 parts by weight of the acrylic copolymer.

[0052] The (meth)acrylic polymer can be produced by (co)polymerizing at least one alkyl (meth)acrylate with other polymerizable monomers. The polymerization reaction method is not particularly limited, but radical polymerization or anionic polymerization is preferred. The (meth)acrylic polymer can be produced by a conventionally known polymerization method such as bulk polymerization, solution polymerization, suspension polymerization, or emulsion polymerization, with solution polymerization or bulk polymerization being preferred. When two or more types of polymerizable monomers are copolymerized, the sequence of the monomers is not particularly limited, and may be random, alternating, or block.

[0053] In the case of radical polymerization, peroxide-based polymerization initiators such as benzoyl peroxide and lauroyl peroxide, azo-based polymerization initiators such as azobisisobutylnitrile, and the like can be used as necessary, as well as acetophenone-based polymerization initiators, benzoin ether-based polymerization initiators, benzil ketal-based polymerization initiators, acylphosphine oxide-based polymerization initiators, benzoin-based polymerization initiators, benzophenone-based polymerization initiators, and the like can be used as photopolymerization initiators.

[0054] On the other hand, as a polymerization initiator for anionic polymerization, alkali metals such as lithium, sodium, potassium, etc.; alkyllithium compounds such as methyllithium, ethyllithium, n-butyllithium, s-butyllithium, t-butyllithium, etc.; alkali metal-naphthalene complexes such as lithium-naphthalene complex, sodium-naphthalene complex, potassium-naphthalene complex, etc.; Grignard reagents; ketyl anion radical complexes; enolate anions; alkoxide anions such as t-butoxypotassium; lithium aluminum hydride, etc. can be used. The amount of the polymerization initiator used is not particularly limited, but is usually 0 to 5 parts by weight per 100 parts by weight of the total amount of the polymerizable monomers used.

[0055] Although a solvent is not required for the polymerization reaction, it may be used to suppress an increase in the viscosity of the reaction solution or to facilitate temperature control during the reaction. For example, in radical polymerization, solvents include esters such as ethyl acetate and methyl acetate, ketones such as acetone and methyl ethyl ketone, alcohols such as methanol, ethanol, and butanol, aliphatic hydrocarbons such as cyclohexane, hexane, and heptane, and aromatic hydrocarbons such as toluene and xylene. On the other hand, in anionic polymerization, solvents include aliphatic hydrocarbons such as hexane, heptane, and cyclohexane, aromatic hydrocarbons such as benzene, toluene, and xylene, ethers such as diethyl ether, tetrahydrofuran, tetrahydropyran, 1,4-dioxane, 1,2-dimethoxyethane, and anisole, tertiary amines such as triethylamine and pyridine, and aprotic polar solvents such as N,N-dimethylformamide and N,N-dimethylacetamide. These solvents may be used alone or in combination.

[0056] The weight average molecular weight of the (meth)acrylic polymer obtained by the above method is preferably 300,000 to 3,000,000, and more preferably 500,000 to 2,500,000, as calculated using standard polystyrene as measured by gel permeation chromatography (GPC).

[0057] The pressure-sensitive adhesive composition of the present invention is obtained by blending 1 to 300 parts by weight, preferably 5 to 100 parts by weight, and more preferably 10 to 60 parts by weight of the hydrogenated terpene polyhydric phenol copolymer resin of the present invention with 100 parts by weight of the base polymer. If the amount of hydrogenated terpene polyhydric phenol copolymer resin is less than 1 part by weight, the effect of blending the hydrogenated terpene polyhydric phenol copolymer resin becomes difficult to see. On the other hand, if the amount exceeds 300 parts by weight, the viscosity of the pressure-sensitive adhesive becomes too high, and the balance of the adhesive properties of ball tack, adhesive strength, and holding power becomes poor.

[0058] The pressure-sensitive adhesive composition of the present invention may contain a crosslinking agent as needed. Examples of crosslinking agents include polyisocyanates, epoxy resins, polycarbodiimide compounds, aziridine compounds, polyvalent metal salts, and metal chelates. By using at least one of these crosslinking agents, the cohesive strength can be improved by bonding with the polymer chains and other compounding ingredients, and the holding power and constant load at high temperatures can be increased.

[0059] The content of the crosslinking agent varies depending on the type, but is typically in the range of 0.005 to 10 parts by weight, and preferably 1.0 to 5 parts by weight, per 100 parts by weight of the (meth)acrylic polymer. If the crosslinking agent content is less than 0.005 parts by weight, this may result in insufficient heat resistance or a decrease in adhesive strength to the adherend. On the other hand, if the content exceeds 10 parts by weight, excessive crosslinking is likely to occur, resulting in a decrease in flexibility, a decrease in adhesion to the adherend, and an insufficient peel strength. Furthermore, excess crosslinking agent may also reduce the adhesive properties.

