KR102629682B1 - Room temperature hardening polyurea resin and manufacturing method thereof - Google Patents

Room temperature hardening polyurea resin and manufacturing method thereof Download PDF

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KR102629682B1
KR102629682B1 KR1020220174274A KR20220174274A KR102629682B1 KR 102629682 B1 KR102629682 B1 KR 102629682B1 KR 1020220174274 A KR1020220174274 A KR 1020220174274A KR 20220174274 A KR20220174274 A KR 20220174274A KR 102629682 B1 KR102629682 B1 KR 102629682B1
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diamine
polyurea resin
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최건철
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주식회사 의련엘엔에스
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30Low-molecular-weight compounds
    • C08G18/32Polyhydroxy compounds; Polyamines; Hydroxyamines
    • C08G18/3203Polyhydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30Low-molecular-weight compounds
    • C08G18/32Polyhydroxy compounds; Polyamines; Hydroxyamines
    • C08G18/3225Polyamines
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30Low-molecular-weight compounds
    • C08G18/32Polyhydroxy compounds; Polyamines; Hydroxyamines
    • C08G18/3225Polyamines
    • C08G18/3253Polyamines being in latent form
    • C08G18/3256Reaction products of polyamines with aldehydes or ketones
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/02Polyureas

Abstract

본 발명은 상온 경화형 폴리우레아 수지 및 이의 제조방법에 관한 것으로, 말단기가 디아민기로 형성되는 주제인 A액과 말단기가 디이소시아네이트기로 형성되는 경화제인 B액의 이액형으로, 디아민과 알데히드의 블록화 반응을 통한 1차 반응물 디아민을 주제 A액의 제조에 일부 사용함으로써, 폴리우레아 수지의 경화시간을 늦춰 방수 및 방청 작업 시, 수작업으로 시공이 가능하도록 하는 상온 경화형 폴리우레아 수지 및 이의 제조방법에 관한 것이다.The present invention relates to a room temperature curable polyurea resin and a method for producing the same. It is a two-component type of solution A, which is a main agent whose terminal group is formed of a diamine group, and solution B, which is a curing agent whose terminal group is formed by a diisocyanate group, and performs a blocking reaction of diamine and aldehyde. This relates to a room temperature curable polyurea resin and its manufacturing method that slow down the curing time of the polyurea resin and enable manual construction during waterproofing and rust prevention work by using a portion of the primary reactant diamine in the production of main solution A.

Description

상온 경화형 폴리우레아 수지 및 이의 제조방법{Room temperature hardening polyurea resin and manufacturing method thereof}Room temperature hardening polyurea resin and manufacturing method thereof}

본 발명은 상온 경화형 폴리우레아 수지 및 이의 제조방법에 관한 것으로, 폴리우레아 수지의 경화시간을 늦춰 수작업 시공이 가능하도록 하는 상온 경화형 폴리우레아 수지 및 이의 제조방법에 관한 것이다. The present invention relates to a room temperature-curable polyurea resin and a method for manufacturing the same, which slows down the curing time of the polyurea resin to enable manual construction.

일반적으로 건축물의 옥상이나, 주차장, 지하실 등의 방수재 및 바닥재로 폴리우레탄이 주로 사용된다. 폴리우레탄(Polyurethane)은 알코올기와 아이소사이안기의 결합으로 만들어진 우레탄 결합으로 결합된 고분자 화합물로, 내열성, 내마모성, 내용제성, 내약품성이 뛰어나며, 탄성 섬유, 도료, 접착제 등으로 사용된다. 그러나 폴리우레탄(Polyurethane)은 도막의 내구성이 떨어져 외부 요인에 의해 도막의 찢김이나 파열이 비교적 쉽게 발생되는 문제가 발생할 수 있다. In general, polyurethane is mainly used as a waterproofing material and flooring material for building rooftops, parking lots, and basements. Polyurethane is a polymer compound made of urethane bonds made by combining alcohol groups and isocyanic groups. It has excellent heat resistance, abrasion resistance, solvent resistance, and chemical resistance, and is used in elastic fibers, paints, adhesives, etc. However, polyurethane has poor film durability, so external factors can cause tearing or rupture of the film relatively easily.

