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JP2023177416A - Adhesive composition and adhesive sheet - Google Patents
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JP2023177416A - Adhesive composition and adhesive sheet - Google Patents

Adhesive composition and adhesive sheet Download PDF

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JP2023177416A
JP2023177416A JP2022090061A JP2022090061A JP2023177416A JP 2023177416 A JP2023177416 A JP 2023177416A JP 2022090061 A JP2022090061 A JP 2022090061A JP 2022090061 A JP2022090061 A JP 2022090061A JP 2023177416 A JP2023177416 A JP 2023177416A
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parts
monomer
mass
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ethyl acetate
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JP7151926B1 (en
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友基 霜村
Tomoki Shimomura
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Artience Co Ltd
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Toyo Ink SC Holdings Co Ltd
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Priority to JP2022148702A priority patent/JP7722306B2/en
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Publication of JP7151926B1 publication Critical patent/JP7151926B1/en
Priority to CN202380040841.2A priority patent/CN119213093A/en
Priority to KR1020247037160A priority patent/KR20250002387A/en
Priority to PCT/JP2023/017324 priority patent/WO2023233933A1/en
Publication of JP2023177416A publication Critical patent/JP2023177416A/en
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/02Non-macromolecular additives
    • C09J11/06Non-macromolecular additives organic
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C09J133/062Copolymers with monomers not covered by C09J133/06
    • C09J133/066Copolymers with monomers not covered by C09J133/06 containing -OH groups
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C09J133/08Homopolymers or copolymers of acrylic acid esters
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/14Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur or oxygen atoms in addition to the carboxy oxygen
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J175/00Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
    • C09J175/04Polyurethanes
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J7/00Adhesives in the form of films or foils
    • C09J7/30Adhesives in the form of films or foils characterised by the adhesive composition
    • C09J7/38Pressure-sensitive adhesives [PSA]
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2203/00Applications of adhesives in processes or use of adhesives in the form of films or foils
    • C09J2203/334Applications of adhesives in processes or use of adhesives in the form of films or foils as a label
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2301/00Additional features of adhesives in the form of films or foils
    • C09J2301/30Additional features of adhesives in the form of films or foils characterized by the chemical, physicochemical or physical properties of the adhesive or the carrier
    • C09J2301/312Additional features of adhesives in the form of films or foils characterized by the chemical, physicochemical or physical properties of the adhesive or the carrier parameters being the characterizing feature

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Adhesives Or Adhesive Processes (AREA)
  • Adhesive Tapes (AREA)

Abstract

【課題】
十分な粘着力、高いタック性を有し、剥離時に粘着剤が残りやすいSUS、鋼板などの高極性被着体であっても良好な再剥離性を示し、かつ貼付した状態で高温または湿熱条件下に長期保管した場合であっても十分な再剥離性を有する粘着剤組成物および粘着シート、また、貼付した状態で高温、高荷重の条件下においてもシートからの粘着剤のはみだしが少なく、高温下でも鋼板などの重量のある被着体同士を重ねて保管することのできる粘着剤組成物および粘着シートの提供。
【解決手段】
アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)、酸性基を有するモノマー(B)、水酸基を有するモノマー(C)からなるモノマー混合物の共重合体であるアクリル酸エステル共重合体と、イソシアネート系硬化剤とを含み、酸性基を有するモノマー(B)の含有率は、モノマー混合物100質量%中、0.01質量%以上6質量%以下であり、水酸基を有するモノマー(C)の含有率は、モノマー混合物100質量%中、0.05質量%以上10質量%以下であり、ゲル分率が55%以上である粘着剤組成物により解決される。
【選択図】なし
【assignment】
It has sufficient adhesive strength and high tackiness, and shows good re-peelability even on highly polar adherends such as SUS and steel plates, where adhesive tends to remain when peeled, and can withstand high temperature or moist heat conditions when attached. The adhesive composition and adhesive sheet have sufficient removability even when stored for a long time, and the adhesive does not protrude from the sheet even under high temperature and high load conditions when attached. To provide an adhesive composition and an adhesive sheet that allow heavy adherends such as steel plates to be stacked and stored even at high temperatures.
[Solution]
Acrylic is a copolymer of a monomer mixture consisting of a (meth)acrylic acid alkyl ester monomer (A) whose alkyl group has 1 to 12 carbon atoms, a monomer (B) having an acidic group, and a monomer (C) having a hydroxyl group. The content of the monomer (B) containing an acid ester copolymer and an isocyanate curing agent and having an acidic group is 0.01% by mass or more and 6% by mass or less based on 100% by mass of the monomer mixture. The content of the monomer (C) is 0.05% by mass or more and 10% by mass or less based on 100% by mass of the monomer mixture, and the adhesive composition has a gel fraction of 55% or more.
[Selection diagram] None

Description

本発明は、粘着剤組成物および粘着シートに関する。 The present invention relates to an adhesive composition and an adhesive sheet.

粘着剤から形成した粘着剤層を有する粘着シートは、接着剤と比べて取り扱いが容易であることから、表示用ラベルや固定用テープとして幅広い分野で使用されており、永久的に固定する強粘着力型と使用後に粘着シートを剥離する再剥離型に大きく分けられる。粘着剤として各樹脂系のものがあり、中でもアクリル系が広く用いられている。アクリル系粘着剤は、粘着力やタックといった粘着基本性能の制御がモノマー組成や相溶する添加剤の調整により容易であるメリットがある。 Adhesive sheets with an adhesive layer formed from adhesives are easier to handle than adhesives, so they are used in a wide range of fields as display labels and fixing tapes. There are two main types: force type and removable type, in which the adhesive sheet is peeled off after use. There are various resin-based adhesives, among which acrylic adhesives are widely used. Acrylic adhesives have the advantage that basic adhesive properties such as adhesive strength and tack can be easily controlled by adjusting the monomer composition and compatible additives.

再剥離型のアクリル系粘着剤として、特許文献1には、アルキル基の炭素数が4~12の(メタ)アクリル酸アクリルエステルを主成分単量体とし、これに少なくとも全単量体の3~20重量%のカルボキシル基含有ラジカル重合性単量体が共重合されてなるアクリル系ポリマーを、分子内にカルボキシル基と反応する官能基を有する架橋剤により、ゲル分率80重量%以上に架橋してなるアクリル系粘着剤層が特徴とする粘着剤組成物が開示されている。また、特許文献2には基材の片面に熱膨張性微小球、重量平均分子量が10万~30万で架橋剤と反応し得る30以上の酸価を有するアクリル系粘着剤及び軟化点が90℃以上、溶解パラメータ値(SP値)が8.9以上である粘着付与樹脂、架橋剤からなる粘着剤組成物を塗布して形成した粘着剤層を設けたことを特徴とする再剥離性粘着シートが開示されている。 As a removable acrylic adhesive, Patent Document 1 discloses that the main monomer is (meth)acrylic acid acrylic ester whose alkyl group has 4 to 12 carbon atoms, and at least 3 of the total monomers are used as a removable acrylic adhesive. An acrylic polymer copolymerized with ~20% by weight of a radically polymerizable monomer containing carboxyl groups is crosslinked to a gel fraction of 80% by weight or more using a crosslinking agent that has a functional group that reacts with carboxyl groups in the molecule. A pressure-sensitive adhesive composition characterized by an acrylic pressure-sensitive adhesive layer is disclosed. Further, Patent Document 2 describes thermally expandable microspheres on one side of a base material, an acrylic adhesive with a weight average molecular weight of 100,000 to 300,000, an acid value of 30 or more that can react with a crosslinking agent, and a softening point of 90. ℃ or higher and a solubility parameter value (SP value) of 8.9 or higher, a removable adhesive comprising an adhesive layer formed by applying an adhesive composition comprising a tackifying resin and a crosslinking agent. The sheet is disclosed.

特開2000-328016号公報Japanese Patent Application Publication No. 2000-328016 特開2003-160765号公報Japanese Patent Application Publication No. 2003-160765

しかしながら、特許文献1の粘着剤組成物は、被着体に貼り付けた状態で高温または湿熱条件下に長期間保管後に粘着シートを剥離すると粘着剤が被着体に残ってしまうという問題点があった。また、特許文献2の粘着シートは、常温での条件下では十分な再剥離性を確保することが難しく、高温下の条件での粘着力低下に伴う剥がれの問題や、高温下での長期保管後の再剥離性が十分ではないという課題があった。 However, the adhesive composition of Patent Document 1 has a problem in that when the adhesive sheet is peeled off after being stored for a long period of time under high temperature or moist heat conditions while being attached to an adherend, the adhesive remains on the adherend. there were. In addition, the adhesive sheet of Patent Document 2 has difficulty in ensuring sufficient removability under room temperature conditions, and has problems with peeling due to decreased adhesive strength under high temperature conditions and long-term storage under high temperature conditions. There was a problem in that the subsequent removability was not sufficient.

そこで本発明が解決しようとする課題は、十分な粘着力、高いタック性を有し、剥離時に粘着剤が残りやすいSUS、鋼板などの高極性被着体であっても良好な再剥離性を示し、かつ貼付した状態で高温または湿熱条件下に長期保管した場合であっても十分な再剥離性を有する粘着剤組成物および粘着シート、また、貼付した状態で高温、高荷重の条件下においてもシートからの粘着剤のはみだしが少なく、高温下でも鋼板などの重量のある被着体同士を重ねて保管することのできる粘着剤組成物および粘着シートを提供することにある。 Therefore, the problem to be solved by the present invention is to have sufficient adhesive strength, high tackiness, and good removability even for highly polar adherends such as SUS and steel plates, where adhesive tends to remain during peeling. Adhesive compositions and adhesive sheets that exhibit sufficient removability even when affixed and stored under high temperature or humid heat conditions for long periods of time; To provide a pressure-sensitive adhesive composition and a pressure-sensitive adhesive sheet, which have a small amount of pressure-sensitive adhesive protruding from the sheet, and which allow heavy adherends such as steel plates to be stored stacked on top of each other even at high temperatures.

本発明者は、上記課題を解決するために、アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)、酸性基を有するモノマー(B)、水酸基を有するモノマー(C)からなるモノマー混合物の共重合体であるアクリル酸エステル共重合体と、イソシアネート系硬化剤を含み、酸性基を有するモノマー(B)の含有率は、モノマー混合物100質量%中、0.01質量%以上6質量%以下であり、水酸基を有するモノマー(C)の含有率は、モノマー混合物100質量%中、0.05質量%以上10質量%以下であり、ゲル分率が55%以上である粘着剤組成物を見出した。 In order to solve the above problems, the present inventors have discovered a (meth)acrylic acid alkyl ester monomer (A) in which the alkyl group has 1 to 12 carbon atoms, a monomer (B) having an acidic group, and a monomer (B) having a hydroxyl group. The content of monomer (B) containing an acrylic ester copolymer which is a copolymer of a monomer mixture consisting of C) and an isocyanate curing agent and having an acidic group is 0.01% by mass in 100% by mass of the monomer mixture. The content of the monomer (C) having a hydroxyl group is 0.05% by mass or more and 10% by mass or less based on 100% by mass of the monomer mixture, and the gel fraction is 55% or more. We have discovered a certain adhesive composition.

即ち、本発明は以下の[1]~[4]に関する。 That is, the present invention relates to the following [1] to [4].

[1]アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)、酸性基を有するモノマー(B)、水酸基を有するモノマー(C)からなるモノマー混合物の共重合体であるアクリル酸エステル共重合体と、イソシアネート系硬化剤とを含み、酸性基を有するモノマー(B)の含有率は、モノマー混合物100質量%中、0.01質量%以上6質量%以下であり、水酸基を有するモノマー(C)の含有率は、モノマー混合物100質量%中、0.05質量%以上10質量%以下であり、ゲル分率が55%以上である粘着剤組成物に関する。 [1] Copolymer of a monomer mixture consisting of a (meth)acrylic acid alkyl ester monomer (A) whose alkyl group has 1 to 12 carbon atoms, a monomer (B) having an acidic group, and a monomer (C) having a hydroxyl group The content of the monomer (B) containing an acrylic ester copolymer and an isocyanate curing agent and having an acidic group is 0.01% by mass or more and 6% by mass or less based on 100% by mass of the monomer mixture. The content of the monomer (C) having a hydroxyl group is 0.05% by mass or more and 10% by mass or less based on 100% by mass of the monomer mixture, and the adhesive composition has a gel fraction of 55% or more.

[2]アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)100質量%中に占めるアルキル基の炭素数8~12である(メタ)アクリル酸アルキルエステルモノマー(a1)の含有率が55質量%以上である前記[1]記載の粘着剤組成物に関する。 [2] (Meth)acrylic acid alkyl ester monomer (A) whose alkyl group has 1 to 12 carbon atoms (meth)acrylic acid alkyl ester monomer (A) whose alkyl group has 8 to 12 carbon atoms; The present invention relates to the pressure-sensitive adhesive composition according to [1] above, wherein the content of a1) is 55% by mass or more.

[3]式1で表される、1Hzで測定した際の25℃の損失弾性率と150℃の損失弾性率の比(P)の値が0.02以上0.3以下である前記[1]または[2]記載の粘着剤組成物に関する。

P=(1Hzで測定した際の150℃の損失弾性率)/(1Hzで測定した際の25℃の損失弾性率) (式1)
[3] The above-mentioned [1] wherein the ratio (P) of the loss modulus at 25 °C and the loss modulus at 150 °C when measured at 1 Hz, expressed by formula 1, is 0.02 or more and 0.3 or less. ] or [2].

P=(loss modulus at 150°C when measured at 1Hz)/(loss modulus at 25°C when measured at 1Hz) (Formula 1)

[4]基材及び、前記[1]~[3]いずれか記載の粘着剤組成物の硬化物からなる粘着剤層を備える粘着シートに関する。 [4] A pressure-sensitive adhesive sheet comprising a base material and a pressure-sensitive adhesive layer made of a cured product of the pressure-sensitive adhesive composition according to any one of [1] to [3] above.

本発明によれば、十分な粘着力、高いタック性を有し、剥離時に粘着剤が残りやすいSUS、鋼板などの高極性被着体であっても良好な再剥離性を示し、かつ貼付した状態で高温または湿熱条件下に長期保管した場合であっても十分な再剥離性を有する粘着剤組成物および粘着シート、また、貼付した状態で高温、高荷重の条件下においてもシートからの粘着剤のはみだしが少なく、高温下でも鋼板などの重量のある被着体同士を重ねて保管することのできる粘着剤組成物および粘着シートを提供することができる。 According to the present invention, the present invention has sufficient adhesive strength and high tackiness, and exhibits good removability even on highly polar adherends such as SUS and steel plates, where adhesive tends to remain when peeled, and can be applied easily. Adhesive compositions and adhesive sheets that have sufficient removability even when stored under high temperature or humid heat conditions for long periods of time, as well as adhesive compositions and adhesive sheets that have sufficient removability even when stored under high temperature or humid heat conditions. It is possible to provide a pressure-sensitive adhesive composition and a pressure-sensitive adhesive sheet that have little oozing out of the adhesive and that allow heavy adherends such as steel plates to be stacked and stored even at high temperatures.

以下、本発明の詳細を説明する。なお、本発明の趣旨に合致する限り、他の実施形態も本発明の範疇に含まれることは言うまでもない。また、本明細書において「~」を用いて特定される数値範囲は、「~」の前後に記載される数値を下限値および上限値の範囲として含むものとする。 The details of the present invention will be explained below. It goes without saying that other embodiments are also included in the scope of the present invention as long as they meet the spirit of the present invention. Furthermore, in this specification, numerical ranges specified using "~" include the numerical values written before and after "~" as the lower limit and upper limit ranges.

本明細書では、「(メタ)アクリル酸」、「(メタ)アクリレート」と表記した場合には、特に説明がない限り、それぞれ、「アクリル酸またはメタクリル酸」、「アクリレートまたはメタクリレート」を表すものとする。また、「(メタ)アクリル酸エステルモノマー」とは、「アクリル酸エステルモノマー」と「メタクリル酸エステルモノマー」の総称を指す。また、アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)を単にモノマー(A)、酸性基を有するモノマー(B)を単にモノマー(B)、水酸基を有するモノマー(C)を単にモノマー(C)と記載する場合がある。 In this specification, "(meth)acrylic acid" and "(meth)acrylate" refer to "acrylic acid or methacrylic acid" and "acrylate or methacrylate," respectively, unless otherwise specified. shall be. Moreover, "(meth)acrylic acid ester monomer" refers to a general term for "acrylic acid ester monomer" and "methacrylic acid ester monomer." In addition, a (meth)acrylic acid alkyl ester monomer (A) in which the alkyl group has 1 to 12 carbon atoms is simply a monomer (A), a monomer having an acidic group (B) is simply a monomer (B), a monomer having a hydroxyl group (C) may be simply referred to as monomer (C).

本明細書において、「Mw」はゲルパーミエーションクロマトグラフィ(GPC)測定によって求めたポリスチレン換算の重量平均分子量である。「Mn」はGPC測定によって求めたポリスチレン換算の数平均分子量である。これらは、[実施例]の項に記載の方法にて測定することができる。 In this specification, "Mw" is the weight average molecular weight in terms of polystyrene determined by gel permeation chromatography (GPC) measurement. "Mn" is the number average molecular weight in terms of polystyrene determined by GPC measurement. These can be measured by the method described in the [Example] section.

本明細書中に出てくる各種成分は特に注釈しない限り、それぞれ独立に1種単独で、あるいは2種以上を混合して用いてもよい。 Unless otherwise noted, the various components appearing in this specification may be used individually or in combination of two or more.