[0060] When a crosslinking agent is used, the pressure-sensitive adhesive composition of the present invention is preferably subjected to a heating step to form a crosslinked structure. The heating step may be carried out before or after application to an adherend. When used as a tape in which a pressure-sensitive adhesive layer is laminated on a substrate, it is preferable in terms of production efficiency to heat the pressure-sensitive adhesive composition after applying it to the substrate. The heating temperature is set appropriately depending on the type of crosslinking agent used, but is usually in the range of 40°C to 130°C, and preferably 50°C to 100°C. The heating time is 30 minutes to 7 days, preferably 1 hour to 5 days.

[0061]

[0043] The pressure-sensitive adhesive composition of the present invention may further contain additives such as plasticizers, softeners, pigments, fillers, diluents, antioxidants, ultraviolet absorbers, antioxidants, light stabilizers, surfactants, release modifiers, and antistatic agents, as required, and the form thereof may be any of a solution type, a water dispersion type, a UV curable type, a hot melt type, etc.

[0062] The pressure-sensitive adhesive composition of the present invention can also be used by being coated on a pressure-sensitive adhesive sheet or tape. In this case, the support is not particularly limited, and examples thereof include plastic films, paper, nonwoven fabrics, and also sheet or tape-shaped materials such as metal foils and plastic or rubber foams.

[0063] The method for processing the pressure-sensitive adhesive composition of the present invention onto the above-mentioned support is not particularly limited. For example, a method for producing a solvent-based acrylic pressure-sensitive adhesive composition containing an acrylic polymer as the main component is to stir and dissolve a mixture of the acrylic polymer, the hydrogenated terpene polyphenol copolymer resin of the present invention, and a crosslinking agent in an organic solvent, such as toluene or ethyl acetate, to prepare a pressure-sensitive adhesive solution with a solids content of 10 to 70 wt %. The pressure-sensitive adhesive composition thus prepared is applied to a support using, for example, a roll coater or bar coater, and heated to volatilize the solvent, thereby obtaining a pressure-sensitive adhesive tape or pressure-sensitive adhesive sheet. The thickness of the pressure-sensitive adhesive layer is not particularly limited, but is usually about 0.01 to 1.0 mm.

[0064] The adhesive composition of the present invention may be applied to any substrate, including, but not limited to, wood, metal, plastic, rubber, concrete, glass, tile, ceramics, and composite materials. Among these, the adhesive composition is preferred for highly polar substrates such as concrete, glass, tile, and ceramics, since it can exhibit good adhesive properties. While the detailed mechanism is unclear, it is believed that this is because multiple hydroxyl groups present in close proximity in the structure of the hydrogenated terpene polyhydric phenol copolymer resin form strong hydrogen bonds with hydroxyl groups on the substrate.

[0065] The pressure-sensitive adhesive composition of the present invention has high fixation properties to highly polar adherends such as glass, etc. Furthermore, it has excellent heat resistance and transparency, and therefore can be used in a variety of applications, including the fields of optics and electronics, architecture, and medicine including dentistry. [Example]

[0066] The present invention will be described in more detail below with reference to examples and comparative examples, but the present invention is not limited to these examples. The softening point and hydroxyl value of the (hydrogenated) terpene polyhydric phenol copolymer resin were measured by the methods described in the respective measurement items in this specification. The hydrogenation rate, molecular weight, and hue were measured by the following methods.

[0067] (Hydrogenation rate) Proton nuclear magnetic resonance (H-NMR) spectra were measured using a nuclear magnetic resonance spectrometer AVANCEIII 600MHz (manufactured by BRUKER). 1,1,2,2-tetrachloroethane-d2 was used as the deuterium solvent. The hydrogenation rate was calculated using the above formula from the integral values ​​of the double bond-derived peaks of each resin before and after hydrogenation. (molecular weight) The molecular weight was measured using gel permeation chromatography (GPC) in terms of standard polystyrene. The detector was a WATERS 2414 differential refractometer (WATERS), the pump was a WATERS 515 high-performance liquid chromatograph (WATERS), and the columns were TSK-gel G2000H8 x 2 and G3000HXL x 1 (TOSOH). The measurement conditions were tetrahydrofuran as the eluent, a flow rate of 1.0 mL / min, and 250 μL of sample solution with a sample concentration of 5 mg / mL was injected. (hue) 10 g of sample was dissolved in 10 g of toluene, and the color was measured on the Gardner scale using a spectrophotometer / haze meter COH7700 (manufactured by Nippon Denshoku Industries Co., Ltd.).

