TW201041645A - Water-based emulsion - Google Patents
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- TW201041645A TW201041645A TW099109034A TW99109034A TW201041645A TW 201041645 A TW201041645 A TW 201041645A TW 099109034 A TW099109034 A TW 099109034A TW 99109034 A TW99109034 A TW 99109034A TW 201041645 A TW201041645 A TW 201041645A
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- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D133/00—Coating compositions 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; Coating compositions based on derivatives of such polymers
- C09D133/04—Homopolymers or copolymers of esters
- C09D133/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
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- C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
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- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
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- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
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- C08J2331/00—Characterised by the use of 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 an acyloxy radical of a saturated carboxylic acid, or carbonic acid, or of a haloformic acid
- C08J2331/02—Characterised by the use of omopolymers or copolymers of esters of monocarboxylic acids
- C08J2331/04—Homopolymers or copolymers of vinyl acetate
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- C08J2333/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
- C08J2333/04—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters
- C08J2333/06—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters of esters containing only carbon, hydrogen, and oxygen, the oxygen atom being present only as part of the carboxyl radical
- C08J2333/08—Homopolymers or copolymers of acrylic acid esters
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- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
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- C08L31/00—Compositions of 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 an acyloxy radical of a saturated carboxylic acid, of carbonic acid or of a haloformic acid; Compositions of derivatives of such polymers
- C08L31/02—Homopolymers or copolymers of esters of monocarboxylic acids
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L33/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
- C08L33/04—Homopolymers or copolymers of esters
- C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
- C08L33/08—Homopolymers or copolymers of acrylic acid esters
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- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K23/00—Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
- C09K23/16—Amines or polyamines
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Abstract
Description
201041645 , 六、發明說明: 【發明所屬之技術領域】 本發明係有關一種水性乳劑。 1 【先前技術】 聚丙稀因加工性及強度優異而用於保險桿(bumper)等 汽車構件方面。汽車構件中,為了裝飾等,通常係塗佈塗 料。然而,因聚丙烯之表面難以與塗料等其他材料接著, 因此,一般係將與聚丙烯之接著性優異的氯化聚烯烴塗佈 〇 在聚丙烯上,再於其上塗佈塗料(例如:參照曰本特開平 5-7832號公報)。 【發明内容】 本發明係提供如下: ' 〈1>一種水性乳劑,係包含如下述之成分(A)、成分(B)及成 分(C): 成分(A):包含源自α,石-不飽和羧酸之構造單元、以及源 ^ 自由具有可具取代基之胺基的碳原子數1至10之脂肪族醇 〇 與ο: , /3 -不飽和缓酸所衍生的α,/5 -不飽和羧酸酯之構造 單元的丙稀酸系樹脂,其中,該丙稀酸系樹脂之親水比率 為9至12 (在此,丙稀酸系樹脂之親水比率係衍生該丙稀 酸系樹脂之構造單元的單體之親水比率的重量平均值,單 體之親水比率係由下述式所求算之值: 單體之親水比率=20χ(單體之親水部分之式量)/(單體之分 子量)); 成分(Β):熱塑性聚合物; 4 321925 201041645 " 成分(c):水。 <2>如<1>記載之水性乳劑,其中,(B)成分係包含:具有源 自乙烯及/或丙烯之構造單元的熱塑性聚合物。 <3>如<1>記載之水性乳劑,其中,(B)成分係包含: . 在含有源自乙烯及/或丙烯之構造單元以及源自式(I) CH2=CH-R (I) (式中,R表示2級烷基、3級烷基或脂環式烴基)所示乙烯 系化合物之構造單元的共聚物中,使α,冷-不飽和羧酸酐 Ο 進行接枝聚合而得之聚合物。 <4>如<3>記載之水性乳劑,其中,式(I)所示之乙烯系化合 . 物為乙烯基環己烷。 <5>如<1>至<4>中任一項記載之水性乳劑,其中,成分(B) 係 MFR(melt flow rate,亦即熔融流動速率)(190°C、2. 16 kgf)達130g/10分鐘以上、300g/10分鐘以下之熱塑性聚 合物。 ◎ <6>如<1>至<5>中任一項記載之水性乳劑,該水性乳劑係以 上述成分(A)以及上述成分(B)為分散質並以上述成分(C) 為分散媒者,其中,該分散質之體積基準中位數直徑 (median diameterAO.Olvu^S/zm。 <7>如<1>至<6>中任一項記載之水性乳劑,其中,源自由具 有可具取代基之胺基的碳原子數1至10之脂肪族醇與α, 冷-不飽和羧酸所衍生的α,不飽和羧酸酯之構造單元 為源自甲基丙烯酸Ν,Ν-二甲胺基乙酯之構造單元。 <8>如<1>至<7>中任一項記載之水性乳劑,其中,源自α, 5 321925 201041645 '不飽和羧酸之構造單元為源自丙烯酸或曱基丙烯酸之 構造單元。 <9>一種水性乳劑之製造方法,其特徵係將成分(A)以及成 分(B)熔融混煉後,將所得熔融混合物與水混合; 、 成分(A):包含源自α,沒~不飽和羧酸之構造單元、以及源 自由具有可具取代基之胺基的碳原子數丨至1Q之脂肪族醇 與α,/3-不飽和叛酸所衍生的α,石_不飽和賴g旨之構^ 單元的丙烯酸系樹脂,其中,該丙稀酸系樹脂之親水 為9至m在此,丙烯酸系樹月旨之親水比率係衍生該 酸系樹脂之構造單元的單體之親水比率的重量平均值 • 體之親水比率係由下述式所求算之值: 早 單體之親水比率=20x(單俨十如,Μ \ , 、子量)). 平體之親水部分之式量)/(單體之分 成分(Β):熱塑性聚合物; 成分(C):水。 〇 <10>-種硬化物’係經由使❿至❿ 乳劑乾燥而得者。 積層體’係具有:由至少-種選自木質材料、纖 維^材料、塑膠材料、陶竞材料以及金屬材料而成组群ί I。料所構成之基材層,與由⑽記載之硬化物所構成之 〈12> 一種積層體之製造方法,係包含下述步驟: 陶奢^至^種選自木質材料、纖維素材料、塑膠材料、 _/、以及金屬材料而成組群中之材料所構成之基材層 321925 6 201041645 上,塗佈<1>至<8>中任一項記載之水性乳劑,得到具有該 基材層與該水性乳劑層之積層體的步驟;以及 將上述步驟所得積層體進行乾燥,得到具有上述基材 層與由上述水性乳劑所得之硬化物層的積層體之步驟。 - < 13 > —種乳化劑,係含有包含源自<2 , /5 -不飽和缓酸之構 造單元、以及源自由具有可具取代基之胺基的碳原子數1 至10之脂肪族醇與a, 不飽和羧酸所衍生的α, /5-不 飽和羧酸酯之構造單元的丙烯酸系樹脂作為有效成分,且 〇 該丙烯酸系樹脂之親水比率為9至12者(在此,丙稀酸系 樹脂之親水比率係衍生該丙烯酸系樹脂之構造單元的單體 . 之親水比率的重量平均值,單體之親水比率係由下述式所 求算之值: 單體之親水比率=20χ(單體之親水部分之式量)/(單體之分 子量))。 <14>如<13>記載之乳化劑,其中,源自由具有可具取代基 Q 之胺基的碳原子數1至10之脂肪族醇與α,石-不飽和羧酸 所衍生的α,石-不飽和羧酸酯之構造單元為源自甲基丙烯 酸Ν,Ν-二曱胺基乙酯之構造單元。 <15>如<13>或<14>記載之乳化劑,其中,源自α , /3 -不飽 和羧酸之構造單元為源自選自由丙烯酸及曱基丙烯酸所成 組群中之至少一種的構造單元。 <16>—種<1>至<8>中任一項記載之水性乳劑之用途,係用 以在由至少·—種選自木質材料、纖維素材料、塑膠材料、 陶瓷材料以及金屬材料而成組群中之材料所構成之基材層 7 321925 201041645 上形成硬化物層。 【實施方式】 本發明之水性乳劑包含下述成分(Α)、成分⑻以及成 分⑹。 成分(Α).包含源自α’厶_不飽和羧酸之構造單元(以下簡 稱為構造單元(al))、q源自由具有可具取代基之胺基的 礙原子數1至1G之脂肪㈣與α,不飽和㈣所衍生的201041645, VI. Description of the invention: [Technical field to which the invention pertains] The present invention relates to an aqueous emulsion. 1 [Prior Art] Polypropylene is used for automotive components such as bumpers because of its excellent workability and strength. In automotive parts, coatings are usually applied for decoration or the like. However, since the surface of the polypropylene is difficult to adhere to other materials such as paints, a chlorinated polyolefin excellent in adhesion to polypropylene is generally coated on the polypropylene, and a coating is applied thereon (for example: Refer to 曰本特开平5-7832号). SUMMARY OF THE INVENTION The present invention provides the following: ' <1> An aqueous emulsion comprising the following components (A), (B) and (C): Component (A): comprising alpha, stone- a structural unit of an unsaturated carboxylic acid, and an aliphatic alcohol oxime having a carbon number of 1 to 10 which may have a substituent-containing amine group, and α,/5 derived from /3 -unsaturated acid. An acrylic resin having a structural unit of an unsaturated carboxylic acid ester, wherein the acrylic resin has a hydrophilic ratio of 9 to 12 (here, the hydrophilic ratio of the acrylic resin is derived from the acrylic acid system) The weight average of the hydrophilic ratio of the monomer of the structural unit of the resin, and the hydrophilic ratio of the monomer is a value calculated by the following formula: Hydrophilic ratio of the monomer = 20 χ (the amount of the hydrophilic portion of the monomer) / ( Molecular weight of monomer)); Component (Β): Thermoplastic polymer; 4 321925 201041645 " Ingredient (c): Water. The aqueous emulsion according to <1>, wherein the component (B) comprises a thermoplastic polymer having a structural unit derived from ethylene and/or propylene. <3> The aqueous emulsion according to <1>, wherein the component (B) comprises: a structural unit derived from ethylene and/or propylene and derived from the formula (I) CH2=CH-R (I) In the copolymer of the structural unit of the vinyl compound represented by the formula (wherein R represents a 2nd alkyl group, a 3rd alkyl group or an alicyclic hydrocarbon group), α, a cold-unsaturated carboxylic anhydride hydrazine is graft-polymerized. The resulting polymer. The aqueous emulsion of the formula (I), wherein the vinyl compound is a vinyl cyclohexane, as described in <3>. The aqueous emulsion according to any one of <1> to <4>, wherein the component (B) is a MFR (melt flow rate) (190 ° C, 2.16). Kgf) A thermoplastic polymer of 130 g/10 min or more and 300 g/10 min or less. The aqueous emulsion according to any one of the above-mentioned (A) and the component (B) is a dispersoid and the component (C) is the above-mentioned component (C). In the case of the dispersion medium, the volume-based median diameter of the dispersoid (median diameter AO.Olvu^S/zm. <7>, the aqueous emulsion according to any one of <1> to <6> Wherein the structural unit derived from an aliphatic alcohol having from 1 to 10 carbon atoms having a substituent-containing amino group and α, a cold-unsaturated carboxylic acid derived from a methyl group An aqueous emulsion according to any one of <1> to <7>, which is derived from α, 5 321925 201041645 'unsaturated. The structural unit of the carboxylic acid is a structural unit derived from acrylic acid or mercaptoacrylic acid. <9> A method for producing an aqueous emulsion characterized in that the obtained molten mixture is obtained by melt-kneading the component (A) and the component (B). Mixed with water; component (A): a structural unit derived from α, a non-unsaturated carboxylic acid, and a source An acrylic resin derived from an aliphatic alcohol having a number of carbon atoms which may have a substituent, and an aliphatic alcohol, which is derived from α,/3-unsaturated tarenic acid, and α-, alkaloid-unsaturated Wherein the hydrophilicity of the acrylic resin is 9 to m. Here, the hydrophilic ratio of the acrylic resin is the weight average of the hydrophilic ratio of the monomer derived from the structural unit of the acid resin. The value calculated by the following formula: The hydrophilic ratio of the early monomer = 20x (single 俨 10, Μ \ , , sub-quantity)). The amount of the hydrophilic part of the flat body / (the sub-component of the monomer) (Β): thermoplastic polymer; component (C): water. 〇 <10>-type hardened material' is obtained by drying a cerium to lanthanum emulsion. The laminated body 'system has: at least one selected from wood a material, a fiber material, a plastic material, a ceramic material, and a metal material. The substrate layer composed of the material and the cured material described in (10) <12> A method for manufacturing a laminate, The system comprises the following steps: Tao Xing ^ to ^ species selected from wood materials, cellulosic materials, plastic materials, _ / And the aqueous layer emulsion according to any one of <1> to <8>, which is obtained by the material in the group of the metal materials, and the substrate layer and the substrate layer a step of laminating the aqueous emulsion layer; and drying the laminate obtained in the above step to obtain a laminate having the substrate layer and the cured layer obtained from the aqueous emulsion. - < 13 > An agent comprising a structural unit derived from a <2, /5-unsaturated acid, and an aliphatic alcohol having a carbon number of 1 to 10 derived from a group having a substituent, and a, an unsaturated carboxylic acid The acrylic resin of the structural unit of the α, /5-unsaturated carboxylic acid ester derived from the acid is used as an active ingredient, and the hydrophilic ratio of the acrylic resin is 9 to 12 (here, the hydrophilicity of the acrylic resin) The ratio is the weight average of the hydrophilic ratio of the monomer derived from the structural unit of the acrylic resin, and the hydrophilic ratio of the monomer is a value calculated by the following formula: Hydrophilic ratio of the monomer = 20 Å (the hydrophilicity of the monomer) Part of the amount) / (single part Sub-quantity)). <14> The emulsifier according to <13>, which is derived from an aliphatic alcohol having 1 to 10 carbon atoms which may have an amine group which may have a substituent Q, and an α, stone-unsaturated carboxylic acid The structural unit of the α,stone-unsaturated carboxylic acid ester is a structural unit derived from ruthenium methacrylate, ruthenium-diguanylaminoethyl ester. The emulsifier according to <13> or <14>, wherein the structural unit derived from the α, /3-unsaturated carboxylic acid is derived from a group selected from the group consisting of acrylic acid and methacrylic acid. At least one of the structural units. The use of the aqueous emulsion according to any one of <1> to <8>, which is selected from at least one selected from the group consisting of wood materials, cellulosic materials, plastic materials, ceramic materials, and A hardened layer is formed on the base material layer 7 321925 201041645 which is composed of a material in a group of metal materials. [Embodiment] The aqueous emulsion of the present invention comprises the following components (Α), component (8), and component (6). Ingredient (Α). Contains a structural unit derived from an α'厶-unsaturated carboxylic acid (hereinafter referred to as a structural unit (al)), and q is derived from a fat having a substituent having an amine group of 1 to 1 G. (d) derived from α, unsaturated (four)
Ο α’石一不飽和竣酸醋之構造單元(以下簡稱為構造單元 (a2))的丙雜系樹脂’其巾,該㈣酸系細旨之親水比率 =9,12(在此’丙㈣系樹脂之親水比率係衍生該丙稀 =系樹脂之構造單元的單體之親水 ,之親水比率係由下述式所求算之值千均值早 單體之親水比率=2〇χ(單體 子量. 之親水部分之式量)/(單體之分 成分(Β):熱塑性聚合物; 成分(C):水。 首先’對成分(Α)進行說明。 ^成分係包含構造單元(al)與構造單元(a2)之丙烯 酉夂系樹脂。衍生構造單》(alka,石一不飽和叛酸可列舉 丙烯酸、曱基丙烯酸、巴豆酸、異巴豆酸、馬來酸、 f馬酸、衣康酸、擰康醭、當歸酸(angelic acid)、山梨 酉夂中康酸等碳原子數3矣20之α,石-不飽和紐。該α, ^不飽和羧酸以具有1個或2個鲮基(-C00H)之不 飽和綾酸為佳。 321925 8 201041645 成分(A)之丙烯酸系樹脂可具有2種以上之構造單元 (al)。 構造單元(al)係以選自由源自丙烯酸之構造單元以及 • 源自甲基丙烯酸之構造單元所成組群中之至少一種為佳。 ' 衍生構造單元(a2)之α,/5-不飽和羧酸酯係由具有可 具取代基之胺基的碳原子數1至10之脂肪族醇與α,/3-不飽和羧酸所衍生。α不飽和羧酸可列舉如與上述者 Q 相同之物,而以丙烯酸或甲基丙烯酸為佳。 可具有取代基之胺基可列舉如:胺基、甲胺基、乙胺 基、丙胺基、異丙胺基、丁胺基、異丁胺基、第二丁胺基、 • 第三丁胺基等具有1個碳原子數1至10之直鏈狀、分枝鏈 . 狀或環狀的烷基之胺基;二曱胺基、曱基乙基胺基、二乙 胺基一丙私基專具有2個破原子數1至1〇之直鏈狀、分 枝鏈狀或環狀的烷基之胺基;以及環狀胺基,其中以具有 2個奴原子數丨至1〇之直鏈狀、分枝鏈狀或環狀的烷基之 〇胺基為佳’以具有2個碳原子數i至3之直鏈狀、分枝鍵 狀或環狀的烧基之胺基更佳。 碳原子數1至10之脂肪族醇可列舉如:曱醇、乙醇、Ο α' stone-unsaturated citric acid vinegar structural unit (hereinafter referred to as structural unit (a2)) of the acrylic resin's towel, the (four) acid system of the purpose of the hydrophilic ratio = 9,12 (here 'c (4) The hydrophilic ratio of the resin is the hydrophilicity of the monomer derived from the structural unit of the propylene = resin, and the hydrophilic ratio is the value calculated by the following formula: the monthly mean hydrophilic ratio of the monomer = 2 〇χ (single The amount of the body. The amount of the hydrophilic part) / (the component of the monomer (Β): thermoplastic polymer; the component (C): water. First, the component (Α) is explained. ^ The component contains the structural unit ( Al) and propylene fluorene resin of structural unit (a2). Derivative structure list (alka, stone-unsaturated oxic acid can be cited as acrylic acid, methacrylic acid, crotonic acid, isocrotonic acid, maleic acid, f-acid , itaconic acid, jingkang, angelic acid, sorbic acid, and other carbon atoms with a carbon number of 3矣20, a stone-unsaturated nucleus. The α, ^ unsaturated carboxylic acid has 1 Or 2 fluorenyl (-C00H) unsaturated decanoic acid is preferred. 321925 8 201041645 The acrylic resin of the component (A) can have 2 kinds of The structural unit (al). The structural unit (al) is preferably at least one selected from the group consisting of structural units derived from acrylic acid and • structural units derived from methacrylic acid. 'Derivative structural unit (a2) The α,/5-unsaturated carboxylic acid ester is derived from an aliphatic alcohol having 1 to 10 carbon atoms which may have a substituent, and an α,/3-unsaturated carboxylic acid. The same as the above Q, and preferably acrylic acid or methacrylic acid. The amine group which may have a substituent may, for example, be an amine group, a methylamino group, an ethylamino group, an propylamino group or an isopropylamine group. Amino group having one linear, branched chain or cyclic alkyl group having 1 to 10 carbon atoms, such as butylamine, isobutylamino, butylamino, and butylamino Diaminoamine, mercaptoethylamino, diethylamino-propyl-propyl group has two linear, branched or cyclic alkyl groups of 1 to 1 Å. And a cyclic amine group in which a decyl group having a linear, branched chain or cyclic alkyl group having 2 slave atoms 丨 to 1 为 is preferred to have 2 carbons The amine group having a linear, branched or cyclic alkyl group having an atomic number of i to 3 is more preferable. The aliphatic alcohol having 1 to 10 carbon atoms may, for example, be decyl alcohol or ethanol.