<アクリル酸エステル共重合体>
アクリル酸エステル共重合体とは、(メタ)アクリル酸エステルモノマー等のエチレン性不飽和結合を有するモノマーの重合体を意味する。
本発明のアクリル酸エステル共重合体は、少なくともアルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)、酸性基を有するモノマー(B)、水酸基を有するモノマー(C)からなるモノマー混合物の共重合体であり、酸性基を有するモノマー(B)の含有率は、モノマー混合物100質量%中、0.01質量%以上6質量%以下であり、水酸基を有するモノマー(C)の含有率は、モノマー混合物100質量%中、0.05質量%以上10質量%以下である。
<Acrylic acid ester copolymer>
The acrylic ester copolymer means a polymer of a monomer having an ethylenically unsaturated bond such as a (meth)acrylic ester monomer.
The acrylic ester copolymer of the present invention comprises a (meth)acrylic acid alkyl ester monomer (A) in which the alkyl group has at least 1 to 12 carbon atoms, a monomer (B) having an acidic group, and a monomer (C) having a hydroxyl group. ), the content of the monomer (B) having an acidic group is 0.01% by mass or more and 6% by mass or less based on 100% by mass of the monomer mixture, and the content of the monomer (B) having a hydroxyl group is 0.01% by mass or more and 6% by mass or less. The content of C) is 0.05% by mass or more and 10% by mass or less in 100% by mass of the monomer mixture.

モノマーは、アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)、酸性基を有するモノマー(B)、水酸基を有するモノマー(C)、その他モノマーに分類される。アクリル共重合体を構成するモノマーとしてはモノマー(A)、(B)、(C)を必須成分とし、必要に応じその他モノマーを用いてもよい。 Monomers are classified into (meth)acrylic acid alkyl ester monomers (A) in which the alkyl group has 1 to 12 carbon atoms, monomers having acidic groups (B), monomers having hydroxyl groups (C), and other monomers. The monomers constituting the acrylic copolymer include monomers (A), (B), and (C) as essential components, and other monomers may be used as necessary.

[モノマー(A)]
モノマー(A)は、アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマーである。アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマーとしては、アルキル基の炭素数が8~12の(メタ)アクリル酸アルキルエステルモノマー(a1)とアルキル基の炭素数が1~7の(メタ)アクリル酸アルキルエステルモノマー(a2)に分類される。アルキル基の炭素数が8~12の(メタ)アクリル酸アルキルエステルモノマー(a1)を用いることが好ましく、(a1)と(a2)を併用することがより好ましい。アルキル基の炭素数が8~12の(メタ)アクリル酸アルキルエステルモノマー(a1)を用いることでタックと再剥離性を高いレベルで両立することができる。
[Monomer (A)]
Monomer (A) is a (meth)acrylic acid alkyl ester monomer in which the alkyl group has 1 to 12 carbon atoms. As the (meth)acrylic acid alkyl ester monomer in which the alkyl group has 1 to 12 carbon atoms, the (meth)acrylic acid alkyl ester monomer (a1) in which the alkyl group has 8 to 12 carbon atoms and the (meth)acrylic acid alkyl ester monomer (a1) in which the alkyl group has 8 to 12 carbon atoms are It is classified into 1 to 7 (meth)acrylic acid alkyl ester monomers (a2). It is preferable to use a (meth)acrylic acid alkyl ester monomer (a1) whose alkyl group has 8 to 12 carbon atoms, and it is more preferable to use (a1) and (a2) together. By using the (meth)acrylic acid alkyl ester monomer (a1) whose alkyl group has 8 to 12 carbon atoms, both tack and removability can be achieved at a high level.

モノマー(a1)としては、(メタ)アクリル酸オクチル、(メタ)アクリル酸2-エチルヘキシル、(メタ)アクリル酸ノニル、(メタ)アクリル酸イソノニル、(メタ)アクリル酸デシル、(メタ)アクリル酸イソデシル(メタ)アクリル酸ラウリル等が挙げられる。これらの中でもアクリル酸2-エチルヘキシル、(メタ)アクリル酸ラウリルが再剥離性の点から好ましい。 Monomer (a1) includes octyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, nonyl (meth)acrylate, isononyl (meth)acrylate, decyl (meth)acrylate, and isodecyl (meth)acrylate. Examples include lauryl (meth)acrylate. Among these, 2-ethylhexyl acrylate and lauryl (meth)acrylate are preferred from the viewpoint of removability.

モノマー(a1)の含有率は、特に限定されないが、アクリル酸エステル共重合体を構成するモノマー混合物100質量%中、55質量%以上であることが好ましく、65質量%以上がより好ましい。上限値の制限は特にないが、強いて設定するならば90質量%以下が好ましく、80質量%以下がより好ましい。この範囲にすることで高いタック性と再剥離性を両立することができる。 The content of the monomer (a1) is not particularly limited, but is preferably 55% by mass or more, more preferably 65% by mass or more based on 100% by mass of the monomer mixture constituting the acrylic ester copolymer. There is no particular restriction on the upper limit, but if it is forced, it is preferably 90% by mass or less, more preferably 80% by mass or less. By setting it within this range, both high tackiness and removability can be achieved.

モノマー(a2)としては、(メタ)アクリル酸メチル、(メタ)アクリル酸エチル、(メタ)アクリル酸プロピル、(メタ)アクリル酸ブチル、(メタ)アクリル酸イソブチル、(メタ)アクリル酸ペンチル、(メタ)アクリル酸ヘキシル、(メタ)アクリル酸ヘプチル等が挙げられる。 これらの中でもアクリル酸ブチル、アクリル酸(イソ)ブチルが各種被着体に対しても良好な粘着力を発現する点から好ましい。 Monomers (a2) include methyl (meth)acrylate, ethyl (meth)acrylate, propyl (meth)acrylate, butyl (meth)acrylate, isobutyl (meth)acrylate, pentyl (meth)acrylate, ( Examples include hexyl meth)acrylate and heptyl (meth)acrylate. Among these, butyl acrylate and (iso)butyl acrylate are preferred because they exhibit good adhesion to various adherends.

[モノマー(B)]
モノマー(B)は、酸性基を有するモノマーである。モノマー(B)を用いることで、各種被着体に対して良好な粘着力、凝集力を発現することができる。
[Monomer (B)]
Monomer (B) is a monomer having an acidic group. By using the monomer (B), it is possible to exhibit good adhesive force and cohesive force to various adherends.

モノマー(B)としては、例えば(メタ)アクリル酸、2-カルボキシエチル(メタ)アクリレート、2-(メタ)アクリロイルオキシエチル-コハク酸、2-(メタ)アクリロイロキシエチルヘキサヒドロフタル酸、2-(メタ)アクリロイロキシエチル-フタル酸、クロトン酸、マレイン酸、イタコン酸、フマル酸、シトラコン酸、メサコン酸等の不飽和結合を有するカルボン酸や、2-(メタ)アクリロイルオキシエチルアシッドフォスフェート、等が挙げられ、得られる粘着剤組成物の凝集力、他モノマーとの共重合性の点から、(メタ)アクリル酸、2-カルボキシエチル(メタ)アクリレートが好ましい。 Examples of the monomer (B) include (meth)acrylic acid, 2-carboxyethyl (meth)acrylate, 2-(meth)acryloyloxyethyl-succinic acid, 2-(meth)acryloyloxyethylhexahydrophthalic acid, - Carboxylic acids with unsaturated bonds such as (meth)acryloyloxyethyl-phthalic acid, crotonic acid, maleic acid, itaconic acid, fumaric acid, citraconic acid, mesaconic acid, and 2-(meth)acryloyloxyethyl acid phos (meth)acrylic acid and 2-carboxyethyl (meth)acrylate are preferred from the viewpoint of cohesive strength of the resulting pressure-sensitive adhesive composition and copolymerizability with other monomers.

モノマー(B)の含有率は、アクリル酸エステル共重合体を構成するモノマー混合物100質量%中0.01質量%以上6質量%以下であり、0.1質量%以上4質量%以下であることが好ましく、0.5質量%以上3.5質量%以下がより好ましく、1質量%以上3質量%以下が特に好ましい。モノマー(B)の含有率が、0.05質量%以上であることで、高い粘着力と凝集力を付与することができる。また、モノマー(B)の含有率が6質量%以下であることで、粘着シートを被着体から剥離した後も、被着体への粘着剤組成物の付着を抑制することができる。 The content of monomer (B) shall be 0.01% by mass or more and 6% by mass or less, and 0.1% by mass or more and 4% by mass or less based on 100% by mass of the monomer mixture constituting the acrylic ester copolymer. It is preferably 0.5% by mass or more and 3.5% by mass or less, more preferably 1% by mass or more and 3% by mass or less. When the content of the monomer (B) is 0.05% by mass or more, high adhesive force and cohesive force can be imparted. Moreover, since the content of the monomer (B) is 6% by mass or less, even after the adhesive sheet is peeled from the adherend, adhesion of the adhesive composition to the adherend can be suppressed.

[モノマー(C)]
モノマー(C)は、水酸基を有するモノマーである。モノマー(C)を用いることで、イソシアネート系硬化剤との反応点となり、高温または湿熱条件下においても良好な再剥離性を付与することができる。
[Monomer (C)]
Monomer (C) is a monomer having a hydroxyl group. By using the monomer (C), it becomes a reaction site with the isocyanate curing agent and can provide good removability even under high temperature or moist heat conditions.

水酸基を有するモノマーとしては、例えば、2-ヒドロキシエチル(メタ)アクリレート、2-ヒドロキシプロピル(メタ)アクリレート、3-ヒドロキシプロピル(メタ)アクリレート、2-ヒドロキシブチル(メタ)アクリレート、3-ヒドロキシブチル(メタ)アクリレート、4-ヒドロキシブチル(メタ)アクリレート等のヒドロキシアルキル(メタ)アクリレートやヒドロキシメチルアクリルアミド、ヒドロキシエチルアクリルアミド等のヒドロキシ(メタ)アクリルアミドが挙げられる。イソシアネート系硬化剤との反応性や得られる凝集力の観点から2-ヒドロキシエチル(メタ)アクリレート、4-ヒドロキシブチル(メタ)アクリレートが好ましい。 Examples of monomers having a hydroxyl group include 2-hydroxyethyl (meth)acrylate, 2-hydroxypropyl (meth)acrylate, 3-hydroxypropyl (meth)acrylate, 2-hydroxybutyl (meth)acrylate, and 3-hydroxybutyl (meth)acrylate. Examples include hydroxyalkyl (meth)acrylates such as meth)acrylate and 4-hydroxybutyl(meth)acrylate, and hydroxy(meth)acrylamides such as hydroxymethylacrylamide and hydroxyethylacrylamide. 2-hydroxyethyl (meth)acrylate and 4-hydroxybutyl (meth)acrylate are preferred from the viewpoint of reactivity with the isocyanate curing agent and cohesive force obtained.

モノマー(C)の含有率は、アクリル酸エステル共重合体を構成するモノマー混合物100質量%中0.05質量%以上10質量%以下であり、0.07質量%以上1.8質量%以下であることが好ましく、0.08質量%以上1質量%以下がより好ましい。モノマー(C)の含有率が、0.05質量%以上であることで、硬化剤反応時に高い凝集力を付与することができる。モノマー(B)の含有率が10質量%以下であることで、硬化剤配合後の溶液の著しい粘度上昇を抑制することができるとともに、良好な再剥離性を付与することができる。 The content of the monomer (C) is 0.05% by mass or more and 10% by mass or less, and 0.07% by mass or more and 1.8% by mass or less based on 100% by mass of the monomer mixture constituting the acrylic ester copolymer. It is preferably at least 0.08% by mass and at most 1% by mass. When the content of the monomer (C) is 0.05% by mass or more, high cohesive force can be imparted during the curing agent reaction. When the content of the monomer (B) is 10% by mass or less, it is possible to suppress a significant increase in the viscosity of the solution after mixing the curing agent, and it is possible to impart good removability.

[その他モノマー]
その他モノマーは、モノマー(A)、モノマー(B)、モノマー(C)以外の、モノマーである。その他モノマーとしては、特に限定されず、モノマー(A)、モノマー(B)、モノマー(C)と共重合可能なモノマーを適宜選択することができるが、例えば、酢酸ビニル、プロピオン酸ビニル、酪酸ビニル等のカルボン酸ビニルモノマー、スチレン、アクリロニトリル等のその他のビニルモノマー、イソボニル(メタ)アクリレート、シクロヘキシル(メタ)アクリレートなどの脂環式構造を有するモノマー、フェニル(メタ)アクリレート、フェノキシエチル(メタ)アクリレート、ベンジル(メタ)アクリレート、ビフェニル(メタ)アクリレートなどの芳香環を有するモノマー、2-メトキシエチルアクリレート、2-エトキシエチルアクリレート、メトキシポリエチレングリコール(メタ)アクリレート、メトキシポリプロピレングリコール(メタ)アクリレート、エトキシポリプロピレングリコール(メタ)アクリレートなどのアルコキシ(ポリ)アルキレンオキサイドを有するモノマー、無水マレイン酸やイタコン酸無水物といった分子内に重合性の不飽和結合を有する酸無水物、アミノ基を有するモノマー、その他の窒素原子を有するモノマー、エポキシ基を有するモノマー、イソシアナト基を有するモノマー等が挙げられる。
[Other monomers]
Other monomers are monomers other than monomer (A), monomer (B), and monomer (C). Other monomers are not particularly limited, and monomers copolymerizable with monomer (A), monomer (B), and monomer (C) can be selected as appropriate; examples include vinyl acetate, vinyl propionate, and vinyl butyrate. other vinyl monomers such as styrene, acrylonitrile, monomers with alicyclic structure such as isobornyl (meth)acrylate, cyclohexyl (meth)acrylate, phenyl (meth)acrylate, phenoxyethyl (meth)acrylate , monomers with aromatic rings such as benzyl (meth)acrylate, biphenyl (meth)acrylate, 2-methoxyethyl acrylate, 2-ethoxyethyl acrylate, methoxypolyethylene glycol (meth)acrylate, methoxypolypropylene glycol (meth)acrylate, ethoxypolypropylene Monomers with alkoxy(poly)alkylene oxides such as glycol (meth)acrylate, acid anhydrides with polymerizable unsaturated bonds in the molecule such as maleic anhydride and itaconic anhydride, monomers with amino groups, other nitrogen Examples include monomers having atoms, monomers having epoxy groups, and monomers having isocyanato groups.

アミノ基を有するモノマーとしては、例えば、モノメチルアミノエチル(メタ)アクリレート、モノエチルアミノエチル(メタ)アクリレート、モノメチルアミノプロピル(メタ)アクリレート、モノエチルアミノプロピル(メタ)アクリレート等の、モノアルキルアミノエステル(メタ)アクリレート等が挙げられる。 Examples of monomers having an amino group include monoalkylamino esters such as monomethylaminoethyl (meth)acrylate, monoethylaminoethyl (meth)acrylate, monomethylaminopropyl (meth)acrylate, and monoethylaminopropyl (meth)acrylate. Examples include (meth)acrylate.

その他の窒素原子を有するモノマーとしては(メタ)アクリルアミド、N-ビニルピロリドン、アクリロイルモルフォリン等が挙げられる。 Other nitrogen atom-containing monomers include (meth)acrylamide, N-vinylpyrrolidone, acryloylmorpholine, and the like.

エポキシ基を有するモノマーとしては、例えば、グリシジル(メタ)アクリレート、メチルグリシジル(メタ)アクリレート、3,4-エポキシシクロヘキシルメチル(メタ)アクリレート、6-メチル-3,4-エポキシシクロヘキシルメチル(メタ)アクリレート等が挙げられる。 Examples of monomers having an epoxy group include glycidyl (meth)acrylate, methylglycidyl (meth)acrylate, 3,4-epoxycyclohexylmethyl (meth)acrylate, and 6-methyl-3,4-epoxycyclohexylmethyl (meth)acrylate. etc.

イソシアナト基を有するモノマーとしては、例えば、2-イソシアナトエチル(メタ)アクリレート等が挙げられる。 Examples of the monomer having an isocyanato group include 2-isocyanatoethyl (meth)acrylate.

[アクリル酸エステル共重合体の製造方法]
アクリル酸エステル共重合体の製造方法としては、特に制限はなく、例えば公知のラジカル重合反応で、上記のモノマー混合物を重合させて得ることができる。反応は無溶剤下でも構わないが、合成安定性およびハンドリングの観点から溶剤を使用することが好ましい。また、分子量制御の観点から、ラジカル重合開始剤(以下、「重合開始剤」と略記することがある)を使用することが好ましい。その他、連鎖移動剤等の公知の添加剤を用いてもよい。
溶剤としては、後述する溶剤が使用できる。
[Method for producing acrylic ester copolymer]
There are no particular restrictions on the method for producing the acrylic ester copolymer, and the acrylic ester copolymer can be obtained, for example, by polymerizing the above monomer mixture using a known radical polymerization reaction. Although the reaction may be carried out without a solvent, it is preferable to use a solvent from the viewpoint of synthesis stability and handling. Moreover, from the viewpoint of molecular weight control, it is preferable to use a radical polymerization initiator (hereinafter sometimes abbreviated as "polymerization initiator"). In addition, known additives such as chain transfer agents may also be used.
As the solvent, the solvents described below can be used.