이러한 문제를 해결하기 위해 최근에는 폴리우레아(Polyurea)가 많이 사용되고 있는 추세이다. 폴리우레아(polyurea)는 윤활유, 기름 및 용매에 대한 적절한 내성을 지닌 것으로, 트럭의 베드 라이너, 균열 메꾸기 및 장식 디자인에 사용되며, 주로 에어리스 장비를 사용하여 이액형의 에어리스 스프레이 방식으로 사용된다. 그러나 폴리우레아는 경화시간이 빨라 소재와의 기밀성 및 접착력이 떨어지는 문제가 있으며, 스프레이 작업시 강한 압력에 의해 분진 발생이 많아 스모그 현상 등의 환경오염이 심각해지는 문제가 있다. 이에 현재 시장에서는 스프레이 작업을 제한하고 있는 실정이며, 환경문제가 발생하지 않는 대체물질과 작업을 요구하고 있어, 특허문헌 1, 2와 같이 친환경적이고, 수작업이 가능하도록 하는 폴리우레아 도료에 대한 개발이 진행되고 있으나, 아직 제품에 미치지는 못하고 있는 상황이다.To solve this problem, polyurea has been widely used recently. Polyurea has adequate resistance to lubricants, oils and solvents and is used in truck bed liners, crack filling and decorative designs, primarily as a two-component airless spray using airless equipment. However, polyurea has the problem of low airtightness and adhesion to materials due to its fast curing time, and the strong pressure during spraying generates a lot of dust, which causes serious environmental pollution such as smog. Accordingly, the current market is restricting spray work, and there is a demand for work with alternative materials that do not cause environmental problems, leading to the development of polyurea paints that are environmentally friendly and allow manual work, as shown in Patent Documents 1 and 2. Progress is being made, but it has not yet reached product level.

특허문헌 1은 수작업이 가능한 폴리우레아 도료에 관한 것으로, 주제부의 이소시아네이트기와 경화제부의 아민기의 몰비가 1:0.8~1로 배합하여 폴리우레아 도료를 제조함으로써, 가사시간이 길어 레기 또는 로라 등으로 도장 작업을 가능하도록 한 것이다.Patent Document 1 relates to a polyurea paint that can be applied by hand. By mixing the isocyanate group in the main part with the amine group in the hardener part at a molar ratio of 1:0.8 to 1, the polyurea paint is manufactured, so the pot life is long, so it can be painted with a resin or roller, etc. It made the work possible.

특허문헌 2는 친환경 하이브리드 폴리우레아수지계 도료조성물 및 그 시공 방법에 관한 것으로, 휘발성 유기화합물인 용제와 촉매를 포함하지 않으며, 과량의 필러를 사용하지 않아 친환경적인 폴리우레아수지계 도료조성물의 제조가 가능하도록 한 것이다.Patent Document 2 relates to an eco-friendly hybrid polyurea resin-based coating composition and its construction method. It does not contain solvents and catalysts that are volatile organic compounds, and does not use excessive fillers, enabling the production of an eco-friendly polyurea resin-based coating composition. It was done.

등록특허공보 제10-1372812호 (공고일자: 2014.03.12)Registered Patent Publication No. 10-1372812 (Publication date: 2014.03.12) 등록특허공보 제10-2163364호 (공고일자: 2020.10.08)Registered Patent Publication No. 10-2163364 (Publication date: 2020.10.08)

본 발명은 상온 경화형 폴리우레아 수지 및 이의 제조방법에 관한 것으로, 디아민과 알데히드를 반응시켜 블록화한 반응물을 사용한 주제 A액과, 경화제인 B액을 각각 제조하여, 현장에서 전문가의 도움 없이도 누구나 쉽게 수작업이 가능한 상온 경화형 폴리우레아 수지 및 이의 제조방법을 제공하는 것을 목적으로 한다.
또한, 본 발명은 에어리스 스프레이 분사로 인한 환경오염을 줄일 수 있는 상온 경화형 폴리우레아 수지 및 이의 제조방법을 제공하는 것을 목적으로 한다.
The present invention relates to a room temperature curable polyurea resin and a method for producing the same. The main liquid A and the curing agent liquid B are respectively prepared using reactants made by reacting diamine and aldehyde to form blocks, so that anyone can easily do it by hand without the help of experts in the field. The purpose is to provide a room temperature curable polyurea resin and a method for producing the same.
Additionally, the purpose of the present invention is to provide a room temperature curable polyurea resin and a manufacturing method thereof that can reduce environmental pollution caused by airless spraying.

