KR100513122B1 - Water-based polyurethane resine containing a ring structure and method for preparing the same - Google Patents
Water-based polyurethane resine containing a ring structure and method for preparing the same Download PDFInfo
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- KR100513122B1 KR100513122B1 KR10-2003-0046790A KR20030046790A KR100513122B1 KR 100513122 B1 KR100513122 B1 KR 100513122B1 KR 20030046790 A KR20030046790 A KR 20030046790A KR 100513122 B1 KR100513122 B1 KR 100513122B1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/0838—Manufacture of polymers in the presence of non-reactive compounds
- C08G18/0842—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents
- C08G18/0861—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers
- C08G18/0866—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers the dispersing or dispersed phase being an aqueous medium
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
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Abstract
본 발명은 환형 구조를 갖는 수성 폴리우레탄 수지 및 이의 제조방법에 관한 것으로, 좀 더 구체적으로, 수성 폴리우레탄 수지의 제조에 있어서, 폴리올 및 분자내 카르복실기를 갖는 단쇄 글리콜을 디이소시아네이트와 반응시켜 프리폴리머를 제조하고, 상기 프리폴리머를 유기용매로 완전 용해시킨 후, 분자내 환형 구조를 갖는 아민으로 중화하여 자기 유화형 프리폴리머를 제조하며, 상기 자기 유화형 프리폴리머에 물을 가해 유화시키고 분자내에 최소한 두개 이상의 일차 아민기를 갖는 아민으로 쇄 연장 반응을 수행한 후, 반응물내의 유기 용매를 제거하는 단계를 포함하며, 여기서 상기 폴리올 1몰에 대하여 상기 분자내에 카르복실기를 갖는 단쇄 글리콜의 함량은 0.05 내지 2.0몰이고, 상기 디이소시아네이트의 함량은 1.5 내지 4.0몰이며, 상기 분자내 환형 구조를 갖는 아민은 0.8 내지 1.1몰인 수성 폴리우레탄 수지의 제조 방법 및 상기 방법으로 제조된 수성 폴리우레탄 수지에 관한 것이다. 본 발명에 따른 수성 폴리우레탄 수지는 기계적 강도, 내열특성, 및 수분산 안정성이 우수하며, 특히 아민 등의 냄새가 없는 장점이 있다.The present invention relates to an aqueous polyurethane resin having a cyclic structure and a method for preparing the same. More specifically, in the preparation of the aqueous polyurethane resin, a prepolymer is prepared by reacting a polyol and a short chain glycol having an intramolecular carboxyl group with a diisocyanate. And completely dissolve the prepolymer in an organic solvent, and then neutralize it with an amine having an intramolecular cyclic structure to prepare a self-emulsifying prepolymer, emulsify the water by adding water to the self-emulsifying prepolymer, and at least two or more primary amines in the molecule. Performing a chain extension reaction with an amine having a group, and then removing the organic solvent in the reactant, wherein the content of the short chain glycol having a carboxyl group in the molecule is 0.05 to 2.0 moles per mole of the polyol, and the di The content of isocyanate is 1.5 to 4.0 moles, the minute Amine having the annular structure is directed to an aqueous polyurethane resin prepared by using 0.8 to 1.1 mole process for producing a water-based polyurethane resin and the above-described way. The aqueous polyurethane resin according to the present invention is excellent in mechanical strength, heat resistance, and water dispersion stability, and especially has no merit such as amine.
Description
본 발명은 환형 구조를 갖는 수성 폴리우레탄 수지 및 이의 제조 방법에 관한 것으로, 좀 더 구체적으로, 프리폴리머 제조시 분자내에 카르복실기를 갖는 단쇄 글리콜을 사용하며, 분자내 환형 구조를 갖는 아민으로 상기 프리폴리머를 중화하여 자기 유화형 프리폴리머를 제조하여 피착재에 대한 접착력, 기계적 강도, 내열특성, 및 수분산 안정성이 우수하고 아민 등의 냄새가 없는 수성 폴리우레탄 수지에 관한 것이다. The present invention relates to an aqueous polyurethane resin having a cyclic structure and a method for preparing the same, and more particularly, to use a short chain glycol having a carboxyl group in a molecule when preparing a prepolymer, and to neutralize the prepolymer with an amine having an intramolecular cyclic structure. By preparing a self-emulsifying prepolymer, the present invention relates to an aqueous polyurethane resin having excellent adhesion to mechanical materials, mechanical strength, heat resistance, and water dispersion stability, and having no odor such as amine.
종래의 접착제는 유기용매가 다량 함유되었지만, 최근에는 환경 보호, 자원 절약, 안전성 등의 사회적 요구에 의하여 수성 폴리우레탄계 수지에 대한 관심 및 개발이 높아가고 있다. Conventional adhesives contain a large amount of organic solvents, but in recent years, interest and development of water-based polyurethane resins are increasing due to social demands such as environmental protection, resource saving, and safety.
수성 폴리우레탄 수지의 제조방법으로는, 다량의 유화제를 사용하여 소수성 폴리우레탄을 강제적으로 분산시키는 방법과 폴리우레탄 골격 중에 친수성기를 도입하여 자기 유화형 수지를 제조한 후 수중에서 분산시키는 방법(미국특허 제4,066,591호, 미국특허 제4,147,679호, 미국특허 제4,857,565호, 및 미국특허 제5,552,496호)등이 있으며 유화제를 사용하는 방법은 수지 자체의 물성이 만족스럽지 않을 뿐만 아니라 환경오염을 일으킬 수 있어, 자기유화형 수성 폴리우레탄의 연구가 활발히 진행되고 있다. As a method of producing an aqueous polyurethane resin, a method of forcibly dispersing a hydrophobic polyurethane using a large amount of emulsifier and a method of introducing a hydrophilic group into a polyurethane skeleton to prepare a self-emulsifying resin and then dispersing it in water (US Patent 4,066,591, U.S. Patent 4,147,679, U.S. Patent 4,857,565, and U.S. Patent 5,552,496) and the method of using an emulsifier not only satisfies the physical properties of the resin itself but also may cause environmental pollution. The study of emulsion type water-based polyurethane is actively progressing.