重合開始剤としては、例えば、ベンゾイルパーオキサイド、tert-ブチルパーベンゾエート、クメンヒドロパーオキシドやジイソプロピルパーオキシジカーボネート、ジ-n-プロピルパーオキシジカーボネート、ジ(2-エトキシエチル)パーオキシジカーボネート、tert-ブチルパーオキシ-2-エチルヘキサノエート、tert-ブチルパーオキシネオデカノエート、tert-ブチルパーオキシビバレート、(3,5,5-トリメチルヘキサノイル)パーオキシド、ジプロピオニルパーオキシド、ジアセチルパーオキシド等の有機過酸化物や、2,2’-アゾビスイソブチロニトリル、2,2’-アゾビス(2-メチルブチロニトリル)、1,1’-アゾビス(シクロヘキサン1-カルボニトリル)、2,2’-アゾビス(2,4-ジメチルバレロニトリル)、2,2’-アゾビス(2,4-ジメチル-4-メトキシバレロニトリル)、ジメチル2,2’-アゾビス(2-メチルプロピオネート)、4,4’-アゾビス(4-シアノバレリック酸)、2,2’-アゾビス(2-ヒドロキシメチルプロピオニトリル)、2,2’-アゾビス[2-(2-イミダゾリン-2-イル)プロパン]等のアゾ系化合物が挙げられる。 Examples of the polymerization initiator include benzoyl peroxide, tert-butyl perbenzoate, cumene hydroperoxide, diisopropyl peroxydicarbonate, di-n-propyl peroxydicarbonate, and di(2-ethoxyethyl)peroxydicarbonate. , tert-butyl peroxy-2-ethylhexanoate, tert-butyl peroxy neodecanoate, tert-butyl peroxy bivalate, (3,5,5-trimethylhexanoyl) peroxide, dipropionyl peroxide, Organic peroxides such as diacetyl peroxide, 2,2'-azobisisobutyronitrile, 2,2'-azobis(2-methylbutyronitrile), 1,1'-azobis(cyclohexane 1-carbonitrile) ), 2,2'-azobis(2,4-dimethylvaleronitrile), 2,2'-azobis(2,4-dimethyl-4-methoxyvaleronitrile), dimethyl 2,2'-azobis(2-methylpropylene) pionate), 4,4'-azobis(4-cyanovaleric acid), 2,2'-azobis(2-hydroxymethylpropionitrile), 2,2'-azobis[2-(2-imidazoline-2 -yl)propane] and the like.

連鎖移動剤としては、例えば、オクチルメルカプタン、ノニルメルカプタン、デシルメルカプタン、ドデシルメルカプタン等のアルキルメルカプタン類、チオグリコール酸オクチル、チオグリコール酸ノニル、チオグリコール酸-2-エチルヘキシル等のチオグリコール酸エステル類、2,4-ジフェニル-4-メチル-1-ペンテン、1-メチル-4-イソプロピリデン-1-シクロヘキセン、α-ピネン、β-ピネン等が挙げられる。特に、チオグリコール酸エステル類、2,4-ジフェニル-4-メチル-1-ペンテン、1-メチル-4-イソプロピリデン-1-シクロヘキセン、α-ピネン、β-ピネン等が、得られる重合体が低臭気となる点で好ましい。 Examples of chain transfer agents include alkyl mercaptans such as octyl mercaptan, nonyl mercaptan, decyl mercaptan, and dodecyl mercaptan; thioglycolic acid esters such as octyl thioglycolate, nonyl thioglycolate, and 2-ethylhexyl thioglycolate; Examples include 2,4-diphenyl-4-methyl-1-pentene, 1-methyl-4-isopropylidene-1-cyclohexene, α-pinene, and β-pinene. In particular, thioglycolic acid esters, 2,4-diphenyl-4-methyl-1-pentene, 1-methyl-4-isopropylidene-1-cyclohexene, α-pinene, β-pinene, etc. are It is preferable because it has low odor.

アクリル酸エステル共重合体の重量平均分子量Mwは、ゲル浸透クロマトグラフィー(GPC)による標準ポリスチレン換算値で、20万~200万であることが好ましく、30万~100万であることがより好ましく、40万~90万であることが更に好ましく、50万~80万であることが特に好ましい。重量平均分子量が20万以上であると、十分な凝集力を得ることができる。重量平均分子量が200万以下であると、粘度の増加を抑制でき、良好な塗工適性を得ることができる。 The weight average molecular weight Mw of the acrylic ester copolymer is preferably 200,000 to 2,000,000, more preferably 300,000 to 1,000,000, as calculated by gel permeation chromatography (GPC) in terms of standard polystyrene. It is more preferably 400,000 to 900,000, and particularly preferably 500,000 to 800,000. When the weight average molecular weight is 200,000 or more, sufficient cohesive force can be obtained. When the weight average molecular weight is 2 million or less, increase in viscosity can be suppressed and good coating suitability can be obtained.

アクリル酸エステル共重合体の分子量分散度Mw/Mnは、ゲル浸透クロマトグラフィー(GPC)による標準ポリスチレン換算値で、2.0~12であることが好ましく、4~10であることがより好ましい。分子量分散度が上記範囲であることによって、粘着力と凝集力を両立させることができる。なお、Mnは数平均分子量を意味する。 The molecular weight dispersity Mw/Mn of the acrylic acid ester copolymer is preferably 2.0 to 12, more preferably 4 to 10, as measured by gel permeation chromatography (GPC) in terms of standard polystyrene. When the degree of molecular weight dispersion is within the above range, both adhesive force and cohesive force can be achieved. In addition, Mn means number average molecular weight.

アクリル酸エステル共重合体のガラス転移温度(Tg)は、特には限定されないが、-70~-25℃であることが好ましく、-65~-30℃であることがより好ましい。ガラス転移温度が-70℃以上であると、十分な凝集力が得ることができる。ガラス転移温度が-25℃以下であると良好な粘着力を発現できる。 The glass transition temperature (Tg) of the acrylic ester copolymer is not particularly limited, but is preferably -70 to -25°C, more preferably -65 to -30°C. When the glass transition temperature is −70° C. or higher, sufficient cohesive force can be obtained. When the glass transition temperature is −25° C. or lower, good adhesive strength can be exhibited.

なお、本発明においてアクリル酸エステル共重合体(A)のガラス転移温度(Tg)は、下記式(2)(Fox式)に基づいて計算された値である。
1/Tg=W1/Tg1+W2/Tg2+・・・+Wn/Tgn (式2)
[式(1)中、Tgはアクリル酸エステル共重合体(A)のTg(単位:K)、Tgi(i=1、2、・・・n)はラジカル重合性モノマーiがホモポリマーを形成した際のTg(単位:K)、Wi(i=1、2、・・・n)はラジカル重合性モノマーiの全モノマー成分中の質量分率を表す。なお、ホモポリマーのTgは文献値やカタログ値などの公表値を使用する。]
上記式(2)は、アクリル酸エステル共重合体(A)が、モノマー1、モノマー2、・・・、モノマーnのn種類のモノマー成分から構成される場合の計算式である。
In the present invention, the glass transition temperature (Tg) of the acrylic ester copolymer (A) is a value calculated based on the following formula (2) (Fox formula).
1/Tg=W1/Tg1+W2/Tg2+...+Wn/Tgn (Formula 2)
[In formula (1), Tg is the Tg (unit: K) of the acrylic ester copolymer (A), and Tgi (i = 1, 2, ... n) is the radically polymerizable monomer i forming a homopolymer. Tg (unit: K) and Wi (i=1, 2, . . . n) represent the mass fraction of the radically polymerizable monomer i in all monomer components. Note that for the Tg of the homopolymer, published values such as literature values and catalog values are used. ]
The above formula (2) is a calculation formula when the acrylic ester copolymer (A) is composed of n types of monomer components: monomer 1, monomer 2, . . . , monomer n.

<イソシアネート系硬化剤)>
本発明の粘着剤組成物は、硬化剤として、イソシアネート系硬化剤を含む。イソシアネート系硬化剤は、アクリル酸エステル共重合体に含まれる水酸基を有するモノマー(C)と架橋点を形成することで、高い粘着力と、凝集力を発現することができる。
<Isocyanate curing agent)>
The adhesive composition of the present invention contains an isocyanate curing agent as a curing agent. The isocyanate curing agent can exhibit high adhesive strength and cohesive strength by forming a crosslinking point with the hydroxyl group-containing monomer (C) contained in the acrylic ester copolymer.

イソシアネート系硬化剤は、例えば、トリレンジイソシアネート、ヘキサメチレンジイソシアネート、イソホロンジイソシアネート、キシリレンジイソシアネート、水添キシ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、水添ジフェニルメタンジイソシアネート、テトラメチルキシリレンジイソシアネート、ナフタレンジイソシアネート、トリフェニルメタントリイソシアネート、およびポリメチレンポリフェニルイソシアネート等のジイソシアネートと、トリメチロールプロパン等のポリオール化合物とのアダクト体、ならびにそのビュレット体、ならびにそのイソシアヌレート体、ならびに上記ジイソシアネートと、ポリエーテルポリオール、ポリエステルポリオール、アクリルポリオール、ポリブタジエンポリオール、およびポリイソプレンポリオール等の内のいずれかのポリオールとのアダクト体などの分子内に3個以上のイソシアネート基を有する化合物;またはこれらのアロファネート体等の分子内に2個のイソシアネート基を有する化合物等が挙げられる。これらの中でも、トリレンジイソシアネートのトリメチロールプロパンアダクト体、キシリレンジイソシアネートのトリメチロールプロパンアダクト体、ヘキサメチレンジイソシアネートのトリメチロールプロパンアダクト体が粘着物性を容易に調整できるため好ましく、トリレンジイソシアネートのトリメチロールプロパンアダクト体が特に好ましい。なお、イソシアネート基の個数は平均個数である。 Examples of the isocyanate curing agent include tolylene diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate, xylylene diisocyanate, hydrogenated xylylene diisocyanate, diphenylmethane diisocyanate, hydrogenated diphenylmethane diisocyanate, tetramethylxylylene diisocyanate, naphthalene diisocyanate, and triphenylmethane diisocyanate. Isocyanates, adducts of diisocyanates such as polymethylene polyphenylisocyanate, and polyol compounds such as trimethylolpropane, burettes thereof, isocyanurates thereof, and the above diisocyanates, polyether polyols, polyester polyols, acrylic polyols Compounds having three or more isocyanate groups in the molecule, such as adducts with any one of polyols such as , polybutadiene polyol, and polyisoprene polyol; or compounds having two or more isocyanate groups in the molecule, such as allophanate bodies Examples include compounds having the following. Among these, trimethylolpropane adducts of tolylene diisocyanate, trimethylolpropane adducts of xylylene diisocyanate, and trimethylolpropane adducts of hexamethylene diisocyanate are preferred because the adhesive properties can be easily adjusted. Particularly preferred are propane adducts. Note that the number of isocyanate groups is the average number.

イソシアネート系硬化剤の含有量は、特に限定されないが、アクリル酸エステル共重合体100質量部に対して、0.1~10質量部であることが好ましく、1~9部がより好ましく、1.5~7部が特に好ましい。イソシアネート系硬化剤の含有量が、0.1質量部以上であると、十分な凝集力が得られ、10質量部以下であると剥離時のジッピングを抑制することができる。 The content of the isocyanate curing agent is not particularly limited, but it is preferably 0.1 to 10 parts by mass, more preferably 1 to 9 parts, 1. Particularly preferred is 5 to 7 parts. When the content of the isocyanate curing agent is 0.1 parts by mass or more, sufficient cohesive force can be obtained, and when the content is 10 parts by mass or less, zipping during peeling can be suppressed.

本発明の粘着剤組成物は、さらに、イソシアネート系硬化剤以外の、他の硬化剤を併用できる。他の硬化剤は、例えば金属キレート系硬化剤、エポキシ系硬化剤またはアジリジン系硬化剤等が挙げられる。これらの硬化剤を含むことで、粘着剤組成物の凝集力がさらに高まり耐熱性が向上する。 The pressure-sensitive adhesive composition of the present invention may further contain other curing agents other than isocyanate-based curing agents. Examples of other curing agents include metal chelate curing agents, epoxy curing agents, and aziridine curing agents. By including these curing agents, the cohesive force of the adhesive composition is further increased and the heat resistance is improved.

金属キレート系硬化剤としては公知のものを使用でき、例えば、アルミニウム、鉄、銅、亜鉛、スズ、チタン、ニッケル、アンチモン、マグネシウム、バナジウム、クロム、ジルコニウム等の多価金属と、アセチルアセトン、アセト酢酸エチル等の配位子との配位化合物等が挙げられる。長期間での貯蔵安定性の観点から、多価金属は、アルミニウムであることが好ましく、配位子は、アセチルアセトンおよびアセト酢酸エステルの少なくともいずれかであることが好ましい。 Known metal chelate curing agents can be used, such as polyvalent metals such as aluminum, iron, copper, zinc, tin, titanium, nickel, antimony, magnesium, vanadium, chromium, and zirconium, acetylacetone, acetoacetic acid, etc. Examples include coordination compounds with a ligand such as ethyl. From the viewpoint of long-term storage stability, the polyvalent metal is preferably aluminum, and the ligand is preferably at least one of acetylacetone and acetoacetate.

金属キレート系硬化剤は、例えば、アルミニウムイソプロピレート、モノsec-ブトキシアルミニウムジイソプロピレート、アルミニウムsec-ブチレート、アルミニウムエチレート等のアルミニウムアルコキシド、
エチルアセトアセテートアルミニウムジイソプロピレート、アルミニウムトリス(エチルアセトアセテート)、アルキルアセトアセテートアルミニウムジイソプロピレート、アルミニウムモノアセチルアセテートビス(エチルアセトアセテート)、アルミニウムトリス(アセチルアセトネート)等のアルミニウムキレート、
チタンテトライソプロポキシド、チタンテトラノルマルブトキシド、チタンブトキシダイマー、チタンテトラ-2-エチルヘキソキシド等のチタンアルコキシド、
チタンイソプロポキシビス(アセチルアセトネート)、チタンテトラアセチルアセトネート、チタンジイソプロポキシビス(エチルアセトアセテート)、リン酸エステルチタン錯体、チタンオクチレングリコレート等のチタンキレート、
ジルコニウムテトラノルマルプロポキシド、ジルコニウムテトラノルマルブトキシド等のジルコニウムアルコキシド、
ジルコニウムテトラアセチルアセトネート、ジルコニウムトリブトキシモノアセチルアセトネート、ジルコニウムテトラアセチルアセトネート、ジルコニウムジブトキシビス(エチルアセトアセテート)等のジルコニウムキレート、
ステアリン酸ジルコニウム等のジルコニウムアシレートが挙げられる。
Examples of metal chelate curing agents include aluminum alkoxides such as aluminum isopropylate, monosec-butoxyaluminum diisopropylate, aluminum sec-butyrate, and aluminum ethylate;
Aluminum chelates such as ethyl acetoacetate aluminum diisopropylate, aluminum tris (ethylacetoacetate), alkyl acetoacetate aluminum diisopropylate, aluminum monoacetylacetate bis (ethylacetoacetate), aluminum tris (acetylacetonate),
Titanium alkoxides such as titanium tetraisopropoxide, titanium tetra-normal butoxide, titanium butoxy dimer, titanium tetra-2-ethylhexoxide,
Titanium chelates such as titanium isopropoxy bis (acetylacetonate), titanium tetraacetylacetonate, titanium diisopropoxy bis (ethylacetoacetate), phosphate ester titanium complex, titanium octylene glycolate,
Zirconium alkoxides such as zirconium tetranormal propoxide, zirconium tetranormal butoxide,
Zirconium chelates such as zirconium tetraacetylacetonate, zirconium tributoxy monoacetylacetonate, zirconium tetraacetylacetonate, zirconium dibutoxybis(ethylacetoacetate),
Examples include zirconium acylates such as zirconium stearate.

これらの中でも、架橋性、粘着力、透明性、貯蔵安定性の点から、アルキルアセトアセテートアルミニウムジイソプロピレート、アルミニウムモノアセチルアセテートビス(エチルアセトアセテート)、アルミニウムトリス(アセチルアセトネート)が好ましい。 Among these, preferred are alkyl acetoacetate aluminum diisopropylate, aluminum monoacetylacetate bis(ethylacetoacetate), and aluminum tris(acetylacetonate) from the viewpoint of crosslinkability, adhesive strength, transparency, and storage stability.

エポキシ硬化剤は、例えば、ビスフェノールA-エピクロロヒドリン型のエポキシ系樹脂、エチレングリコールジグリシジルエーテル、ポリエチレングリコールジグリシジルエーテル、グリセリンジグリシジルエーテル、グリセリントリグリシジルエーテル、1,6-ヘキサンジオールジグリシジルエーテル、トリメチロールプロパントリグリシジルエーテル、ジグリシジルアニリン、N,N,N',N'-テトラグリシジル-m-キシリレンジアミン、1、3-ビス(N、N’-ジグリシジルアミノメチル)シクロヘキサン、およびN,N,N',N'-テトラグリシジルアミノフェニルメタン等が挙げられる。 Examples of the epoxy curing agent include bisphenol A-epichlorohydrin type epoxy resin, ethylene glycol diglycidyl ether, polyethylene glycol diglycidyl ether, glycerin diglycidyl ether, glycerin triglycidyl ether, 1,6-hexanediol diglycidyl Ether, trimethylolpropane triglycidyl ether, diglycidylaniline, N,N,N',N'-tetraglycidyl-m-xylylenediamine, 1,3-bis(N,N'-diglycidylaminomethyl)cyclohexane, and N,N,N',N'-tetraglycidylaminophenylmethane.