丙醇、異丙醇、丁醇、第三丁醇、戊醇、3_曱基丁醇、H 二甲基丙醇、3-甲基-2-丁醇、2-乙基己醇、壬醇、癸醇、 環己醇等碳原子數1至1〇之直鏈狀、分枝鏈狀或環狀的脂 肪族醇,以碳原子數丨至4之直鏈狀、分枝鏈狀或環^ 脂肪族醇為佳。 < 的 具有可具取代基之胺基的碳原子數〗至1〇之脂肪族醇 321925 9 201041645 、 可列舉如:N,N-二甲胺基乙醇、N,N-二乙胺基乙醇、N-甲 基-N-乙胺基乙醇、N,N-二丙胺基乙醇、N_曱基-N-丙胺基 乙醇、N-乙基-N-丙胺基乙醇、N, N-二甲胺基丙醇以及N,N-• 二甲胺基丁醇。 . 由具有可具取代基之胺基的碳原子數1至10之脂肪族 醇與α,沒-不飽和羧酸所衍生之〇:,点-不飽和羧酸酯可列 舉如:丙烯酸Ν,Ν-二乙胺基乙酯、甲基丙烯酸Ν,Ν-二乙胺 基乙酯、丙烯酸Ν,Ν-二曱胺基乙酯、曱基丙晞酸ν,Ν-二甲 〇 胺基乙酯、丙烯酸Ν-曱基-Ν-乙胺基乙酯以及曱基丙烯酸 Ν-甲基-Ν-乙胺基乙酯,而以甲基丙稀酸ν,Ν-二甲胺基乙 δ旨為佳。 成分(Α)之丙烯酸系樹脂可具有2種以上之構造單元 (a2)。 成分(A)之丙烯酸系樹脂中的構造單元(al)之含量,相 對於構成該丙烯酸系樹脂之全部構造單元1 〇 〇莫耳,一般 〇 為20至99莫耳,以50至99莫耳為佳。 成分(A)之丙烯酸系樹脂中的構造單元(&2)之含量,相 對於構成該丙烯酸系樹脂之全部構造單元1〇〇莫耳,一般 為1至80莫耳,以1至50莫耳為佳。 成分(A)之丙稀酸系樹脂可含有2種以上之丙晞酸系 樹脂。 成分(Α)之丙烯酸系樹脂除了構造單元(al)以及構造 單元(a2)以外,亦可具有其它之構造單元。 其它之構造單元可列舉如:源自由碳原子數丨至2〇之 10 321925 201041645 脂肪族醇與α I不飽和㈣所衍生之α 酯的構造單元(以下簡稱為楢,不飽和羧醆 數1曼心卜昨 早疋⑽)、源自由碳原子 0之夕以日肪族醇與α,/5-不飽和_所衍生 石-不飽和羧酸酯的構造單 , rK9,, r η再1^早兀(以下簡稱為構造單元 :2)):源自由具有㈣基之碳原子數…。之 與H不飽和《_生之aj_不飽 單元(以下簡稱為構造單元⑽)、以及源自由聚St Ο ❹ 不飽和㈣所衍生之“,^不飽和㈣㈣構造單 元(以下簡稱為構造單元(b4 ))。 衍生上述其它構造單元的H不飽和㈣可列舉如 與上述者相同之物,而以丙締酸或甲基丙婦酸為佳。 知生構k單70⑽之α,点_不飽和幾酸醋係由碳原子 數1至20之脂肪族醇與α,万_不飽和羧酸所衍生。該碳原 子數1至20之脂肪族醇可列舉如:甲醇、乙醇、丙醇、異 丙醇、丁醇、第三丁醇、戊醇、3_甲基丁醇、2,2_二甲基 丙醇、3-甲基一 2-丁醇、2-乙基己醇、壬醇、癸醇、十二醇 (d〇decanol)、十三醇、十六醇、十八醇、環己醇等碳原子 數1至20之直鏈狀、分枝鏈狀或環狀的脂肪族醇。 由石反原子數1至20之脂肪族醇與α,不飽和鲮酸所 衍生之α,石-不飽和羧酸酯可列舉如:丙烯酸甲酯、丙烯 酸乙酯、丙烯酸丙酯、丙烯酸丁酯、丙烯酸戊酯、丙烯酸 3-甲基丁酯、丙烯酸2, 2-二甲基丙酯、丙烯酸3_甲基一2一 丁酉曰、丙烯酸2-乙基己酯、丙烯酸壬酯、丙烯酸癸酯、丙 烯酸十二酯、丙烯酸十三酯、丙烯酸十六酯、丙烯酸十八 321925 11 201041645 , 酯、丙稀酸環己酯、甲基丙烯酸甲酯、曱基丙烯酸乙酯、 曱基丙烯酸丙酯、甲基丙烯酸丁酯、甲基丙烯酸戊酯、甲 基丙烯酸2-甲基-2-丁酯、曱基丙烯酸2-乙基己酯、τ基 • 丙烯酸壬醋、甲基丙烯酸癸酯、曱基丙烯酸十二醋、甲基 • 丙烯酸十三醋、甲基丙烯酸十六醋、甲基丙稀酸十八醋以 及丙烯酸環己酯。 成分(A)之丙烯酸系樹脂可含有2種以上之構造單元 (M)。 ^ 衍生構造單元(b2)之α,/5 -不飽和羧酸酯係由碳原子 數1至10之多元脂肪族醇與α,/3 -不飽和缓酸所衍生。該 碳原子數1至10之多元脂肪族醇可列舉如:羥基甲醇、羥 基乙醇、羥基丙醇、羥基丁醇、羥基戊醇及羥基己醇。 由碳原子數1至10之多元脂肪族醇與α,/3-不飽和羧 酸所衍生之〇:,万-不飽和羧酸酯可列舉如:丙烯酸羥基曱 酉旨、丙稀酸經基乙S旨、丙細酸經基丙S旨、丙稀酸經基丁醋、 Q 丙烯酸羥基戊酯、丙烯酸羥基己酯、曱基丙烯酸羥基曱酯、 曱基丙稀酸羥基乙酯、甲基丙烯酸經基丙酯、曱基丙烯酸 羥基丁酯、曱基丙烯酸羥基戊酯及曱基丙烯酸羥基己酯。 成分(Α)之丙烯酸系樹脂可含有2種以上之構造單元 ⑽。 構造單元(b3)係源自由具有羧酸基之碳原子數1至10 的脂肪族醇與α,/5 -不飽和叛酸所衍生之α,/5 -不飽和叛 酸酯。此處之“羧酸基”意指具有羧基(-COOH)之有機基, 可列舉如:羧曱基、1, 2-二羧乙基、2-羧苯基以及2, 3-二 12 321925 201041645 、 羧苯基。 由具有該竣酸基之碳原子數!至10的脂肪族醇與^ /5-不飽和羧酸所衍生之α,β 一不飽和羧酸酯可列舉如:琥 ί白酸2-丙烯ϋ氧基乙g旨、㈣2_㈣醯氧基乙自旨、號站酸 • 2_甲基丙_氧基乙S旨以及酞酸2-甲基丙_氧基乙\旨。 成分(A)之丙烯酸系樹脂可含有2種以上之構造單元 ⑽。 Ο 構造單元(b4)係源自由聚烷二醇與《,冷-不飽和羧酸 所衍生之(2,/5 -不飽和羧酸酯。該聚烧二醇係聚乙二醇、 聚丙二醇、聚乙二醇聚丙二醇、聚乙二醇聚四亞曱二醇、 • 甲氧基聚乙二醇等介由氧原子而鍵結1至50個碳原子數1 至4的伸烷基而成之聚烷二醇,以及該等聚烷二醇之末端 的羥基可經碳原子數1至2〇之烷基、丙烯醯基、甲基丙烯 酿基等保護。 由聚烷二醇與a,y5_不飽和羧酸所衍生之α,沒―不飽 0 和羧酸酯可列舉如:丙烯酸聚丙二醇酯、丙烯酸聚乙二醇 酯、丙烯酸聚乙二醇聚丙二醇酯、單丙烯酸聚乙二醇聚四 亞甲二醇酯、丙烯酸曱氧基聚乙二醇酯、甲基丙烯酸聚丙 二醇酯、甲基丙烯酸聚乙二醇酯、甲基丙烯酸聚乙二醇聚 丙一醇S曰、單曱基丙烯酸聚乙二醇聚四亞甲二醇醋以及甲 基丙烯酸甲氧基聚乙二醇酯。 成分(Α)之丙烯酸系樹脂以含有構造單元(bl)或構造 單元(b3)者為佳,以含有構造單元(bl)及構造單元(b3)者 更佳。 321925 13 201041645 當成分(A)之丙烯酸系樹脂含有構造單元(bl)時,作為 構造單元(bl)之含量,相對於構成該丙烯酸系樹脂之全部 構造單元100莫耳,一般為5至95莫耳,以10至80莫耳 為佳。 成分(A)之丙烯酸系樹脂中之構造單元(b2)之含量,相 對於構成該丙烯酸系樹脂之全部構造單元100莫耳,一般 為0至50莫耳,以0至30莫耳為佳,又以0至1莫耳更 佳。 當成分(A)之丙烯酸系樹脂含有構造單元(b3)時,作為 構造單元(b3)之含量,相對於構成該丙烯酸系樹脂之全部 構造單元100莫耳,一般為0. 1至80莫耳,以5至40莫 耳為佳。 成分(A)之丙烯酸系樹脂中之構造單元(b4)之含量,相 對於構成該丙烯酸系樹脂之全部構造單元100莫耳,一般 為0至50莫耳,以0至30莫耳為佳,又以0至1莫耳更 佳。 成分(A)之丙烯酸系樹脂中,構造單元(al)、構造單元 (b3)等具有陰離子性基的構造單元之含量,從由本發明之 水性乳劑所得之硬化物對聚丙烯之接著性的觀點而言,相 對於構成該丙烯酸系樹脂之全部構造單元100莫耳,以45 至85莫耳為佳,以50至80莫耳更佳。 作為成分(A)之丙烯酸系樹脂,相對於構成該丙烯酸系 樹脂之全部構造單元100莫耳,係以含有5至80莫耳之構 造單元(al)、1至50莫耳之構造單元(a2)、10至80莫耳 14 321925 201041645 之構造單元(bl)以及5至30莫耳之構造單元(b3)且構造單 元(al)、(a2)、(bl)以及(b3)之合計量為100莫耳的丙烯 酸系樹脂為佳。 成分(A)之丙烯酸系樹脂可含有源自乙烯之構造單 - 元、源自丙烯之構造單元、源自下述之碳原子數4以上的 直鏈狀烯烴之構造單元、源自後述式(I)所示之乙烯系 化合物的構造單元、源自下述之可加成聚合的單體之構造 _ 單元等,惟該含量如為無損及由本發明之水性乳劑所得之 ❹ 硬化物的接著性之量即可,相對於構成該丙烯酸系樹脂之 全部構造單元100莫耳,以約5莫耳以下為佳,源自可加 、 成聚合的單體之構造單元係以1莫耳以下為佳。 成分(Α)之丙烯酸系樹脂可藉由使衍生各構造單元之 單體加成聚合而製造。其例可列舉如:將異丙醇等醇溶媒、 水等溶媒與單體混合,將所得混合物與自由基起始劑等聚 合起始劑在一般為70至100°C、以75至95°C為佳、以75 〇 至85°C更佳之下混合,再將所得混合物經由一般1至24 小時左右之攪拌而進行聚合反應之方法;將前述溶媒與單 體之一部分予以混合,並將所得混合物與聚合起始劑與殘 餘的單體在一般為70至100°C、以75至95°C為佳、以75 至85°C更佳之下混合,再將所得混合物經由一般1至24 小時左右之攪拌而進行聚合反應之方法。為了易於控制聚 合反應,亦可使用使聚合起始劑或殘餘的單體溶解於有機 溶媒而得的溶液。 聚合起始劑之使用量,相對於單體之總量100重量 15 321925 201041645 份’ 一般為0.01至5重量份,以2至3重量份為佳。 聚合起始劑可列舉如:2, 2,-偶氮二異丁腈、2 2, 一偶 甲基丁腈)、“,—偶氣(環己境小甲腈):2,2,_ 虱一(2,4-一甲基戊腈)、2,2’-偶氮二(24_二曱某_4_ ::基戊腈)、二甲基-2,2,_偶氣二(2〜甲基丙酸醋)、〔2’_ — 甲基丙腈)等偶氮化合物;過氧化月桂酿、氫 Ο „弟三丁基、過氧化苯曱醯、過氧化苯甲酸第三丁酯、 氫過氧化異丙苯、過氧化二礙酸二異^旨、過氧化二碳酸 二丙醋、過氧化新癸酸第三丁醋、過氧化特戊酸第三丁醋、 ?(3,5’5-三曱基己醯)過氧化物等有機過氧化物;以及過 硫酸钟、過硫酸銨、過氧化氫等無機過氧化物。將聚合起 始劑與還原劑併用之氧化還原起始劑(redGx ^仏恤) 亦可作為聚合起始劑使用。 成刀(A)之丙;酸系樹脂的聚合物親水比率為9至 12以9. 1至π為佳,以9丨至1〇更佳。含有聚合物親 〇 水比率在上述範圍内之丙烯酸系樹脂的本發明之水性乳 齊J例如經由在90 C至120左右乾燥,即可賦予對丙嫦等 基材的接著性優異之硬化物。更且,乾燥溫度即使為仍至 9〇t左右的低溫,亦可賦予對丙烯等基材的接著性優異之 硬化物。 ^丙烯酸系樹脂之聚合物親水比率係衍生該丙烯酸系樹 脂之構造單元的單體之親水比率的重量平均值,單體之親 水比率係由下述式而算出。 單體之親水比率=2〇χ(單體之親水部分之式量)/(單體之分 321925 16 201041645 子量)) 單體之親水部分係指單體中之羧基(_C00H)、羥基 (-0H)、胺基(-)、磺酸基(-s〇3H)、羰氧基(-c〇2-)、二 烷胺基(-NR2)之氮原子(N)等極性部分。 羧基之式量為45. 02、羥基之式量為17. 〇2、胺基之式 量為16.02、磺酸基之式量為81.07、羰氧基之式量為 44.01、二院胺基之氮原子的式量為hoi。 例如:由於丙烯酸(分子量:72. 06)具有丨個羧基作為 親水部分’故丙稀酸之親水比率為12. 5。 丙烯酸之親水比率=20x45. 02/72. 06=12. 5 例如:琥珀酸2-甲基丙烯醯氧基乙酯(分子量:230. 21) 具有1個叛基與2個幾氧基作為親水部分,故琥珀酸2_甲 基丙烯醯氧基乙酯之親水比率為1丨.6。 琥珀酸2-甲基丙烯醯氧基乙酯之親水比率=2〇χ133. 〇4 /230.21=11.6 例如:由於甲基丙烯酸N,N_二甲胺基乙酯(分子量: 157· 21)具有1個羰氧基與丨個二烷胺基之氮原子作為親水 部分,故甲基丙烯酸N,N-二甲胺基乙酯之親水比率為7 4。 甲基丙烯酸N,N-二甲胺基乙酯之親水比率=20x58. 02/ 157. 21=7. 4 以相同做法,曱基丙烯酸曱酯之親水比率為8 8'曱 基丙烯酸月桂酯之親水比率為3.5、甲基丙烯酸十三酯之 親水比率為3. 3。 例如:藉由使丙烯酸24. 5重量份、琥珀酸2-曱基丙 321925 17 201041645 烯醯氧基乙酯22.5重量份、曱基丙烯酸N,N_二曱胺基乙 酯28. 0重量份、甲基丙烯酸曱酯15. 〇重量份、甲基丙烯 酸月桂酯3· 8重量份以及甲基_酸十三g| 6. 2重量份聚 合而得之丙烯酸系樹脂的聚合物親水比率為9.4〇。 丙烯酸系樹脂之聚合物親水比率= (12 5χ24. 5+11·6χ 22. 5 + 7. 4 χ 28. 0 + 8. 8 χ 15. 〇 + 3. 5 χ 3. 8 + 3. 3 χ 6. 2)/ 100=9. 40 經由將源自丙烯酸或琥Ϊ白 Ο 〇 一入U Τ丞㈧种職乳卷G酿寻 高親水比率之單體的構造單元之含量與源自低親水比率之 Τ體的構造單元之含量適當地調整,即可調製丙烯酸系樹 月曰之聚合物親水比率為9至12的丙婦酸系樹脂。 八本發明之水性乳劑中,係作為用以峨 刀政在成刀(C)之乳化劑而發揮功用。 發明==含有成分(Α),又以含有水為更佳。本 氨為佳。本發明之乳化她二^ 指相對Μ自至2Gi)m處之“肌中和度”存 ==含的具有陰離子性基之單二 之比例《)數’_中所含之鍵陽離子的莫耳數 其次,對成分(Β)進行說明。 成分(Β)係熱塑性聚合物,盆且 ^乙婦之構造單元的熱塑性聚合、物;含^列舉如^有源 早7L的熱雜聚合物 m丙烯之構造 有源自醋系蠟、棕櫚蠟、費托 321925 18 201041645 (Fischer-Tropsch)蠟、微晶蠟、石蠟以及該等之氧化物、 低分子量聚酿胺以及脂肪醯胺等醯胺化合物之構造單元的 熱塑性聚合物等。 熱塑性聚合物以含有源自乙烯及/或丙稀之構造單元 .的熱塑性聚合物為佳’含有源自乙烯及/或丙稀之構造單元 的熱塑性聚合物可列舉如:低密度聚乙稀等聚乙稀、聚乙 稀蠛、乙稀-乙酸乙_共聚物、乙婦一丙婦一乙酸乙稀醋共 〇聚物乙歸-丙稀酸共聚物、乙稀一丙稀一丙稀酸共聚物、乙 稀—丙稀酸醋共聚物、乙稀-丙婦-丙浠酸酯共聚物、乙稀一 丙烯酸共聚物、乙豨—丙稀一甲基丙稀酸共聚物、乙烤-甲基 _酸酯共聚物、乙烯_丙烯—甲基丙烯酸酯共聚物、聚丙 烯、乙稀—丙歸共聚物、乙稀-己稀共聚物、丙稀-己稀共聚 物、乙烯-丙稀-己烯共聚物、乙稀—丁烯共聚物、丙稀_丁 稀共聚物、乙稀-丙埽—丁稀共聚物以及該等之馬來酸野改 質物。 ) 八一中以含有源自乙婦及/或丙烯之構造單元與源自式 ⑴所示乙婦系化合物(以下簡稱為乙稀系化合物⑴)之構 造單元的共聚物(以下簡稱為聚合物(B-1))、以及藉由使α 义-不,和緩酸針與聚合物(β—υ接枝聚合而得之聚合物 (以下簡稱為聚合物(β_2乃為佳。 CH2=CH-R (!) (式中,R表示2級烧基、3級貌基或脂環式烴基) R表示之2級炫基係以碳原子數3至2〇之2級炫基為 佳,3級烧基係以碳原子數4至2〇之3級烧基為佳,脂環 321925 19 201041645 -式烴基係以3至16員環之鱗式烴基為佳。㈣式煙基可 列舉如:環炫基、環埽基以及環炔基,以環烧基為佳。 R係以3至1G㈣之碳原子數3至2{)之脂環式煙基 - 以及碳原子數4至20之3級烷基更佳。 乙烯系化合物可列舉如:3_甲基―卜丁烯、3_曱基一卜 戊烯、3-甲基-1-己烯、3-甲基-1-庚烯、3一曱基q —辛烯、 3, 4-二甲基-卜戊烯、3, 4-二甲基一卜己烯、3, 4_二甲基一卜 庚烯、3, 4一一曱基一辛烯、3, 5-二曱基-1-己烯、3, 5-二 甲基-1-庚烯、3, 5-二甲基-1 —辛稀、3, 6一二甲基y庚烯、 3, 6-二曱基-1-辛烯、3, 7-二甲基—1-辛烯、3, 4, 4—三曱基 _卜戊烯、3, 4, 4-三甲基-1-己烯、3, 4, 4_三甲基―卜庚烯、 3,4’4-三曱基-1-辛烯等R為2級烷基的乙烯系化合物 (I) ; 3, 3-二曱基-1 -丁烯、3, 3-二甲基-1-戊烯、3, 3-二甲 基-1-己烯、3, 3-二甲基-1-庚烯、3, 3-二甲基-1-辛烯、 3, 3, 4_三曱基-1 -戊烯、3, 3, 4-三甲基-1 —己烯、3, 3, 4-三 Ο 曱基庚烯、3, 3, 4一三甲基-1-辛烯等R為3級烷基的乙 烯系化合物(I); 乙烯基環丙烷、乙烯基環丁烷、乙烯基環戊烷、乙烯基環 己烷、乙烯基環庚烷、乙烯基環辛烷等r為環烷基的乙烯 系化合物(1);卜乙烯基金剛烷、5-乙烯基-2-降冰片烯以 及4-乙稀基-1-環己烯。 其中,較佳者為3-曱基-1-丁烯、3-曱基-1-戊烯、3-曱基-1-己烯、3, 4-二曱基-1-戊烯、3, 5—二曱基-卜己烯、 3’4’4-三甲基-1 —戊烯、3, 3_二曱基丁烯、3,3一二甲基 20 321925 201041645 -1-戊烯、3, 3, 4-三曱基-1_戊烯、乙烯基環戊烷、乙烯基 環己烧、乙烯基環庚烷、乙烯基環辛烷以及5_乙烯基一2__ 降冰片稀;更佳者為3-曱基-1-丁烯、3一曱基_1一戊烯、3, 4-二甲基-1-戊烯、3, 3-二甲基-1-丁烯、3, 3, 4-三曱基-1- 戊烯、乙烯基環己烷以及乙烯基降冰片烯;又以3, 3—二甲 基-1-丁烯以及乙烯基環己烷為特佳,更以乙烯基環己烷為 最佳。 〇 聚合物(B-1)中之源自乙烯系化合物(I)的構造單元之 含里,相對於構成聚合物(B-1)之全部構造單元1〇〇莫耳, 般為5至40莫耳,從使本發明之水性乳劑經乾燥而得之 硬化物的接著性之觀點而言 以10至30莫耳為佳,以10 至20莫耳更佳。 曰聚合物(B-1)中之源自乙稀系化合物⑴的構造單元之 含里’可經由將聚合物(B—1)進行1H-臓分析或I3c-NMR分 析而求得。Propanol, isopropanol, butanol, tert-butanol, pentanol, 3-mercaptobutanol, H-dimethylpropanol, 3-methyl-2-butanol, 2-ethylhexanol, hydrazine a linear, branched chain or cyclic aliphatic alcohol having 1 to 1 carbon atom such as an alcohol, a decyl alcohol or a cyclohexanol, which has a linear number of carbon atoms of 4 or a branched chain or Ring ^ aliphatic alcohol is preferred. < An aliphatic alcohol having a carbon atom group having a substituent which may have a substituent of from 1 to 1 321 321 925 9 201041645, and examples thereof include N,N-dimethylaminoethanol and N,N-diethylaminoethanol , N-methyl-N-ethylaminoethanol, N,N-dipropylaminoethanol, N-mercapto-N-propylaminoethanol, N-ethyl-N-propylaminoethanol, N, N-dimethyl Aminopropanol and N,N-•dimethylaminobutanol. An anthracene derived from an aliphatic alcohol having 1 to 10 carbon atoms having a substituent group and an α-unsaturated carboxylic acid; the point-unsaturated carboxylic acid ester may, for example, be cerium acrylate. Ν-diethylaminoethyl ester, hydrazine methacrylate, hydrazine-diethylaminoethyl acrylate, hydrazine acrylate, hydrazine-diguanidinoethyl ester, decyl propyl decanoate Ν, Ν-dimethyl hydrazine Ester, fluorenyl-fluorenyl-hydrazine-ethylaminoethyl acrylate and hydrazine-methyl-hydrazine-ethylaminoethyl methacrylate, and ν, Ν-dimethylaminoethyl methacrylate It is better. The acrylic resin of the component (Α) may have two or more structural units (a2). The content of the structural unit (al) in the acrylic resin of the component (A) is generally 20 to 99 moles, and 50 to 99 moles per mole of the structural unit 1 constituting the acrylic resin. It is better. The content of the structural unit (& 2) in the acrylic resin of the component (A) is generally 1 to 80 m, and 1 to 50 m with respect to the entire structural unit constituting the acrylic resin. The ear is better. The acrylic resin of the component (A) may contain two or more kinds of propionic acid resins. The acrylic resin of the component (Α) may have other structural units in addition to the structural unit (al) and the structural unit (a2). Other structural units include, for example, a source free carbon atom 丨 to 2 〇 10 321 925 201041645 an aliphatic alcohol and an α I unsaturated (d) derived α ester structural unit (hereinafter referred to as 楢, unsaturated carboxy 醆 1 Manxin Bu 昨 昨 (10)), the source of free carbon atoms 0 eve of the Japanese aliphatic alcohol and α,/5-unsaturated _ derived stone-unsaturated carboxylic acid ester structure, rK9,, r η 1 ^早兀 (hereinafter referred to as tectonic unit: 2)): The source free has the number of carbon atoms in the (four) group. And H-unsaturated "_ raw aj_ unsaturated unit (hereinafter referred to as structural unit (10)), and source free poly St Ο ❹ unsaturated (four) derived ", ^ unsaturated (four) (four) structural unit (hereinafter referred to as structural unit) (b4)) The H-unsaturated (four) derived from the above other structural units may be the same as those described above, and preferably the propionic acid or methyl procyanoic acid. The structure of the k-unit 70 (10) α, point _ The saturated acid vinegar is derived from an aliphatic alcohol having 1 to 20 carbon atoms and an α, 10,000-unsaturated carboxylic acid. The aliphatic alcohol having 1 to 20 carbon atoms may, for example, be methanol, ethanol or propanol. Isopropanol, butanol, tert-butanol, pentanol, 3-methylbutanol, 2,2-dimethylpropanol, 3-methyl-2-butanol, 2-ethylhexanol, hydrazine a linear, branched chain or cyclic fat having 1 to 20 carbon atoms such as an alcohol, a sterol, a dodecanol, a tridecyl alcohol, a hexadecanol, an octadecyl alcohol or a cyclohexanol. Alcohols. Alpha, stone-unsaturated carboxylic acid esters derived from an aliphatic alcohol having a stone inverse number of 1 to 20 and α, unsaturated citric acid may, for example, be methyl acrylate, ethyl acrylate or propylene. Propyl ester, butyl acrylate, amyl acrylate, 3-methylbutyl acrylate, 2,2-dimethylpropyl acrylate, 3-methyl-2-butanyl acrylate, 2-ethylhexyl acrylate, acrylic acid Oxime ester, decyl acrylate, dodecyl acrylate, tridecyl acrylate, hexadecyl acrylate, acrylic acid 18 321925 11 201041645 , ester, cyclohexyl acrylate, methyl methacrylate, ethyl methacrylate Propyl methacrylate, butyl methacrylate, amyl methacrylate, 2-methyl-2-butyl methacrylate, 2-ethylhexyl methacrylate, τ-based • Acetate vinegar, methyl Acrylate acrylate, decyl acrylate decanoic acid, methyl acrylate tridecyl vinegar, hexadecyl methacrylate, methacrylic acid octadecyl acrylate and cyclohexyl acrylate. The acrylic resin of component (A) may contain Two or more structural units (M). ^ The α,/5-unsaturated carboxylic acid ester of the derived structural unit (b2) is composed of a polyhydric aliphatic alcohol having 1 to 10 carbon atoms and α,/3 -unsaturated Derived by an acid, the polyhydric alcohol having 1 to 10 carbon atoms may, for example, be hydroxymethanol , hydroxyethanol, hydroxypropanol, hydroxybutanol, hydroxypentanol and hydroxyhexanol. Derived from a polyhydric aliphatic alcohol having 1 to 10 carbon atoms and an α,/3-unsaturated carboxylic acid: 10,000- Examples of the unsaturated carboxylic acid ester include hydroxy acrylate, acrylic acid, propyl benzoic acid, acrylic acid, butyl hydroxy valerate, hydroxy hydroxy acrylate. Ester, hydroxydecyl methacrylate, hydroxyethyl methacrylate, propyl methacrylate, hydroxybutyl methacrylate, hydroxy amyl methacrylate and hydroxyhexyl methacrylate. The acrylic resin may contain two or more structural units (10). The structural unit (b3) is derived from an aliphatic alcohol having a carboxylic acid group of 1 to 10 and an α,/5-unsaturated acid. α,/5 - unsaturated tartrate. The "carboxylic acid group" herein means an organic group having a carboxyl group (-COOH), and examples thereof include a carboxymethyl group, a 1,2-dicarboxyethyl group, a 2-carboxyphenyl group, and a 2,3-two 12 321925 201041645, carboxyphenyl. The number of carbon atoms with this decanoic acid group! The α,β-unsaturated carboxylic acid ester derived from the aliphatic alcohol to 10 and the /5-unsaturated carboxylic acid may, for example, be a succinic acid 2-propenyloxy ethoxy group, (4) 2 _(tetra) fluorenyloxy B. From the purpose, the station acid • 2_methyl propyl oxy-S, and 2-methyl propyl oxy-acetate. The acrylic resin of the component (A) may contain two or more kinds of structural units (10).