[0068] Production Example 1 (Production of terpene polyphenol copolymer resin) A flask equipped with a stirrer, reflux condenser, thermometer, dropping pump, and nitrogen gas inlet was charged with 300 g of toluene, 55 g (0.5 mol) of catechol, and 20 g of boron trifluoride diethyl ether complex, and stirring was initiated. 272 ​​g (2.0 mol) of α-pinene was added dropwise over 6 hours at a reaction temperature of 25-30°C. The mixture was allowed to react for 1 hour, then washed with water and distilled under reduced pressure at 245°C and 3 mmHg to obtain 225 g of a reddish-brown terpene polyphenol copolymer resin with a softening point of 126°C. The Mn (number-average molecular weight), Mw (weight-average molecular weight), and Mz (Z-average molecular weight) were 610,745,870, respectively. The hydroxyl value was 120 mgKOH / g, and the color (Gardner scale) was 14. The GPC chart and 1H-NMR chart of the obtained terpene-polyhydric phenol copolymer resin are shown in Figs. 1 and 2, respectively.

[0069] Production Example 2 (Production of hydrogenated terpene polyphenol copolymer resin) 100 g of the terpene polyhydric phenol copolymer resin obtained in Production Example 1, 100 g of 2-propanol, and 5 g of powdered 5% palladium-supported alumina catalyst were charged into an autoclave, which was then sealed. The atmosphere was replaced with hydrogen gas, and hydrogen gas was then introduced under a pressure of 1 MPa. The mixture was heated with stirring to 180°C, at which point the hydrogen pressure was increased to 5 MPa. The reaction was continued for 1 hour while maintaining the pressure at 5 MPa by replacing the absorbed hydrogen. After the reaction, the catalyst was filtered, and the 2-propanol was removed by vacuum distillation to obtain 100 g of hydrogenated terpene polyhydric phenol copolymer resin with a softening point of 130°C. The Mn, Mw, and Mz values ​​were 620, 750, and 870, respectively. The hydroxyl value was 119 mgKOH / g, the color (Gardner scale) was 2, and the hydrogenation rate was 30%.

[0070] Manufacturing Examples 3-20 Copolymerization reactions and, if necessary, hydrogenation reactions were carried out in the same manner as in Production Examples 1 and 2, except that the types of terpene compounds and polyhydric phenol compounds used, their mixing ratios, and the hydrogenation time were changed as shown in Table 1, to obtain resins having the properties listed in each item in Table 1. The GPC chart and 1H-NMR chart of the hydrogenated terpene polyhydric phenol copolymer resin obtained in Production Example 4 are shown in FIGS. 3 and 4, respectively.

[0071] [Table 1]

[0072] Examples 1 to 15, Comparative Examples 1 to 9 (Evaluation of adhesive composition) An acrylic pressure-sensitive adhesive composition was prepared by mixing 100 parts by weight of an acrylic block copolymer (CLARITY LA2140 (manufactured by Kuraray Co., Ltd.)), 30 parts by weight of the (hydrogenated) terpene polyhydric phenol copolymer resin produced above or a commercially available tackifier resin, and 20 parts by weight of a liquid acrylic polymer (ALFON UP-1061 (manufactured by Toagosei Co., Ltd.)) as a plasticizer. This pressure-sensitive adhesive composition was applied to a 38 μm thick PET film to form a 30 μm thick pressure-sensitive adhesive layer, and then dried to produce a pressure-sensitive adhesive sheet.

[0073] The commercially available tackifying resins used were as follows: Comparative Example 6: Terpene phenol resin A (YS Polystar T115, manufactured by Yasuhara Chemical Co., Ltd.) Comparative Example 7: Terpene phenol resin B (YS Polystar K125, manufactured by Yasuhara Chemical Co., Ltd.) Comparative Example 8: Hydrogenated terpene phenol resin (YS Polystar NH, manufactured by Yasuhara Chemical Co., Ltd.) Comparative Example 9: Rosin ester resin (Super Ester A100, manufactured by Arakawa Chemical Industries, Ltd.)

[0074] The obtained PSA sheets were evaluated for loop tack (to SUS, glass, PE), adhesive strength (to SUS, glass, PE), holding power (to SUS, PE), and weather resistance using the methods described below. The results are shown in Table 2.