アジリジン硬化剤は、例えばN,N’-ジフェニルメタン-4,4'-ビス(1-アジリジンカルボキサイト)、N,N’-トルエン-2,4-ビス(1-アジリジンカルボキサイト)、ビスイソフタロイル-1-(2-メチルアジリジン)、トリ-1-アジリジニルホスフィンオキサイド、N,N’-ヘキサメチレン-1,6-ビス(1-アジリジンカルボキサイト)、2,2’-ビスヒドロキシメチルブタノール-トリス[3-(1-アジリジニル)プロピオネート]、トリメチロールプロパントリ-β-アジリジニルプロピオネート、テトラメチロールメタントリ-β-アジリジニルプロピオネート、およびトリス-2,4,6-(1-アジリジニル)-1、3、5-トリアジン等が挙げられる。 Examples of aziridine curing agents include N,N'-diphenylmethane-4,4'-bis(1-aziridinecarboxite), N,N'-toluene-2,4-bis(1-aziridinecarboxite), and bisisophthalocarbonate. yl-1-(2-methylaziridine), tri-1-aziridinylphosphine oxide, N,N'-hexamethylene-1,6-bis(1-aziridinecarboxite), 2,2'-bishydroxymethyl Butanol-tris[3-(1-aziridinyl)propionate], trimethylolpropane tri-β-aziridinylpropionate, tetramethylolmethanetri-β-aziridinylpropionate, and tris-2,4,6 -(1-aziridinyl)-1,3,5-triazine and the like.

他の硬化剤の含有量は、特に限定されないが、アクリル酸エステル共重合体100質量部に対して、10質量部以下であることが好ましく、5質量部以下であることが更に好ましい。 The content of the other curing agent is not particularly limited, but is preferably 10 parts by mass or less, more preferably 5 parts by mass or less, based on 100 parts by mass of the acrylic ester copolymer.

本発明の粘着剤組成物は、粘着剤のポットライフを向上させる目的で、公知の触媒作用抑制剤を添加することができる。
触媒作用抑制剤として具体的には、ケト-エノール互変異性体形成化合物等が挙げられる。ケト-エノール互変異性体形成化合物はケト-エノール互変異性体を形成できる化合物であり、アセチルアセトン、アセト酢酸エステル、マロン酸エステル等が好ましい。
A known catalytic action inhibitor may be added to the adhesive composition of the present invention for the purpose of improving the pot life of the adhesive.
Specific examples of the catalytic action inhibitor include compounds that form keto-enol tautomers. The keto-enol tautomer-forming compound is a compound capable of forming a keto-enol tautomer, and acetylacetone, acetoacetate, malonic acid ester, etc. are preferable.

アセト酢酸エステルは、例えばアセト酢酸メチル、アセト酢酸エチル、アセト酢酸イソプロピル。アセト酢酸ブチル、アセト酢酸イソブチル、アセト酢酸tert-ブチル等が挙げられる。 Examples of acetoacetate include methyl acetoacetate, ethyl acetoacetate, and isopropyl acetoacetate. Examples include butyl acetoacetate, isobutyl acetoacetate, tert-butyl acetoacetate, and the like.

マロン酸エステルは、例えばマロン酸ジメチル、マロン酸ジエチル、マロン酸ジブチル等が挙げられる。
これらの中でもケト-エノール互変異性体形成化合物は、乾燥時の揮発し易さからアセチルアセトンが好ましい。
Examples of malonic acid esters include dimethyl malonate, diethyl malonate, and dibutyl malonate.
Among these, acetylacetone is preferred as the keto-enol tautomer-forming compound because of its ease of volatilization during drying.

触媒作用抑制剤の含有量は、アクリル酸エステル共重合体100質量部に対して、0.05~10.0質量部であることが好ましく、0.1~5.0質量部であることがより好ましく、0.5~3.0質量部であることが更に好ましい。触媒作用抑制剤の配合量が0.05質量部以上であるとポットライフが良好であり、10.0質量部以下であると良好な初期硬化性が得られる。 The content of the catalytic action inhibitor is preferably 0.05 to 10.0 parts by mass, and preferably 0.1 to 5.0 parts by mass, based on 100 parts by mass of the acrylic ester copolymer. The amount is more preferably 0.5 to 3.0 parts by mass. When the amount of the catalytic action inhibitor is 0.05 parts by mass or more, the pot life is good, and when it is 10.0 parts by mass or less, good initial curability is obtained.

<溶剤>
本発明の粘着剤組成物は、溶剤を含んでもよい。
溶剤を配合するタイミングは特に問わず、アクリル酸エステル共重合体の製造時に使用してもよく、粘着剤組成物の製造時に粘度を調整する希釈溶剤として使用してもよい。溶剤は、塗工の際のレベリング性、および乾燥性、ならびに環境、および人体への影響などの観点で選択できる。溶剤は、脂肪族炭化水素、脂環族炭化水素、芳香族炭化水素、エステル、ケトン、アルコール等が好ましい。
<Solvent>
The adhesive composition of the present invention may contain a solvent.
The timing of blending the solvent is not particularly limited, and it may be used during the production of the acrylic ester copolymer, or may be used as a diluting solvent to adjust the viscosity during the production of the adhesive composition. The solvent can be selected from the viewpoints of leveling properties and drying properties during coating, as well as effects on the environment and the human body. Preferred solvents include aliphatic hydrocarbons, alicyclic hydrocarbons, aromatic hydrocarbons, esters, ketones, and alcohols.

溶剤としては、例えば、酢酸メチル、酢酸エチル、酢酸プロピル、酢酸ブチル等のエステル系溶剤、アセトン、メチルエチルケトン、メチルブチルケトン、シクロヘキサノン等のケトン系溶剤、トルエン、キシレン、アニソール等の炭化水素系溶剤、メタノール、エタノール、ノルマルプロパノール、イソプロパノール等のアルコール溶剤が挙げられるが、粘着剤組成物のポットライフの観点から、エステル系溶剤および/またはアルコール溶剤を含むことが好ましい。 Examples of the solvent include ester solvents such as methyl acetate, ethyl acetate, propyl acetate, and butyl acetate; ketone solvents such as acetone, methyl ethyl ketone, methyl butyl ketone, and cyclohexanone; hydrocarbon solvents such as toluene, xylene, and anisole; Examples include alcohol solvents such as methanol, ethanol, normal propanol, and isopropanol, but from the viewpoint of the pot life of the adhesive composition, it is preferable to include an ester solvent and/or an alcohol solvent.

溶剤の使用量としては、アクリル酸エステル共重合体100重量部に対して、10重量質量部以上含むことが好ましく、30重量質量部以上含むことがより好ましい。上限値としては特に制限はされないが、塗工性の観点から2000質量部以下であることが好ましい。 The amount of the solvent to be used is preferably 10 parts by weight or more, more preferably 30 parts by weight or more, based on 100 parts by weight of the acrylic ester copolymer. The upper limit is not particularly limited, but from the viewpoint of coatability, it is preferably 2000 parts by mass or less.

<粘着付与樹脂>
本発明の粘着剤組成物は、さらに粘着付与樹脂を含むことができる。粘着付与樹脂は、溶液重合の際に使用する方法、アクリル酸エステル共重合体に配合する方法等任意の方法で使用できる。粘着付与樹脂は、溶液重合の際に使用すると連鎖移動剤として作用しアクリル酸エステル共重合体の分子量調整が容易になる。また、アクリル酸エステル共重合体に配合すると粘着力をより向上できる。
<Tackifying resin>
The adhesive composition of the present invention can further contain a tackifying resin. The tackifying resin can be used by any method such as a method used during solution polymerization or a method of blending it into an acrylic ester copolymer. When the tackifier resin is used during solution polymerization, it acts as a chain transfer agent, making it easier to adjust the molecular weight of the acrylic ester copolymer. Moreover, when it is blended with an acrylic acid ester copolymer, the adhesive strength can be further improved.

粘着付与樹脂の軟化点は、70℃~170℃が好ましく、75℃~160℃がより好ましく、100℃~150℃が更に好ましい。
粘着付与樹脂の軟化点が上記範囲であることで粘着力と凝集力を高いレベルで両立し易くなる。なお、軟化点は、JIS SK5902に規定されている乾球法に従って測定した軟化温度である。
The softening point of the tackifying resin is preferably 70°C to 170°C, more preferably 75°C to 160°C, and even more preferably 100°C to 150°C.
When the softening point of the tackifying resin is within the above range, it becomes easy to achieve both high levels of adhesive force and cohesive force. Note that the softening point is a softening temperature measured according to the dry bulb method specified in JIS SK5902.

粘着付与樹脂としては、以下の例には限定されないが、ロジン系樹脂、重合ロジン系樹脂、ロジンエステル系樹脂、重合ロジンエステル系樹脂、テルペン系樹脂、テルペンフェノール系樹脂、クマロン系樹脂、クマロンインデン系樹脂、スチレン系樹脂、キシレン系樹脂、フェノール系樹脂、石油系樹脂等が挙げられる。これらの中でもアクリル酸エステル共重合体(A)との相溶性が良く粘着性能がより向上できる点から、ロジン系樹脂、重合ロジン系樹脂、ロジンエステル系樹脂および重合ロジンエステル系樹脂、石油樹脂、スチレン系樹脂が好ましい 粘着付与樹脂は、1種を単独で用いてもよいし、2種以上を組み合わせて用いてもよい。 Examples of tackifying resins include, but are not limited to, rosin resins, polymerized rosin resins, rosin ester resins, polymerized rosin ester resins, terpene resins, terpene phenol resins, coumaron resins, and coumarons. Examples include indene resins, styrene resins, xylene resins, phenol resins, petroleum resins, and the like. Among these, rosin resin, polymerized rosin resin, rosin ester resin, polymerized rosin ester resin, petroleum resin, Styrenic resins are preferred. The tackifying resins may be used alone or in combination of two or more.

粘着付与樹脂の含有量としては、アクリル酸エステル共重合体100質量部に対して、1~60質量部が好ましく、1.5~20質量部がより好ましく、2~10質量部がさらに好ましい。粘着付与樹脂を1質量部以上添加することで粘着力を底上げすることが可能であり、60質量部以下にすることで再剥離性を維持することができる。 The content of the tackifying resin is preferably 1 to 60 parts by weight, more preferably 1.5 to 20 parts by weight, and even more preferably 2 to 10 parts by weight, based on 100 parts by weight of the acrylic ester copolymer. By adding 1 part by mass or more of the tackifying resin, it is possible to increase the adhesive strength, and by adding the tackifying resin to 60 parts by mass or less, removability can be maintained.

<可塑剤>
剥離時のジッピングを抑制する目的で、本発明の粘着剤組成物はさらに必要に応じて、可塑剤を含むことができる。可塑剤としては特に制限されないが、アクリル酸エステル共重合体との相溶性等の観点から、有機酸エステルが好ましい。
<Plasticizer>
For the purpose of suppressing zipping during peeling, the adhesive composition of the present invention may further contain a plasticizer, if necessary. The plasticizer is not particularly limited, but organic acid esters are preferred from the viewpoint of compatibility with the acrylic ester copolymer.

一塩基酸または多塩基酸とアルコールとのエステルとしては、例えば、ラウリン酸イソステアリル、ミリスチン酸イソプロピル、ミリスチン酸イソセチル、ミリスチン酸オクチルドデシル、パルミチン酸イソステアリル、ステアリン酸イソセチル、オレイン酸オクチルドデシル、フタル酸ジブチル、フタル酸ジオクチル、フタル酸ジヘプチル、フタル酸ジベンジル、フタル酸ブチルベンジル、アジピン酸ジイソデシル、アジピン酸ジイソステアリル、セバシン酸ジブチル、セバシン酸ジイソセチル、アセチルクエン酸トリブチル、トリメリット酸トリブチル、トリメリット酸トリオクチル、トリメリット酸トリヘキシル、トリメリット酸トリオレイル、およびトリメリット酸トリイソセチル等が挙げられる。 Examples of esters of monobasic acids or polybasic acids and alcohols include isostearyl laurate, isopropyl myristate, isocetyl myristate, octyldodecyl myristate, isostearyl palmitate, isocetyl stearate, octyldodecyl oleate, and phthalate. dibutyl acid, dioctyl phthalate, diheptyl phthalate, dibenzyl phthalate, butylbenzyl phthalate, diisodecyl adipate, diisostearyl adipate, dibutyl sebacate, diisocetyl sebacate, tributyl acetyl citrate, tributyl trimellitate, trimellit Examples include trioctyl acid, trihexyl trimellitate, trioleyl trimellitate, and triisocetyl trimellitate.

その他の酸とアルコールとのエステルとしては、例えば、ミリストレイン酸、オレイン酸、リノール酸、リノレン酸、イソパルミチン酸、およびイソステアリン酸等の不飽和脂肪酸または分岐酸と、エチレングリコール、プロピレングリコール、グリセリン、トリメチロールプロパン、ペンタエリスリトール、およびソルビタン等のアルコールとのエステルが挙げられる。 Examples of esters of other acids and alcohols include unsaturated fatty acids or branched acids such as myristoleic acid, oleic acid, linoleic acid, linolenic acid, isopalmitic acid, and isostearic acid, and ethylene glycol, propylene glycol, and glycerin. , trimethylolpropane, pentaerythritol, and esters with alcohols such as sorbitan.

一塩基酸または多塩基酸とポリアルキレングリコールとのエステルとしては、例えば、ジヘキシル酸ポリエチレングリコール、ジ-2-エチルヘキシル酸ポリエチレングリコール、ジラウリル酸ポリエチレングリコール、ジオレイン酸ポリエチレングリコール、およびアジピン酸ジポリエチレングリコールメチルエーテル等が挙げられる。 Examples of esters of monobasic acids or polybasic acids and polyalkylene glycols include polyethylene glycol dihexylate, polyethylene glycol di-2-ethylhexylate, polyethylene glycol dilaurate, polyethylene glycol dioleate, and dipolyethylene glycol methyl adipate. Examples include ether.

リン酸エステル系可塑剤としては、例えば、トリクレジルホスフェート(TCP)、トリフェニルホスフェート(TPP)、トリ-2-エチルヘキシルホスフェート(TOP)、トリキシレニルホスフェート(TXP)、トリエチルホスフェート(TEP)等が挙げられる。 Examples of phosphate ester plasticizers include tricresyl phosphate (TCP), triphenyl phosphate (TPP), tri-2-ethylhexyl phosphate (TOP), tricylenyl phosphate (TXP), and triethyl phosphate (TEP). can be mentioned.

エポキシ系可塑剤としては、エポキシ化大豆油、エポキシ化アマニ油、エポキシ化ステアリン酸オクチル、エポキシ化脂肪酸ブチル及びエポキシ化アマニ油脂肪酸ブチル等が挙げられる。 Examples of the epoxy plasticizer include epoxidized soybean oil, epoxidized linseed oil, epoxidized octyl stearate, epoxidized butyl fatty acid, and epoxidized butyl fatty acid in linseed oil.

可塑剤の分子量(式量またはMn)は、好ましくは250~1000、より好ましくは400~900、特に好ましくは500~850である。分子量が250以上であれば粘着層の耐熱性が良好となり、分子量が1000以下であれば十分なジッピング抑制効果が得られる。 The molecular weight (formula weight or Mn) of the plasticizer is preferably 250 to 1000, more preferably 400 to 900, particularly preferably 500 to 850. If the molecular weight is 250 or more, the heat resistance of the adhesive layer will be good, and if the molecular weight is 1000 or less, a sufficient zipping suppressing effect will be obtained.

可塑剤の含有量としては、特には制限されないが、アクリル酸エステル共重合体100質量部に対して、0.01~30質量部が好ましく、4~20質量部以下がより好ましい。可塑剤の含有量が0.01質量部以上であれば十分な剥離時のジッピング抑制効果が得られ、30質量部以下であれば、粘着力の低下を抑制できる。 The content of the plasticizer is not particularly limited, but is preferably from 0.01 to 30 parts by weight, more preferably from 4 to 20 parts by weight, based on 100 parts by weight of the acrylic ester copolymer. If the content of the plasticizer is 0.01 parts by mass or more, a sufficient effect of suppressing zipping during peeling can be obtained, and if the content is 30 parts by mass or less, a decrease in adhesive strength can be suppressed.

<酸化防止剤>
本発明の粘着剤組成物はさらに必要に応じて、酸化防止剤を含むことができる。
酸化防止剤としては、ラジカル捕捉剤および過酸化物分解剤等が挙げられる。ラジカル捕捉剤としては、フェノール系化合物およびアミン系化合物等が挙げられる。過酸化物分解剤としては、硫黄系化合物およびリン系化合物等が挙げられる。
<Antioxidant>
The adhesive composition of the present invention may further contain an antioxidant, if necessary.
Examples of antioxidants include radical scavengers and peroxide decomposers. Examples of the radical scavenger include phenolic compounds and amine compounds. Examples of peroxide decomposers include sulfur-based compounds and phosphorus-based compounds.