본 발명은 상온 경화형 폴리우레아 수지 및 이의 제조방법에 관한 것으로, 상기 상온 경화형 폴리우레아 수지는 디아민 100중량부에 대하여 글리콜류 5~10중량부, 안료 2~15중량부, 필러10~30중량부, 증점제 1~10중량부, 소포제 0.2~0.5중량부, 분산제 0.5~1.0중량부, 촉진제 0.2~1.0중량부를 혼합되는 주제 A액, 글리콜류 100중량부에 디이소시아네이트 100 중량부를 반응시켜 제조한 경화제 B액을 혼합하여 제조되되, 상기 A액의 디아민 100중량부에는 디아민과 알데히드를 반응시켜 제조한 1차 반응물 디아민이 일부 포함되며, 상기 주제 A액의 디아민은 디에틸톨루엔디아민, 에틸렌디아민, 디메틸피오톨루엔디아민, 이소포론디아민, 폴리옥시프로필렌 디아민 중 어느 1종 또는 2종 이상이 사용되고, 상기 1차 반응물 디아민의 알데히드는 부틸알데히드, 이소부틸알데히드, 신남알데히드 중 어느 1종 또는 2종 이상이 사용되고, 상기 주제 A액과 경화제 B액의 글리콜류는 폴리옥시프로필렌 글리콜, 폴리에틸렌글리콜, 폴리테트라메틸렌에테르글리콜, 1.4부틸렌글리콜 중 어느 1종 또는 2종 이상 사용되며, 상기 경화제 B액의 디이소시아네이트는 TDI, MDI, IPDI, HDI, XMDI 중 어느 1종 또는 2종 이상 사용되는 것을 특징으로 한다.The present invention relates to a room temperature curable polyurea resin and a method for producing the same, wherein the room temperature curable polyurea resin contains 5 to 10 parts by weight of glycols, 2 to 15 parts by weight of pigment, and 10 to 30 parts by weight of filler based on 100 parts by weight of diamine. , 1 to 10 parts by weight of thickener, 0.2 to 0.5 parts by weight of antifoaming agent, 0.5 to 1.0 parts by weight of dispersant, and 0.2 to 1.0 parts by weight of accelerator. Liquid A, a hardener prepared by reacting 100 parts by weight of diisocyanate with 100 parts by weight of glycols. It is prepared by mixing solution B, and 100 parts by weight of diamine in solution A includes some primary reactant diamine prepared by reacting diamine and aldehyde, and the diamine in solution A is diethyltoluenediamine, ethylenediamine, and dimethyl. One or two or more types of piotoluenediamine, isophorone diamine, and polyoxypropylene diamine are used, and the aldehyde of the primary reactant diamine is one or two or more types of butyraldehyde, isobutyraldehyde, and cinnamaldehyde. , the glycols of the main liquid A and the hardener B liquid are any one or two or more of polyoxypropylene glycol, polyethylene glycol, polytetramethylene ether glycol, and 1.4 butylene glycol, and the diisocyanate of the hardener liquid B is It is characterized in that one or two or more types of TDI, MDI, IPDI, HDI, and XMDI are used.