수성 폴리우레탄 수지는, 각종 피착재에 대한 접착력, 수지자체의 내수성, 기계적 강도, 내열성, 내굴곡성, 및 수분산 안정성등의 제반 물성이 동시에 우수하여야 하고 잔류 용매가 아주 적거나 없어서 사용시 냄새가 나지 않아야 하나, 아직 상기의 특성을 동시에 만족시키는 제품이 개발되지 않았다. Water-based polyurethane resin must have excellent physical properties such as adhesion to various adherends, water resistance of the resin itself, mechanical strength, heat resistance, flex resistance, and water dispersion stability, and have little or no residual solvent, resulting in no smell. Should not, yet a product that satisfies the above characteristics has not been developed yet.
이에 본 발명에서는 상술한 문제점을 해결하기 위하여 광범위한 연구를 거듭한 결과, 프리폴리머 제조시 분자내에 카르복실기를 갖는 단쇄 글리콜을 사용하고, 상기 프리폴리머를 분자내 환형구조를 갖는 아민으로 중화시켜 각종 피착재에 대한 접착력, 내수성, 내굴곡성, 및 수분산 안정성이 동시에 우수하고 분자내에 환형구조를 가지고 있어서 내열특성 및 기계적 강도가 우수할 뿐만 아니라 잔류 유기용매 또는 아민 냄새가 나지 않는 수성 폴리우레탄 수지를 제조하였고, 본 발명은 이를 기초로 완성되었다.Therefore, in the present invention, extensive research has been conducted to solve the above-mentioned problems. As a result, when preparing a prepolymer, short chain glycol having a carboxyl group in a molecule is used, and the prepolymer is neutralized with an amine having an intramolecular cyclic structure. Adhesion, water resistance, bending resistance, and water dispersion stability are excellent at the same time, and have a ring-shaped structure in the molecule, which is excellent in heat resistance and mechanical strength, and does not produce residual organic solvent or amine odor. The invention has been completed based on this.
따라서, 본 발명의 목적은 접착력, 내수성, 내굴곡성, 수분산 안정성 및 내용제성이 우수할 뿐만 아니라, 내열특성 및 기계적 강도가 우수하고 잔류 유기 용매 또는 아민 냄새가 나지 않는 환형 구조를 갖는 수성 폴리우레탄 수지를 제조하는 방법을 제공하는데 있다. Accordingly, an object of the present invention is an aqueous polyurethane having a cyclic structure that is excellent in adhesion, water resistance, flex resistance, water dispersion stability, and solvent resistance, as well as excellent in heat resistance and mechanical strength, and does not smell of residual organic solvent or amine. It is to provide a method for producing a resin.
본 발명의 다른 목적은 상기 방법으로 제조된 환형 구조를 갖는 수성 폴리우레탄 수지를 제공하는데 있다.Another object of the present invention is to provide an aqueous polyurethane resin having a cyclic structure produced by the above method.
상기 본 발명의 목적을 달성하기 위한 환형 구조를 갖는 수성 폴리우레탄 수지의 제조 방법은 수성 폴리우레탄 수지의 제조에 있어서, 폴리올 및 분자내 카르복실기를 갖는 단쇄 글리콜을 디이소시아네이트와 반응시켜 프리폴리머를 제조하고, 상기 프리폴리머를 유기용매로 완전 용해시킨 후, 분자내 환형 구조를 갖는 아민으로 중화하여 자기 유화형 프리폴리머를 제조하며, 상기 자기 유화형 프리폴리머에 물을 가해 유화시키고 분자내에 최소한 두개 이상의 일차 아민기를 갖는 아민으로 쇄 연장 반응을 수행한 후, 반응물내의 유기 용매를 제거하는 단계를 포함하며, 여기서 상기 폴리올 1몰에 대하여 상기 분자내에 카르복실기를 갖는 단쇄 글리콜의 함량은 0.05 내지 2.0몰이고, 상기 디이소시아네이트의 함량은 1.5 내지 4.0몰이며, 상기 분자내 환형 구조를 갖는 아민은 0.8 내지 1.1몰인 것으로 구성된다.The method for producing an aqueous polyurethane resin having a cyclic structure for achieving the object of the present invention, in the preparation of an aqueous polyurethane resin, to prepare a prepolymer by reacting a short chain glycol having a polyol and intramolecular carboxyl groups with diisocyanate, After completely dissolving the prepolymer with an organic solvent, it is neutralized with an amine having an intramolecular cyclic structure to prepare a self-emulsifying prepolymer. The water is emulsified by adding water to the self-emulsifying prepolymer, and an amine having at least two primary amine groups in the molecule. After performing the chain extension reaction, the step of removing the organic solvent in the reactant, wherein the content of the short chain glycol having a carboxyl group in the molecule with respect to 1 mol of the polyol is 0.05 to 2.0 mol, the content of the diisocyanate Is 1.5 to 4.0 mol, the intramolecular cyclic The amine having a structure consists of 0.8 to 1.1 moles.
본 발명의 다른 목적을 달성하기 위한 환형 구조를 갖는 수성 폴리우레탄 수지는 상기 방법으로 제조된다.An aqueous polyurethane resin having a cyclic structure for achieving another object of the present invention is produced by the above method.
이하 본 발명을 좀 더 구체적으로 설명하면 다음과 같다.Hereinafter, the present invention will be described in more detail.