フェノール系化合物としては、例えば、2,6-ジ-t-ブチル-p-クレゾール、ブチル化ヒドロキシアニソール、2,6-ジ-t-ブチル-4-エチルフェノール、ステアリン-β-(3,5-ジ-t-ブチル-4-ヒドロキシフェニル)プロピオネート、2,2’-メチレンビス(4-メチル-6-t-ブチルフェノール)、2,2’-メチレンビス(4-エチル-6-t-ブチルフェノール)、4,4’-チオビス(3-メチル-6-t-ブチルフェノール)、4,4’-ブチリデンビス(3-メチル-6-t-ブチルフェノール)、3,9-ビス[1,1-ジメチル-2-[β-(3-t-ブチル-4-ヒドロキシ-5-メチルフェニル)プロピオニルオキシ]エチル]2,4,8,10-テトラオキサスピロ[5,5]ウンデカン、ベンゼンプロパン酸,3,5-ビス(1,1-ジメチルエチル)-4-ヒドロキシ-,C7-C9側鎖アルキルエステル、1,1,3-トリス(2-メチル-4-ヒドロキシ-5-t-ブチルフェニル)ブタン、1,3,5-トリメチル-2,4,6-トリス(3,5-ジ-t-ブチル-4-ヒドロキシベンジル)ベンゼン、テトラキス-[メチレン-3-(3’,5’-ジ-t-ブチル-4’-ヒドロキシフェニル)プロピオネート]メタン、ビス[3,3’-ビス-(4’-ヒドロキシ-3’-t-ブチルフェニル)ブチリックアシッド]グリコールエステル、1,3,5-トリス(3’,5’-ジ-t-ブチル-4’-ヒドロキシベンジル)-S-トリアジン-2,4,6-(1H,3H,5H)トリオン、およびトコフェロール等が挙げられる。 Examples of phenolic compounds include 2,6-di-t-butyl-p-cresol, butylated hydroxyanisole, 2,6-di-t-butyl-4-ethylphenol, stearin-β-(3,5 -di-t-butyl-4-hydroxyphenyl) propionate, 2,2'-methylenebis(4-methyl-6-t-butylphenol), 2,2'-methylenebis(4-ethyl-6-t-butylphenol), 4,4'-thiobis(3-methyl-6-t-butylphenol), 4,4'-butylidenebis(3-methyl-6-t-butylphenol), 3,9-bis[1,1-dimethyl-2- [β-(3-t-butyl-4-hydroxy-5-methylphenyl)propionyloxy]ethyl]2,4,8,10-tetraoxaspiro[5,5]undecane, benzenepropanoic acid, 3,5- Bis(1,1-dimethylethyl)-4-hydroxy-, C7-C9 side chain alkyl ester, 1,1,3-tris(2-methyl-4-hydroxy-5-t-butylphenyl)butane, 1, 3,5-trimethyl-2,4,6-tris(3,5-di-t-butyl-4-hydroxybenzyl)benzene, tetrakis-[methylene-3-(3',5'-di-t-butyl) -4'-hydroxyphenyl)propionate] methane, bis[3,3'-bis-(4'-hydroxy-3'-t-butylphenyl)butyric acid] glycol ester, 1,3,5-tris(3 ',5'-di-t-butyl-4'-hydroxybenzyl)-S-triazine-2,4,6-(1H,3H,5H)trione, tocopherol, and the like.

硫黄系酸化防止剤としては、ジラウリル3,3’-チオジプロピオネート、ジミリスチル3,3’-チオジプロピオネート、およびジステアリル3,3’-チオジプロピオネート等が挙げられる。 Examples of the sulfur-based antioxidant include dilauryl 3,3'-thiodipropionate, dimyristyl 3,3'-thiodipropionate, and distearyl 3,3'-thiodipropionate.

リン系化合物としては、例えば、トリフェニルホスファイト、ジフェニルイソデシルホスファイト、4,4’-ブチリデン-ビス(3-メチル-6-tert-ブチルフェニルジトリデシル)ホスファイト、サイクリックネオペンタンテトライルビス(オクタデシルホスファイト)、トリス(ノニルフェニル)ホスファイト、トリス(モノノニルフェニル)ホスファイト、トリス(ジノニルフェニル)ホスファイト、ジイソデシルペンタエリスリトールジフォスファイト、9,10-ジヒドロ-9-オキサ-10-ホスファフェナントレン-10-オキサイド、10-(3,5-ジ-tert-ブチル-4-ヒドロキシベンジル)-9,10-ジヒドロ-9-オキサ-10-ホスファフェナントレン-10-オキサイド、10-デシロキシ-9,10-ジヒドロ-9-オキサ-10-ホスファフェナントレン、トリス(2,4-ジ-tert-ブチルフェニル)ホスファイト、サイクリックネオペンタンテトライルビス(2,4-ジ-tert-ブチルフェニル)ホスファイト、サイクリックネオペンタンテトライルビス(2,6-ジ-tert-ブチル-4-メチルフェニル)ホスファイト、および2,2-メチレンビス(4,6-ジ-tert-ブチルフェニル)オクチルホスファイト等が挙げられる。 Examples of phosphorus compounds include triphenyl phosphite, diphenylisodecyl phosphite, 4,4'-butylidene-bis(3-methyl-6-tert-butylphenylditridecyl) phosphite, and cyclic neopentanetetrayl. Bis(octadecyl phosphite), tris(nonylphenyl) phosphite, tris(monononylphenyl) phosphite, tris(dinonylphenyl) phosphite, diisodecylpentaerythritol diphosphite, 9,10-dihydro-9-oxa- 10-phosphaphenanthrene-10-oxide, 10-(3,5-di-tert-butyl-4-hydroxybenzyl)-9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide, 10 -Desyloxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene, tris(2,4-di-tert-butylphenyl)phosphite, cyclic neopentanetetrayl bis(2,4-di-tert -butylphenyl) phosphite, cyclic neopentanetetrayl bis(2,6-di-tert-butyl-4-methylphenyl) phosphite, and 2,2-methylenebis(4,6-di-tert-butylphenyl) ) Octyl phosphite and the like.

酸化防止剤を用いることで、アクリル酸エステル共重合体の熱劣化を防ぐことができ耐熱性を向上できる。
酸化防止剤の添加量は特に制限されず、アクリル酸エステル共重合体100質量部に対して、0.01~5質量部が好ましく、0.1~3質量部がより好ましく、0.2~2質量部が更に好ましい。
By using an antioxidant, thermal deterioration of the acrylic ester copolymer can be prevented and heat resistance can be improved.
The amount of the antioxidant added is not particularly limited, and is preferably 0.01 to 5 parts by weight, more preferably 0.1 to 3 parts by weight, and 0.2 to 3 parts by weight, based on 100 parts by weight of the acrylic ester copolymer. 2 parts by mass is more preferred.

酸化防止剤としては、透明性と重合禁止効果の点から、ラジカル捕捉剤であるフェノール系化合物が好ましい。フェノール系化合物は、アクリル酸エステル共重合体(A)の合成時残留モノマー成分が継時で低分子量成分を生成し耐熱性を低下させるのを効果的に抑制することができる。 As the antioxidant, a phenolic compound, which is a radical scavenger, is preferable from the viewpoint of transparency and polymerization inhibiting effect. The phenolic compound can effectively suppress the monomer components remaining during the synthesis of the acrylic acid ester copolymer (A) from producing low molecular weight components over time and reducing heat resistance.

本発明の粘着剤組成物は、さらに、触媒、帯電防止剤(AS剤)、紫外線吸収剤、光安定剤、潤滑剤、腐食防止剤、耐熱安定剤、耐候安定剤、加水分解防止剤、防黴剤、増粘剤、充填剤(タルク、炭酸カルシウム、および酸化チタン等)、シランカップリング剤、重合禁止剤、消泡剤、スリップ剤、アンチブロッキング剤、防曇剤、滑剤、染料、ワックス、乳剤、磁性体、誘電特性調整剤等の公知の添加剤を必要に応じて配合することができる。 The adhesive composition of the present invention further includes a catalyst, an antistatic agent (AS agent), an ultraviolet absorber, a light stabilizer, a lubricant, a corrosion inhibitor, a heat stabilizer, a weather stabilizer, a hydrolysis inhibitor, and a Mildew agents, thickeners, fillers (talc, calcium carbonate, titanium oxide, etc.), silane coupling agents, polymerization inhibitors, antifoaming agents, slip agents, antiblocking agents, antifogging agents, lubricants, dyes, waxes , emulsions, magnetic materials, dielectric property modifiers, and other known additives may be blended as necessary.

≪粘着剤組成物≫
本発明における粘着剤組成物は、アルキル基の炭素数が1~12である(メタ)アルキルアクリル酸エステルモノマー(A)、酸性基を有するモノマー(B)、水酸基を有するモノマー(C)からなるモノマー混合物の共重合体であるアクリル酸エステル共重合体と、イソシアネート系硬化剤とを含む。また、酸性基を有するモノマー(B)の含有率は、モノマー混合物100質量%中、0.01質量%以上6質量%以下であり、水酸基を有するモノマー(C)の含有率は、モノマー混合物100質量%中、0.05質量%以上10質量%以下であり、ゲル分率が55%以上である。
≪Adhesive composition≫
The adhesive composition of the present invention consists of a (meth)alkyl acrylate monomer (A) in which the alkyl group has 1 to 12 carbon atoms, a monomer (B) having an acidic group, and a monomer (C) having a hydroxyl group. It contains an acrylic ester copolymer, which is a copolymer of a monomer mixture, and an isocyanate curing agent. Further, the content of the monomer (B) having an acidic group is 0.01% by mass or more and 6% by mass or less in 100% by mass of the monomer mixture, and the content of the monomer (C) having a hydroxyl group is 0.01% by mass or more and 6% by mass or less in 100% by mass of the monomer mixture. In mass%, it is 0.05% by mass or more and 10% by mass or less, and the gel fraction is 55% or more.

<ゲル分率>
ゲル分率は下記式(3)により算出される値である。
(ゲル分率)={(W2-W0-W3)/(W1-W0-W3)}×100 (式3)
W0:金網の重量
W1:金網+試験片の重量
W2:金網+試験片の乾燥後の重量
W3:試験片の基材の重量
ゲル分率の測定方法は、実施例の欄に詳細を記載する。
<Gel fraction>
The gel fraction is a value calculated by the following formula (3).
(Gel fraction) = {(W2-W0-W3)/(W1-W0-W3)}×100 (Formula 3)
W0: Weight of wire mesh W1: Weight of wire mesh + test piece W2: Weight of wire mesh + test piece after drying W3: Weight of base material of test piece Details of the method for measuring the gel fraction are described in the Examples column. .

本発明の粘着剤組成物のゲル分率は55%以上100%以下であり、70%以上98%以下が好ましく、80%以上95%以下がより好ましい。ゲル分率が55%以上であることで高温下での保管後でも良好な再剥離性を発現することができる。 The gel fraction of the adhesive composition of the present invention is 55% or more and 100% or less, preferably 70% or more and 98% or less, and more preferably 80% or more and 95% or less. When the gel fraction is 55% or more, good removability can be exhibited even after storage at high temperatures.

<粘弾性>
本発明の粘着剤組成物から形成される粘着剤層の貯蔵弾性率(G’)、損失弾性率(G’’)、損失正接(tanδ)は、TA Instruments(株)社製粘弾性測定装置「Ares-G2」を用い、周波数:1Hz、ひずみ0.1%、温度:-50℃~200℃(昇温速度10℃/分)の条件で温度依存性測定を実施し、25℃、150℃での値を用いた。
<Viscoelasticity>
The storage modulus (G'), loss modulus (G''), and loss tangent (tan δ) of the adhesive layer formed from the adhesive composition of the present invention were measured using a viscoelasticity measuring device manufactured by TA Instruments Co., Ltd. Temperature dependence measurements were carried out using "Ares-G2" under the conditions of frequency: 1 Hz, strain 0.1%, temperature: -50°C to 200°C (heating rate 10°C/min), 25°C, 150°C. The value in °C was used.

本発明の粘着剤組成物は式1で表される、1Hzで測定した際の25℃の損失弾性率と150℃の損失弾性率の比(P)の値が0.02以上0.3以下であり、0.03以上0.15以下が好ましく、0.04以上0,07以下がより好ましく、0.05以上0.06以下が特に好ましい。(P)の値がこの範囲にあることで貼り付け時に良好な粘着力、タックを発現できるとともに、高温下の条件で長期間貼付した状態でも良好な再剥離性を示し、かつ高温下で荷重がかかった場合でも粘着剤の染み出しを抑えることができる。

(P)=(1Hzで測定した際の150℃の損失弾性率)/(1Hzで測定した際の25℃の損失弾性率) (式1)
The adhesive composition of the present invention has a ratio (P) of the loss modulus at 25°C and the loss modulus at 150°C when measured at 1 Hz, which is expressed by Formula 1, and has a value of 0.02 or more and 0.3 or less. and is preferably 0.03 or more and 0.15 or less, more preferably 0.04 or more and 0.07 or less, particularly preferably 0.05 or more and 0.06 or less. By having a value of (P) within this range, it is possible to develop good adhesive strength and tack when pasting, and also to exhibit good removability even after being pasted for a long time under high temperature conditions, and to be able to exhibit good removability even under high temperature conditions under load. Even if it gets wet, it can prevent the adhesive from seeping out.

(P) = (loss modulus at 150°C when measured at 1Hz)/(loss modulus at 25°C when measured at 1Hz) (Formula 1)

本発明の粘着剤組成物から形成される粘着剤層の25℃の貯蔵弾性率(G’)は特に限定されないが15,000Pa以上90,000Pa以下が好ましく、30,000Pa以上65,000Pa以下がより好ましい。15,000Pa以上であることで十分な凝集力を得られ、90,000Pa以下であることで使用時に良好な粘着力を得ることができる。 The storage modulus (G') at 25°C of the adhesive layer formed from the adhesive composition of the present invention is not particularly limited, but is preferably 15,000 Pa or more and 90,000 Pa or less, and 30,000 Pa or more and 65,000 Pa or less. More preferred. If it is 15,000 Pa or more, sufficient cohesive force can be obtained, and if it is 90,000 Pa or less, good adhesive force can be obtained during use.

本発明の粘着剤組成物から形成される粘着剤層の150℃の貯蔵弾性率(G’)は特に限定されないが10,000Pa以上50,000Pa以下が好ましい。15,000Pa以上であることで高温下においてもはみだしの少ない粘着剤が得られ、50,000Pa以下であることで高温下においても良好な粘着力を得ることができる。 The storage modulus (G') at 150°C of the adhesive layer formed from the adhesive composition of the present invention is not particularly limited, but is preferably 10,000 Pa or more and 50,000 Pa or less. When the pressure is 15,000 Pa or more, an adhesive with little oozing out can be obtained even under high temperatures, and when the pressure is 50,000 Pa or less, good adhesive strength can be obtained even under high temperatures.

本発明の粘着剤組成物から形成される粘着剤層の25℃の損失弾性率(G’’)は特に限定されないが10,000Pa以上40,000Pa以下が好ましく、15,000Pa以上30,000Pa以下がより好ましい。10,000Pa以上であることで十分な粘着力、タックを得られ、40,000Pa以下であることで使用時に良好な再剥離性を得ることができる。 The loss modulus (G'') at 25°C of the adhesive layer formed from the adhesive composition of the present invention is not particularly limited, but is preferably 10,000 Pa or more and 40,000 Pa or less, and 15,000 Pa or more and 30,000 Pa or less. is more preferable. When the pressure is 10,000 Pa or more, sufficient adhesive force and tack can be obtained, and when the pressure is 40,000 Pa or less, good removability during use can be obtained.

本発明の粘着剤組成物から形成される粘着剤層の150℃の損失弾性率(G’’)は特に限定されないが800Pa以上8,000Pa以下が好ましく、900Pa以上2,500Pa以下がより好ましい。800Pa以上であることで高温下でも十分な粘着力、タックを得られ、8,000Pa以下であることで高温下でも良好な再剥離性を得ることができる。 The loss modulus (G'') at 150°C of the adhesive layer formed from the adhesive composition of the present invention is not particularly limited, but is preferably 800 Pa or more and 8,000 Pa or less, more preferably 900 Pa or more and 2,500 Pa or less. When the pressure is 800 Pa or more, sufficient adhesive strength and tack can be obtained even at high temperatures, and when the pressure is 8,000 Pa or less, good removability can be obtained even at high temperatures.

<粘着剤組成物の製造方法>
本発明の粘着剤組成物の製造方法は、特に制限されない。
アクリル酸エステル共重合体に対して、イソシアネート系硬化剤、および溶剤、および必要に応じて任意成分を添加混合することで、本発明の粘着剤組成物を製造することができる。
<Method for manufacturing adhesive composition>
The method for producing the adhesive composition of the present invention is not particularly limited.
The pressure-sensitive adhesive composition of the present invention can be produced by adding and mixing an isocyanate curing agent, a solvent, and optional components as necessary to the acrylic ester copolymer.

本発明の粘着剤組成物は、不揮発分濃度が30~75質量%が好ましく、38~65質量%がより好ましく、40~60質量%が更に好ましい。粘着剤組成物の不揮発分濃度を高く設定することで、相対的に溶剤の含有量を抑制できるため、塗工時の乾燥コスト抑制、ならびに環境および人体への負荷を抑制できる。 The adhesive composition of the present invention preferably has a nonvolatile content concentration of 30 to 75% by mass, more preferably 38 to 65% by mass, and even more preferably 40 to 60% by mass. By setting the nonvolatile content concentration of the adhesive composition to be high, the content of the solvent can be relatively suppressed, so that drying costs during coating can be suppressed, and the burden on the environment and the human body can be suppressed.

粘着剤組成物の粘度は、25℃における粘度が1,000~20,000mPa・sであることが好ましく、1,500~10,000mPa・sがより好ましく、2,500~7,000mPa・sが更に好ましい。粘着剤組成物の粘度が上記範囲にあることによって塗工性が向上し、表面が平滑な粘着剤層が得やすくなる。なお、粘度は、25℃雰囲気下、B L型粘度計を使用して、#3ローター、回転数12rpmで回転開始1分後に測定した粘度である。 The viscosity of the adhesive composition at 25° C. is preferably 1,000 to 20,000 mPa·s, more preferably 1,500 to 10,000 mPa·s, and 2,500 to 7,000 mPa·s. is even more preferable. When the viscosity of the pressure-sensitive adhesive composition is within the above range, coating properties are improved and a pressure-sensitive adhesive layer with a smooth surface can be easily obtained. Note that the viscosity is the viscosity measured 1 minute after the start of rotation using a BL type viscometer in an atmosphere of 25° C. with a #3 rotor and a rotation speed of 12 rpm.