삭제delete

또한, 본 발명은 디아민 100중량부에 대하여 글리콜류 5~10중량부, 안료 2~15중량부, 필러10~30중량부, 증점제 1~10중량부, 소포제 0.2~0.5중량부, 분산제 0.5~1.0중량부, 촉진제 0.2~1.0중량부를 혼합하여주제 A액을 제조하는 A액 제조단계, 글리콜류 100중량부에 디이소시아네이트 100 중량부를 반응시켜 NC0기의 함량이 14.5~15.5 중량%내에 포함되도록 경화제 B액을 제조하는 B액 제조단계, 상기 A액 제조단계 및 B액 제조단계에서 제조된 주제 A액과 경화제 B액을 A액 100중량부에 B액 70중량부를 혼합하여 시공표면에 도포하여 시공하는 혼합 및 시공단계;를 포함하며, 상기 A액 제조단계는 디아민을 반응기에 투입하고, 알데히드를 개량하여 드랍핑 탱크(dropping tank)에 투입한 후, 반응기 내부 온도를 서서히 승온하여 알데히드를 드랍핑(dropping)하여 반응시킨 후, 진공 탈수시켜 제조하는 1차 반응물 디아민 제조단계를 포함하는 것을 특징으로 한다.In addition, the present invention contains 5 to 10 parts by weight of glycols, 2 to 15 parts by weight of pigment, 10 to 30 parts by weight of filler, 1 to 10 parts by weight of thickener, 0.2 to 0.5 parts by weight of antifoam, and 0.5 to 0.5 parts by weight of dispersant, based on 100 parts by weight of diamine. Liquid A manufacturing step of preparing main liquid A by mixing 1.0 parts by weight and 0.2 to 1.0 parts by weight of accelerator, reacting 100 parts by weight of diisocyanate with 100 parts by weight of glycols to form a curing agent so that the content of NC0 group is within 14.5 to 15.5% by weight. The main liquid A and the hardener liquid B prepared in the liquid B manufacturing stage, the liquid A manufacturing stage, and the liquid B manufacturing stage are mixed with 100 parts by weight of liquid A and 70 parts by weight of liquid B, and applied to the construction surface. A mixing and construction step is included, wherein the solution A production step is to add diamine to the reactor, improve aldehyde and add it to the dropping tank, and then drop the aldehyde by gradually increasing the temperature inside the reactor. It is characterized in that it includes a step of preparing the first reactant diamine by reacting by dropping and then vacuum dehydrating.

삭제delete

본 발명은 상온 경화형 폴리우레아 수지 및 이의 제조방법에 관한 것으로, 아민과 알데히드를 반응시켜 블록화한 1차 반응물을 주제에 사용함으로써, 경화시간을 늦춰 수작업이 가능하도록 하는 이점이 있다. The present invention relates to a room temperature curable polyurea resin and a method for manufacturing the same. By using a primary reactant formed by reacting an amine and an aldehyde into a block, it has the advantage of slowing the curing time and allowing manual work.

또한, 본 발명은 누구나 손쉽게 수작업으로 시공이 가능하고, 아주 작은 면적의 시공에도 손쉽게 마무리 할 수 있는 효과가 있다.In addition, the present invention allows anyone to easily construct it by hand, and has the effect of allowing construction to be easily completed even in a very small area.

또한, 본 발명은 수작업으로 시공이 가능하여 에어리스 스프레이 분사로 인한 환경오염을 줄일 수 있는 효과가 있다.In addition, the present invention can be constructed manually, which has the effect of reducing environmental pollution caused by airless spraying.

도 1은 본 발명에 따른 상온 경화형 폴레우레아 수지 및 이의 제조방법의 전체 제조단계를 도시한 도면.Figure 1 is a diagram showing the overall manufacturing steps of the room temperature curable polyurea resin and its manufacturing method according to the present invention.

본 발명은 상온 경화형 폴리우레아 수지 및 이의 제조방법에 관한 것이다. 본 발명은 말단기가 디아민기로 형성되는 주제 A액과 말단기가 디이소시아네이트기로 형성되는 경화제 B액의 이액형으로, 주제인 A액 제조단계와 경화제인 B액 제조단계 및 혼합 및 시공단계로 나뉜다. 본 발명에서는 각 단계의 설명 및 실시 예를 통해 상세한 내용을 설명하고자 한다. The present invention relates to a room temperature curable polyurea resin and a method for producing the same. The present invention is a two-component type of main solution A, where the terminal group is formed of a diamine group, and hardener B solution, where the terminal group is formed of a diisocyanate group. It is divided into a main solution A preparation step, a curing agent solution B preparation step, and mixing and construction steps. In the present invention, details will be explained through descriptions and examples of each step.

도 1은 본 발명의 전체 제조단계를 도시한 것이다. 도 1에 도시된 바와 같이 본 발명은 주제인 A액과 경화제인 B액이 각각 제조되는 것으로, A액 제조단계→ B액 제조단계→ 혼합 및 시공단계를 포함한다. Figure 1 shows the overall manufacturing steps of the present invention. As shown in Figure 1, in the present invention, Liquid A, which is the main agent, and Liquid B, which is the hardener, are each manufactured, and includes the steps of preparing Liquid A → preparing Liquid B → mixing and construction steps.

먼저, A액 제조단계이다. A액 제조단계는 1차 반응물 디아민 제조단계→ 기타 첨가물 혼합 및 포장 단계를 포함한다. 상세한 설명은 다음과 같다.First, the liquid A manufacturing stage. The liquid A preparation step includes the first reactant diamine preparation step → other additive mixing and packaging steps. The detailed explanation is as follows.