전술한 바와 같이, 본 발명에 의한 수성 폴리우레탄 수지의 제조방법은 수성 폴리우레탄 수지의 제조에 있어서, 폴리올 및 분자내 카르복실기를 갖는 단쇄 글리콜을 디이소시아네이트와 반응시켜 분자의 양쪽 말단에 이소시아네이트기를 갖는 프리폴리머를 얻는다. As described above, the method for producing an aqueous polyurethane resin according to the present invention is a prepolymer having an isocyanate group at both ends of a molecule by reacting a polyol and short-chain glycol having an intramolecular carboxyl group with diisocyanate in the preparation of the aqueous polyurethane resin. Get
본 발명에 사용되는 폴리올은 분자의 양 말단에 적어도 2개의 일차수산기를 갖는 폴리에스터계 폴리올로서 이의 수평균 분자량은 200 내지 10,000인 것을 사용하며, 바람직하게는 500 내지 3,000인 것을 사용한다.The polyol used in the present invention is a polyester-based polyol having at least two primary hydroxyl groups at both ends of the molecule, and has a number average molecular weight of 200 to 10,000, preferably 500 to 3,000.
상기 폴리에스터계 폴리올은 이염기산과 이가알콜의 축합반응을 통해 얻게 되며 상기 이염기산은 아디프산, 아젤라산, 및 숙신산으로부터 단독 또는 두 종류 이상을 혼합하여 사용할 수 있으나 아디프산을 단독으로 사용하는 것이 바람직하다. 상기 이가알콜은 에틸렌 글리콜, 1,3-프로판디올, 1,4-부탄디올, 1,6-헥산디올, 네오펜틸글리콜, 2-메틸프로판디올, 1,4-시클로헥산디메탄올, 및 비스페놀 A로 부터 단독 또는 두 종류 이상을 혼합하여 사용할 수 있으나 1,4-부탄디올 및 1,6-헥산디올을 단독 또는 혼합하여 사용하는 것이 바람직하다.The polyester-based polyol is obtained through the condensation reaction of dibasic acid and dihydric alcohol, and the dibasic acid may be used alone or in combination of two or more kinds from adipic acid, azelaic acid, and succinic acid, but adipic acid is used alone. It is desirable to. The dihydric alcohol is ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,6-hexanediol, neopentylglycol, 2-methylpropanediol, 1,4-cyclohexanedimethanol, and bisphenol A It can be used alone or in combination of two or more, but it is preferable to use 1,4-butanediol and 1,6-hexanediol alone or mixed.
본 발명에 사용되는 분자내에 카르복실기를 갖는 단쇄 글리콜은 2,2-디메틸올 프로피온산(DMPA), 또는 2,2-디메틸올 부탄산(DMBA)을 사용하며, 바람직하게는 2,2-디메틸올 부탄산(DMBA)를 사용한다. 이의 사용량은 상기 폴리올 1몰에 대하여 0.05 내지 2.0몰의 범위에서 사용하며 0.05몰 미만이면 수분산 안정성이 불량하고 2.0몰을 초과하면 수분산된 수지의 점도가 지나치게 높고 내수성이 불량하다.The short-chain glycol having a carboxyl group in the molecule used in the present invention uses 2,2-dimethylol propionic acid (DMPA), or 2,2-dimethylol butanoic acid (DMBA), preferably 2,2-dimethylol moiety. Carbonic acid (DMBA) is used. Its amount is used in the range of 0.05 to 2.0 moles per 1 mole of the polyol, if less than 0.05 moles of water dispersion stability is poor, if it exceeds 2.0 moles the viscosity of the water-dispersed resin is too high and water resistance is poor.
본 발명에서 사용되는 디이소시아네이트는 지방족, 지환족, 방향족 모두 사용 가능하나, 내굴곡성, 내황변성, 및 수분산 안정성의 제반 물성을 만족하기 위해서는 지방족 및 지환족 디이소시아네이트를 단독 또는 두 종류 이상을 혼합하여 사용한다. 이의 예로는 이소포론 디이소시아네이트(IPDI), 1,6-헥사메틸렌 디이소시아네이트(1,6-HDI), 4,4'-메틸렌비스시클로헥산 디이소시아네이트(4-4'-H12MDI), 1,3-자일렌 디이소시아네이트(1,3-XDI), 및/또는 1,3-테트라메틸자일렌 디이소시아네이트(1,3-TMXDI)가 있다. The diisocyanate used in the present invention can be used for both aliphatic, cycloaliphatic, and aromatic, but in order to satisfy various physical properties of flex resistance, yellowing resistance, and water dispersion stability, aliphatic and cycloaliphatic diisocyanates may be used alone or in combination of two or more. Use it. Examples thereof include isophorone diisocyanate (IPDI), 1,6-hexamethylene diisocyanate (1,6-HDI), 4,4'-methylenebiscyclohexane diisocyanate (4-4'-H12MDI), 1,3 Xylene diisocyanate (1,3-XDI), and / or 1,3-tetramethylxylene diisocyanate (1,3-TMXDI).
상기 디이소시아네이트의 사용량은 폴리올 1몰에 대하여 1.5 내지 4.0몰의 범위이며, 사용량이 1.5몰 미만이면 프리폴리머의 점도가 지나치게 높아 수분산이 어려울 뿐만 아니라 최종 수지의 기계적 강도가 취약하고 4.0몰을 초과하면 수분산 안정성 및 최종수지의 내굴곡성이 저하된다.The amount of diisocyanate used is in the range of 1.5 to 4.0 moles per 1 mole of polyol. When the amount of diisocyanate is less than 1.5 moles, the viscosity of the prepolymer is too high, making it difficult to disperse water, and the mechanical strength of the final resin is weak and exceeds 4.0 moles. The dispersion stability and the bending resistance of the final resin are lowered.