≪粘着シート≫
粘着シートは、基材と、本発明の粘着剤組成物の硬化物からなる粘着剤層とを備える。粘着剤層は、基材の片面または両面に形成することができる。必要に応じて、粘着剤層の露出面は、剥離シートで被覆することができる。なお、剥離シートは、粘着シートを被着体に貼着する際に剥離される。
≪Adhesive sheet≫
The pressure-sensitive adhesive sheet includes a base material and a pressure-sensitive adhesive layer made of a cured product of the pressure-sensitive adhesive composition of the present invention. The adhesive layer can be formed on one or both sides of the base material. If necessary, the exposed surface of the adhesive layer can be covered with a release sheet. Note that the release sheet is peeled off when the adhesive sheet is attached to the adherend.

粘着剤組成物を塗工するに際し、前述した溶剤を用いて粘度を調整することもできるし、粘着剤組成物を加熱して粘度を低下させることもできる。 When applying the adhesive composition, the viscosity can be adjusted using the above-mentioned solvent, or the viscosity can be lowered by heating the adhesive composition.

基材としては特に制限されず、樹脂シート、紙、および金属箔等が挙げられる。基材は、これら基材の少なくとも一方の面に任意の1つ以上の層が積層された積層シートであってもよい。基材の粘着層を形成する側の面には、必要に応じて、コロナ放電処理およびアンカーコート剤塗布等の易接着処理が施されていてもよい。 The base material is not particularly limited, and examples include resin sheets, paper, and metal foils. The base material may be a laminated sheet in which one or more arbitrary layers are laminated on at least one surface of the base material. The surface of the base material on which the adhesive layer is to be formed may be subjected to adhesion-facilitating treatment such as corona discharge treatment and application of an anchor coating agent, if necessary.

樹脂シートの構成樹脂としては特に制限されず、ポリエチレンテレフタレート(PET)等エステル系樹脂;ポリエチレン(PE)およびポリプロピレン(PP)等のオレフィン系樹脂;ポリ塩化ビニル等のビニル系樹脂;ナイロン66等のアミド系樹脂;ウレタン系樹脂(発泡体を含む);これらの組合せ等が挙げられる。
ポリウレタンシートを除く樹脂シートの厚みは特に制限されず、好ましくは15~300μmである。ポリウレタンシート(発泡体を含む)の厚みは特に制限されず、好ましくは20~50000μmである。
The constituent resin of the resin sheet is not particularly limited, and may include ester resins such as polyethylene terephthalate (PET); olefin resins such as polyethylene (PE) and polypropylene (PP); vinyl resins such as polyvinyl chloride; Examples include amide resin; urethane resin (including foam); combinations thereof, and the like.
The thickness of the resin sheet excluding the polyurethane sheet is not particularly limited, and is preferably 15 to 300 μm. The thickness of the polyurethane sheet (including foam) is not particularly limited, and is preferably 20 to 50,000 μm.

紙としては特に制限されず、普通紙、コート紙、およびアート紙等が挙げられる。
金属箔の構成金属としては特に制限されず、アルミニウム、銅、およびこれらの組合せ等が挙げられる。
The paper is not particularly limited, and examples include plain paper, coated paper, and art paper.
The constituent metal of the metal foil is not particularly limited, and examples thereof include aluminum, copper, and combinations thereof.

剥離シートとしては特に制限されず、樹脂シートまたは紙等の基材シートの表面に剥離剤塗布等の公知の剥離処理が施された公知の剥離シートを用いることができる。 The release sheet is not particularly limited, and any known release sheet that has been subjected to a known release treatment such as coating a release agent on the surface of a base sheet such as a resin sheet or paper can be used.

粘着シートは、公知方法にて製造することができる。
はじめに、基材の表面に本発明の粘着剤組成物を塗工して、本発明の粘着組成物剤からなる塗工層を形成する。塗布方法は公知方法を適用でき、ロールコーター法、コンマコーター法、ダイコーター法、リバースコーター法、シルクスクリーン法、およびグラビアコーター法等が挙げられる。
次に、塗工層を乾燥および硬化して、本発明の粘着剤組成物の硬化物からなる粘着剤層を形成する。加熱乾燥温度は特に制限されず、60~150℃程度が好ましい。粘着剤層の厚み(乾燥後の厚み)は用途によって異なるが、好ましくは0.1~200μmである。
次に必要に応じて、公知方法により粘着剤層の露出面に剥離シートを貼着する。
以上のようにして、片面粘着シートを製造することができる。
上記操作を両面に行うことで、両面粘着シートを製造することができる。
The adhesive sheet can be manufactured by a known method.
First, the pressure-sensitive adhesive composition of the present invention is applied to the surface of a substrate to form a coating layer made of the pressure-sensitive adhesive composition of the present invention. As the coating method, known methods can be applied, such as a roll coater method, a comma coater method, a die coater method, a reverse coater method, a silk screen method, and a gravure coater method.
Next, the coating layer is dried and cured to form a pressure-sensitive adhesive layer made of a cured product of the pressure-sensitive adhesive composition of the present invention. The heat drying temperature is not particularly limited, and is preferably about 60 to 150°C. The thickness of the adhesive layer (thickness after drying) varies depending on the application, but is preferably 0.1 to 200 μm.
Next, if necessary, a release sheet is attached to the exposed surface of the adhesive layer by a known method.
A single-sided adhesive sheet can be manufactured in the manner described above.
By performing the above operation on both sides, a double-sided pressure-sensitive adhesive sheet can be manufactured.

上記方法とは逆に、剥離シートの表面に本発明の粘着剤組成物を塗工して、本発明の粘着剤組成物からなる塗工層を形成し、次いで塗工層を乾燥および硬化して、本発明の粘着剤組成物の硬化物からなる粘着剤層を形成し、粘着層の露出面に基材シートを積層してもよい。 Contrary to the above method, the pressure-sensitive adhesive composition of the present invention is applied to the surface of a release sheet to form a coating layer made of the pressure-sensitive adhesive composition of the present invention, and then the coating layer is dried and cured. Then, a pressure-sensitive adhesive layer made of a cured product of the pressure-sensitive adhesive composition of the present invention may be formed, and a base sheet may be laminated on the exposed surface of the pressure-sensitive adhesive layer.

粘着シートの製造方法は好ましくは、基材上に粘着剤を塗工する塗工工程と、形成された塗工層を加熱乾燥処理して粘着剤組成物の硬化物を含む粘着層を形成する加熱工程と、得られた粘着シートを巻芯に巻取って粘着シートロールの形態とする巻取工程と、粘着シートロールを養生する養生工程とを含む。 The method for producing a pressure-sensitive adhesive sheet preferably includes a coating step of coating a pressure-sensitive adhesive onto a base material, and heating and drying the formed coating layer to form a pressure-sensitive adhesive layer containing a cured product of the pressure-sensitive adhesive composition. The method includes a heating step, a winding step of winding the obtained adhesive sheet around a core to form an adhesive sheet roll, and a curing step of curing the adhesive sheet roll.

以下、合成例、本発明に係る実施例、および比較例について説明する。なお、以下の記載において、特に明記しない限り、「部」は質量部を意味し、「%」は質量%を意味し、「RH」は相対湿度を意味するものとする。 Synthesis examples, examples according to the present invention, and comparative examples will be described below. In the following description, unless otherwise specified, "parts" means parts by mass, "%" means % by mass, and "RH" means relative humidity.

[重量平均分子量(Mw)の測定]
重量平均分子量(Mw)は、ゲルパーミエーションクロマトグラフィ(GPC)法により測定した。測定条件は以下の通りとした。なお、Mwはポリスチレン換算値である。
<測定条件>
装置:島津製作所社製、LC-GPCシステム「Prominence」、
カラム:東ソー社製GMHXL 4本、東ソー社製HXL-H 1本を直列に連結、
検出器:示差屈折率検出器(RID-10A)、
溶媒:テトラヒドロフラン(THF)、
流速:1mL/分、
溶媒温度:40℃、
試料濃度:0.2%、
試料注入量:100μL
[Measurement of weight average molecular weight (Mw)]
The weight average molecular weight (Mw) was measured by gel permeation chromatography (GPC). The measurement conditions were as follows. Note that Mw is a polystyrene equivalent value.
<Measurement conditions>
Equipment: Shimadzu Corporation, LC-GPC system “Prominence”,
Column: 4 Tosoh GMHXL, 1 Tosoh HXL-H connected in series,
Detector: differential refractive index detector (RID-10A),
Solvent: tetrahydrofuran (THF),
Flow rate: 1 mL/min,
Solvent temperature: 40°C,
Sample concentration: 0.2%,
Sample injection volume: 100μL

<アクリル酸エステル共重合体の製造>
(合成例1)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル17.2部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は79万であった。
<Production of acrylic ester copolymer>
(Synthesis example 1)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 17.2 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 790,000.

(合成例2)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、アクリル酸4-ヒドロキシブチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、アクリル酸4-ヒドロキシブチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル17.2部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は77万であった。
(Synthesis example 2)
In a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"), 30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and acrylic acid were added. After charging 0.4 parts of 4-hydroxybutyl acid, 35 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 4-hydroxybutyl acrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 17.2 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 770,000.

(合成例3)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸2-カルボキシエチル0.84部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル16.4部、アクリル酸2-カルボキシエチル1.96部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始した後、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は82万であった。
(Synthesis example 3)
30 parts of 2-ethylhexyl acrylate and 0.0 parts of 2-carboxyethyl acrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 84 parts of 2-hydroxyethyl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 35 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Replaced with. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 16.4 parts of butyl acrylate, 1.96 parts of 2-carboxyethyl acrylate, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and then the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 820,000.

(合成例4)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル7.2部、アクリル酸エチル10部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始した後、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は88万であった。
(Synthesis example 4)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 parts of lonitrile (AIBN) was charged, and 7.2 parts of butyl acrylate, 10 parts of ethyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and then the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 880,000.

(合成例5)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル12部、アクリル酸イソノニル7.5部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル28部、アクリル酸イソノニル17.5部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル17.2部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始した後、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は81万であった。
(Synthesis example 5)
In a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"), 12 parts of 2-ethylhexyl acrylate, 7.5 parts of isononyl acrylate, After charging 0.6 parts of acrylic acid, 0.4 parts of 2-hydroxyethyl methacrylate, 35 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), The air was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 28 parts of 2-ethylhexyl acrylate, 17.5 parts of isononyl acrylate, 15 parts of lauryl methacrylate, 0.4 part of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, 2 , 0.02 parts of 2'-azobisisobutyronitrile (AIBN), and 17.2 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and then the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Further, the weight average molecular weight (Mw) of the acrylic ester copolymer was 810,000.

(合成例6)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル19.15部、アクリル酸0.05部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は80万であった。
(Synthesis example 6)
30 parts of 2-ethylhexyl acrylate and 0.0 parts of 2-hydroxyethyl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 4 parts of ethyl acetate, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 19.15 parts of butyl acrylate, 0.05 part of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 800,000.

(合成例7)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル18.4部、アクリル酸0.8部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は80万であった。
(Synthesis example 7)
30 parts of 2-ethylhexyl acrylate and 0.0 parts of 2-hydroxyethyl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 4 parts of ethyl acetate, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 18.4 parts of butyl acrylate, 0.8 part of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 800,000.

(合成例8)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル18.2部、アクリル酸1部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は80万であった。
(Synthesis example 8)
30 parts of 2-ethylhexyl acrylate and 0.0 parts of 2-hydroxyethyl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 4 parts of ethyl acetate, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 18.2 parts of butyl acrylate, 1 part of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 800,000.

(合成例9)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.84部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル16.4部、アクリル酸1.96部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は81万であった。
(Synthesis example 9)
30 parts of 2-ethylhexyl acrylate, 0.84 part of acrylic acid, and methacrylic acid were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 16.4 parts of butyl acrylate, 1.96 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Further, the weight average molecular weight (Mw) of the acrylic ester copolymer was 810,000.

(合成例10)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸1.05部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル15.7部、アクリル酸2.45部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は82万であった。
(Synthesis example 10)
30 parts of 2-ethylhexyl acrylate, 1.05 parts of acrylic acid, and methacrylic acid were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 15.7 parts of butyl acrylate, 2.45 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 820,000.

(合成例11)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸1.65部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル13部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル15.7部、アクリル酸3.85部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は85万であった。
(Synthesis example 11)
30 parts of 2-ethylhexyl acrylate, 1.65 parts of acrylic acid, and methacrylic acid were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 13 parts of lauryl methacrylate, 0.4 part of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 15.7 parts of butyl acrylate, 3.85 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 850,000.

(合成例12)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.02部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.03部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル17.95部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は79万であった。
(Synthesis example 12)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.02 part of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.03 part of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 17.95 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 790,000.

(合成例13)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.04部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.03部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル17.93部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は79万であった。
(Synthesis example 13)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.04 part of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.03 part of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 17.93 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 790,000.

(合成例14)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.08部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.07部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル17.85部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は78万であった。
(Synthesis example 14)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.08 parts of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.07 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 17.85 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 780,000.

(合成例15)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.5部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル17.1部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は79万であった。
(Synthesis example 15)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.5 part of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 17.1 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 790,000.

(合成例16)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.8部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル15部、メタクリル酸2-ヒドロキシエチル0.7部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル16.5部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は79万であった。
(Synthesis example 16)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.8 parts of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 0.7 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 16.5 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 790,000.

(合成例17)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル35部、メタクリル酸ラウリル11部、メタクリル酸2-ヒドロキシエチル2部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル16部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は81万であった。
(Synthesis example 17)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 4 parts of 2-hydroxyethyl acid, 35 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 35 parts of 2-ethylhexyl acrylate, 11 parts of lauryl methacrylate, 2 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutyronitrile were added. (AIBN), and 16 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Further, the weight average molecular weight (Mw) of the acrylic ester copolymer was 810,000.

(合成例18)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル65部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル15部、メタクリル酸ラウリル5部、アクリル酸ブチル32.2部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル15部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は83万であった。
(Synthesis example 18)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 65 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 15 parts of 2-ethylhexyl acrylate, 5 parts of lauryl methacrylate, 32.2 parts of butyl acrylate, 0.4 part of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, 2 , 0.02 parts of 2'-azobisisobutyronitrile (AIBN), and 15 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Further, the weight average molecular weight (Mw) of the acrylic ester copolymer was 830,000.

(合成例19)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル65部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル15部、メタクリル酸ラウリル15部、アクリル酸ブチル22.2部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル10部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル15部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は80万であった。
(Synthesis example 19)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 65 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 15 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 22.2 parts of butyl acrylate, 0.4 part of 2-hydroxyethyl methacrylate, 10 parts of ethyl acetate, 2 , 0.02 parts of 2'-azobisisobutyronitrile (AIBN), and 15 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 800,000.

(合成例20)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル65部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル22.2部、メタクリル酸ラウリル15部、アクリル酸ブチル15部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル10部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル15部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は77万であった。
(Synthesis example 20)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 65 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 22.2 parts of 2-ethylhexyl acrylate, 15 parts of lauryl methacrylate, 15 parts of butyl acrylate, 0.4 part of 2-hydroxyethyl methacrylate, 10 parts of ethyl acetate, 2 , 0.02 parts of 2'-azobisisobutyronitrile (AIBN), and 15 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 770,000.

(合成例21)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル40部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル34部、メタクリル酸ラウリル5部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル35部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル28.2部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は70万であった。
(Synthesis example 21)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 parts of 2-hydroxyethyl acid, 40 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 34 parts of 2-ethylhexyl acrylate, 5 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 35 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 28.2 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 700,000.

(合成例22)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル45部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル15部、メタクリル酸ラウリル42部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル20部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにアクリル酸ブチル10.2部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は72万であった。
(Synthesis example 22)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 part of 2-hydroxyethyl acid, 45 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 15 parts of 2-ethylhexyl acrylate, 42 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 20 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 part of lonitrile (AIBN) was charged, and 10.2 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic acid ester copolymer was 720,000.

(合成例23)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル30部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル40部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル16部、メタクリル酸ラウリル36部、メタクリル酸2-ヒドロキシエチル0.4部、酢酸エチル5部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込み、容器Bにメタクリル酸ラウリル10部、アクリル酸ブチル5.2部、アクリル酸1.4部、酢酸エチル5部仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。その際、同時に容器Bの内容物を容器Aへ2.0時間かけて撹拌しながら供給した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は80万であった。
(Synthesis example 23)
30 parts of 2-ethylhexyl acrylate, 0.6 part of acrylic acid, and methacrylic acid were added to a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser tube, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 0.4 parts of 2-hydroxyethyl acid, 40 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 16 parts of 2-ethylhexyl acrylate, 36 parts of lauryl methacrylate, 0.4 parts of 2-hydroxyethyl methacrylate, 5 parts of ethyl acetate, and 2,2'-azobisisobutylene were added. 0.02 parts of lonitrile (AIBN) was charged, and 10 parts of lauryl methacrylate, 5.2 parts of butyl acrylate, 1.4 parts of acrylic acid, and 5 parts of ethyl acetate were charged into container B. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. At the same time, the contents of container B were supplied to container A while stirring for 2.0 hours. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 800,000.