1차 반응물 디아민 제조단계이다.This is the first reactant diamine production step.

주제인 A액의 디아민은 디아민과 알데히드를 반응시켜 1차 반응물을 제조한다. 디아민을 반응기에 투입 후, 알데히드를 개량하여 드랍핑 탱크(dropping tank)에 투입한다. 이후, 반응 활성화를 위해 반응기 내부 온도를 서서히 승온하여 알데히드를 드랍핑(dropping) 시킨다. 이후, 반응이 종결되면 서서히 승온시켜 진공탈수를 통해 반응생성 수분을 제거하고, 수분이 완전히 제거되면 1차 반응물의 반응을 종결한다.The main reactant, diamine in solution A, is prepared as a primary reactant by reacting diamine with aldehyde. After diamine is added to the reactor, aldehyde is improved and added to the dropping tank. Afterwards, to activate the reaction, the temperature inside the reactor is gradually raised to drop the aldehyde. Afterwards, when the reaction is completed, the temperature is gradually raised and the moisture generated by the reaction is removed through vacuum dehydration. When the moisture is completely removed, the reaction of the first reactant is terminated.

디아민(diamine)은 분자 속에 2개의 아미노기(-NH₂)를 가지고 있는 화합물로, 아미노기의 수소원자가 알킬기 또는 아릴기 등으로 치환된 화합물도 포함한다. 디아민은 니켈, 코발트, 철, 금 등의 금속과 결합하여 착염을 만들고, 또 지방족 디아민은 다이카복실산 등과 축합반응을 일으켜 고분자 화합물을 만들기로 하여, 합성섬유, 색소의 원료로 사용되는 것이다. 본 발명에서는 디에틸톨루엔디아민, 에틸렌디아민, 디메틸피오톨루엔디아민, 이소포론디아민, 폴리옥시프로필렌 디아민 등이 사용되며, 이 중 어느 1종 또는 2종 이상이 사용될 수 있다.Diamine is a compound that has two amino groups (-NH₂) in the molecule, and also includes compounds in which the hydrogen atom of the amino group is replaced with an alkyl group or aryl group. Diamine combines with metals such as nickel, cobalt, iron, and gold to form complex salts, and aliphatic diamine undergoes a condensation reaction with dicarboxylic acid to create polymer compounds, which are used as raw materials for synthetic fibers and pigments. In the present invention, diethyltoluenediamine, ethylenediamine, dimethylpiotoluenediamine, isophorone diamine, polyoxypropylene diamine, etc. are used, and any one or two or more types of these may be used.

알데히드는 포르밀기(-CHO)를 가지고 있는 탄소 화합물을 말하는 것으로, 탄소수가 적은 알데히드는 물과 잘 섞이며, 환원성을 갖는 것이다. 본 발명에서 알데히드는 부틸알데히드, 이소부틸알데히드, 신남알데히드 등이 사용되며, 이 중 어느 1종 또는 2종 이상이 사용될 수 있다.Aldehyde refers to a carbon compound that has a formyl group (-CHO). Aldehydes with fewer carbon atoms mix well with water and have reducing properties. In the present invention, the aldehyde used is butyraldehyde, isobutyraldehyde, cinnamaldehyde, etc., and any one or two or more types of these may be used.

이때, 1차 반응물 제조단계에서는 디아민과 알데히드를 반응시켜 블록화한 것으로, 수작업에 사용할 수 있도록 경화시간을 늦추는 것이 가능하도록 한다.At this time, in the first reactant manufacturing stage, diamine and aldehyde are reacted to form blocks, making it possible to slow down the curing time so that it can be used in manual work.

다음, 기타첨가물 혼합 단계이다. Next is the other additive mixing step.

디아민 100중량부에 대하여 안정제 5~10중량부, 안료 2~15중량부, 필러 10~30중량부, 증점제1~10중량부, 소포제0.2~0.5중량부, 분산제0.5~1.0중량부, 촉진제0.2~1.0중량부를 혼합하여 디졸버 믹서기에 균일하게 분산시켜 필러 분산상태를 확인하여 제조한 후, 제조된 A액을 포장한다.Based on 100 parts by weight of diamine, 5 to 10 parts by weight of stabilizer, 2 to 15 parts by weight of pigment, 10 to 30 parts by weight of filler, 1 to 10 parts by weight of thickener, 0.2 to 0.5 parts by weight of defoamer, 0.5 to 1.0 parts by weight of dispersant, 0.2 parts by weight of accelerator. Mix ~1.0 parts by weight and disperse evenly in a dissolver mixer to check the dispersion state of the filler, and then package the prepared solution A.