构造 The structural unit (b4) is derived from a free polyalkylene glycol and a (2,/5-unsaturated carboxylic acid ester derived from a cold-unsaturated carboxylic acid. The polyglycol diol is a polyethylene glycol or a polypropylene glycol. , polyethylene glycol polypropylene glycol, polyethylene glycol polytetramethylene glycol, • methoxy polyethylene glycol, etc., through an oxygen atom, bonding 1 to 50 alkyl groups having 1 to 4 carbon atoms The polyalkylene glycol and the hydroxyl group at the terminal of the polyalkylene glycol can be protected by an alkyl group having 1 to 2 carbon atoms, an acryloyl group, a methacrylic group, or the like. Y5_α derived from unsaturated carboxylic acid, not “unsaturated” and carboxylic acid esters, for example, polypropylene glycol acrylate, polyethylene glycol acrylate, polyethylene glycol polypropylene glycol ester, polyacrylic acid polyethyl acrylate Glycol polytetramethylene glycol ester, decyl acrylate polyethylene glycol ester, polypropylene glycol methacrylate, polyethylene glycol methacrylate, methacrylic acid polyethylene glycol polypropanol S 曰, single Mercaptoacrylic acid polyethylene glycol polytetramethylene glycol vinegar and methoxy polyethylene glycol methacrylate. The acrylic resin of the component (Α) It is preferable to have a structural unit (bl) or a structural unit (b3), and it is preferable to contain a structural unit (bl) and a structural unit (b3). 321925 13 201041645 When the acrylic resin of the component (A) contains a structural unit (bl When the content of the structural unit (bl) is generally 5 to 95 moles, preferably 10 to 80 moles, relative to the entire structural unit 100 constituting the acrylic resin. The acrylic of the component (A). The content of the structural unit (b2) in the resin is generally 0 to 50 m, relative to the entire structural unit constituting the acrylic resin, preferably 0 to 30 m, and 0 to 1 mol. The content of the structural unit (b3) is generally 0. 1 with respect to the total structural unit 100 constituting the acrylic resin, the content of the structural unit (b3). To 80 mol, preferably 5 to 40 mol. The content of the structural unit (b4) in the acrylic resin of the component (A) is generally 0 with respect to the entire structural unit 100 constituting the acrylic resin. Up to 50 m, preferably 0 to 30 m, and 0 to 1 In the acrylic resin of the component (A), the content of the structural unit having an anionic group such as the structural unit (al) or the structural unit (b3), the cured product obtained from the aqueous emulsion of the present invention, and the polypropylene From the viewpoint of the structure, it is preferably 45 to 85 mol, more preferably 50 to 80 mol, based on the entire structural unit 100 constituting the acrylic resin. The acrylic resin as the component (A), With respect to all of the structural units 100 constituting the acrylic resin, a structural unit (al) containing 5 to 80 moles, a structural unit (a2) of 1 to 50 moles, and 10 to 80 moles of 14 321925 201041645 The structural unit (bl) and the structural unit (b3) of 5 to 30 moles and the structural units (al), (a2), (bl), and (b3) are preferably 100-mole acrylic resin. The acrylic resin of the component (A) may contain a structural unit derived from ethylene, a structural unit derived from propylene, a structural unit derived from a linear olefin having 4 or more carbon atoms described below, and derived from the following formula ( The structural unit of the vinyl compound shown in I), the structure derived from the following addition polymerizable monomer, and the like, but the content is such that it is nondestructive and the adhesion of the cured product obtained from the aqueous emulsion of the present invention. The amount of the structural unit may be about 5 m or less with respect to all the structural units constituting the acrylic resin, and the structural unit derived from the monomer which can be added and polymerized is preferably 1 mol or less. . The acrylic resin of the component (Α) can be produced by subjecting a monomer derived from each structural unit to addition polymerization. For example, a solvent such as an alcohol solvent such as isopropyl alcohol or water may be mixed with a monomer, and the polymerization initiator such as the obtained mixture and a radical initiator may be usually 70 to 100 ° C and 75 to 95 °. a method in which C is preferably mixed at a temperature of 75 Torr to 85 ° C, and the resulting mixture is subjected to polymerization by stirring for about 1 to 24 hours; the solvent and a part of the monomer are mixed, and the obtained The mixture is mixed with the residual monomer and the residual monomer at 70 to 100 ° C, preferably 75 to 95 ° C, more preferably 75 to 85 ° C, and the resulting mixture is passed through generally 1 to 24 hours. A method of carrying out a polymerization reaction by stirring left and right. In order to easily control the polymerization reaction, a solution obtained by dissolving a polymerization initiator or a residual monomer in an organic solvent may also be used. The amount of the polymerization initiator to be used is 100 parts by weight relative to the total amount of the monomers. 15 321925 201041645 parts ' is generally 0.01 to 5 parts by weight, preferably 2 to 3 parts by weight. The polymerization initiator may, for example, be: 2, 2,-azobisisobutyronitrile, 2 2 , methacrylonitrile, ", - (a cyclohexane): 2, 2, _虱 one (2,4-monomethylvaleronitrile), 2,2'-azobis(24_diindole_4_:::), dimethyl-2,2, _diox Azo compounds such as 2~methylpropionic acid vinegar, [2'_-methylpropionitrile); peroxidized laurel, hydroquinone, benzotriphenyl, benzoyl peroxide, benzoic acid benzoic acid Ester, cumene hydroperoxide, peroxidic acid disulfide, dipropylene glycol peroxydicarbonate, tributyl vinegar peroxy neodecanoic acid, third vinegar peroxypivalate, ?(3 , 5'5-trimethyl hexanyl) an organic peroxide such as a peroxide; and an inorganic peroxide such as a persulfate clock, ammonium persulfate or hydrogen peroxide. A redox initiator (redGx^仏) which is used together with a polymerization initiator and a reducing agent can also be used as a polymerization initiator. The acrylic resin has a hydrophilic ratio of from 9 to 12, preferably from 9.1 to π, more preferably from 9 Å to 1 Torr. The aqueous emulsion J of the present invention containing the acrylic resin having a polymer affinity in the above-mentioned range is, for example, dried at a temperature of from about 90 C to about 120, thereby imparting a cured product excellent in adhesion to a substrate such as propylene. Further, even if the drying temperature is at a low temperature of about 9 Torr, it is possible to impart a cured product excellent in adhesion to a substrate such as propylene. The polymer hydrophilic ratio of the acrylic resin is the weight average of the hydrophilic ratio of the monomer derived from the structural unit of the acrylic resin, and the hydrophilic ratio of the monomer is calculated by the following formula. The hydrophilic ratio of the monomer = 2 〇χ (the amount of the hydrophilic portion of the monomer) / (the monomer is divided into 321925 16 201041645 sub-quantity)) The hydrophilic portion of the monomer refers to the carboxyl group (_C00H), hydroxyl group in the monomer ( -0H), a polar moiety such as an amine group (-), a sulfonic acid group (-s〇3H), a carbonyloxy group (-c〇2-), or a nitrogen atom (N) of a dialkylamino group (-NR2). The amount of the carboxyl group is 45. 02, and the amount of the hydroxyl group is 17. 〇2, the formula of the amine group is 16.02, the formula of the sulfonic acid group is 81.07, the formula of the carbonyloxy group is 44.01, and the amine of the second compound is The formula of the nitrogen atom is hoi. 5。 The hydrophilic ratio of the acrylic acid is 12. 5, because the acrylic acid (molecular weight: 72. 06) has a carboxyl group as a hydrophilic part. Hydrophilic ratio of acrylic acid = 20x45. 02/72. 06=12. 5 For example: 2-methylpropenyloxyethyl succinate (molecular weight: 230.21) with 1 thiol and 2 methoxy groups as hydrophilic In part, the hydrophilic ratio of 2-methacryloxyethyl succinate is 1丨.6. Hydrophilic ratio of 2-methylpropenyloxyethyl succinate = 2〇χ133. 〇4 /230.21=11.6 For example: due to N,N-dimethylaminoethyl methacrylate (molecular weight: 157·21) The nitrogen atom of one carbonyloxy group and the dialkylamine group is a hydrophilic portion, so the hydrophilic ratio of N,N-dimethylaminoethyl methacrylate is 7 4 . The hydrophilic ratio of N,N-dimethylaminoethyl methacrylate = 20x58. 02/ 157. 21=7. 4 In the same way, the hydrophilic ratio of decyl methacrylate is 8 8 'decyl methacrylate 5。 The hydrophilic ratio was 3.5, the hydrophilic ratio of tridecyl methacrylate was 3.3. 0重量份。 By way of example, by weight of 24. 5 parts by weight of acrylic acid 2-mercaptopropyl 321925 17 201041645 olefinic ethyl oxyethyl 22.5 parts by weight, N,N-diguanidinoethyl methacrylate 20.8 parts by weight Ethyl methacrylate 15. 〇 by weight, 3.8 parts by weight of lauryl methacrylate and 13 g of methyl-acid; 6.2 parts by weight of the polymer obtained by polymerization of the acrylic resin has a hydrophilic ratio of 9.4. Hey. The hydrophilic ratio of the polymer of the acrylic resin = (12 5χ24. 5+11·6χ 22. 5 + 7. 4 χ 28. 0 + 8. 8 χ 15. 〇+ 3. 5 χ 3. 8 + 3. 3 χ 6. 2) / 100=9. 