(合成例24)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル13.5部、メタクリル酸ラウリル1.5部、アクリル酸ブチル14.2部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.24部、酢酸エチル50部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル31.5部、メタクリル酸ラウリル3.5部、アクリル酸ブチル33部、アクリル酸1.4部、メタクリル酸2-ヒドロキシエチル0.56部、酢酸エチル30部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は83万であった。
(Synthesis example 24)
13.5 parts of 2-ethylhexyl acrylate and 1.5 parts of lauryl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). 14.2 parts of butyl acrylate, 0.6 parts of acrylic acid, 0.24 parts of 2-hydroxyethyl methacrylate, 50 parts of ethyl acetate, 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN) After charging the reactor, the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 31.5 parts of 2-ethylhexyl acrylate, 3.5 parts of lauryl methacrylate, 33 parts of butyl acrylate, 1.4 parts of acrylic acid, and 0.2 parts of 2-hydroxyethyl methacrylate were added. 56 parts of ethyl acetate, 30 parts of ethyl acetate, and 0.02 part of 2,2'-azobisisobutyronitrile (AIBN) were charged. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Further, the weight average molecular weight (Mw) of the acrylic ester copolymer was 830,000.

(合成例25)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル8.4部、メタクリル酸ラウリル0.9部、アクリル酸ブチル14部、アクリル酸エチル6部、アクリル酸0.6部、メタクリル酸2-ヒドロキシエチル0.3部、酢酸エチル50部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル19.6部、アクリル酸ブチル32.9部、メタクリル酸ラウリル2.1部、アクリル酸エチル14部、アクリル酸1.4部、メタクリル酸2-ヒドロキシエチル0.7部、酢酸エチル30部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は70万であった。
(Synthesis example 25)
8.4 parts of 2-ethylhexyl acrylate and 0.9 parts of lauryl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). 14 parts of butyl acrylate, 6 parts of ethyl acrylate, 0.6 parts of acrylic acid, 0.3 parts of 2-hydroxyethyl methacrylate, 50 parts of ethyl acetate, 2,2'-azobisisobutyronitrile (AIBN) ) After charging 0.02 parts, the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 19.6 parts of 2-ethylhexyl acrylate, 32.9 parts of butyl acrylate, 2.1 parts of lauryl methacrylate, 14 parts of ethyl acrylate, 1.4 parts of acrylic acid, 0.7 parts of 2-hydroxyethyl methacrylate, 30 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN) were charged. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 700,000.

(比較合成例1)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル13.5部、メタクリル酸ラウリル1.5部、アクリル酸ブチル14部、アクリル酸0.8部、酢酸エチル60部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル31.5部、アクリル酸ブチル33.2部、メタクリル酸ラウリル3.5部、アクリル酸2.0部、酢酸エチル30部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は81万であった。
(Comparative synthesis example 1)
13.5 parts of 2-ethylhexyl acrylate and 1.5 parts of lauryl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 14 parts of butyl acrylate, 0.8 parts of acrylic acid, 60 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), the air in the reaction vessel was replaced with nitrogen. Replaced with gas. Furthermore, in a container A equipped with a stirrer, 31.5 parts of 2-ethylhexyl acrylate, 33.2 parts of butyl acrylate, 3.5 parts of lauryl methacrylate, 2.0 parts of acrylic acid, 30 parts of ethyl acetate, 2 , 0.02 part of 2'-azobisisobutyronitrile (AIBN) was charged. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Further, the weight average molecular weight (Mw) of the acrylic ester copolymer was 810,000.

(比較合成例2)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル13.5部、メタクリル酸ラウリル1.5部、アクリル酸ブチル14部、メタクリル酸2-ヒドロキシエチル0.6部、酢酸エチル60部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル31.5部、アクリル酸ブチル34部、メタクリル酸ラウリル3.5部、メタクリル酸2-ヒドロキシエチル1.4部、酢酸エチル30部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は81万であった。
(Comparative synthesis example 2)
13.5 parts of 2-ethylhexyl acrylate and 1.5 parts of lauryl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). After charging 14 parts of butyl acrylate, 0.6 parts of 2-hydroxyethyl methacrylate, 60 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN), The air was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 31.5 parts of 2-ethylhexyl acrylate, 34 parts of butyl acrylate, 3.5 parts of lauryl methacrylate, 1.4 parts of 2-hydroxyethyl methacrylate, and 30 parts of ethyl acetate. , 0.02 part of 2,2'-azobisisobutyronitrile (AIBN) were charged. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Further, the weight average molecular weight (Mw) of the acrylic ester copolymer was 810,000.

(比較合成例3)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル13.5部、メタクリル酸ラウリル1.5部、アクリル酸ブチル10.5部、アクリル酸2.7部、メタクリル酸2-ヒドロキシエチル1.8部、酢酸エチル55部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル31.5部、アクリル酸ブチル24.5部、メタクリル酸ラウリル3.5部、アクリル酸6.3部、メタクリル酸2-ヒドロキシエチル4.2部、酢酸エチル15部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は88万であった。
(Comparative synthesis example 3)
13.5 parts of 2-ethylhexyl acrylate and 1.5 parts of lauryl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). 10.5 parts of butyl acrylate, 2.7 parts of acrylic acid, 1.8 parts of 2-hydroxyethyl methacrylate, 55 parts of ethyl acetate, 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN) After charging the reactor, the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 31.5 parts of 2-ethylhexyl acrylate, 24.5 parts of butyl acrylate, 3.5 parts of lauryl methacrylate, 6.3 parts of acrylic acid, and 2-hydroxyethyl methacrylate. 4.2 parts of ethyl acetate, 15 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN) were charged. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 880,000.

(比較合成例4)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル13.5部、メタクリル酸ラウリル1.5部、アクリル酸ブチル9.3部、アクリル酸1.2部、メタクリル酸2-ヒドロキシエチル4.5部、酢酸エチル55部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル31.5部、アクリル酸ブチル21.7部、メタクリル酸ラウリル3.5部、アクリル酸2.8部、メタクリル酸2-ヒドロキシエチル10.5部、酢酸エチル10部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は85万であった。
(Comparative synthesis example 4)
13.5 parts of 2-ethylhexyl acrylate and 1.5 parts of lauryl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). 9.3 parts of butyl acrylate, 1.2 parts of acrylic acid, 4.5 parts of 2-hydroxyethyl methacrylate, 55 parts of ethyl acetate, 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN) After charging the reactor, the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 31.5 parts of 2-ethylhexyl acrylate, 21.7 parts of butyl acrylate, 3.5 parts of lauryl methacrylate, 2.8 parts of acrylic acid, and 2-hydroxyethyl methacrylate. 10.5 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN) were charged. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic ester copolymer was 850,000.

(比較合成例5)
撹拌機、温度計、還流冷却管、窒素導入管を備えた反応容器(以下、単に「反応容器」と称することがある)に、アクリル酸2-エチルヘキシル13.5部、メタクリル酸ラウリル1.5部、アクリル酸ブチル7.8部、アクリル酸2.7部、メタクリル酸2-ヒドロキシエチル4.5部、酢酸エチル55部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ後、反応容器内の空気を窒素ガスで置換した。更に、撹拌機を備えた容器Aに、アクリル酸2-エチルヘキシル31.5部、アクリル酸ブチル18.2部、メタクリル酸ラウリル3.5部、アクリル酸6.3部、メタクリル酸2-ヒドロキシエチル10.5部、酢酸エチル10部、2,2'-アゾビスイソブチロニトリル(AIBN)0.02部を仕込んだ。次いで、反応容器内を窒素雰囲気下で撹拌しながら、80℃まで加熱し、反応を開始し、容器Aの内容物を滴下ポンプで2時間かけて滴下した。窒素雰囲気下にて還流温度で8時間重合反応を行った。反応終了後、冷却し、酢酸エチルを加えて希釈し、不揮発分35%のアクリル酸エステル共重合体溶液を得た。また、アクリル酸エステル共重合体の重量平均分子量(Mw)は87万であった。
(Comparative synthesis example 5)
13.5 parts of 2-ethylhexyl acrylate and 1.5 parts of lauryl methacrylate were placed in a reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen introduction tube (hereinafter sometimes simply referred to as the "reaction vessel"). 7.8 parts of butyl acrylate, 2.7 parts of acrylic acid, 4.5 parts of 2-hydroxyethyl methacrylate, 55 parts of ethyl acetate, 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN) After charging the reactor, the air in the reaction vessel was replaced with nitrogen gas. Furthermore, in a container A equipped with a stirrer, 31.5 parts of 2-ethylhexyl acrylate, 18.2 parts of butyl acrylate, 3.5 parts of lauryl methacrylate, 6.3 parts of acrylic acid, and 2-hydroxyethyl methacrylate were added. 10.5 parts of ethyl acetate, and 0.02 parts of 2,2'-azobisisobutyronitrile (AIBN) were charged. Next, the inside of the reaction container was heated to 80° C. while stirring under a nitrogen atmosphere to start the reaction, and the contents of container A were added dropwise over 2 hours using a dropping pump. The polymerization reaction was carried out at reflux temperature for 8 hours under a nitrogen atmosphere. After the reaction was completed, the mixture was cooled and diluted with ethyl acetate to obtain an acrylic ester copolymer solution with a nonvolatile content of 35%. Moreover, the weight average molecular weight (Mw) of the acrylic acid ester copolymer was 870,000.

表1記載の略語を下記に示す。
2EHA:アクリル酸2-エチルヘキシル
INA:アクリル酸イソノニル
LMA:メタクリル酸ラウリル
EA:アクリル酸エチル
BA:アクリル酸ブチル
AA:アクリル酸
BCEA:アクリル酸2-カルボキシエチル
HEMA:メタクリル酸2-ヒドロキシエチル
4HBA:アクリル酸4-ヒドロキシブチル
The abbreviations listed in Table 1 are shown below.
2EHA: 2-ethylhexyl acrylate INA: Isononyl acrylate LMA: Lauryl methacrylate EA: Ethyl acrylate
BA: Butyl acrylate
AA: acrylate BCEA: 2-carboxyethyl acrylate HEMA: 2-hydroxyethyl methacrylate 4HBA: 4-hydroxybutyl acrylate

(実施例1)
<粘着剤組成物の製造>
アクリル酸エステル共重合体(合成例1)100部に対し、イソシアネート系硬化剤としてとしてTDI-TMP2.5部を不揮発分換算にてそれぞれ配合し、更に、溶剤として酢酸エチルを不揮発分が30%となるように加え、均一になるよう混合して粘着剤組成物を得た。
(Example 1)
<Manufacture of adhesive composition>
To 100 parts of acrylic acid ester copolymer (synthesis example 1), 2.5 parts of TDI-TMP was added as an isocyanate curing agent in terms of non-volatile content, and ethyl acetate was added as a solvent with a non-volatile content of 30%. The adhesive composition was obtained by adding the following ingredients and mixing them uniformly to obtain a pressure-sensitive adhesive composition.

<粘着シートの製造>
得られた粘着剤組成物を、厚さ38μmの剥離性シート(ポリエチレンテレフタレート製)以下「剥離性フィルム基材」という)の剥離処理面上に、乾燥後の厚みが25μmとなるように上記で得られた粘着剤組成物を塗工し、熱風オーブンにて100℃、90秒間乾燥して粘着剤層を作製した。乾燥後、厚さ50μmの基材(ポリエチレンテレフタレート製)にラミネートし、さらに23℃-50%RHで7日間養生し、粘着シートを得た。
<Manufacture of adhesive sheet>
The resulting pressure-sensitive adhesive composition was applied to the release-treated surface of a 38-μm-thick releasable sheet (made of polyethylene terephthalate, hereinafter referred to as "releasable film base material") in the manner described above so that the thickness after drying would be 25 μm. The obtained adhesive composition was applied and dried in a hot air oven at 100° C. for 90 seconds to prepare an adhesive layer. After drying, it was laminated onto a 50 μm thick base material (made of polyethylene terephthalate) and further cured at 23° C. and 50% RH for 7 days to obtain an adhesive sheet.

(実施例2~32、比較例1~7)
アクリル酸エステル共重合体および各種添加剤を表2の組成および配合量(質量部)に変更した以外は、実施例1の粘着シートと同様の方法でそれぞれの粘着剤組成物、および粘着シートを製造した。
(Examples 2 to 32, Comparative Examples 1 to 7)
The respective adhesive compositions and adhesive sheets were prepared in the same manner as for the adhesive sheet of Example 1, except that the acrylic ester copolymer and various additives were changed to the composition and blending amount (parts by mass) shown in Table 2. Manufactured.


使用した材料は、以下の通りである。
<イソシアネート系硬化剤>
TDI-TMP:トリレンジイソシアネートとトリメチロールプロパンのアダクト体
<その他の硬化剤>
Azd:アジリジン系硬化剤、(株)ケミタイトPZ-33、日本触媒社製
<可塑剤>
ATBC:アセチルクエン酸トリブチル
The materials used are as follows.
<Isocyanate curing agent>
TDI-TMP: Adduct of tolylene diisocyanate and trimethylolpropane <Other curing agents>
Azd: Aziridine curing agent, Chemitite PZ-33, manufactured by Nippon Shokubai Co., Ltd. <Plasticizer>
ATBC: acetyl tributyl citrate

[評価項目および評価方法]
得られた粘着剤組成物および粘着シートを用いて、下記の方法で評価した。
[Evaluation items and evaluation method]
The obtained adhesive composition and adhesive sheet were evaluated by the following method.

(ゲル分率)
塗工後、23℃-50%RHの雰囲気下で7日間養生した粘着シートから幅30mm長さ100mmの試験片を切り出した。試験片から剥離シートを剥離し、露出した粘着層を300メッシュのステンレススチール製金網に貼り付け、試験片が剥がれないように金網を折りたたみ、試験片を包んだ状態で酢酸エチルに浸漬し、50℃で24時間静置した。浸漬後、金網を取り出し、少量の酢酸エチルで洗浄し、100℃で30分間乾燥した後、重量を測定した。ゲル分率は下記式(3)により算出した。
(ゲル分率)={(W2-W0-W3)/(W1-W0-W3)}×100 (式3)
W0:金網の重量
W1:金網+試験片の重量
W2:金網+試験片の乾燥後の重量
W3:試験片の基材の重量
(gel fraction)
After coating, a test piece with a width of 30 mm and a length of 100 mm was cut out from the adhesive sheet that was cured for 7 days in an atmosphere of 23° C. and 50% RH. The release sheet was peeled off from the test piece, the exposed adhesive layer was pasted on a 300 mesh stainless steel wire mesh, the wire mesh was folded to prevent the test piece from peeling off, the test piece was immersed in ethyl acetate with the test piece wrapped, It was left standing at ℃ for 24 hours. After immersion, the wire mesh was taken out, washed with a small amount of ethyl acetate, dried at 100° C. for 30 minutes, and then weighed. The gel fraction was calculated using the following formula (3).
(Gel fraction) = {(W2-W0-W3)/(W1-W0-W3)}×100 (Formula 3)
W0: Weight of wire mesh W1: Weight of wire mesh + test piece W2: Weight of wire mesh + test piece after drying W3: Weight of base material of test piece

(粘弾性)
厚さ38μmの剥離性シート(ポリエチレンテレフタレート製)以下「剥離性フィルム基材」という)の剥離処理面上に、乾燥後の厚みが25μmとなるように上記で得られた粘着剤組成物を塗工し、熱風オーブンにて100℃、90秒間乾燥して粘着剤層を作製した。乾燥後、厚さ75μmの別の剥離性シート(ポリエチレンテレフタレート製)以下「剥離性フィルム基材」という)にラミネートし、23℃-50%RHの雰囲気下で7日間養生し、「剥離性シート/粘着剤層/剥離性シート」という構成の2枚の剥離性シートで挟まれた粘着剤層を作成した。次いで、片方の剥離性シートを剥がし、粘着剤層が重なるように積層を繰り返し、厚みが1mmの粘着剤層を得た。オートクレーブで気泡を除去した後、直径8mmの円柱形に型抜きして貯蔵弾性率測定用の試験片を作成し、両側の剥離シートを剥離し、粘弾性を測定した。粘着剤層の貯蔵弾性率(G’)、損失弾性率(G’’)、損失正接(tanδ)は、TA Instruments(株)社製粘弾性測定装置「Ares-G2」を用いて周波数:1Hz、ひずみ0.1%、温度:-50℃~200℃(昇温速度10℃/分)の条件で温度依存性測定を実施した。得られた25℃、150℃での損失弾性率(G’’)値を用い下記(式1)からPの値を算出した。
P=(1Hzで測定した際の150℃の損失弾性率)/(1Hzで測定した際の25℃の損失弾性率) (式1)
(viscoelasticity)
The adhesive composition obtained above was applied onto the release-treated surface of a 38 μm thick releasable sheet (made of polyethylene terephthalate, hereinafter referred to as "releasable film base material") so that the thickness after drying was 25 μm. The adhesive layer was prepared by drying in a hot air oven at 100° C. for 90 seconds. After drying, it was laminated onto another releasable sheet (made of polyethylene terephthalate) with a thickness of 75 μm (hereinafter referred to as "releasable film base material"), and cured for 7 days in an atmosphere of 23°C and 50% RH. An adhesive layer sandwiched between two releasable sheets having the following structure was created: /adhesive layer/releasable sheet. Next, one of the releasable sheets was peeled off, and lamination was repeated so that the adhesive layers overlapped to obtain an adhesive layer with a thickness of 1 mm. After removing air bubbles in an autoclave, a test piece for measuring storage elastic modulus was prepared by cutting out a cylinder with a diameter of 8 mm, and the release sheets on both sides were peeled off, and the viscoelasticity was measured. The storage modulus (G'), loss modulus (G''), and loss tangent (tan δ) of the adhesive layer were measured using a viscoelasticity measuring device "Ares-G2" manufactured by TA Instruments Co., Ltd. at a frequency of 1 Hz. Temperature dependence measurements were carried out under the following conditions: , strain 0.1%, temperature: -50°C to 200°C (heating rate 10°C/min). Using the obtained loss modulus (G'') values at 25° C. and 150° C., the value of P was calculated from the following (Equation 1).
P=(loss modulus at 150°C when measured at 1Hz)/(loss modulus at 25°C when measured at 1Hz) (Formula 1)