본 발명에서는 상기 프리폴리머를 분자내에 환형 구조를 가지는 아민으로 중화시켜 자기 유화형 프리폴리머를 제조한다. In the present invention, a self-emulsifying prepolymer is prepared by neutralizing the prepolymer with an amine having a cyclic structure in the molecule.
상기 분자 내에 환형구조를 갖는 아민으로는 2-아미노피리미딘, 2-아미노피리딘, 2-아미노-4-히드록시-6-메틸피리미딘, 아미노피라진, 2-아미노-4,6-디메톡시피리미딘, 2-아미노-2-시클로헥센-1-온, 2-아미노-2-티아졸, 2-(2-아미노에틸)피리딘, 6-메틸이소시토신, 2-아미노-4-피리돈, 6-페닐이소시토신, 6-메틸-2-아미노-4-피리미딘, 2-아미노-4,6-디메톡시-1,3,5-트리아진, 2-아미노-4-디메톡시아미노-6-메틸-1,3,5-티아진, 2-아미노-4,6-디메틸-1,3,5-트리아진, 2-아미노-4-에톡시-6-메틸-1,3,5-트리아진, 2-아미노-4-에틸-6-메톡시-1,3,5-트리아진, 2-아미노-4-메톡시-6-메틸-1,3,5-트리아진 및 2-아미노-4-메틸-6-페닐-1,3,5-트리아진으로부터 단독 또는 둘 이상을 혼합하여 사용하며 그 사용량은 분자내에 카르복실기를 갖는 단쇄 글리콜(DMPA 또는 DMBA) 1몰에 대하여 0.8 내지 1.1몰의 범위에서 사용한다.Amines having a cyclic structure in the molecule include 2-aminopyrimidine, 2-aminopyridine, 2-amino-4-hydroxy-6-methylpyrimidine, aminopyrazine, 2-amino-4,6-dimethoxypy Limidine, 2-amino-2-cyclohexen-1-one, 2-amino-2-thiazole, 2- (2-aminoethyl) pyridine, 6-methylisocytosine, 2-amino-4-pyridone, 6-phenylisocytosine, 6-methyl-2-amino-4-pyrimidine, 2-amino-4,6-dimethoxy-1,3,5-triazine, 2-amino-4-dimethoxyamino-6 -Methyl-1,3,5-thiazine, 2-amino-4,6-dimethyl-1,3,5-triazine, 2-amino-4-ethoxy-6-methyl-1,3,5- Triazine, 2-amino-4-ethyl-6-methoxy-1,3,5-triazine, 2-amino-4-methoxy-6-methyl-1,3,5-triazine and 2-amino Used alone or in combination of two or more from -4-methyl-6-phenyl-1,3,5-triazine, the amount of use is 0.8 to 1.1 moles per 1 mole of short-chain glycol (DMPA or DMBA) having a carboxyl group in the molecule. In the range of Use.
상기 사용량이 0.8몰 미만이면 수분산 안정성 및 내수성이 부족하고 1.1몰을 초과하면 최종 수성 폴리우레탄 수지의 외관이 불량하다. If the amount of use is less than 0.8 mol, water dispersion stability and water resistance is insufficient, and if the amount exceeds 1.1 mol, the appearance of the final aqueous polyurethane resin is poor.
이렇게 제조된 상기 프리폴리머는 수분산을 용이하게 하기 위하여, 비점이 낮은 유기용매에 완전 용해시킨다. The prepolymer thus prepared is completely dissolved in an organic solvent having a low boiling point in order to facilitate water dispersion.
본 발명에 사용되는 유기용매는 아세톤, 메틸에틸케톤, 시클로헥산온, 메틸이소부틸케톤, N,N-디메틸포름아미드, 및 N,N-디메틸아세트아미드로 부터 단독 또는 두 종류이상을 혼합하여 사용하며, 바람직하게는 아세톤 또는 메틸에틸케톤을 사용한다. 유기 용매의 사용량은 상기 프리폴리머 100중량부에 대하여 60 내지 250중량부가 바람직하다. 상기 사용량이 60중량부 미만이면 프리폴리머 용액의 점도가 너무 높아 수분산이 어렵고, 250중량부를 초과하면 생산성 및 경제성이 좋지 않다.The organic solvent used in the present invention may be used singly or in combination of two or more from acetone, methyl ethyl ketone, cyclohexanone, methyl isobutyl ketone, N, N-dimethylformamide, and N, N-dimethylacetamide. Preferably, acetone or methyl ethyl ketone is used. The amount of the organic solvent is preferably 60 to 250 parts by weight based on 100 parts by weight of the prepolymer. If the amount is less than 60 parts by weight, the viscosity of the prepolymer solution is too high, it is difficult to disperse the water, and if it exceeds 250 parts by weight, productivity and economy are not good.
한편, 본 발명에서는 프리폴리머를 유기용매에 완전 용해시킨 후, 분자내에 에틸렌 옥시드와 프로필렌 옥시드 반복단위구조를 갖는 일차아민을 더욱 첨가시킬 수 있다. 본 발명에 사용되는 분자내에 에틸렌 옥시드와 프로필렌 옥시드 반복단위구조를 갖는 일차아민은 미국 헌츠만사(Huntsman Corporation)의 상품명 제파민(Jeffamine) XTJ-505, XTJ-506, XTJ-507, XTJ-508, 및 XTJ-234 등을 단독 또는 두 종류 이상을 혼합하여 사용하며 상기 폴리올 1몰에 대하여 1몰 이하를 사용한다. 사용량이 1몰을 초과하면 최종 수지의 기계적 강도, 내열특성 및 내수성이 불량한 단점이 있다.Meanwhile, in the present invention, after completely dissolving the prepolymer in an organic solvent, a primary amine having an ethylene oxide and a propylene oxide repeating unit structure in the molecule may be further added. Primary amines having ethylene oxide and propylene oxide repeating unit structures in the molecule used in the present invention are those of Jeffamine XTJ-505, XTJ-506, XTJ-507, XTJ- of Huntsman Corporation, USA. 508, and XTJ-234 or the like are used alone or in combination of two or more thereof, and 1 mol or less is used per 1 mol of the polyol. If the amount of use exceeds 1 mol, there is a disadvantage in that the mechanical strength, heat resistance and water resistance of the final resin are poor.