40 The content of the structural unit derived from the monomer of the high hydrophilic ratio derived from the acrylic acid or the amber sputum into the U Τ丞 (eight) seed milk roll G and the low hydrophilicity The content of the structural unit of the carcass of the ratio is appropriately adjusted, and the acrylic acid-based resin having a hydrophilic ratio of the polymer of the acrylic tree of 9 to 12 can be prepared. In the aqueous emulsion of the invention, it is used as an emulsifier for the knife (C). Invention == Contains ingredients (Α), and it is more preferable to contain water. This ammonia is preferred. The emulsification of the present invention refers to the "muscle neutralization degree" of the relative enthalpy to 2Gi)m == the ratio of the single cation having the anionic group contained in the number of the "2" The number of ears is second, and the component (Β) is explained. The composition (Β) is a thermoplastic polymer, a thermoplastic polymer of a potted structural unit, and a thermal hybrid polymer, such as an active 7L, which is derived from vinegar wax and palm wax. , Fischer-Tropsch 321925 18 201041645 (Fischer-Tropsch) waxes, microcrystalline waxes, paraffin waxes, and thermoplastic polymers of structural units such as oxides, low molecular weight polyamines, and fatty guanamines. The thermoplastic polymer is preferably a thermoplastic polymer containing a structural unit derived from ethylene and/or propylene. The thermoplastic polymer containing structural units derived from ethylene and/or propylene may be, for example, low-density polyethylene. Polyethylene, polyethylene, bismuth-acetic acid, ethylene-copolymer, ethoxylate, ethyl acetate, acetic acid, ethylene glycol, eupolymer, ethylene-acrylic acid copolymer, ethylene-propylene-acrylic acid Copolymer, ethylene-acrylic acid vinegar copolymer, ethylene-propylene-acrylic acid ester copolymer, ethylene-acrylic acid copolymer, ethyl acetonitrile-acrylic acid copolymer, baking Methyl-ester copolymer, ethylene-propylene-methacrylate copolymer, polypropylene, ethylene-propylene copolymer, ethylene-hexadiene copolymer, propylene-hexane copolymer, ethylene-propylene a hexene copolymer, an ethylene-butene copolymer, a propylene-butylene copolymer, an ethylene-propylene-butadiene copolymer, and the maleic acid wild modification. a copolymer containing a structural unit derived from a woman and/or propylene and a structural unit derived from a compound of the formula (1) (hereinafter referred to as an ethylenic compound (1)) (hereinafter referred to as a polymer) (B-1)), and a polymer obtained by graft-polymerizing α-n- and a slow-acid needle with a polymer (β-υ) (hereinafter referred to as a polymer (β_2 is preferably. CH2=CH- R (!) (wherein, R represents a 2-stage alkyl group, a 3-stage appearance group or an alicyclic hydrocarbon group). R represents a second-order leuco group which is preferably a choline group having a carbon number of 3 to 2 Å, 3 The calcining base is preferably a 3-stage alkyl group having 4 to 2 carbon atoms, and the alicyclic ring 321925 19 201041645 is preferably a 3- to 16-membered ring-shaped hydrocarbon group. The (iv) type of smog group can be exemplified by: a cyclononyl group, a cyclodecyl group, and a cycloalkynyl group, preferably a cycloalkyl group. R is an alicyclic group of 3 to 2 G (3) having 3 to 2 carbon atoms, and a carbon number of 4 to 20 The alkyl group is more preferable. Examples of the vinyl compound include 3-methyl-butene, 3-mercapto-p-pentene, 3-methyl-1-hexene, and 3-methyl-1-heptene. , 3-indolyl q-octene, 3,4-dimethyl-p-pentene, 3, 4-di Methyl-p-hexene, 3,4-dimethyl-p-heptene, 3,4-monodecyl-octene, 3,5-dimercapto-1-hexene, 3,5-dimethyl 1-heptene, 3,5-dimethyl-1 -octyl, 3,6-dimethyl yheptene, 3,6-dimercapto-1-octene, 3,7-dimethyl 1-octene, 3, 4, 4-trimethyl-p-pentene, 3, 4, 4-trimethyl-1-hexene, 3, 4, 4-trimethyl-p-heptene, 3 a vinyl compound (I) wherein R is a 2nd alkyl group such as 4'4-trimercapto-1-octene; 3,3-dimercapto-1 -butene, 3,3-dimethyl-1 -pentene, 3,3-dimethyl-1-hexene, 3,3-dimethyl-1-heptene, 3,3-dimethyl-1-octene, 3, 3, 4_three Mercapto-1 -pentene, 3,3,4-trimethyl-1-hexene, 3,3,4-trimethylsulfonylheptene, 3,3,4-trimethyl-1-octene A vinyl compound (I) wherein R is a tertiary alkyl group; vinylcyclopropane, vinylcyclobutane, vinylcyclopentane, vinylcyclohexane, vinylcycloheptane, vinylcyclooctane, etc. The vinyl compound (1) wherein r is a cycloalkyl group; vinyl adamantane, 5-vinyl-2-norbornene, and 4-ethylene-1-cyclohexene. Among them, preferred is 3- Mercapto-1-butene, 3-mercapto-1-pentene, 3-mercapto-1-hexene, 3,4-dimercapto-1-pentene, 3,5-dimercapto-p-hexene, 3'4'4 -trimethyl-1 -pentene, 3,3-didecylbutene, 3,3-dimethylene 20 321925 201041645-1-pentene, 3,3,4-tridecyl-1-pentene , vinyl cyclopentane, vinyl cyclohexane, vinyl cycloheptane, vinyl cyclooctane and 5-vinyl-2__ norbornazole; more preferably 3-mercapto-1-butene, 3 Monomethyl-1-pentene, 3,4-dimethyl-1-pentene, 3,3-dimethyl-1-butene, 3,3,4-tridecyl-1-pentene, Vinylcyclohexane and vinyl norbornene; particularly preferred are 3,3-dimethyl-1-butene and vinylcyclohexane, and more preferably vinylcyclohexane. The content of the structural unit derived from the vinyl compound (I) in the ruthenium polymer (B-1) is generally 5 to 40 with respect to all the structural units constituting the polymer (B-1). Mohr is preferably from 10 to 30 mols, more preferably from 10 to 20 mols, from the viewpoint of the adhesion of the cured product obtained by drying the aqueous emulsion of the present invention. The inner portion of the structural unit derived from the ethylenic compound (1) in the ruthenium polymer (B-1) can be determined by subjecting the polymer (B-1) to 1H-臓 analysis or I3c-NMR analysis.
烯、1-十五烯、1 烯以及1-二十# 1-辛烯為佳。Alkene, 1-pentadecene, 1-ene and 1-tap #1-octene are preferred.
20之 321925 21 201041645 :物(B?)之全部構造單元100莫耳’ -般為95至60莫 斗至70莫耳%為佳,以9〇至8〇莫耳更佳。、 單元聚σ 可另具有源自可加絲合之單體的構造 可加成聚合之單體係乙稀、丙烯、碳原子數4至2〇之 大α烯蛵以及乙烯系化合物(丨)以外之單體,並 與^烯、丙歸、碳原子數4至20之直鏈狀^稀煙二及乙20 321925 21 201041645: All construction units of the object (B?) 100 Mohrs - generally 95 to 60 Moto to 70 Molar% is better, 9 to 8 Mo is better. The unit poly σ may additionally have a structure derived from a monomer which can be added to the addition polymerization, a single system of ethylene, propylene, a large alpha olefin having 4 to 2 carbon atoms, and a vinyl compound (丨). a monomer other than a olefin, a propylene, a linear one with a carbon number of 4 to 20, and a second
炸乐化σ物⑴加絲合之單體’而該單體之碳原子數 為3至20左右。 _可加成聚合之單體的具體例可列舉如:環#烴、式⑴) 所不之烯烴、一烯化合物、鹵化乙烯、脂肪族羧酸乙烯酯、 :烯醚化合物、氰基乙烯系化合物、上述不飽和羧 酸、上述α,石-不飽和羧酸g|以及後述之&万一不飽和羧The stagnation product (1) is added to the monomer of the merging, and the monomer has a carbon number of about 3 to 20. Specific examples of the monomer capable of addition polymerization include, for example, a ring # hydrocarbon, a compound of the formula (1), an olefin compound, a halogenated ethylene, an aliphatic carboxylic acid vinyl ester, an alkylene compound, and a cyanoethylene system. a compound, the above unsaturated carboxylic acid, the above α, a stone-unsaturated carboxylic acid g|, and a &
(II) (式中’ R,以及R"各自獨立,表示碳原子數J至18之直 鏈狀、分枝狀或環狀之烷基或鹵原子)。 環烯烴可列舉如:環丁稀、環輯、環⑽、環辛婦、 3-甲基環戊稀、4-甲基環戊烯、3_甲基環己稀、2_降冰片 烯、5-曱基-2-降冰片稀、5_乙基_2_降冰片晞、5_丁基_2_ 降冰片烯、5-苯基-2-降冰片稀、5_苯f基_2_降冰片婦、 2-四環十二烯、2-三環癸歸、2_三環十—烯、2_五環十五 321925 22 201041645(II) (wherein R and R" each independently represent a linear, branched or cyclic alkyl group or a halogen atom having a carbon number of J to 18). Examples of the cycloolefins include cyclobutene, ring, ring (10), cyclosin, 3-methylcyclopentene, 4-methylcyclopentene, 3-methylcyclohexene, 2-norbornene, 5-mercapto-2-norborner, 5_ethyl_2_norbornene, 5_butyl_2_norbornene, 5-phenyl-2-norborn, 5_benzenef-based_2 _Ice film woman, 2-tetracyclododecene, 2-tricyclic quinone, 2_tricyclotetraene, 2_five ring fifteen 321925 22 201041645
烯、2-五環十六烯、甲I 产+一,法,7甲基I—四環十二烯、8-乙基-2-四 衣稀乙酿基'2、降冰片烯、5-乙醯氧基—2·降冰片 烯、5-甲氧幾基-2-降冰κ秘c c m , c匕 降冰片烯、5-乙氧羰基-2-降冰片烯、 5-甲基-5-甲氧羰基-2-降# κ ”m〜 片~、5-氰基-2_降冰片烯、8- &、 ^ 碲8—甲基-8-甲氧羰基-2-四環十二 烯以及8-氰基-2-四環十-、膝甘 〜略〜, 歸。其中’以環戍烤、環己烯、 壤辛稀、2_降冰㈣、5~甲基I降冰片晞、卜苯基—2—降 Ο ❹ 冰片烯、2-四環十二烯、2一二j罗八Λ ^ —%癸烯、2-三環十一烯、2_ 五環十五埽、2-五料六烯、5乂醯基_2—降冰料、5_ 乙醒乳基-2-降冰片稀、5_甲氧縣_2_降冰片烯、5_甲基 -5-曱氧絲-2-降冰片稀以及5_氰基_2_降冰片稀為佳, 以2-降冰片烯以及2_四環十二烯為更佳。 式(II)所示之烯烴可列舉如:異丁烯、2_甲基_丨一丁 烯、2-甲基+戊烯、2_甲基+己烯、"基+庚土稀、2_ 甲基-1-辛浠、2’3-二甲基+ 丁烯、2, 3一二甲基卜戊烯、 2, 3-二甲基-1-己烯、2, 3一二甲基+庚烯、2, 3—二甲基+ 辛稀、2’4-二甲基戊烯、2,4,4_三甲基_卜戊烯以及偏 軋乙烯(vinylene chloride),其中以異丁烯、2,3一二甲基 -卜丁烯以及2, 4, 4-三甲基-1-戊烯為佳。 土 二烯化合物可列舉如:1,3-丁二烯、;I,4_戊二烯、丨5_ 己二烯、1,6-庚二烯、l,7-辛二烯、1,5_環辛二烯、2 5_ 降冰片二烯、二環戊二稀、5_乙縣I降冰片烯、5缔丙 基-2-降冰片烯、4-乙烯基-1-環己烯以及5_亞乙美_2_降 冰片烯,其中以U—戊二烯、-己二烯、2,5_降;片二 321925 23 201041645 ^烯、一%戊二稀、5-乙烯基-2、降冰片烯、4_乙烯基4一環 己晞以及5-亞乙基-2-降冰片埽更佳。 脂肪族賴乙㈣刊舉如Λ酸乙烯自旨、丙酸乙烯 酉旨以及丁酸乙稀醋;乙稀St化合物可列舉如:甲基乙稀醚、 乙基⑽_及了基乙_° _化乙烯可列舉如:氣乙婦; 氰基乙烯系化合物可列舉如:丙烯腈以及曱基丙烯腈。 聚合物CB-υ中之源自可加成聚合的單體之構造單元 〇之含篁,如為無損及本發明之水性乳劑經乾燥而得之硬化 物的接著性之量即可’相對於構成聚合物之全部構造 單元100莫耳,以5莫耳以下為佳,α i莫耳以下更佳。 • 聚合物(B—1)係例如可將含有具備茚基陰離子骨架或 經交聯之環戊二烯陰離子骨架之基的過渡金屬化合物作為 觸媒,經由使所對應之單體進行聚合而製造。其中亦以曰 本特開2003-82028號公報、日本特開2〇〇3_16〇621號公報 以及日本特開2000-128932號公報之方法為適宜。 ◎纟聚合物(B—1)之製造中,依所使用之觸媒種類及聚合 條件’除了聚合物之外’有時會生成乙稀之均聚物、 之均聚物及/或乙烯基環己烧之均聚物。在此情況下, 由使用索式萃取器(Soxhlet extractor)等而進行溶媒 的萃取,即可容易地取出聚合物(B-1)。使用甲苯作為溶媒 時’可去除作為不溶成分之乙烯基環己烷的均聚物。使用 氯仿作為溶媒時,可去除作為不溶成分之乙稀之均聚物、 丙歸之均聚物等烯煙的均聚物。聚合物(B-1)可作為該等溶 媒之可洛成分而分離。在其用途上如無問題,亦可使用含 24 321925 201041645 有如上述之副產物的聚合物(Β-l)。 聚合物(B-1)之分子量分佈(Mw/Mn=[重量平均分子量] /[數目平均分子量])一般為1. 5至10. 〇左右,從本發明之 水性乳劑經乾燥而得之硬化物的機械性強度以及透明性之 觀點而言’以1. 5至7. 0左右為佳,以1. 5至5. 0左右更 佳。 聚合物(Β-l)之重量平均分子量(Mw)—般為5, 000至 ^ I 000, 000左右,從本發明之水性乳劑經乾燥而得之硬化 物的機械性強度以及聚合物(B_i)之流動性的觀點而言,以 10, 000至500, 〇〇〇左右為佳,以15, 000至400, 000左右 . 更佳。 聚合物(Β-l)之分子量分佈可依凝膠滲透層析法(GPC) 而求得。 聚合物(Β-l)之極限黏度[η ]—般為0· 25至l〇dl/g左 右’從本發明之水性乳劑經乾燥而得之硬化物的機械性強 〇 度之觀點而言’以0.3至3dl/g左右為佳。 依據JIS K 7210之基準,使用熔融指數測定儀(melt indexer)(L217-E14011 ; techno7 公司製造),在 19(TC、 2. 16kgf之條件下測定之聚合物(B-i)的熔融流動速率(肝尺) 之值,一般為130至300g/l〇分鐘,從本發明之水性乳劑 中之聚合物(Β-l)的分散性之觀點而言,以⑽至__ 分鐘左右為佳。 聚合物(B-2)係指使《,沒〜不飽和羧酸酐與聚合物 (Β -1)接枝聚合而得之聚合物。 321925 25 201041645 、 α , /3 -不飽和羧酸酐之接枝聚合量,相對於聚合物 (Β-2)100重量份,一般為0. 01至20重量份左右,以0. 05 至10重量份左右為佳,以0. 1至5重量份左右更佳。 - 含有α,/3-不飽和羧酸酐之接枝聚合量為0. 01重量 份以上的聚合物(Β-2)之本發明的水性乳劑,由於該接著性 有提高之傾向而佳。含有α,卢-不飽和羧酸酐之接枝聚合 量為20重量%以下的聚合物(B-2)之本發明的水性乳劑,由 於該熱安定性有提高之傾向而佳。 ν/ α,冷-不飽和羧酸酐可咧舉如:馬來酸酐、衣康酸酐、 檸康酸酐等碳原子數4至20之α, /3-不飽和羧酸酐,以馬 來酸酐為佳。亦可將2種以上之α , /5 -不飽和羧酸酐組合 使用。 聚合物(Β-2)係可依例如下述方法等而製造:在使聚合 物(Β-1)熔融而得之熔融聚合物(Β-1)中,添加α,不飽 和羧酸酐並使其接枝聚合的方法;或是在甲苯、二曱笨等 q 溶媒中溶解聚合物(B-1),在所得的溶液中添加α ,泠-不飽 和羧酸酐並使其接枝聚合的方法等。 接枝聚合一般是在自由基起始劑的存在下進行。 如自由基起始劑之使用量少時,則α , β -不飽和羧酸 酐之接枝聚合量變少,本發明之水性乳劑經乾燥而得之硬 化物有難以提高接著性之傾向,並且,使用量多時,聚合 物(Β-2)中所含之未反應之自由基起始劑的量有增多之傾 向,因此,相對於聚合物(Β-1) 100重量份,一般為0.01 至10重量份,以0. 01至1重量份為佳。 26 321925 201041645 自由基起始劑-般可使时機過 在使用t解溫度為50°c以上之有機過氧化物時,Μ-不 針之接枝聚合量有提高之傾向,在使用分解溫度 二妒Τ下之有機過氧化物時,接枝聚合中之聚合物(Β-1) 二之傾向。經分解而產生自由基後,以具有從 ’ 口 中拔取質子之機能的有機過氧化物為佳。Alkene, 2-pentacyclohexadecene, methyl I production + one, method, 7 methyl I-tetracyclododecene, 8-ethyl-2-tetrazene distillate '2, norbornene, 5 -Ethyloxy-2,norbornene,5-methoxybenzyl-2-norborn κ secret ccm, c匕norbornene, 5-ethoxycarbonyl-2-norbornene, 5-methyl- 5-methoxycarbonyl-2-lower# κ ”m~ piece~,5-cyano-2_norbornene, 8-&, 碲8-methyl-8-methoxycarbonyl-2-tetracyclic Decadiene and 8-cyano-2-tetracyclo---, knee-gum ~ slightly ~, return. Among them, 'ring ring roast, cyclohexene, soil diarrhea, 2_ ice (four), 5 ~ methyl I Norborn 晞, phenyl phenyl-2, Ο Ο ❹ borneene, 2-tetracyclododecene, 2 1-2 j Rosin Λ ^ — decene, 2-tricycloundecene, 2 _ five ring埽, 2-pentahexaene, 5 fluorenyl _2—icing material, 5_ ke ke ke ke -2- borneol thin, 5 methoxy county _2 _ norbornene, 5-methyl-5 - Oxyfluoride-2-norbornium and 5-cyano-2_norborn are preferred, 2-norbornene and 2-tetracyclododecene are preferred. The olefin represented by formula (II) For example, isobutylene, 2-methyl-nonylbutene, 2-methyl+pentene, 2-methyl+hexene Alkene, "base + heptareth, 2_methyl-1-octyl, 2'3-dimethyl+butene, 2,3-dimethylpentene, 2,3-dimethyl-1 -hexene, 2,3-dimethylene + heptene, 2,3-dimethyl + octyl, 2'4-dimethylpentene, 2,4,4-trimethyl-p-pentene and Nickelene chloride, wherein isobutylene, 2,3-dimethyl-butene and 2,4,4-trimethyl-1-pentene are preferred. The earthy diene compound can be exemplified as: , 3-butadiene, I, 4-pentadiene, 丨5_ hexadiene, 1,6-heptadiene, 1,7-octadiene, 1,5-cyclooctadiene, 2 5_ Borneadiene, dicyclopentadiene, 5_Bxian I norbornene, 5 propyl-2-norbornene, 4-vinyl-1-cyclohexene, and 5_Asian Borneene, in which U-pentadiene, -hexadiene, 2,5_ drop; sheet II 321925 23 201041645 ^ene, mono-pentylene, 5-vinyl-2, norbornene, 4_ethylene The base 4-cyclohexanium and 5-ethylidene-2-norbornate are more preferred. The aliphatic Lai B (4) is published, such as ethylene citrate, vinyl propionate, and ethyl butyrate; For example, methyl ether ether Ethyl (10) _ and ethane _ ° _ ethylene can be exemplified by: gas acetylene; cyano vinyl compounds can be exemplified by: acrylonitrile and mercapto acrylonitrile. The polymer CB-υ derived from the addition The enthalpy of the structural unit of the polymerized monomer, such as the amount of adhesion of the cured product obtained by drying the aqueous emulsion of the present invention, can be 'relatively relative to the total structural unit 100 constituting the polymer, 5 moles are better, and alpha i moles are better. • The polymer (B-1) can be produced, for example, by using a transition metal compound having a sulfhydryl anion skeleton or a crosslinked cyclopentadienyl anion skeleton as a catalyst, by polymerizing the corresponding monomer. . The method of the Japanese Patent Publication No. 2003-82028, the Japanese Patent Application Laid-Open No. Hei. No. Hei. ◎In the manufacture of bismuth polymer (B-1), ethylene homopolymer, homopolymer and/or vinyl may be formed depending on the type of catalyst used and the polymerization conditions 'other than polymer'. A homopolymer of cyclohexane. In this case, the polymer (B-1) can be easily taken out by extracting the solvent using a soxhlet extractor or the like. When toluene is used as a solvent, a homopolymer of vinylcyclohexane as an insoluble component can be removed. When chloroform is used as a solvent, a homopolymer of an olefin such as a homopolymer of ethylene which is an insoluble component or a homopolymer of propylene is removed. The polymer (B-1) can be isolated as the coluene component of the solvents. If there is no problem in its use, it is also possible to use a polymer (Β-l) having 24 321925 201041645 as a by-product as described above. The molecular weight distribution of the polymer (B-1) (Mw / Mn = [weight average molecular weight] / [number average molecular weight]) is generally 1.5 to 10. About 〇, the aqueous emulsion of the present invention is hardened by drying. 