[0075] (Loop Tuck) A test piece of the pressure-sensitive adhesive sheet was looped with the adhesive side facing outwards, and a 25mm x 25mm area was attached to the adherend. The strength when the piece was immediately pulled away was measured using a tensile tester. The pulling speed was 300mm / min and the measurement temperature was 23°C.

[0076] (Adhesive strength) The sheet was cut to a width of 25 mm and a length of approximately 200 mm and laminated to a SUS plate, glass plate, or polyethylene (PE) plate using a 2 kg roller in a 23°C atmosphere, with two passes. 30 minutes after lamination, the 180° peel adhesive strength was measured in a 23°C atmosphere. A tensile tester was used for the measurement, and the tensile speed was 300 mm / min.

[0077] (Shear Adhesion Failure Temperature Test (SAFT)) The sheet was cut to a width of 25 mm and a length of approximately 200 mm and bonded to a SUS or PE plate in a 23°C atmosphere by rolling a 25mm long, 2kg roller back and forth twice. 30 minutes after bonding, the sheet was left to stand in a 40°C atmosphere for 30 minutes, after which a 1kg load was applied. At the same time as applying the load, the temperature was raised at a rate of 2°C every 5 minutes, and the temperature was recorded when the test piece fell from the adherend.

[0078] (weather resistance) Using a Table Sun XT750 manufactured by Suga Testing Instruments Co., Ltd., the condition of the adhesive was observed after irradiating the test pieces with 48,000 lx light for 100 hours in a 50°C environment. If the adhesive had yellowed and the surface had cracked, it was marked x, and if there was no change, it was marked o.

[0079] [Table 2]

[0080] As is clear from Table 2, when the hydrogenated terpene polyphenol copolymer resin of the present invention is blended with an acrylic pressure-sensitive adhesive, the weather resistance is better than that of unhydrogenated terpene polyphenol copolymer resins, and the adhesive properties, particularly the tack and adhesive strength to glass, can be improved. [Industrial Applicability]

[0081] The hydrogenated terpene polyhydric phenol copolymer resin of the present invention has an excellent modifying effect on rubber, thermoplastic elastomers, etc., and is useful as a pressure-sensitive adhesive, adhesive, polymer modifier, sealant, rubber additive, paint modifier, etc. In addition, they can be used in a wide variety of applications, such as polymer materials, compatibilizers, crystal nucleating agents, surface modifiers, filler dispersion improvers, fiber dispersion improvers, plasticizers, lubricants, hardeners, binders, oils and fats, traffic paints, inks, printing inks, toners, adhesives, sizing agents, paper strength agents, road paving compositions, civil engineering and construction materials, raw materials for polymer materials, and modifiers, and have extremely useful industrial effects.

Claims

1. A hydrogenated terpene polyhydric phenol copolymer resin obtained by hydrogenating a terpene polyhydric phenol copolymer resin obtained by copolymerizing a terpene compound and a polyhydric phenol compound, The polyhydric phenol compound is represented by the general formula (1) 【Chemistry 1】 (R1 is a hydrogen atom, R2 is an alkyl or alkenyl group having 1 to 15 carbon atoms, n is an integer of 1 to 3, and m is an integer of 0 to 2, provided that the sum of n and m is 3 or less. When m is 2 or more, two or more R2's may be the same or different from each other. the copolymerization ratio of the terpene compound is 50 to 90 mol %, The softening point is 70 to 180°C, a hydroxyl value of 10 to 300 mgKOH / g; The hydrogenation rate is 30 to 90%. Hydrogenated terpene polyphenol copolymer resin.

2. 2. The hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, wherein the terpene compound is at least one selected from the group consisting of α-pinene, β-pinene, limonene, dipentene, Δ3-carene, alloocimene, ocimene, and myrcene.

3. 3. The hydrogenated terpene-polyphenol copolymer resin according to claim 1, wherein the polyphenol compound is at least one selected from the group consisting of catechol, resorcinol, and pyrogallol.

4. 4. The hydrogenated terpene polyhydric phenol copolymer resin according to claim 1, wherein the weight average molecular weight (Mw) of the hydrogenated terpene polyhydric phenol copolymer resin is 400 to 5,000 in terms of polystyrene as determined by a GPC (gel permeation chromatography) method.

5. The method for producing a hydrogenated terpene polyhydric phenol copolymer resin according to any one of claims 1 to 4, which comprises hydrogenating a terpene polyhydric phenol copolymer resin obtained by copolymerizing a terpene compound and a polyhydric phenol compound.

6. A pressure-sensitive adhesive composition comprising 100 parts by weight of a base polymer and 1 to 300 parts by weight of the hydrogenated terpene polyhydric phenol copolymer resin according to any one of claims 1 to 4.

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