본 발명에 따르면, 상기 자기유화형 프리폴리머는 물을 가해 유화시키고, 쇄 연장제로 쇄 연장반응을 수행한 후 최종적으로 유기용매를 감압하에서 제거하여 수성 폴리우레탄을 얻게 된다.According to the present invention, the self-emulsifying prepolymer is emulsified by adding water, performing a chain extension reaction with a chain extender, and finally removing the organic solvent under reduced pressure to obtain an aqueous polyurethane.
상기 쇄 연장제는 분자내에 최소한 일차 아민기를 2개 이상 함유하는 폴리아민 화합물을 사용하게 되며, 히드라진, 에틸렌 디아민, 1,3-프로판 디아민, 1,4-부탄 디아민, 1,5-펜탄 디아민, 디에틸렌 트리아민, 트리에틸렌 테트라아민, 디아미노헥산, 이소포론 디아민, 디시클로헥실메틸렌 디아민 및 1,6-헥사메틸렌 디아민으로 부터 단독 또는 둘 이상을 선택하여 혼합하여 사용한다. 상기 쇄 연장제의 사용량은 최종 폴리우레탄 중합체를 제조하기 위해 필용한 이론 당량의 80 내지 100%가 바람직하다.The chain extender is a polyamine compound containing at least two primary amine groups in the molecule, hydrazine, ethylene diamine, 1,3-propane diamine, 1,4-butane diamine, 1,5-pentane diamine, di One or more selected from ethylene triamine, triethylene tetraamine, diaminohexane, isophorone diamine, dicyclohexylmethylene diamine and 1,6-hexamethylene diamine may be used and mixed. The amount of the chain extender used is preferably 80 to 100% of the theoretical equivalent required to prepare the final polyurethane polymer.
이렇게 본 발명에 따라 제조된 수성 폴리우레탄 수지는 수분성 안정성, 내수성, 내굴곡성, 내열성등이 우수하며, 특히 잔류 용매 냄새가 나지 않는다.Thus, the aqueous polyurethane resin prepared according to the present invention is excellent in moisture stability, water resistance, flex resistance, heat resistance and the like, in particular, does not smell of residual solvent.
이하, 하기 실시예를 통하여 본 발명을 좀 더 구체적으로 설명하지만, 하기 예에 본 발명의 범주가 한정되는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to the following examples, but the scope of the present invention is not limited to the following examples.
실시예 1 Example 1
1,6-헥산디올 1500g과 아디프산 1500g으로 부터 제조한 분자량이 2000인 폴리에스테르 폴리올 1몰, 2,2-디메틸올부탄산 0.5몰, 1,6-헥사메틸렌디이소시아네이트 1.5몰, 및 이소포론 디이소시아네이트 1몰을 가하여 90℃에서 3시간 반응시킨 후 0.5몰의 2-아미노피리딘으로 중화하여 분자의 양쪽말단에 이소시아네이트기를 가지는 폴리우레탄 프리폴리머를 제조한다. 1 mol of polyester polyol having a molecular weight of 2000 prepared from 1500 g of 1,6-hexanediol and 1500 g of adipic acid, 0.5 mol of 2,2-dimethylolbutanoic acid, 1.5 mol of 1,6-hexamethylene diisocyanate, and isophorone After adding 1 mole of diisocyanate and reacting at 90 ° C. for 3 hours, neutralization was performed with 0.5 mole of 2-aminopyridine to prepare a polyurethane prepolymer having an isocyanate group at both ends of the molecule.
제조된 폴리우레탄 프리폴리머를 60℃으로 냉각시킨 후 아세톤을 2700g을 가하여 프리폴리머를 완전히 용해하고, 물 3700g을 가하고 1,6-헥사메틸렌 디아민 1몰을 물에 용해시켜 적가한다. 이를 2시간 동안 교반하여 사슬연장 반응을 진행하고 용액중의 아세톤을 감압 증류로 제거하여 수성 폴리우레탄 수지를 제조한다.The prepared polyurethane prepolymer was cooled to 60 ° C., and then 2700 g of acetone was added to completely dissolve the prepolymer. 3700 g of water was added thereto, and 1 mole of 1,6-hexamethylene diamine was added dropwise thereto. This was stirred for 2 hours to proceed the chain extension reaction, and acetone in the solution was removed by distillation under reduced pressure to prepare an aqueous polyurethane resin.
실시예 2 Example 2
1,4-부탄디올 1200g과 아디프산 1500g으로부터 제조한 분자량이 2000인 폴리에스테르 폴리올 1몰, 2,2-디메틸올부탄산 0.5몰, 1,6-헥사메틸렌디이소시아네이트 1.5몰, 및 이소포론 디이소시아네이트 1몰을 가하여 90℃에서 3시간 반응시킨 후 0.5몰의 2-아미노피리딘으로 중화하여 분자의 양쪽말단에 이소시아네이트기를 가지는 폴리우레탄 프리폴리머를 제조한다.1 mol of polyester polyol having a molecular weight of 2000 prepared from 1200 g of 1,4-butanediol and 1500 g of adipic acid, 0.5 mol of 2,2-dimethylolbutanoic acid, 1.5 mol of 1,6-hexamethylene diisocyanate, and isophorone diisocyanate 1 mole was added and reacted at 90 ° C. for 3 hours, followed by neutralization with 0.5 mole of 2-aminopyridine to prepare a polyurethane prepolymer having an isocyanate group at both ends of the molecule.