(粘着力)
23℃-50%RHの雰囲気下で5時間養生した後の粘着シートから幅25mm長さ150mmの試験片を切り出した。切り出した粘着シートから剥離性シートを剥がして露出した粘着剤層を、ステンレス板(SUS304)の表面に貼着し、2kgロールを1往復して圧着した。その後、23℃-50%RHの雰囲気下に24時間放置した。次いで、JISZ0237に準拠し、引張試験機(テンシロン:オリエンテック社製)を用いて、剥離速度300mm/分、剥離角度180°の条件で粘着力(加熱前の粘着力)を測定した。評価基準は以下の通りである。
[評価基準]
◎:3N/25mm以上、優良。
○:1N/25mm以上3N/25mm未満、良好。
△:0.6N/25mm以上1N/25mm未満、実用可。
×:0.6N/25mm未満、実用不可。
(Adhesive force)
A test piece with a width of 25 mm and a length of 150 mm was cut from the adhesive sheet after curing for 5 hours in an atmosphere of 23° C. and 50% RH. The adhesive layer exposed by peeling off the releasable sheet from the cut-out adhesive sheet was adhered to the surface of a stainless steel plate (SUS304), and the adhesive layer was pressed with a 2 kg roll back and forth once. Thereafter, it was left in an atmosphere of 23° C. and 50% RH for 24 hours. Next, in accordance with JIS Z0237, the adhesive strength (adhesive strength before heating) was measured using a tensile tester (Tensilon, manufactured by Orientech Co., Ltd.) at a peeling rate of 300 mm/min and a peeling angle of 180°. The evaluation criteria are as follows.
[Evaluation criteria]
◎: 3N/25mm or more, excellent.
○: 1N/25mm or more and less than 3N/25mm, good.
△: 0.6N/25mm or more and less than 1N/25mm, practical.
×: Less than 0.6N/25mm, impractical.

(ボールタック)
得られた粘着シートを幅25mm・縦250mmの大きさに準備した。粘着シートから剥離性シートを剥がして傾斜角30度の傾斜版に粘着面を上にして固定した。助走路用のPETフィルムを上部に貼り付け、助走10cm糊面10cmとした試料にスチールボール(1/32~32/32インチ)を転がし、糊面の中央付近に停止するボールの径の番号を記録した。測定は23℃、相対湿度50%雰囲気下で実施した。
23℃、相対湿度50%雰囲気下での評価基準
◎:ボール径が11以上。非常に良好。
○:ボール径が8から10。良好。
△:ボール径が5から7。実用可。
×:ボール径が4以下。実用不可。
(ball tuck)
The obtained pressure-sensitive adhesive sheet was prepared in a size of 25 mm in width and 250 mm in length. The releasable sheet was peeled off from the adhesive sheet, and it was fixed on an inclined plate with an inclined angle of 30 degrees with the adhesive side facing up. A steel ball (1/32 to 32/32 inches) is pasted on the top of the sample for the run-up track, and the run-up track is 10 cm long, and the glue surface is 10 cm. Recorded. The measurements were carried out at 23°C under an atmosphere of 50% relative humidity.
Evaluation criteria under an atmosphere of 23° C. and 50% relative humidity ◎: Ball diameter is 11 or more. Very good.
○: Ball diameter is 8 to 10. Good.
△: Ball diameter is 5 to 7. Practical.
×: Ball diameter is 4 or less. Not practical.

(再剥離試験)
23℃-50%RHの雰囲気下で7日間養生した後の粘着シートから幅25mm長さ150mmの試験片を切り出した。切り出した粘着シートから剥離性シートを剥がして露出した粘着剤層を、ステンレス板(SUS304)の表面に貼着し、2kgロールを1往復して圧着した。その後、23℃-50%RH、40℃、60℃、55℃-80%RHの環境下に10日間保管した。10日後、試験片を23℃-50%RHに3時間放置し、次いで、JISZ0237に準拠し、引張試験機(テンシロン:オリエンテック社製)を用いて、剥離速度300mm/分、剥離角度180°の条件で粘着力(加熱前の粘着力)を測定し、測定後のステンレス板の状態を観察した。評価基準は以下の通りである。
[評価基準]
◎:ステンレス板への粘着剤の付着なし、優良。
○:ステンレス板への粘着剤の付着が貼り付け面積の0%を超え3%未満、良好。
△:ステンレス板への粘着剤の付着が貼り付け面積の3%以上5%未満、実用可。
×:ステンレス板への粘着剤の付着が貼り付け面積の5%以上、使用不可。
(Repeel test)
A test piece with a width of 25 mm and a length of 150 mm was cut from the adhesive sheet after curing for 7 days in an atmosphere of 23° C. and 50% RH. The adhesive layer exposed by peeling off the releasable sheet from the cut-out adhesive sheet was adhered to the surface of a stainless steel plate (SUS304), and the adhesive layer was pressed with a 2 kg roll back and forth once. Thereafter, it was stored for 10 days in an environment of 23° C.-50% RH, 40° C., 60° C., and 55° C.-80% RH. After 10 days, the test piece was left at 23°C - 50% RH for 3 hours, and then tested in accordance with JIS Z0237 using a tensile tester (Tensilon, manufactured by Orientec) at a peeling rate of 300 mm/min and a peeling angle of 180°. The adhesive strength (adhesive strength before heating) was measured under the following conditions, and the state of the stainless steel plate after the measurement was observed. The evaluation criteria are as follows.
[Evaluation criteria]
◎: No adhesive attached to stainless steel plate, excellent.
○: Adhesion of the adhesive to the stainless steel plate is more than 0% and less than 3% of the pasting area, good.
△: Adhesion of adhesive to stainless steel plate is 3% or more and less than 5% of the pasting area, practical.
×: Adhesion of adhesive to stainless steel plate exceeds 5% of pasting area, unusable.

(はみだし試験)
23℃-50%RHの雰囲気下で5時間または7日間養生した後の粘着シートを幅10mm・縦10mmの大きさに準備した。粘着シートから剥離性シートを剥がして、上下を厚さ38μmの剥離性シート(ポリエチレンテレフタレート製)で挟み、プレス試験機を用いて60℃の環境下、50Kg/cmの圧力を加え、2時間放置した。試験終了後サンプルを取り出し試験片端部からはみ出している糊の幅を(最大値)測定した。
評価基準
◎:はみだしが0.2mm未満。非常に良好。
○:はみだしが0.2以上0.4mm未満。良好。
△:はみだしが0.4以上0.6mm未満。実用可。
×:はみだしが0.6mm以上。実用不可。
(Protrusion test)
After curing in an atmosphere of 23° C. and 50% RH for 5 hours or 7 days, a pressure-sensitive adhesive sheet with a width of 10 mm and a length of 10 mm was prepared. Peel off the release sheet from the adhesive sheet, sandwich the top and bottom with a release sheet (made of polyethylene terephthalate) with a thickness of 38 μm, and apply a pressure of 50 kg/cm 2 at 60°C using a press tester for 2 hours. I left it alone. After the test was completed, the sample was taken out and the width (maximum value) of the glue protruding from the edge of the test piece was measured.
Evaluation criteria ◎: Protrusion is less than 0.2 mm. Very good.
○: Protrusion is 0.2 or more and less than 0.4 mm. Good.
Δ: Protrusion is 0.4 or more and less than 0.6 mm. Practical.
×: Protrusion is 0.6 mm or more. Not practical.

(貯蔵安定性)
硬化剤を配合後、均一に混合した粘着剤組成物を23℃-50%RHの雰囲気下に静置し、下記式(4)から粘度の上昇率を算出した。
(粘度の上昇率)={(硬化剤配合後7日後の粘度)/(硬化剤配合後1時間後の粘度)×100} (式4)
[評価基準]
◎:粘度の上昇率が150%未満、優良。
○:粘度の上昇率が150%以上160%未満、良好。
△:粘度の上昇率が160%以上170%未満、実用可。
×:粘度の上昇率が170%以上、使用不可。
(Storage stability)
After blending the curing agent, the uniformly mixed adhesive composition was left standing in an atmosphere of 23° C. and 50% RH, and the rate of increase in viscosity was calculated from the following formula (4).
(Rate of increase in viscosity) = {(Viscosity 7 days after mixing the curing agent)/(Viscosity 1 hour after mixing the curing agent) x 100} (Formula 4)
[Evaluation criteria]
◎: Increase rate of viscosity is less than 150%, excellent.
○: Increase rate of viscosity is 150% or more and less than 160%, good.
Δ: Viscosity increase rate is 160% or more and less than 170%, practical.
×: Viscosity increase rate is 170% or more, unusable.

アルキル基の炭素数が1~12である(メタ)アクリル酸エステルモノマー(A)、酸性基を有するモノマー(B)、水酸基を有するモノマー(C)からなるモノマー混合物の共重合体であるアクリル酸エステル共重合体と、イソシアネート系硬化剤を含む粘着剤組成物であり、酸性基を有するモノマー(B)の含有率は、モノマー混合物100質量%中、0.01質量%以上6質量%以下であり、水酸基を有するモノマー(C)の含有率は、モノマー混合物100質量%中、0.05質量%以上10質量%以下であり、ゲル分率が55%以上である、本発明の粘着剤組成物はいずれも粘着物性が良好であり、また各条件で長期間保管後の再剥離性が良好であり、高温高荷重下での粘着剤のはみだしも少なく、硬化剤配合後の貯蔵安定性にも優れた粘着シートを製造することができた。
Acrylic acid, which is a copolymer of a monomer mixture consisting of a (meth)acrylic acid ester monomer (A) whose alkyl group has 1 to 12 carbon atoms, a monomer (B) having an acidic group, and a monomer (C) having a hydroxyl group. It is an adhesive composition containing an ester copolymer and an isocyanate curing agent, and the content of the monomer (B) having an acidic group is 0.01% by mass or more and 6% by mass or less based on 100% by mass of the monomer mixture. The adhesive composition of the present invention, wherein the content of the monomer (C) having a hydroxyl group is 0.05% by mass or more and 10% by mass or less based on 100% by mass of the monomer mixture, and the gel fraction is 55% or more. All products have good adhesive physical properties, have good removability after long-term storage under various conditions, have little adhesive extrusion under high temperature and high load, and have good storage stability after adding a hardening agent. We were also able to produce an excellent adhesive sheet.

(実施例2~32、比較例1~7)
アクリル酸エステル共重合体および各種添加剤を表2の組成および配合量(質量部)に変更した以外は、実施例1の粘着シートと同様の方法でそれぞれの粘着剤組成物、および粘着シートを製造した。
ただし、実施例5、21、22、27~32は参考例である。
(Examples 2 to 32, Comparative Examples 1 to 7)
The respective adhesive compositions and adhesive sheets were prepared in the same manner as for the adhesive sheet of Example 1, except that the acrylic ester copolymer and various additives were changed to the composition and blending amount (parts by mass) shown in Table 2. Manufactured.
However, Examples 5, 21, 22, 27 to 32 are reference examples.

Claims (4)

アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)、酸性基を有するモノマー(B)、水酸基を有するモノマー(C)からなるモノマー混合物の共重合体であるアクリル酸エステル共重合体と、イソシアネート系硬化剤とを含み、酸性基を有するモノマー(B)の含有率は、モノマー混合物100質量%中、0.01質量%以上6質量%以下であり、水酸基を有するモノマー(C)の含有率は、モノマー混合物100質量%中、0.05質量%以上10質量%以下であり、ゲル分率が55%以上である粘着剤組成物。 Acrylic is a copolymer of a monomer mixture consisting of a (meth)acrylic acid alkyl ester monomer (A) whose alkyl group has 1 to 12 carbon atoms, a monomer (B) having an acidic group, and a monomer (C) having a hydroxyl group. The content of the monomer (B) containing an acid ester copolymer and an isocyanate curing agent and having an acidic group is 0.01% by mass or more and 6% by mass or less based on 100% by mass of the monomer mixture. A pressure-sensitive adhesive composition in which the content of the monomer (C) is 0.05% by mass or more and 10% by mass or less based on 100% by mass of the monomer mixture, and the gel fraction is 55% or more. アルキル基の炭素数が1~12である(メタ)アクリル酸アルキルエステルモノマー(A)100質量%中に占めるアルキル基の炭素数8~12である(メタ)アクリル酸アルキルエステルモノマー(a1)の含有率が55質量%以上である請求項1記載の粘着剤組成物。 (meth)acrylic acid alkyl ester monomer (A) whose alkyl group has 1 to 12 carbon atoms (meth)acrylic acid alkyl ester monomer (a1) whose alkyl group has 8 to 12 carbon atoms in 100% by mass; The adhesive composition according to claim 1, wherein the content is 55% by mass or more. 式1で表される、1Hzで測定した際の25℃の損失弾性率と150℃の損失弾性率の比(P)の値が0.02以上0.3以下である請求項1記載の粘着剤組成物。
P=(1Hzで測定した際の150℃の損失弾性率)/(1Hzで測定した際の25℃の損失弾性率) (式1)
The adhesive according to claim 1, wherein the ratio (P) of the loss modulus at 25°C and the loss modulus at 150°C when measured at 1 Hz, expressed by Formula 1, is 0.02 or more and 0.3 or less. agent composition.
P=(loss modulus at 150°C when measured at 1Hz)/(loss modulus at 25°C when measured at 1Hz) (Formula 1)
基材及び、請求項1~3いずれか1項記載の粘着剤組成物の硬化物からなる粘着剤層を備える粘着シート。

A pressure-sensitive adhesive sheet comprising a base material and a pressure-sensitive adhesive layer comprising a cured product of the pressure-sensitive adhesive composition according to any one of claims 1 to 3.

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006274151A (en) * 2005-03-30 2006-10-12 Nitto Denko Corp Adhesive composition, adhesive layer and method for producing the same, and adhesive sheets
WO2008004650A1 (en) * 2006-07-06 2008-01-10 Lintec Corporation Adhesive sheet
WO2009037990A1 (en) * 2007-09-21 2009-03-26 Sekisui Chemical Co., Ltd. Pressure-sensitive adhesive and surface-protecting pressure-sensitive adhesive sheet made with the same
JP2012149181A (en) * 2011-01-19 2012-08-09 Nitto Denko Corp Double-sided adhesive tape or sheet, and method for processing adherend
JP2017077687A (en) * 2015-10-21 2017-04-27 リンテック株式会社 Window film

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3486698B2 (en) * 1994-10-04 2004-01-13 一方社油脂工業株式会社 Pressure-sensitive adhesive composition and pressure-sensitive adhesive product
JP3834162B2 (en) 1999-05-18 2006-10-18 積水化学工業株式会社 Removable adhesive tape
JP3897236B2 (en) 2001-11-26 2007-03-22 ソマール株式会社 Removable adhesive sheet
JP5120587B2 (en) 2006-05-30 2013-01-16 Dic株式会社 Adhesive composition
JP5649280B2 (en) 2009-01-28 2015-01-07 リンテック株式会社 Re-peeling pressure-sensitive adhesive composition and pressure-sensitive adhesive sheet
JP5436394B2 (en) 2010-10-29 2014-03-05 チェイル インダストリーズ インコーポレイテッド Adhesive composition
JP5607565B2 (en) 2011-03-28 2014-10-15 リンテック株式会社 Adhesive and adhesive sheet
JP2020033424A (en) 2018-08-28 2020-03-05 三菱ケミカル株式会社 Adhesive composition, adhesive obtained by crosslinking the same and adhesive film
JP6838090B2 (en) 2019-02-07 2021-03-03 藤森工業株式会社 Adhesive composition and surface protective film
JP6906560B2 (en) 2019-04-03 2021-07-21 リンテック株式会社 Adhesive sheet and display
JP7346898B2 (en) 2019-05-09 2023-09-20 Dic株式会社 adhesive film
JP7310582B2 (en) 2019-12-09 2023-07-19 日本カーバイド工業株式会社 PSA COMPOSITION FOR FOLDABLE DISPLAY AND OPTICAL MEMBER FOR FOLDABLE DISPLAY

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006274151A (en) * 2005-03-30 2006-10-12 Nitto Denko Corp Adhesive composition, adhesive layer and method for producing the same, and adhesive sheets
WO2008004650A1 (en) * 2006-07-06 2008-01-10 Lintec Corporation Adhesive sheet
WO2009037990A1 (en) * 2007-09-21 2009-03-26 Sekisui Chemical Co., Ltd. Pressure-sensitive adhesive and surface-protecting pressure-sensitive adhesive sheet made with the same
JP2012149181A (en) * 2011-01-19 2012-08-09 Nitto Denko Corp Double-sided adhesive tape or sheet, and method for processing adherend
JP2017077687A (en) * 2015-10-21 2017-04-27 リンテック株式会社 Window film

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