이때, 디아민 100중량부에는 상기 1차 반응물 디아민 제조단계에서 제조된 디아민이 일부 포함된다. 또한, 이때, 분산 속도는 RPM 800이 가장 바람직하다.At this time, 100 parts by weight of diamine includes some of the diamine produced in the first reactant diamine production step. Also, at this time, the dispersion speed is most preferably RPM 800.

또한, 이때, 필러 분산상태는 입자가 고르게 분산되어 흐름이 일정할 때의 상태가 가장 바람직하다.Also, at this time, the filler dispersion state is most desirable when the particles are evenly dispersed and the flow is constant.

또한, 이때, 필러는 10~30 중량부임이 바람직하며, 이는 필러가 30중량부보다 많이 첨가되면, 인장강도 및 연신율 등의 기능이 저하되는 문제가 발생할 수 있어, 이를 방지하기 위함이다.In addition, at this time, it is preferable that the filler is added in an amount of 10 to 30 parts by weight. This is to prevent the problem that functions such as tensile strength and elongation may decrease if the filler is added in more than 30 parts by weight.

글리콜류는 안정제로, 안정제는 물질을 방치 또는 보존할 때 자연히 생기는 화학 변화나 상태의 변화를 방지하기 위해 첨가되는 물질이다. 본 발명에서는 폴리옥시프로필렌 글리콜, 폴리에틸렌글리콜, 폴리테트라메틸렌에테르글리콜, 1.4부틸렌글리콜 등이 사용되며, 이 중 어느 1종 또는 2종 이상이 사용될 수 있다.Glycols are stabilizers. Stabilizers are substances added to prevent chemical changes or changes in state that naturally occur when a material is left or preserved. In the present invention, polyoxypropylene glycol, polyethylene glycol, polytetramethylene ether glycol, 1.4 butylene glycol, etc. are used, and any one or two or more of these may be used.

안료는 물 및 대부분의 유기용제에 녹지 않는 분말상의 착색제로, 백색 또는 유색이며, 아마인유니스, 합성수지액, 아라비아고무 등 전색제에 섞어서 도료, 인쇄잉크, 그림물감 등을 만들어 물체 표면에 착색하거나, 고무, 합성수지 등에 직접 섞어서 착색하는 것이다. 본 발명에서는 안료로 산화철의 무기안료나 유기안료 등이 사용되며, 이 중 어느 1종 또는 2종 이상이 사용될 수 있다.Pigments are powdery colorants that are insoluble in water and most organic solvents, and are white or colored. They are mixed with colorants such as linseed varnish, synthetic resin, and gum arabic to make paints, printing inks, paints, etc., and are used to color the surface of objects or to use rubber. It is colored by directly mixing it with synthetic resin, etc. In the present invention, inorganic pigments or organic pigments of iron oxide are used as pigments, and any one or two or more types of these may be used.

필러(filler)는 증량, 물성 개선 및 성형 가공성을 향상할 목적으로 고분자 재료 중에서 분산시켜 첨가되는 입자상, 섬유상, 플레이트상의 물질이다. 본 발명에서는 중탄, 실리카, 경탄 등이 사용되며, 이 중 어느 1종 또는 2종 이상이 사용될 수 있다.Filler is a particulate, fibrous, or plate-shaped material that is added by dispersing it in a polymer material for the purpose of increasing weight, improving physical properties, and improving molding processability. In the present invention, heavy carbon, silica, light coal, etc. are used, and any one or two or more types of these may be used.

증점제는 콜로이드 용액, 고분자 용액 등에 가하여 이들의 것의 점도를 증진시켜, 틱소트로피성을 부여하는 것으로, 접착제, 시멘트, 라텍스, 도료, 화장품 등에 사용된다. 본 발명에서는 실리카나 벤토네이트 등이 사용되며, 이 중 어느 1종 또는 2종 이상이 사용될 수 있다.Thickeners are added to colloidal solutions, polymer solutions, etc. to increase their viscosity and provide thixotropic properties, and are used in adhesives, cement, latex, paints, cosmetics, etc. In the present invention, silica, bentonate, etc. are used, and any one or two or more types of these may be used.