5至优选。 Preferably, it is preferably from about 1.5 to about 5.0. The weight average molecular weight (Mw) of the polymer (Β-1) is generally from about 5,000 to about 10,000 000, and the mechanical strength of the cured product obtained by drying the aqueous emulsion of the present invention and the polymer (B_i) From the viewpoint of liquidity, it is preferably about 10,000 to 500, and about 1,500 to 400,000. More preferably. The molecular weight distribution of the polymer (Β-1) can be determined by gel permeation chromatography (GPC). The ultimate viscosity [η ] of the polymer (Β-l) is generally from about 0·25 to about 10 dl/g, from the viewpoint of the mechanical strength of the cured product obtained by drying the aqueous emulsion of the present invention. 'It is preferably about 0.3 to 3 dl/g. Melt flow rate of polymer (Bi) measured under conditions of 19 (TC, 2.16 kgf) using a melt indexer (L217-E14011; manufactured by techno7) according to JIS K 7210 The value of the ruler) is usually from 130 to 300 g/l min, preferably from about 10 minutes to about _ minutes from the viewpoint of dispersibility of the polymer (Β-1) in the aqueous emulsion of the present invention. (B-2) means a polymer obtained by graft-polymerizing a non-unsaturated carboxylic anhydride with a polymer (Β-1). 321925 25 201041645, Graft polymerization amount of α, /3 - unsaturated carboxylic anhydride至约约重量重量左右。 Preferably, about 0.1 to 20 parts by weight, preferably from about 0.1 to about 5 parts by weight, more preferably from about 0.1 to about 5 parts by weight, more preferably from about 0.1 to about 5 parts by weight, based on 100 parts by weight of the polymer (Β-2). The aqueous emulsion of the present invention containing the polymer of the α,/3-unsaturated carboxylic anhydride having a graft polymerization amount of 0.01 parts by weight or more (Β-2) preferably has a tendency to improve the adhesion. An aqueous emulsion of the present invention in which the graft polymerization amount of the lu-unsaturated carboxylic anhydride is 20% by weight or less based on the polymer (B-2), due to the heat ν/α, cold-unsaturated carboxylic anhydrides such as maleic anhydride, itaconic anhydride, citraconic anhydride, etc., having 4 to 20 carbon atoms, /3-unsaturated carboxylic acid The acid anhydride is preferably maleic anhydride. Two or more kinds of α, /5-unsaturated carboxylic anhydrides may be used in combination. The polymer (Β-2) may be produced by, for example, the following method: (Β-1) a method of adding α, an unsaturated carboxylic anhydride and graft-polymerizing a molten polymer (Β-1) obtained by melting; or dissolving a polymer in a q solvent such as toluene or dioxane (B-1), a method of adding α, hydrazine-unsaturated carboxylic anhydride to a solution obtained by graft polymerization, etc. Graft polymerization is generally carried out in the presence of a radical initiator. When the amount of the starting agent used is small, the amount of graft polymerization of α,β-unsaturated carboxylic anhydride is small, and the cured product obtained by drying the aqueous emulsion of the present invention tends to have difficulty in improving adhesion, and when used in a large amount The amount of unreacted radical initiator contained in the polymer (Β-2) tends to increase, and therefore, relative to the polymerization The compound (Β-1) is 100 parts by weight, generally 0.01 to 10 parts by weight, preferably 0.01 to 1 part by weight. 26 321925 201041645 Free radical initiator generally allows the timing to be used at the solution temperature In the case of an organic peroxide of 50 ° C or more, the amount of graft polymerization of ruthenium-non-needle tends to increase, and the polymer in the graft polymerization is used when an organic peroxide at a decomposition temperature of two is used. -1) The tendency of two. After decomposing to generate free radicals, it is preferred to have an organic peroxide having a function of extracting protons from the mouth.
^ /衰期成為1分鐘之分解溫度為50至210Χ:的有機過 m可,舉如:㉟氧化二醯基化合物、過氧化二烧基化 口=過氧化縮酮化合物、烷基過氧化酯化合物以及過碳 1§曰化° A ’其中以過氧化二絲化合物、過氧化二酿基 化&物碳酸醋化合物以及烧基過氧化醋化合物為佳。 具體上可列舉如:過氧化二碳酸三(十六㈣旨)、過氧化二 板1-(3-甲氧基丁酯)、過氧化二碳酸二(2_乙基己酯)、 過氧化—碳酸二(4-第三丁基環己基g旨)、過氧化碳酸二異 丙面曰過氧化異丙基碳酸第三丁酯、過氧化碳酸二肉豆蔻 酉曰^氧化新癸酸1,1,3, 3-四甲基丁酯、過氧化新癸酸α 異丙笨§曰、過氧化新癸酸第三丁酯、1,1-雙(過氧化第三 丁基)裏己烷、2, 2-雙(4, 4-二第三丁基過氧化環己基)丙 烷雙(過氧化第三丁基)環十二烷、過氧化異丙基單 石厌西文第二己®旨、過氧化'3, 5, 5-三曱基己酸第三丁醋、過氧 化月桂H"1"®旨、2, 5-二甲基-2, 5-雙(過氧化苯甲酿) 己烷,氧化乙酸第三丁酯、2, 2_雙(過氧化第三丁基)丁 晞、過氧化苯甲酸第三丁S旨、4, 4-雙(過氧化第三丁基)戊 27 321925 201041645 、酸丁酯、過氧化異酞酸二(第三丁酯)、過氧化二異丙苯、 α,α -雙(第三丁基過氧化間異丙基)苯、2,5_二甲基 -2’5-雙(過氧化第三丁基)己烷、丨,3_雙(第三丁基過氧化 異丙基)苯、過氧化第三丁基異丙笨、過氧化二第三丁基、 氩過氧化對薄荷焼*(Pnenthane hydroperoxide)以及2, 5- 二甲基-2, 5-雙(過氧化第三丁基)_3_己炔。 有機過氧化物之添加量,相對於聚合物(8_丨)1〇〇重 量份,一般為〇. 01至20重量份,以〇. 01至10重量份為 Ό佳。 k使用擠壓機即可進行熔融混煉,並可採用使複數的 聚合物、或者聚合物與固體或液體的添加物混合之習知的 各種方法之觀點來看,以在使聚合物(Β_υ熔融而得的熔融 聚合物(Β-1)中添加α,点_不飽和羧酸酐而使其接枝聚合 的方法為佳。又以將全部或部分之進行接枝聚合的各成分 組合,分別以亨舍爾攪拌機、帶式混合機(rib〇n ❹blender)、混合機等進行混合,得到均勻混合物後,將該 混合物熔融混煉之方法為更佳。熔融混煉之手段可廣泛地 採用班布里密閉式混煉機(Banbury mixer)、布拉斯特擠壓 機(?1&31;〇11^11)、塑譜儀(31^1:^1:1(^1'?1狀七0§1^此)、單軸 或雙軸之擠壓機專習知之混煉手段。從可連續生產聚合物 (B-1)而提高生產性之觀點而言,係以將聚合物(B-1)、〇 石-不飽和羧酸酐及自由基起始劑預先充分混合而得的混 合物,由單轴或雙軸之擠壓機的供給口供給並進行混煉之 方法為佳。擠壓機進行熔融混煉之部分的溫度(例如擠壓機 32192s 28 201041645 之缸筒(cylinder)溫度)一般為50至300°C,以80至270 °C為佳。溫度為50°C以上時,接枝量有提高之傾向,溫度 為300°C以下時,聚合物(B-1)之分解有受到抑制之傾向。 熔融混煉以二階段進行者為佳,以設定第二階段之熔融混 煉的溫度高於第一階段之熔融混煉的溫度者為佳。熔融混 煉時間一般為0. 1至30分鐘,以0. 1至5分鐘為佳。熔融 混煉時間為0. 1分鐘以上時,接枝量有提高之傾向,並且, 熔融混煉時間為30分鐘以下時,聚合物(B-1)之分解有受 到抑制之傾向。 聚合物(B-2)中之源自α,冷-不飽和羧酸酐的構造單 元可為維持酸酐構造之構造單元,亦可為源自酸酐構造經 開環之《,/3-不飽和羧酸的構造單元,亦可為同時含有維 持酸酐構造之構造單元與源自酸酐構造經開環之α,沒-不 飽和羧酸之構造單元的構造單元。 聚合物(Β-2)之分子量分佈(Mw/Mn)—般為1. 5至10, 以1. 5至7為佳,以1. 5至5更佳。聚合物(B-2)之分子量 分佈可依與上述聚合物(B-1)之分子量分佈的相同方法進 行測定。 聚合物(B-2)之極限黏度[7/ ]之值一般為0.25至10 dl /g左右,從本發明之水性乳劑經乾燥而得之硬化物的機械 性強度之觀點而言,以0. 3至3dl/g左右為佳。 依據JIS K 7210之基準,使用熔融指數測定儀(L217-E14011 ; techno7 公司製造),在 190°C、2. 16kgf 之條件 下測定之聚合物(B-2)的熔融流動速率(MFR)之值,一般為 29 321925 201041645 130g/10分鐘以上、300g/10分鐘以下,從本發明之水性乳 劑中之聚合物(B-2)的分散性之觀點而言,以130g/10分鐘 以上、200g/10分鐘以下為佳。 本發明之水性乳劑係除了含有成分(A)以及成分(B)之 外,亦含有作為成分(C)之水,且以成分(A)以及成分(B) 為分散質,並以成分(C)為分散媒的乳劑。 分散質之體積基準中位數直徑一般為〇.〇l/zm至3// m,以 0.1/zm 至 2/ζιη 為佳,以 0.5/zm 至 更佳。 體積基準中位數直徑為0.01//m以上時,水性乳劑之 製造較為容易,如為3/im以下時,水性乳劑之靜置安定性 以及水性乳劑經乾燥而得之硬化物的接著性有提高之傾 向。“靜置安定性”意指水性乳劑不經攪拌而保持3天 時,水性乳劑為均勻之性質,亦即,在水性乳劑中難以生 成成分(B)豐富之層及/或成分(C)豐富之層的性質。“體積 基準中位數直徑”意指以體積基準計,累積粒徑分佈之值 相當於50%的粒徑。 本發明之水性乳劑中的成分(A)之含量,相對於(B) 100 重量份,一般為1至30重量份,以2至10重量份為佳。 本發明之水性乳劑中的成分(A)與成分(B)之總含量, 相對於水性乳劑100重量份,一般為10至90重量份,以 30至70重量份為佳,以40至60重量份更佳。 本發明之水性乳劑中的成分(C)之含量,相對於水性乳 劑100重量份,一般為90至10重量份,以70至30重量 份為佳,以60至40重量份更佳。 30 321925 201041645 ' 本發明之水性乳劑可列舉如:成分(A)及成分(B)經熔 融混煉後,將所得熔融混合物與水進行混合之方法;包含 將成分(A)混入經加熱之成分(B)中之步驟的方法;成分(A) - 及成分(B)經加熱及混煉後,將所得混煉混合物分散於成分 (C)中之方法;以及包含使成分(B)溶於甲苯等有機溶媒 後,將所得溶液與成分(A)混合,再從所得混合物中去除上 述有機溶媒之步驟的方法。 此外,亦可使用自行乳化等化學乳化法。 〇 其中,以成分(A)及成分(B)經熔融混煉後將所得熔融 混合物與水進行混合之方法、以及包含將成分(A)混入經加 _ 熱之成分(B)中之步驟的方法為適宜。 將成分(A)及成分(B)進行熔融混煉之步驟中所使用的 裝置可列舉如:雙轴擠壓機、實驗級布拉斯特擠壓機(labo plast mill ;東洋精機製作所(股)製造)、微實驗級布拉斯 特擠壓機(labo plast mill micro;東洋精機製作所(股) Q 製造)等多軸擠壓機;均質機、T.K. FILMIX(譜莱密克司 (primix)(股)製造)等具有桶(barrel)(缸筒)的機器;攪拌 槽、化學攪拌器、璇渦混合機、射流喷射混合器、膠體研 磨機(colloid mill)、超音波產生器、高壓均質機、分散 君(富士金(股)之註冊商標)、靜態攪拌器、微混合器等不 具有桶(缸筒)的機器等。 具有桶之機器的剪切速率一般為200至100000秒_1左 右,以1000至2500秒-1左右為佳。剪切速率為200秒M以 上時,水性乳劑經乾燥而得之硬化物有提高接著性之傾 31 321925 201041645 、 向,如為100000秒1以下時,則水性乳劑有易於工業性製 造之傾向。“剪切速率”意指將螺桿元件最外圍部分之圓 周速度[mm/sec]除以螺桿與桶之間隙[mm]所得之數值。 - 將成分(A)及成分(B)進行熔融混煉之方法可列舉如: 從雙軸撥壓機之給料斗(hopper)或供給口連續地供給(B) 成分,進行(B)成分之加熱熔融混煉,並由裝設在該擠壓機 之壓縮區、計量區或脫氣區的至少1個供給口加壓供給成 分(A),再將成分(A)以及成分(B)進行混煉,接著,由裝設 ^ 在該擠壓機之壓縮區的至少1個供給口供給成分(C),藉此 將水性乳劑連續地由模孔(die)擠出而製造之方法。 包含將成分(A)混入經加熱之成分(B)中的步驟之方 法,可列舉如:將捏合機之缸筒加熱後,在該缸筒内投入 成分(B),一面使其旋轉,同時亦使成分(B)溶融,接著, 投入成分(A),一面其使旋轉,同時亦使成分(A)及成分(B) 混合,將所得混合物投入溫水中,藉此使成分(A)及成分(B) Q 分散於成分(C)中而得水性乳劑之方法。 包含將成分(A)混入經加熱之成分(B)中的步驟之方 法,係以使用多軸擠壓機之方法為適宜。具體上可列舉如: 首先,從箱内具有2支以上螺桿之多軸擠壓機的給料斗供 給成分(B),進行成分(B)之加熱溶融混煉,其次,由裝設 在該擠壓機之壓縮區及/或計量區的至少1個液體供給口 供給成分(A),一面使成分(A)以及成分(B)混煉,同時亦分 散於成分(C)中之方法。 本發明之水性乳劑可含有:聚胺酯水性乳劑、乙烯- 32 321925 201041645 乙酸乙烯酯共聚物水性乳劑等其它水性乳劑;脲樹脂、二 聚氰胺樹脂、酚(Phenol)樹脂等熱硬化性樹脂;黏土、二 嶺土、滑石、碳酸鈣等充填劑;防腐劑;防鏽劑;消泡门 發泡劑;聚丙烯酸、聚驗、甲基纖維素、敌甲基纖維^、’ 聚乙烯醇、澱粉等增黏劑;黏度調整劑;阻燃劑;氧化鈦 等顏料;琥辑酸二甲醋、己二酸二甲等高沸點溶劑丨= 化劑等。 , Ο^ / The decay time becomes 1 minute, the decomposition temperature is 50 to 210 Χ: the organic over m can be, for example, 35 bismuth oxy compound, peroxydialkylation port = peroxy ketal compound, alkyl peroxyester The compound and the percarbon 1 曰 ° ° A ' are preferably a peroxo-filament compound, a peroxydicarbonate & carbonated vinegar compound, and a mercapto peroxide vinegar compound. Specific examples thereof include: diperoxide dicarbonate (16 (four)), peroxidized two-plate 1-(3-methoxybutyl), di(2-ethylhexyl) peroxydicarbonate, peroxidation - bis(4-tert-butylcyclohexylglycolate), diisopropyl sulfonate, butyl peroxy isopropyl carbonate, oxidized dimethicone, oxidized neodecanoic acid 1, 1,3, 3-tetramethylbutyl ester, peroxy neodecanoic acid α isopropyl hydrazine, peroxy neodecanoic acid tert-butyl ester, 1,1-bis(t-butylperoxide) hexane , 2, 2-bis(4,4-di-t-butylperoxycyclohexyl)propane bis(butylated butyl peroxide) cyclododecane, isopropyl sulphide monolithic succinct The purpose of peroxidation of '3,5,5-tridecylhexanoic acid, third vinegar, peroxidized laurel H"1"®, 2, 5-dimethyl-2, 5-double (peroxide benzoate) Hexane, oxidized acetic acid tert-butyl ester, 2, 2_bis(t-butylperoxy)butyl hydrazine, benzoic acid benzoic acid, third butyl s, 4, 4- bis (perbutyl tributyl peroxide)戊27 321925 201041645, butyl acrylate, iso-isophthalic acid di(tributyl acrylate), Dicumyl, α,α-bis(t-butylperoxyisopropylidene)benzene, 2,5-dimethyl-2'5-bis(t-butylperoxy)hexane, hydrazine , 3_bis(t-butylperoxyisopropyl)benzene, tributylisopropyl peroxide, dibutylbutyl peroxide, argon peroxide, pnenthane hydroperoxide, and 2, 5 - Dimethyl-2, 5-bis(t-butylperoxy)_3-hexyne. The amount of the organic peroxide added is usually from 0.1 to 20 parts by weight, preferably from 0.1 to 10 parts by weight, based on 1 part by weight of the polymer (8 Å). k can be melt-kneaded using an extruder, and can be used to make a polymer (Β_υ) from the viewpoint of various methods of mixing a plurality of polymers or a polymer with a solid or liquid additive. It is preferred to add α, a point-unsaturated carboxylic anhydride to the molten polymer (Β-1) to carry out graft polymerization, and to combine all or part of the components for graft polymerization. Mixing with a Henschel mixer, a belt mixer, a mixer, etc. to obtain a homogeneous mixture, and then melting and kneading the mixture is more preferable. The means of melt-kneading can be widely used. Bianbury mixer, Brass extruder (?1&31;〇11^11), plastic spectrometer (31^1:^1:1 (^1'?1 shape) VII § 1 ^ this), uniaxial or biaxial extruder specializing in the mixing method. From the viewpoint of continuous production of polymer (B-1) to improve productivity, the polymer ( B-1), a mixture of vermiculite-unsaturated carboxylic anhydride and a radical initiator which are sufficiently mixed in advance, from uniaxial or biaxial The method of supplying and kneading the supply port of the extruder is preferred. The temperature of the portion where the extruder is melt-kneaded (for example, the cylinder temperature of the extruder 32192s 28 201041645) is generally 50 to 300 ° C. It is preferably 80 to 270 ° C. When the temperature is 50 ° C or higher, the graft amount tends to increase, and when the temperature is 300 ° C or lower, the decomposition of the polymer (B-1) tends to be suppressed. The smelting time is generally from 0.1 to 30 minutes, and the temperature is preferably from 0.1 to 30 minutes, so that the temperature of the melt-kneading in the second stage is higher than the temperature of the melt-kneading in the first stage. 0. 