제조된 폴리우레탄 프리폴리머를 60℃으로 냉각시킨 후 아세톤을 2700g을 가하여 프리폴리머를 완전히 용해한 후, 0.1몰의 제파민(Jeffamine) XTJ507을 물 3700g과 함께 가하고 1,6-헥사메틸렌 디아민 1몰을 물에 용해시켜 적가한다. 이를 2시간 동안 교반하여 사슬연장 반응을 진행하고 용액중의 아세톤을 감압 증류로 제거하여 수성 폴리우레탄 수지를 제조한다.The prepared polyurethane prepolymer was cooled to 60 ° C., and then 2700 g of acetone was added to completely dissolve the prepolymer. Then, 0.1 mol of Jeffamine XTJ507 was added together with 3700 g of water, and 1 mol of 1,6-hexamethylene diamine was added to water. Dissolve and add dropwise. This was stirred for 2 hours to proceed the chain extension reaction, and acetone in the solution was removed by distillation under reduced pressure to prepare an aqueous polyurethane resin.
실시예 3Example 3
1,4-부탄디올 1200g과 아디프산 1500g으로부터 제조한 분자량이 2000인 폴리에스테르 폴리올 1몰, 2,2-디메틸올부탄산 0.7몰, 1,6-헥사메틸렌디이소시아네이트 2.5몰, 및 이소포론 디이소시아네이트 1.5몰을 가하여 90℃에서 3시간 반응시킨 후 0.7몰의 2-아미노피리딘으로 중화하여 분자의 양쪽말단에 이소시아네이트기를 가지는 폴리우레탄 프리폴리머를 제조한다.1 mol of polyester polyol prepared from 1200 g of 1,4-butanediol and 1500 g of adipic acid, 0.7 mol of 2,2-dimethylolbutanoic acid, 2.5 mol of 1,6-hexamethylene diisocyanate, and isophorone diisocyanate After adding 1.5 mol, the mixture was reacted at 90 DEG C for 3 hours, and neutralized with 0.7 mol of 2-aminopyridine to prepare a polyurethane prepolymer having an isocyanate group at both ends of the molecule.
제조된 폴리우레탄 프리폴리머를 60℃으로 냉각시킨 후 아세톤을 3200g을 가하여 프리폴리머를 완전히 용해한 후 물 4100g을 가하고 헥사메틸렌 디아민 1.3몰을 물에 용해시켜 적가한다. 이를 2시간 동안 교반하여 사슬연장 반응을 진행하고 용액중의 아세톤을 감압 증류로 제거하여 수성 폴리우레탄 수지를 제조한다.The prepared polyurethane prepolymer was cooled to 60 ° C., 3200 g of acetone was added to completely dissolve the prepolymer, and then 4100 g of water was added thereto, and 1.3 mol of hexamethylene diamine was added dropwise thereto. This was stirred for 2 hours to proceed the chain extension reaction, and acetone in the solution was removed by distillation under reduced pressure to prepare an aqueous polyurethane resin.
실시예 4 Example 4
1,4-부탄디올 1200g과 아디프산 1500g으로부터 제조한 분자량이 2000인 폴리에스테르 폴리올 1몰, 2,2-디메틸올부탄산 0.1몰, 1,6-헥사메틸렌디이소시아네이트 1.5몰, 및 이소포론 디이소시아네이트 1몰을 가하여 90℃에서 3시간 반응시킨 후 0.1몰의 2-아미노피리딘으로 중화하여 분자의 양쪽말단에 이소시아네이트기를 가지는 폴리우레탄 프리폴리머를 제조한다. 제조된 폴리우레탄 프리폴리머를 60℃으로 냉각시킨 후 아세톤을 1900g을 가하여 프리폴리머를 완전히 용해한 후 물 3300g을 가하고 1,6-헥사메틸렌 디아민 1.4몰을 물에 용해시켜 적가한다. 이를 2시간 동안 교반하여 사슬연장 반응을 진행하고 용액중의 아세톤을 감압 증류로 제거하여 수성 폴리우레탄 수지를 제조한다.1 mol of polyester polyol prepared from 1200 g of 1,4-butanediol and 1500 g of adipic acid, 0.1 mol of 2,2-dimethylolbutanoic acid, 1.5 mol of 1,6-hexamethylene diisocyanate, and isophorone diisocyanate 1 mole was added and reacted at 90 ° C. for 3 hours, followed by neutralization with 0.1 mole of 2-aminopyridine to prepare a polyurethane prepolymer having an isocyanate group at both ends of the molecule. The prepared polyurethane prepolymer was cooled to 60 ° C., 1900 g of acetone was added to completely dissolve the prepolymer, and then 3300 g of water was added thereto, and 1.4 mole of 1,6-hexamethylene diamine was added dropwise thereto. This was stirred for 2 hours to proceed the chain extension reaction, and acetone in the solution was removed by distillation under reduced pressure to prepare an aqueous polyurethane resin.
비교예 1 Comparative Example 1
1,4-부탄디올 1200g과 아디프산 1500g으로부터 제조한 분자량이 2000인 폴리에스테르 폴리올 1몰, 2,2-디메틸올부탄산 0.1몰, 1,6-헥사메틸렌디이소시아네이트 1.5몰, 및 이소포론 디이소시아네이트 1몰을 가하여 90℃에서 3시간 반응시킨 후 0.1몰의 트리에틸 아민으로 중화하여 분자의 양쪽말단에 이소시아네이트기를 가지는 폴리우레탄 프리폴리머를 제조한다.1 mol of polyester polyol prepared from 1200 g of 1,4-butanediol and 1500 g of adipic acid, 0.1 mol of 2,2-dimethylolbutanoic acid, 1.5 mol of 1,6-hexamethylene diisocyanate, and isophorone diisocyanate After 1 mole was added and reacted at 90 ° C. for 3 hours, neutralization was performed with 0.1 mole triethyl amine to prepare a polyurethane prepolymer having an isocyanate group at both ends of the molecule.