소포제는 생겨난 거품에 뿌려서 거품을 지우는 작용을 하는 물질이다. An antifoaming agent is a substance that is sprayed on foam that has formed and acts to remove the foam.

분산제는 큰 입자와 응집한 입자를 분쇄하여 보다 작은 입자와 콜로이드 입자로 만들 때 생성된 미소 입자의 응집을 방지하기 위해 가하는 물질이다.A dispersant is a substance added to prevent agglomeration of fine particles generated when large particles and aggregated particles are pulverized into smaller particles and colloidal particles.

촉진제는 반응계 내 혹은 고체 촉매 제조시 첨가함으로써 화학반응 속도에 변화를 주는 물질을 말하는 것으로, 본 발명에서는 비스무트 용액이 사용될 수 있다.An accelerator refers to a substance that changes the speed of a chemical reaction by adding it in the reaction system or during the manufacture of a solid catalyst. In the present invention, a bismuth solution can be used.

다음, 경화제인 B액 제조단계이다. 상세한 설명은 다음과 같다.Next is the manufacturing step of liquid B, which is a hardener. The detailed explanation is as follows.

글리콜류 100중량부에 대하여 디이소사이네이트 100중량부를 반응기에 투입후, 반응 활성화를 위해 서서히 승온시켜 반응 후, 종결하여 B액을 제조하고, 제조된 B액을 포장한다.After adding 100 parts by weight of diisocyanate to the reactor for 100 parts by weight of glycols, the temperature is slowly raised to activate the reaction, and after the reaction is terminated, Liquid B is prepared, and the prepared Liquid B is packaged.

이때, B액은 말단기 디이소시아네이트를 제조하는 것으로, NCO기(이소시아네이트기) 함량은 14.5~15.5 중량%인 것이 바람직하다. 이는 주제 A액과 혼합 시, NCO기 함량이 너무 15.5 중량%보다 많으면, 경화가 되지 않고, 공기 중의 수분과 반응하므로, 물성이 떨어지는 문제가 발생할 수 있으며, NCO기 함량이 14.5 중량%보다 적으면 점도가 높아지는 문제가 발생하게 되어, 이를 방지하기 위함이다.At this time, solution B is for producing terminal diisocyanate, and the NCO group (isocyanate group) content is preferably 14.5 to 15.5% by weight. When mixing with main liquid A, if the NCO group content is too much more than 15.5% by weight, it does not harden and reacts with moisture in the air, which may cause problems with poor physical properties. If the NCO group content is less than 14.5% by weight, the product may not harden. This is to prevent the problem of increased viscosity.

이때, 디이소시아네이트로서 TDI(Toluene diisocyanate), MDI(Methylene Diphenyl diisocyanate), IPDI(Isophorone diisocyanate), HDI(Hexamethylene diisocyanate), XMDI(Xylyene diiscocyanate) 등이 사용될 수 있으며, 이 중 어느 1종 또는 2종 이상이 사용될 수 있다.At this time, as diisocyanate, TDI (Toluene diisocyanate), MDI (Methylene Diphenyl diisocyanate), IPDI (Isophorone diisocyanate), HDI (Hexamethylene diisocyanate), This can be used.

또한, 이때, 글리콜류는 폴리옥시 플로필렌글리콜, 폴리테트라메틸렌에테르글리콜, 1.4부틸렌글리콜, 폴리에틸렌글리콜 등이 사용될 수 있으며, 이 중 어느 1종 또는 2종 이상이 사용될 수 있다.Also, at this time, the glycols may be polyoxy propylene glycol, polytetramethylene ether glycol, 1.4 butylene glycol, polyethylene glycol, etc., and any one or two or more of these may be used.

다음, 혼합 및 시공단계이다.Next is the mixing and construction stage.

시공 시, 상기의 단계에서 제조된 주제 A액 100중량부에 대하여, 경화제 B액 70 중량부를 믹서기로 균일하게 혼합하여, 시공표면에 균일하게 시공 마무리한다. During construction, 70 parts by weight of hardener liquid B are uniformly mixed with a mixer for 100 parts by weight of main liquid A prepared in the above step, and the construction is finished evenly on the construction surface.