1 to 5 minutes is preferred. When the melt-kneading time is 0.1 minutes or more, the graft amount tends to increase, and when the melt-kneading time is 30 minutes or less, the decomposition of the polymer (B-1) There is a tendency to be suppressed. The structural unit derived from α, cold-unsaturated carboxylic anhydride in the polymer (B-2) may be a structural unit for maintaining an acid anhydride structure, or may be an open-loop structure derived from an acid anhydride structure. The structural unit of the /3-unsaturated carboxylic acid may also be a structure containing both a maintenance anhydride structure And the molecular weight distribution (Mw/Mn) of the polymer (Β-2) is generally 1.5 to 10, in terms of a molecular weight distribution (Mw/Mn) of the polymer (Β-2). 1. 5 to 7 is preferable, more preferably 1.5 to 5. The molecular weight distribution of the polymer (B-2) can be measured in the same manner as the molecular weight distribution of the above polymer (B-1).至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至至3dl/g is better. The melt flow rate (MFR) of the polymer (B-2) measured at 190 ° C, 2.16 kgf using a melt indexer (L217-E14011; manufactured by techno7) according to JIS K 7210 The value is generally 29 321925 201041645 130 g/10 minutes or more and 300 g/10 minutes or less, and is 130 g/10 minutes or more and 200 g from the viewpoint of dispersibility of the polymer (B-2) in the aqueous emulsion of the present invention. Below /10 minutes is preferred. The aqueous emulsion of the present invention contains water as the component (C) in addition to the component (A) and the component (B), and the component (A) and the component (B) are dispersed, and the component (C) ) is an emulsion of a dispersion medium. The volume reference median diameter of the dispersoid is generally from 〇.〇l/zm to 3//m, preferably from 0.1/zm to 2/ζιη, preferably from 0.5/zm to more preferably. When the volume-based median diameter is 0.01/m or more, the aqueous emulsion is easy to manufacture. For example, when it is 3/im or less, the static stability of the aqueous emulsion and the adhesion of the cured product obtained by drying the aqueous emulsion are The tendency to improve. "Stabilization stability" means that the aqueous emulsion is uniform when it is kept for 3 days without being stirred, that is, it is difficult to form a component in the aqueous emulsion (B), and the layer and/or the component (C) is rich. The nature of the layer. The "volume-based median diameter" means that the value of the cumulative particle size distribution corresponds to 50% of the particle diameter on a volume basis. The content of the component (A) in the aqueous emulsion of the present invention is usually from 1 to 30 parts by weight, preferably from 2 to 10 parts by weight, per 100 parts by weight of the (B). The total content of the component (A) and the component (B) in the aqueous emulsion of the present invention is generally 10 to 90 parts by weight, preferably 30 to 70 parts by weight, and preferably 40 to 60 parts by weight based on 100 parts by weight of the aqueous emulsion. Better. The content of the component (C) in the aqueous emulsion of the present invention is usually 90 to 10 parts by weight, preferably 70 to 30 parts by weight, more preferably 60 to 40 parts by weight, per 100 parts by weight of the aqueous emulsion. 30 321925 201041645 The aqueous emulsion of the present invention may, for example, be a method in which the obtained molten mixture is mixed with water after melt-kneading the component (A) and the component (B); and the component (A) is mixed with the heated component. (B) the method of the step; the component (A) - and the component (B), after heating and kneading, dispersing the obtained kneaded mixture in the component (C); and containing the component (B) After the organic solvent such as toluene, the obtained solution is mixed with the component (A), and the step of removing the organic solvent from the obtained mixture is carried out. In addition, chemical emulsification methods such as self-emulsification can also be used. In the above, the method in which the component (A) and the component (B) are melt-kneaded, and the obtained molten mixture is mixed with water, and the step of mixing the component (A) into the component (B) of the addition-heating The method is suitable. The apparatus used in the step of melt-kneading the component (A) and the component (B) may be, for example, a twin-screw extruder or an experimental-stage Brass extruder (labo plast mill; Toyo Seiki Co., Ltd.) ) Manufacturing), micro-experimental Brass extruder (labo plast mill micro; manufactured by Toyo Seiki Co., Ltd. Q) and other multi-axis extruders; homogenizer, TK FILMIX (primix) (manufacturing), etc. Machines with barrels; cylinders, chemical mixers, vortex mixers, jet jet mixers, colloid mills, ultrasonic generators, high pressure homogenizers , such as a machine that does not have a barrel (cylinder), such as a static mixer (a registered trademark of Fujitsu Co., Ltd.), a static mixer, or a micro-mixer. The shear rate of a machine having a barrel is generally from 200 to 100,000 seconds _1, preferably from about 1000 to 2500 sec-1. When the shear rate is 200 sec or more, the cured product obtained by drying the aqueous emulsion has an improved adhesion. 31 321 925 201041645. If it is 100000 sec or less, the aqueous emulsion tends to be industrially easy to manufacture. "Shear rate" means the value obtained by dividing the circumferential speed [mm/sec] of the outermost portion of the screw member by the gap [mm] between the screw and the barrel. - A method of melt-kneading the component (A) and the component (B), for example, continuously supplying the component (B) from a hopper or a supply port of a biaxial press, and performing the component (B) Heating and melt-kneading, and supplying the component (A) to at least one supply port installed in the compression zone, the metering zone or the degassing zone of the extruder, and then performing the component (A) and the component (B) The kneading is followed by a method in which the component (C) is supplied from at least one supply port in the compression zone of the extruder, whereby the aqueous emulsion is continuously extruded from a die. The method including the step of mixing the component (A) into the heated component (B), for example, after heating the cylinder of the kneader, the component (B) is placed in the cylinder and rotated while being rotated. Further, the component (B) is melted, and then the component (A) is charged, and the component (A) and the component (B) are mixed while being rotated, and the resulting mixture is poured into warm water to thereby cause the component (A) and Component (B) Q A method in which the component (C) is dispersed to obtain an aqueous emulsion. The method comprising the step of mixing the component (A) into the heated component (B) is preferably a method using a multiaxial extruder. Specifically, first, the component (B) is supplied from a hopper of a multi-axis extruder having two or more screws in a tank, and the component (B) is heated and melted and kneaded, and secondly, it is installed in the extrusion. At least one liquid supply port of the compression zone of the press and/or at least one liquid supply port of the metering zone is supplied with the component (A), and the component (A) and the component (B) are kneaded and dispersed in the component (C). The aqueous emulsion of the present invention may contain: an aqueous polyurethane emulsion, ethylene-32 321925 201041645 vinyl acetate copolymer aqueous emulsion and other aqueous emulsions; thermosetting resin such as urea resin, melamine resin, phenol (Phenol) resin; clay Filling agent such as sorghum, talc, calcium carbonate; preservative; rust preventive; defoaming door foaming agent; polyacrylic acid, polyacrylic acid, methyl cellulose, dimethomethyl fiber, 'polyvinyl alcohol, starch Such as tackifiers; viscosity modifiers; flame retardants; pigments such as titanium oxide; humic acid dimethyl vinegar, adipic acid dimethyl and other high boiling solvents 丨 = chemicals. , Ο
G 、:藉由使本發明之水性乳劑乾燥,即可得到與木質 料、纖維素材料、塑膠材料、陶竟材料以及金屬材料等^ 材的接著性優異之硬化物。乾燥溫度—般為3()至 乂 60至150 C為佳。乾燥時間一般為1分鐘至12小萨 右,以10分鐘至6小時左右為佳。乾燥可在通風下進^左 亦可在減壓下進行。本發明之硬化物即使乾燥溫 ⑽U右的低溫,與紐之接絲亦佳。χ,使本 水I·生乳劑經乾燥而得的硬化物,即使對難以與塗料等其A 材料,著的料烴(例如Μ料),亦具有優異之接著性匕。 藉由將本發明之水性乳劑塗佈在基材上,即可得到在 基材上層積著該水性乳劑層之積層體,而經由乾燥該積層 體即可形成具有基材層與由硬化物所構成之層的積層體。 由該硬化物所構成之層可作為塗料、錢、底材、、ς著劑 等使用。 基材如為可塗佈本發明之水性乳劑者即可,可為任竟 形狀。 … 基材可列舉如:木材、合板、MDFOnedium density 321925 33 201041645 ' fiberboard,中密度纖維板)、粒片板(particle board)、 纖維板等木質材料;壁紙、包裝紙等紙質材料;棉布、麻 布、螺縈(rayon)等纖維素材料;聚乙稀(以源自乙晞之構 . 造單元為主成分的聚烯烴,以下相同)、聚丙烯(以源自丙 烯之構造單元為主成分的聚烯烴,以下相同)、聚笨乙烯等 聚烯烴;聚碳酸酯、丙烯腈/丁二烯/苯乙烯共聚物(ABS樹 脂)、(甲基)丙烯酸系樹脂聚酯、聚醚、聚氯乙烯、聚胺酯、 發泡胺酯等塑膠材料;玻璃、陶瓷器等陶瓷材料;以及鐵、 〇 不鏽鋼、銅、鋁等金屬材料。 該基材可為由複數之材料所構成的複合材料。亦可為 滑石、氧化矽、活性碳等無機充填劑或碳纖維等與塑膠材 料之混煉成型品。 此處,聚胺酯係經由胺酯鍵而交聯的高分子,一般可 經由醇(具有-0H之化合物)與異氰酸酯(具有-NC0之化合 物)之反應而得。發泡聚胺酯係因由異氰酸酯與作為交聯劑 q 之水的反應所產生之二氧化碳或氟利昂(Freon)等揮發性 溶劑而發泡的聚胺酯。汽車之内裝用構材一般係使用半硬 質的聚胺酯,塗料一般係使用硬質的聚胺酯。 基材之中,以聚丙烯、聚苯乙稀、聚碳酸醋、丙烯腈/ 丁二烯/苯乙烯共聚物(ABS樹脂)、聚對酞酸乙二酯、聚氣 乙烯、(甲基)丙烯酸系樹脂、玻璃、鋁以及聚胺酯為佳, 又以聚丙烯、聚氣乙烯、玻璃、鋁以及聚胺酯為更佳。 由本發明之乳劑所得的硬化物可作為將2種類之基材 進行接著之接著層使用。一邊的基材如為木質材料、紙質 34 321925 201041645 材料、纖維素材料等吸水性之基材時,若將本發明之水性 乳劑塗佈在該吸水性之基材,則水性乳劑中所含的成分(c) 會被吸水性之基材吸收,在吸水性之基材上形成含有成分 • (A)以及成分(B)之接著層。因此,在該接著層上經由貼合 . 另一邊之基材,即可得到由吸水性之基材、接著層以及另 一邊之基材依序層積而成之積層體。 一邊之基材如為聚烯烴等非吸水性之基材時,則將本 發明之水性乳劑塗佈在該非吸水性之基材上後,經加熱而 〇 在非吸水性之基材上形成硬化物,然後將另一邊之基材貼 合在該硬化物上,再經由加熱即可得到積層體。加熱溫度 一般為60至200°C。本發明之水性乳劑,即使加熱溫度為 60至90°C,亦可賦予接著性優異之硬化物,更且,即使加 熱溫度為65至80°C之低溫,亦可賦予接著性優異之硬化 物。 對於本發明之硬化物,可再以液狀材料作為塗料而進 Q 行塗佈。塗料可列舉如聚胺S旨等上述基材的材料,如為液 狀材料,則與該硬化物之接著性優異。 (實施例) 以下,藉由實施例而更詳加說明本發明,然本發明並 不受限於該等實施例。 [固形分] 固形分係依以JIS K-6828為準則之方法而測定。 [分子量以及分子量分佈] 成分(B)之分子量係依凝膠滲透層析法(GPC)而測定。 35 321925 201041645 以聚苯乙烯(分子量688至400, 000)標準物質進行校正, 並在下述條件中求取。同時,分子量分佈係以相對於數目 平均分子量(以下稱為Μη)之重量平均分子量(以下稱為Mw) 的比(Mw/Mn)進行評估。G: By drying the aqueous emulsion of the present invention, it is possible to obtain a cured product excellent in adhesion to wood materials, cellulose materials, plastic materials, ceramic materials, and metal materials. The drying temperature is generally from 3 () to 乂 60 to 150 C. The drying time is generally from 1 minute to 12 hours, preferably from 10 minutes to 6 hours. Drying can be carried out under ventilation and left under reduced pressure. The cured product of the present invention is excellent even when it is dried at a low temperature of (10) U right. In addition, the cured product obtained by drying the water I and the raw emulsion has excellent adhesion properties even when it is difficult to form a hydrocarbon (for example, a feedstock) with a material such as a coating material. By coating the aqueous emulsion of the present invention on a substrate, a laminate in which the aqueous emulsion layer is laminated on the substrate can be obtained, and by drying the laminate, the substrate layer and the cured product can be formed. The layered body of the layer formed. The layer composed of the cured product can be used as a paint, a money, a substrate, a squeegee or the like. The substrate may be any one which can coat the aqueous emulsion of the present invention, and may have any shape. ... The substrate can be listed as: wood, plywood, MDFOnedium density 321925 33 201041645 'fiberboard, medium density fiberboard), particle board, fiberboard and other wooden materials; paper, wrapping paper and other paper materials; cotton, linen, snail Cellulose material such as rayon; polyethylene (contained from acetamidine, polyolefin based on the unit, the same as below), polypropylene (polyolefin based on structural units derived from propylene) , the same as below), polyolefin such as polystyrene; polycarbonate, acrylonitrile/butadiene/styrene copolymer (ABS resin), (meth)acrylic resin polyester, polyether, polyvinyl chloride, polyurethane , plastic materials such as foaming amine ester; ceramic materials such as glass and ceramics; and metal materials such as iron, tantalum stainless steel, copper and aluminum. The substrate can be a composite of a plurality of materials. It can also be an inorganic filler such as talc, cerium oxide or activated carbon, or a mixture of carbon fiber and other plastic materials. Here, the polymer in which the polyurethane is crosslinked via an amine ester bond is generally obtained by a reaction of an alcohol (a compound having -OH) with an isocyanate (a compound having -NC0). The foamed polyurethane is a polyurethane which is foamed by a volatile solvent such as carbon dioxide or Freon which is produced by the reaction of isocyanate