제조된 폴리우레탄 프리폴리머를 60℃으로 냉각시킨 후 아세톤을 1900g을 가하여 프리폴리머를 완전히 용해한 후 물 3300g을 가하고 헥사메틸렌 디아민 1.4몰을 물에 용해시켜 적가한다. 이를 2시간 동안 교반하여 사슬연장 반응을 진행하고 용액중의 아세톤을 감압 증류로 제거하여 수성 폴리우레탄 수지를 제조한다.The prepared polyurethane prepolymer was cooled to 60 ° C., 1900 g of acetone was added to completely dissolve the prepolymer, and then 3300 g of water was added thereto, and 1.4 mol of hexamethylene diamine was added dropwise thereto. This was stirred for 2 hours to proceed the chain extension reaction, and acetone in the solution was removed by distillation under reduced pressure to prepare an aqueous polyurethane resin.
비교예 2 Comparative Example 2
1,4-부탄디올 1200g과 아디프산 1500g으로부터 제조한 분자량이 2000인 폴리에스테르 폴리올 1몰, 2,2-디메틸올부탄산 3몰, 1,6-헥사메틸렌디이소시아네이트 3몰, 및 이소포론 디이소시아네이트 2몰을 가하여 90℃에서 3시간 반응시킨 후 3몰의 2-아미노피리딘으로 중화하여 분자의 양쪽말단에 이소시아네이트기를 가지는 폴리우레탄 프리폴리머를 제조한다.1 mole of polyester polyol having a molecular weight of 2000 prepared from 1200 g of 1,4-butanediol and 1500 g of adipic acid, 3 moles of 2,2-dimethylolbutanoic acid, 3 moles of 1,6-hexamethylene diisocyanate, and isophorone diisocyanate After adding 2 mol and reacting at 90 DEG C for 3 hours, neutralization was performed with 3 mol of 2-aminopyridine to prepare a polyurethane prepolymer having an isocyanate group at both ends of the molecule.
제조된 폴리우레탄 프리폴리머를 60℃으로 냉각시킨 후 아세톤을 4200g을 가하여 프리폴리머를 완전히 용해한 후 물 5700g을 가하고 1,6-헥사메틸렌 디아민 2몰을 물에 용해시켜 적가한다. 이를 2시간 동안 교반하여 사슬연장 반응을 진행하고 용액중의 아세톤을 감압 증류로 제거하여 수성 폴리우레탄 수지를 제조한다.The prepared polyurethane prepolymer was cooled to 60 ° C., 4200 g of acetone was added to completely dissolve the prepolymer, 5700 g of water was added thereto, and 2 moles of 1,6-hexamethylene diamine was added dropwise thereto. This was stirred for 2 hours to proceed the chain extension reaction, and acetone in the solution was removed by distillation under reduced pressure to prepare an aqueous polyurethane resin.
비교예 3 Comparative Example 3
1,6-헥산디올 1500g과 아디프산 1500g으로부터 제조한 분자량이 2000인 폴리에스테르 폴리올 1몰, 2,2-디메틸올부탄산 0.01몰, 1,6-헥사메틸렌디이소시아네이트 1.5몰, 및 이소포론 디이소시아네이트 1몰을 가하여 90℃에서 3시간 반응시킨 후 0.01몰의 2-아미노피리딘으로 중화하여 분자의 양쪽말단에 이소시아네이트기를 가지는 폴리우레탄 프리폴리머를 제조한다.1 mole of polyester polyol having a molecular weight of 2000 prepared from 1500 g of 1,6-hexanediol and 1500 g of adipic acid, 0.01 mol of 2,2-dimethylolbutanoic acid, 1.5 mol of 1,6-hexamethylene diisocyanate, and isophorone di After adding 1 mole of isocyanate and reacting at 90 ° C. for 3 hours, it is neutralized with 0.01 mole of 2-aminopyridine to prepare a polyurethane prepolymer having an isocyanate group at both ends of the molecule.
제조된 폴리우레탄 프리폴리머를 60℃으로 냉각시킨 후 아세톤을 2700g을 가하여 프리폴리머를 완전히 용해한 후 물 3700g을 가하고 1,6-헥사메틸렌 디아민 1.49몰을 물에 용해시켜 적가한다. 이를 2시간 동안 교반하여 사슬연장 반응을 진행하고 용액중의 아세톤을 감압 증류로 제거하여 수성 폴리우레탄 수지를 제조한다.The prepared polyurethane prepolymer was cooled to 60 ° C., 2700 g of acetone was added to completely dissolve the prepolymer, and then 3700 g of water was added thereto, and 1.49 mol of 1,6-hexamethylene diamine was added dropwise thereto. This was stirred for 2 hours to proceed the chain extension reaction, and acetone in the solution was removed by distillation under reduced pressure to prepare an aqueous polyurethane resin.
상기의 실시예 및 비교예에 의해 제조된 수성 폴리우레탄 수지의 특성을 하기 표 1에 요약하였다.The properties of the aqueous polyurethane resins prepared by the Examples and Comparative Examples above are summarized in Table 1 below.
*비교예 3의 경우 수분산이 안됨.* In case of Comparative Example 3, no dispersion.