with water as a crosslinking agent q. The interior components of automobiles are generally made of semi-rigid polyurethane, and the coatings are generally made of rigid polyurethane. Among the substrates, polypropylene, polystyrene, polycarbonate, acrylonitrile/butadiene/styrene copolymer (ABS resin), polyethylene terephthalate, polyethylene, (methyl) Acrylic resins, glass, aluminum, and polyurethane are preferred, and polypropylene, polyethylene, glass, aluminum, and polyurethane are more preferred. The cured product obtained from the emulsion of the present invention can be used as a substrate for carrying out two types of substrates. When the substrate on one side is a water-absorbent substrate such as a wood material, a paper material 34 321 925 201041645 material, or a cellulose material, if the aqueous emulsion of the present invention is applied to the water-absorbent substrate, the aqueous emulsion contains The component (c) is absorbed by the water-absorptive substrate, and an adhesive layer containing the component (A) and the component (B) is formed on the water-absorbent substrate. Therefore, a laminate obtained by laminating the water-absorbent substrate, the adhesive layer, and the other substrate in this order can be obtained by bonding the other substrate to the adhesive layer. When the substrate on one side is a non-absorbent substrate such as polyolefin, the aqueous emulsion of the present invention is applied onto the non-absorbent substrate, and then heated to form a hardened layer on the non-absorbent substrate. Then, the other side of the substrate is bonded to the cured product, and then the laminate is obtained by heating. The heating temperature is usually 60 to 200 °C. The aqueous emulsion of the present invention can impart a cured product excellent in adhesion even when the heating temperature is 60 to 90 ° C, and can provide a cured product excellent in adhesion even at a low temperature of 65 to 80 ° C. . For the cured product of the present invention, the liquid material can be further applied as a coating material. The coating material may, for example, be a material of the above-mentioned base material such as polyamine S. If it is a liquid material, it is excellent in adhesion to the cured material. (Embodiment) Hereinafter, the present invention will be described in more detail by way of examples, but the invention is not limited by the examples. [Solid fraction] The solid fraction was measured in accordance with the method of JIS K-6828. [Molecular Weight and Molecular Weight Distribution] The molecular weight of the component (B) was measured by gel permeation chromatography (GPC). 35 321925 201041645 Calibration with polystyrene (molecular weight 688 to 400,000) reference material and obtained under the following conditions. Meanwhile, the molecular weight distribution is evaluated in a ratio (Mw/Mn) of a weight average molecular weight (hereinafter referred to as Mw) with respect to a number average molecular weight (hereinafter referred to as Μη).
機種 Waters 製 150-CModel Waters System 150-C
管柱 shodex packed column A-80MColumn shodex packed column A-80M
測定溫度 140°C 測定溶媒 鄰二氯苯Measuring temperature 140 ° C Determination of solvent o-dichlorobenzene
測定濃度 lmg/ml [NH3中和度] 乳化劑之NH3中和度係指相對於乳化劑中所含的成分 (A)之源自丙烯酸的構造單元之莫耳數與源自琥珀酸2-曱 基丙烯醯氧基乙酯的構造單元之莫耳數的總數,以所使用 之氨的莫耳數比例(%)表示者。此處,各構造單元之莫耳數 假定為與製造成分(A)時所使用之各單體的莫耳數相同。 [源自乙烯基環己烷之構造單元的含量] 成分(B)中之源自乙烯基環己烷的構造單元之含量係 指將成分(B)之13C-丽R光譜以藉下述條件所測得之結果與 下述式(X)作為基準而算出者。 13C-NMR 裝置:BRUKER 公司製 DRX600 測定溶媒: 鄰二氣苯與鄰二氣苯-d4為4 : 1(容積比) 之混合液Determination of concentration lmg/ml [NH3 neutralization degree] The NH3 neutralization degree of the emulsifier means the molar number of the structural unit derived from acrylic acid relative to the component (A) contained in the emulsifier and the succinic acid-derived 2- The total number of moles of the structural unit of the mercaptopropenyloxyethyl ester is represented by the molar ratio (%) of the ammonia used. Here, the number of moles of each structural unit is assumed to be the same as the number of moles of each monomer used in the production of the component (A). [Content of structural unit derived from vinylcyclohexane] The content of the structural unit derived from vinylcyclohexane in the component (B) means that the 13C-Li spectrum of the component (B) is based on the following conditions The measured result was calculated based on the following formula (X). 13C-NMR device: DRX600 manufactured by BRUKER Co., Ltd. Solvent: A mixture of o-dibenzene and o-diphenyl-d4 in a ratio of 4:1 (volume ratio)
測定溫度: 135°C 測定方法: Powergate Decouping法脈波角度:45度 36 321925 201041645 ' 測定基準: 四甲基矽烷 源自乙烯基環己烧之構造單元的含量(mo 1 %) =100xA/(B-2A) (X) (式(1)中,A表示45ppm至40ppm之信號的積分累積值,B . 表示35ppm至25ppm之信號的積分累積值)。 [接枝量] 成分(B)中之馬來酸if的接枝量係如下進行操作而求 得。 〇 (i) 使試料1. 〇g溶解於二甲苯20ml而調製試料溶液。 (ii) 將所調製之溶液一邊攪拌一邊滴入曱醇300ml中。 (iii) 回收曱醇中所析出之沉澱物,並在80°C中乾燥8小 時。 (iv) 使用乾燥之固體,經熱壓而製作厚度100/zm之膜。 (v) 測定所製作之膜的紅外線吸收光譜,並依據1780CHT1 附近之吸收峰以定量馬來酸的接枝量。 〇 [極限黏度] 成分(B)之極限黏度([7/ ];單位:dl/g)係使用烏別洛 德黏度計(Ubbelohde type viscometer),以四氫萘作為溶 媒在135°C中測定。 [玻璃轉換溫度以及融點] 成分(B)之玻璃轉換溫度([Tg];單位:°C)以及融點 ([Tin];單位:°C)係使用示差掃描量熱儀(精工電子工業公 司製造,SSC-5200),以下述條件測定示差掃描熱量測定曲 線,並依步驟(c)所得之示差掃描熱量測定曲線而求得。 37 321925 201041645 、 〈測定條件〉 (a)將試料以10°C/分鐘從20°C升溫至200°C後,在200°C 下維持10分鐘。Measurement temperature: 135 ° C Measurement method: Powergate Decouping pulse angle: 45 degrees 36 321925 201041645 'Base of measurement: Tetramethyl decane derived from the content of structural units of vinyl cyclohexane (mo 1 %) = 100xA / ( B-2A) (X) (In the formula (1), A represents an integral cumulative value of a signal of 45 ppm to 40 ppm, and B. represents an integrated integrated value of a signal of 35 ppm to 25 ppm). [Graft amount] The graft amount of maleic acid if in the component (B) was determined by the following operation. 〇 (i) The sample solution was prepared by dissolving the sample 1. 〇g in 20 ml of xylene. (ii) The prepared solution was added dropwise to 300 ml of decyl alcohol while stirring. (iii) The precipitate precipitated from the sterol was recovered and dried at 80 ° C for 8 hours. (iv) A film having a thickness of 100/zm was produced by hot pressing using a dried solid. (v) The infrared absorption spectrum of the produced film was measured, and the graft amount of maleic acid was quantified based on the absorption peak near 1780 CHT1. 〇[limit viscosity] The ultimate viscosity of component (B) ([7/ ]; unit: dl/g) is determined by using Ubbelohde type viscometer with tetrahydronaphthalene as solvent at 135 °C. . [Glass conversion temperature and melting point] The glass transition temperature ([Tg]; unit: °C) of the component (B) and the melting point ([Tin]; unit: °C) are using a differential scanning calorimeter (Seiko Electronics Industry) The company's manufacturing, SSC-5200), measured the differential scanning calorimetry curve under the following conditions, and obtained the differential scanning calorimetry curve obtained in the step (c). 37 321925 201041645, <Measurement conditions> (a) The sample was heated from 20 ° C to 200 ° C at 10 ° C / min, and then maintained at 200 ° C for 10 minutes.
. (b)將(a)所得試料以10°C/分鐘從200°C降溫至-100°C 後,在-100°C下維持10分鐘。 (c)將(b)所得試料以10°C/分鐘從-100°C升溫至200°C。 衍生構造單元(al)之單體係使用丙烯酸(三菱化學(股) 製造,以下簡稱為AA);衍生構造單元(a2)之單體係使用 ^ 甲基丙烯酸N,N-二曱胺基乙酯(三洋化成工業(股)製造, 以下簡稱為DMA);衍生構造單元(bl)之單體係使用曱基丙 烯酸曱酯(三菱螺縈(股)製造,以下簡稱為匪A)、甲基丙 烯酸月桂酯(三菱螺縈(股)製造,以下簡稱為LMA)以及曱 基丙烯酸十三酯(三菱螺縈(股)製造,以下簡稱為TDMA); 衍生構造單元(b3)之單體係使用琥珀酸2-甲基丙烯醯氧基 乙酯(共榮社化學(股)製造,以下簡稱為H0-MS),以製造 q 成分(A)。另外,以下之例中的“份”以及“Γ ,如無特 別限定,則表示重量基準。 〈成分(A)之製造例1> 將 AA 24. 5 份(42. 3 莫耳比)、HO-MS 22. 5 份(12. 2 莫 耳比)、DMA 28. 0 份(22. 2 莫耳比)、MM 15. 0 份(18. 6 莫 耳比)、LMA 3. 8份(1.8莫耳比)以及TDMA 6.2份(2. 9莫 耳比)在10至30°C中混合,調製單體混合物100份。此處 之“莫耳比”表示當上述單體之總莫耳數為100時的各單 體之莫耳數。 38 321925 201041645 在具備冷凝器、氮氣導入管、攪拌機以及滴液漏斗之 具有加熱用套管的1L反應器中,饋入異丙醇150份與離子 交換水100份。一面將所得溶液攪拌,一面將其内溫調整 • 至80°C。反應容器内的氣體以氮氣置換後,將上述調製之 . 單體混合物20份一次全部投入。進一步添加作為聚合起始 劑之2, 2’ -偶氮二異丁腈2份,將所得混合物在80°C中攪 拌。接著,於80°C下,費時4小時將單體混合物80份一 ^ 面攪拌一面滴入所得混合物中。從滴入開始起,每隔1小 〇 時添加一次2, 2’ -偶氮二異丁腈0. 15份,分成四次添加。 再將所得混合物於同溫度下攪拌3小時。將所得反應混合 .物加熱至沸騰程度以餾除異丙醇。將所得濃縮物之内溫冷 卻至50°C後,混合28%氨水溶液39. 9份(81. 7莫耳比,該 莫耳比係表示當上述單體之總莫耳數為100時的氨之莫耳 數),得到含有聚合物親水比率9.40之丙烯酸系樹脂且中 和度為150%的黏稠乳化劑。收率為90%。所得乳化劑稱為 〇 (A-1)。將結果呈示於表1。 〈成分(A)之製造例2至4> 除了所使用單體之種類及使用量、以及氨的使用量變 更為表1所記載者之外,進行與上述成分(A)之製造例1相 同之操作,得到含有丙烯酸系樹脂之黏稠乳化劑。將所得 乳化劑分別稱為(A-2)、(A-3)以及(A-4)。將結果呈示於表 39 321925 201041645 、 [表 1] 製造例1 製造例2 製造例3 製造例4 (A- 1) (A-2) (A-3) (A-4) 份 莫耳比 份 莫耳比 份 莫耳比 份 莫耳比 單 體 AA 24. 5 42. 3 34. 5 54. 5 34. 5 54. 5 49. 5 69. 3 H0-MS 22. 5 12. 2 22. 5 11. 1 22. 5 11. 1 22. 5 9. 9 DMA 28. 0 22. 2 18. 0 13. 0 18. 0 13. 0 3. 0 1.9 ΜΜΛ 15. 0 18. 6 15.0 17.1 15. 0 17. 1 15. 0 15· 1 LMA 3. 8 1.8 3.8 1.6 3. 8 1.6 3. 8 1.4 TDMA 6. 2 2. 9 6. 2 2. 7 6. 2 2. 7 6. 2 2.4 總和 100 100 100 100 100 100 100 100 NHa使用量 (莫耳比) 81.7 98.4 78. 7 95 • 0 NH3申和度(¾) 150 150 120 120 單體親水比率 9.40 9. 91 9. 91 10. 68 〈成分(B)之製造例1> 將不鏽鋼製反應器之内部氣體以氬氣置換後,於其中 投入乙烯基環己烷386份與甲苯3640份。將所得混合物升 溫至50C後,將乙烯一面以〇.6MPa加壓一面饋入反應器 〇 中。進一步饋入三異丁基銨的甲苯溶液(東曹.阿克蘇 (股)(Tosoh Akzo Corporation)製造;濃度 20%)10 份,接 著,將藉由使二乙基矽烷基(四甲基環戊二烯基)(3_第三丁 基-5-曱基-2-苯氧基)二氯化鈦〇 001份溶解於脫水甲苯 87份而得的溶液、與藉由使二甲基苯胺鑌四(五氟苯基)硼 酸鹽0. 03份溶解於脫水甲苯122份而得的溶液饋入反應器 中。將所得混合物攪拌2小時。再將所得反應混合物注入 丙酮約10, 000份中,將沉澱之白色固體經過濾而取出。所 取出之固體以丙酮清洗後進行減壓乾燥,得到乙烯_乙烯基 321925 40 201041645 環己烷共聚物300份。所得共聚物之[π ]為0. 48dl/g ; Μη 為 15, 600 ; Mw/Mn 為 2 ; Tm 為 57°C ; Tg 為-28°C ;源自乙 烯基環己烷之構造單元的含有率為13莫耳%。所得共聚物 稱為(B-1 a)。 〈成分(B)之製造例2> 於(B-la)lOO份中添加馬來酸酐0.4份以及1,3-雙(第 三丁基過氧化異丙基)苯0.04份,將所得混合物充分攪 拌,進行預備混合。將所得混合物從雙軸擠壓機之供給口 供給並進行熔融混煉。同時,熔融混煉分成前半段與後半 段之二階段進行,分別將擠壓機之進行熔融混煉的部分之 前半部分的溫度設為180°C,而後半部分的溫度設為260 °C,然後進行熔融混煉。其結果,得到經由使乙烯-乙烯基 環己烷共聚物與馬來酸酐接枝聚合而得的共聚物。所得共 聚物之馬來酸接枝量為0. 2%;MFR為180g/10分鐘(190°C ; 荷重:2. 16kgf)。所得共聚物稱為(B-2a)。 〈成分(B)之製造例3> 〈成分(B)之製造例1>中,除了使用丙烯取代乙烯之 外,進行與〈成分(B)之製造例1>之相同操作,得到丙烯-乙烯基環己烷共聚物。該共聚物稱為(B-lb)。 〈成分(B)之製造例4> 〈成分(B)之製造例2>中,除了使用(B-lb)取代(B-la) 之外,進行與〈成分(B)之製造例2>之相同操作,得到經由 使丙烯-乙烯基環己烷共聚物與馬來酸酐接枝聚合而得的 共聚物。該共聚物稱為(B-2b)。 41 321925 201041645 、 實施例1 將桌上变捏合機ρβνυ型(購自入江商會)的缸筒溫 度設為97。(:後’在該缸筒内投入(B-2a)110份,並以每分 . 鐘順時鐘旋轉1〇次’同時使(B-2a)在10分鐘内溶融。然 後,投入固形分量成為10份之量的(A-1),以每分鐘旋轉 60次並不時地打開玻璃蓋,進行3分鐘之混煉乳化。接著, 投入9(TC之溫水11 〇份,得到水性乳劑。 所得水性乳劑中之分散質的體積基準中位數直徑為 〇 1.3从m。該體積基準中位數直禋係經由雷射繞射/散射式粒 徑分佈測定裝置(堀場製作所(股)製造)測定。 由該水性乳劑所得之硬化物之接著性係以下述試驗方 法(棋盤格膠帶剝離法)評估。將結果呈示於表2。 此外,將所得水性乳劑在無攪拌下保存3日後,其外 觀以及均句性並無變化,其靜置安定性亦佳。 〈接著性之試驗方法〉 〇 =厚度3_之聚㈣板的表面以異丙醇清洗後,使用 乳劑塗佈在聚丙婦板上,使乾燥後得到之硬 r燥5Ί」、1G//m。。以熱風乾燥機在8(rc下使所得塗膜 硬^物Γ &,再於7GC之烤箱巾加熱乾燥 3 0分鐘而得到 將厚度3mm之聚丙烯板的 塗佈棒將水性乳佈面以異丙醇清洗後,使用 化物膜厚成為10// ^ i烯板上,使乾燥後得到之硬 乾燥5八於’ m以”,、風乾燥機在8(TC下使所得塗膜 、 ;90。之烤箱中加熱乾燥 30分鐘而得到 321925 42 201041645 硬化物。 以JIS-K5400(棋盤格膠帶剝離法試驗)為基準,對於 所得之各硬化物施加空隙間隔為lmm之棋盤格狀的割痕 • 後,再於其上貼附透明膠帶。經過1至2分鐘後,提著膠 • 帶一角以直角撕剝,依據下述評估基準進行接著性的評估。 ◎:毫無觀察到硬化物的剝離。 〇:雖觀察到硬化物的剝離,惟剝離面積未達正方形面積 的 40%。 〇 X :觀察到硬化物的剝離,且剝離面積為正方形面積的40% 以上。 實施例2 將以相同方向旋轉之嚙合式雙軸螺桿擠壓機(日本製 鋼所(股)製造:ΤΕΧ30Φ ; L/D=30)之缸筒溫度設為110°C 後,從該播壓機之給料斗以螺桿之旋轉數35Orpm將 (B-2a)110份連續地供給至缸筒内。從該擠壓機之設於通 Q 氣孔(vent)部的供給口,一面以齒輪幫浦加壓,一面連續 地供給固形分量成為10份之量的(A-1),然後將(B-2a)及 (A-1)連續地擠出並同時混合,得到乳白色之水性乳劑。 所得水性乳劑中之分散質的體積基準中位數直徑為 1. 0 Am。該體積基準中位數直徑係經由雷射繞射/散射式粒 徑分佈測定裝置(堀場製作所(股)製造)測定。 由該水性乳劑所得之硬化物之接著性係以實施例1所 記載之試驗方法評估。將結果呈示於表2。 實施例3 43 321925 201041645 、 實施例1中,除了以(A-2)取代(A-l)之外,進行與實 施例1之相同操作,得到乳白色之水性乳劑。 將所得水性乳劑在無攪拌下保存3日後,其外觀以及 均勻性並無變化,其靜置安定性亦佳。 . 將所得水性乳劑中之分散質的體積基準中位數直徑以 及由該水性乳劑所得硬化物之接著性的評估結果呈示於表 2 ° 實施例4 ^ 實施例1中,除了以(A-3)取代(A-1)之外,進行與實 施例1之相同操作,得到乳白色之水性乳劑。 將所得水性乳劑在無攪拌下保存3日後,其外觀以及 均勻性並無變化,其靜置安定性亦佳。 將所得水性乳劑中之分散質的體積基準中位數直徑以 及由該水性乳劑所得硬化物之接著性的評估結果呈示於表 2 ° Q 實施例5 實施例1中,除了以(A-4)取代(A-1)之外,進行與實 施例1之相同操作,得到乳白色之水性乳劑。 將所得水性乳劑在無攪拌下保存3日後,其外觀以及 均勻性並無變化,其靜置安定性亦佳。 將所得水性乳劑中之分散質的體積基準中位數直徑以 及由該水性乳劑所得硬化物之接著性的評估結果呈示於表 2。 44 321925 201041645 ο(b) The sample obtained in (a) was cooled from 200 ° C to -100 ° C at 10 ° C / min, and maintained at -100 ° C for 10 minutes. (c) The sample obtained in (b) was heated from -100 ° C to 200 ° C at 10 ° C / min. The single system of the derived structural unit (al) is made of acrylic acid (Mitsubishi Chemical Co., Ltd., hereinafter referred to as AA); the single system of the derived structural unit (a2) is used ^ N,N-diamine-based methacrylate Ester (manufactured by Sanyo Chemical Industry Co., Ltd., hereinafter referred to as DMA); the single system of the derivatized structural unit (bl) uses decyl decyl acrylate (Mitsubishi snail (manufactured by Miki), hereinafter referred to as 匪A), methyl Lauryl acrylate (Mitsubishi snail (manufactured by the company), hereinafter referred to as LMA) and decyl decyl acrylate (Mitsubishi snail (manufactured), hereinafter referred to as TDMA); derived structural unit (b3) single system use 2-Methyl propylene methoxyethyl succinate (manufactured by Kyoeisha Chemical Co., Ltd., hereinafter abbreviated as H0-MS) to produce the q component (A). In addition, "parts" and "Γ" in the following examples are based on the weight limit. <Production Example 1 of the component (A)> AA 24. 