1) 수분산 안정성: 실시예 1∼4 및 비교예 1∼3에 의하여 수성 폴리우레탄 수지를 제조시, 분산시 또는 최종 수성 폴리우레탄 용액을 상온에서 1주일 방치시의 침전물의 유무. 1) Water dispersion stability: The presence or absence of the deposit at the time of manufacturing an aqueous polyurethane resin according to Examples 1-4 and Comparative Examples 1-3, when disperse | distributing or leaving the final aqueous polyurethane solution at room temperature for 1 week.
양호: 침점물 발생하지 않음, 불량: 침전물 발생Good: No deposits generated, Poor: Deposits
2) 내수성: 실시예 1∼4 및 비교예 1∼3에 의해 제조된 수성 폴리우레탄 용액을 50℃에서 3일 방치 후 필름을 제조하여 방치전 대비 인장강도의 유지율 비교.2) Water resistance: The aqueous polyurethane solution prepared in Examples 1 to 4 and Comparative Examples 1 to 3 was left at 50 ° C. for 3 days to prepare a film to compare the retention of tensile strength compared to that before leaving.
양호: [(방치후 인장강도)×100÷(방치전 인장강도)]이 80%이상Good: [(Tension strength after standing) × 100 ÷ (Tension strength before standing)] is 80% or more
불량: [(방치후 인장강도)×100÷(방치전 인장강도)]이 80%미만Poor: [(Tension strength after neglect) × 100 ÷ (Tension strength before neglect)] is less than 80%
3) 내굴곡성: 실시예 1∼4 및 비교예 1∼3에 의해 제조된 수성 폴리우레탄 용액을 신발용 폴리우레탄 폼에 스프레이식 코팅 및 건조한 후 Demattia Flexion Tester를 이용하여 내굴곡성 시험시 표면에 크랙이 발생하는 시점을 측정.3) Flex resistance: The aqueous polyurethane solution prepared in Examples 1-4 and Comparative Examples 1-3 was spray-coated and dried on the polyurethane foam for shoes, and then cracked on the surface during the flex resistance test using a Demattia Flexion Tester. Measure when this happens.
양호: 100,000회 이상, 불량: 100,000회 미만Good: 100,000 or more, Poor: less than 100,000
4) 기계적 강도: 실시예 1∼4 및 비교예 1∼3에 의해 제조된 수성 폴리우레탄 필름시편을 제조 후 인장강도 시험기를 이용하여 시편이 파단시의 강도측정4) Mechanical strength: After the aqueous polyurethane film specimens prepared in Examples 1 to 4 and Comparative Examples 1 to 3 were prepared, the tensile strength of the specimen was measured using a tensile strength tester.
양호: 300Kgf/㎠이상, 불량: 300Kgf/㎠이상Good: More than 300Kgf / ㎠, Bad: More than 300Kgf / ㎠
5) 내열성: 실시예 1∼4 및 비교예 1∼3에 의해 제조된 수성 폴리우레탄 필름시편을 제조 후 시편을 70℃ 오븐에 일주일 방치 후 인장강도 시험기를 이용하여 시편이 파단시의 강도와 방치 전 시편의 파단 강도를 비교.5) Heat resistance: After preparing the water-based polyurethane film specimens prepared according to Examples 1 to 4 and Comparative Examples 1 to 3, the specimens were placed in an oven at 70 ° C. for one week, and then the tensile strength tester was used to break the specimens. Compare the breaking strength of the entire specimen.
양호: [(방치후 인장강도)×100÷(방치전 인장강도)]이 90%이상Good: [(Tension strength after standing) × 100 ÷ (Tension strength after standing)] is over 90%
불량: [(방치후 인장강도)×100÷(방치전 인장강도)]이 90%미만Poor: [(tensile strength after neglect) × 100 ÷ (tensile strength before neglect)] is less than 90%
6) 아민 냄새: 실시예 1∼4 및 비교예 1∼3에 의해 제조된 수성 폴리우레탄 요액 자체에서 아민류 등의 냄새 유무 확인. 6) Amine odor: The presence of odors such as amines in the aqueous polyurethane urine solution prepared in Examples 1 to 4 and Comparative Examples 1 to 3 itself.
양호: 냄새 없음, 불량: 냄새 있음 Good: No smell, Bad: Odor
표 1에서 알 수 있듯이 상기 실시예 1∼4에 의해 합성된 수성 풀리우레탄 수지의 경우 수분산 안정성, 내수성, 내굴곡성, 기계적 강도, 내열성, 냄새 등이 동시에 양호하나 비교예 1∼3에서 합성된 수성 폴리우레탄의 수지의 경우 수분산 안정성, 내수성, 내굴곡성, 기계적 강도, 내열성, 및 냄새 등이 동시에 양호하지는 않다.As can be seen from Table 1, in the case of the aqueous pulley polyurethane resins synthesized according to Examples 1 to 4, water dispersion stability, water resistance, flex resistance, mechanical strength, heat resistance, odor, etc. are simultaneously good, but are synthesized in Comparative Examples 1-3. In the case of the resin of the water-based polyurethane, the water dispersion stability, water resistance, flex resistance, mechanical strength, heat resistance, and odor are not good at the same time.
상기 실시예 및 비교예의 결과로부터 알수 있는 바와 같이, 본 발명에 의해 제조된 수성 폴리우레탄 수지는 수분산 안정성, 내수성이 우수할 뿐만 아니라, 내굴곡성, 기계적 강도, 내열성도 동시에 만족스러우며, 잔류 용매 냄새도 나지 않아 다양한 피착재에 대한 접착제로 사용될 수 있는 장점이 있다. As can be seen from the results of the above examples and comparative examples, the aqueous polyurethane resin prepared by the present invention not only has excellent water dispersion stability and water resistance, but also satisfies bending resistance, mechanical strength, and heat resistance at the same time. There is also an advantage that can be used as an adhesive for various adherends.
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