5 parts (42. 3 molar ratio), HO -MS 22. 5 parts (12. 2 mole ratio), DMA 28. 0 parts (22. 2 mole ratio), MM 15. 0 parts (18.6 mole ratio), LMA 3. 8 parts (1.8 Mohrby) and TDMA 6.2 parts (2.9 mole ratio) are mixed at 10 to 30 ° C to prepare 100 parts of the monomer mixture. Here, "Morby" means the total number of moles of the above monomers. The number of moles of each monomer at 100. 38 321925 201041645 150 parts of isopropanol and ions were fed into a 1 L reactor equipped with a heating jacket with a condenser, a nitrogen inlet tube, a stirrer, and a dropping funnel. 100 parts of water were exchanged, and while the obtained solution was stirred, the internal temperature was adjusted to 80 ° C. After the gas in the reaction vessel was replaced with nitrogen, 20 parts of the monomer mixture prepared above was added at once. 2 parts of 2, 2'-azobisisobutyronitrile as a polymerization initiator, and the resulting mixture was stirred at 80 ° C. Then, at 80 ° C, the fee was charged.份份份。 2, 2'-azobisisobutyronitrile 0. 15 parts, every 1 hour, from the beginning of the dropwise addition, the mixture of the mixture was added to the mixture. The mixture was added in four portions. The resulting mixture was stirred at the same temperature for 3 hours. The resulting reaction was mixed and heated to a boiling degree to distill off the isopropanol. After the internal temperature of the obtained concentrate was cooled to 50 ° C, the mixture was mixed. % of aqueous ammonia solution 39. 9 parts (81. 7 mole ratio, the molar ratio of ammonia when the total number of moles of the above monomers is 100), to obtain acrylic acid containing a polymer hydrophilic ratio of 9.40. A viscous emulsifier having a degree of neutralization of 150%, and a yield of 90%. The obtained emulsifier is referred to as hydrazine (A-1). The results are shown in Table 1. <Production Examples 2 to 4 of Component (A) The same operation as in Production Example 1 of the above component (A) was carried out except that the type and amount of the monomer to be used and the amount of use of the ammonia were changed as shown in Table 1, and a viscous emulsified product containing an acrylic resin was obtained. The obtained emulsifiers are referred to as (A-2), (A-3) and (A-4), respectively, and the results are presented in the table. 39 321925 201041645, [Table 1] Production Example 1 Production Example 2 Production Example 3 Production Example 4 (A-1) (A-2) (A-3) (A-4) Parts Mo Erbi Mo Mobi Ear ratio molar ratio monomer AA 24. 5 42. 3 34. 5 54. 5 34. 5 54. 5 49. 5 69. 3 H0-MS 22. 5 12. 2 22. 5 11. 1 22. 5 11. 1 22. 5 9. 9 DMA 28. 0 22. 2 18. 0 13. 0 18. 0 13. 0 3. 0 1.9 ΜΜΛ 15. 0 18. 6 15.0 17.1 15. 0 17. 1 15. 0 15· 1 LMA 3. 8 1.8 3.8 1.6 3. 8 1.6 3. 8 1.4 TDMA 6. 2 2. 9 6. 2 2. 7 6. 2 2. 7 6. 2 2.4 Total 100 100 100 100 100 100 100 100 NHa usage (Mo Erbi) 81.7 98.4 78. 7 95 • 0 NH3 application (3⁄4) 150 150 120 120 Monomer hydrophilic ratio 9.40 9. 91 9. 91 10. 68 <Manufacture of component (B) 1> After replacing the internal gas of the stainless steel reactor with argon gas, 386 parts of vinylcyclohexane and 3640 parts of toluene were charged therein. After the resulting mixture was warmed to 50 C, ethylene was fed into the reactor while being pressurized at a pressure of 66 MPa. Further, a toluene solution of triisobutylammonium (manufactured by Tosoh Akzo Corporation; 20% by weight) was added, and then, by using diethyl decyl (tetramethylcyclopentane) a solution of a dienyl)(3_t-butyl-5-fluorenyl-2-phenoxy)titanium dichloride 001 solution dissolved in 87 parts of dehydrated toluene, and by dimethylanilide Tetrakis(pentafluorophenyl)borate 0.03 parts of a solution obtained by dissolving 122 parts of dehydrated toluene was fed into the reactor. The resulting mixture was stirred for 2 hours. The resulting reaction mixture was poured into about 10,000 parts of acetone, and the precipitated white solid was taken out by filtration. The solid which was taken out was washed with acetone and dried under reduced pressure to give 300 parts of ethylene-vinyl 321925 40 201041645 cyclohexane copolymer. The obtained copolymer had [π] of 0.48 dl/g; Μη was 15,600; Mw/Mn was 2; Tm was 57 ° C; Tg was -28 ° C; and structural units derived from vinylcyclohexane The content rate was 13 mol%. The resulting copolymer is referred to as (B-1 a). <Production Example 2 of Component (B)> 0.4 parts of maleic anhydride and 0.04 parts of 1,3-bis(t-butylperoxyisopropyl)benzene were added to 100 parts of (B-la), and the obtained mixture was sufficiently Stir and prepare for mixing. The resulting mixture was supplied from a supply port of a twin-screw extruder and melt-kneaded. At the same time, the melt-kneading is carried out in two stages of the first half and the second half, and the temperature of the first half of the portion in which the extruder is melt-kneaded is set to 180 ° C, and the temperature of the second half is set to 260 ° C. Then, melt kneading is carried out. As a result, a copolymer obtained by graft-polymerizing an ethylene-vinylcyclohexane copolymer with maleic anhydride was obtained. 2%; MFR was 180 g/10 min (190 ° C; load: 2.16 kgf). The resulting copolymer is referred to as (B-2a). <Production Example 3 of the component (B)> In the production example 1 of the component (B), the same operation as in the production example 1 of the component (B) was carried out, except that propylene was used instead of ethylene, to obtain propylene-ethylene. A cyclohexane copolymer. This copolymer is referred to as (B-lb). <Production Example 4 of the component (B)> In the production example 2 of the component (B), the production example 2 of the component (B) is carried out except that the (B-lb) substitution (B-la) is used. In the same manner, a copolymer obtained by graft-polymerizing a propylene-vinylcyclohexane copolymer with maleic anhydride was obtained. This copolymer is referred to as (B-2b). 41 321925 201041645, Example 1 The cylinder temperature of the table kneading machine ρβνυ type (purchased from the Jinjiang Chamber of Commerce) was set to 97. (: After 'injection (B-2a) 110 parts in the cylinder, and rotate clockwise by 1 minute per minute.] (B-2a) melts in 10 minutes. Then, the solid component becomes The amount of (A-1) was 10 parts per minute, and the glass lid was opened from time to time, and the mixture was emulsified for 3 minutes. Then, 9 parts of warm water of TC was added to obtain an aqueous emulsion. The volume-based median diameter of the dispersoid in the obtained aqueous emulsion is 〇1.3 from m. The volume-based median direct enthalpy is produced by a laser diffraction/scattering particle size distribution measuring device (manufactured by Horiba, Ltd.) The adhesion of the cured product obtained from the aqueous emulsion was evaluated by the following test method (checkerboard tape peeling method). The results are shown in Table 2. Further, the appearance of the obtained aqueous emulsion after storage for 3 days without stirring was observed. There is no change in the uniformity of the sentence, and the static stability is also good. <Test method for adhesion> 〇 = thickness 3_ The surface of the plate (4) is washed with isopropyl alcohol and then coated on the polypropylene board with an emulsion. , to make the hard r after drying, 5 Ί", 1G / / m. The air dryer dries the obtained coating film at 8 (rc), and then dried and dried in a 7GC oven towel for 30 minutes to obtain a coating rod of a polypropylene plate having a thickness of 3 mm. After the cleaning of the propanol, the thickness of the compound film was changed to 10//^, and the hardened film was dried to a hardness of 5 Å to 'm", and the air dryer was used to obtain the coating film at 8 (TC). The oven was heated and dried for 30 minutes to obtain a cured product of 321925 42 201041645. Based on JIS-K5400 (checkerboard tape peeling test), a checker-shaped cut with a gap interval of 1 mm was applied to each of the obtained cured products. After that, the scotch tape was attached thereto. After 1 to 2 minutes, the glue was attached. • The tape was peeled off at a right angle, and the adhesion was evaluated according to the following evaluation criteria. ◎: No peeling of the cured product was observed. 〇: Although peeling of the cured product was observed, the peeling area was less than 40% of the square area. 〇X: peeling of the cured product was observed, and the peeling area was 40% or more of the square area. Example 2 will be in the same direction Rotating meshing twin screw extruder (Day Steelmaking (stock) manufacturing: ΤΕΧ30Φ; L/D=30) After the cylinder temperature is set to 110 °C, 110 parts of (B-2a) are continuously and continuously from the feeding hopper of the weaving machine at a screw rotation number of 35Orpm. It is supplied to the inside of the cylinder. From the supply port of the venting portion of the venting portion of the ejector, the gear member is pressurized, and the solid component is continuously supplied in an amount of 10 parts (A-1). And the volume-based median diameter of the dispersion of the obtained aqueous emulsion is 1. 0 Am. The volume-based median diameter was measured by a laser diffraction/scattering particle size distribution measuring apparatus (manufactured by Horiba, Ltd.). The adhesion of the cured product obtained from the aqueous emulsion was evaluated by the test method described in Example 1. The results are presented in Table 2. Example 3 43 321925 201041645 In Example 1, except that (A-1) was substituted for (A-1), the same operation as in Example 1 was carried out to obtain a milky white aqueous emulsion. After the obtained aqueous emulsion was stored for 3 days without stirring, its appearance and uniformity did not change, and the standing stability was also good. The evaluation results of the volume-based median diameter of the dispersoid in the obtained aqueous emulsion and the adhesion of the cured product obtained from the aqueous emulsion are shown in Table 2 ° Example 4 ^ Example 1, except (A-3 The same operation as in Example 1 was carried out, except for (A-1), to obtain a milky white aqueous emulsion. After the obtained aqueous emulsion was stored for 3 days without stirring, its appearance and uniformity did not change, and the standing stability was also good. The results of the evaluation of the volume-based median diameter of the dispersoid in the obtained aqueous emulsion and the adhesion of the cured product obtained from the aqueous emulsion are shown in Table 2 ° Q Example 5, except that (A-4) The same operation as in Example 1 was carried out, except for (A-1), to obtain a milky white aqueous emulsion. After the obtained aqueous emulsion was stored for 3 days without stirring, its appearance and uniformity did not change, and the standing stability was also good. The results of the evaluation of the volume-based median diameter of the dispersoid in the obtained aqueous emulsion and the adhesion of the cured product obtained from the aqueous emulsion are shown in Table 2. 44 321925 201041645 ο
實施例6 實施例2中’除了使用(B_la)取代(B_2a)之外, • 與實施例2之相同操作,藉此而得到水性乳劑。 實施例7 ,進 ^例2中’除了使用(B-lb)取代(B-2a)之外 與實施例2之相同操作,藉此而得到水性乳劑。 實施例8 實施例2中,除了使用(B_2b)取代(B—2a)之外 與實施例2之相同操作,藉此而得到水性乳劑。 [產業之可利用性] 本發明之水性礼劑可賦予與聚丙婦等難以與塗 它材料接著的基材之接著性優異的硬化物。 【圖式簡單說明】 無0 321925 45 201041645 【主要元件符號說明】Example 6 In Example 2, except that (B_la) was substituted (B_2a), the same operation as in Example 2 was carried out, whereby an aqueous emulsion was obtained. In Example 7, the same procedure as in Example 2 was carried out except that (B-lb) was used instead of (B-2a), whereby an aqueous emulsion was obtained. Example 8 In Example 2, an aqueous emulsion was obtained by the same operation as in Example 2 except that (B_2b) was used instead of (B-2a). [Industrial Applicability] The aqueous ritual agent of the present invention can provide a cured product which is excellent in adhesion to a substrate which is difficult to adhere to a material such as a polypropylene material. [Simple diagram description] No 0 321925 45 201041645 [Main component symbol description]
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