이때, 주제 A액과 B액은 A액 100중량부에 B액 70중량부를 혼합하는 것이 가장 바람직하며, 이는 아민 당량과 NCO 당량이 1:1인 것이 가장 바람직하며, 이에 해당하는 것이 주제 A액 100중량부, B액 70중량부 이기 때문이다. At this time, it is most preferable to mix main solution A and solution B with 100 parts by weight of solution A and 70 parts by weight of solution B. It is most preferable that the amine equivalent and NCO equivalent are 1:1, which corresponds to main solution A. This is because it is 100 parts by weight and 70 parts by weight of liquid B.

이하, 아래에서는 본 발명의 하나의 구체적인 실시 예로, 상세한 설명은 다음과 같다. Hereinafter, a specific embodiment of the present invention will be described below, and a detailed description is as follows.

먼저, A액 제조단계로, 1차 반응물 디아민 제조단계이다.First, the preparation step for solution A is the preparation step for the first reactant, diamine.

이소포론디아민 53.97 중량%를 반응기에 투입한다. 여기에 이소부틸알데히드 46.03 중량%를 개량하여 드랍핑 탱크(dropping tank)에 투입한다. 다음, 반응기 내부 온도를 서서히 60℃까지 승온하여 이소부틸알데히드를 8시간에 걸쳐 드랍핑(dropping)한다. 이후, 반응 종결 후 서서히 승온시켜 100℃를 유지하며 진공탈수 시켜 반응생성 수분을 제거한다. 수분이 완전히 제거되면 1차 반응물의 반응을 종결한다. 53.97% by weight of isophorone diamine is added to the reactor. Here, 46.03% by weight of isobutyraldehyde is improved and added to the dropping tank. Next, the temperature inside the reactor is gradually raised to 60°C and isobutyraldehyde is dropped over 8 hours. After completion of the reaction, the temperature is gradually raised, maintained at 100°C, and vacuum dehydration is performed to remove reaction-generated moisture. When moisture is completely removed, the reaction of the first reactant is completed.

이때, 분자의 구조식은 다음과 같이 형성된다.At this time, the structural formula of the molecule is formed as follows.

이때, 반응기 내에서는 이소포론디아민과 이소부틸알데히드의 반응에 의해 발열이 진행되므로, 65℃이상 온도 상승을 억제하면서 반응을 진행하는 것이 가장 바람직하다. 이는 이소부틸알데히드의 비점이 63~64℃이므로, 이소부틸알데히드의 비점 보다 너무 높은 온도로 상승되지 않도록 억제해줌으로써, 내부팽창이 발생하는 것을 제어하기 위함이다.At this time, since heat is generated by the reaction between isophoronediamine and isobutyraldehyde in the reactor, it is most desirable to proceed with the reaction while suppressing the temperature rise above 65°C. Since the boiling point of isobutyraldehyde is 63 to 64°C, this is to prevent internal expansion from occurring by preventing the temperature from rising to a temperature too high above the boiling point of isobutyraldehyde.

이때, 반응 종결 후, 반응 생성물인 수분을 제거해 주는 것이 바람직하다. 이는 수분이 존재할 경우 NCO와 반응하여 요소 결합 형성을 하므로, 이를 방지하기 위함이다.At this time, after completion of the reaction, it is desirable to remove the moisture that is the reaction product. This is to prevent the formation of urea bonds by reacting with NCO when moisture is present.

또한, 디아민과 알데히드를 반응시켜 블록화한 1차 반응물을 주제 A액 제조에 일부 사용함으로써, 폴리우레아 수지의 경화시간을 늦춰 수작업의 시공이 가능하도록 한다. In addition, by partially using the primary reactant obtained by reacting diamine and aldehyde to form a block, the curing time of the polyurea resin is slowed down, allowing manual construction.

다음, 기타첨가물 혼합 및 포장단계이다.Next is the mixing and packaging stage of other additives.

상기 1차 반응물 디아민 제조단계를 통해 제조된 1차 반응물 디아민 38중량부, 디에틸톨루엔디아민 2중량부, 폴리옥시프로필렌디아민 60중량부를 혼합한 디아민 100 중량부에 대하여, TiO₂(이산화타이타늄) 9중량부, 철흑 1중량부, 중탄 25중량부, 실리카 3중량부, 소포제 0.2중량부, 폴리옥시프로필렌글리콜 10중량부, 분산제 0.5 중량부, 비스무트 9%용액 0.3중량부를 혼합하여 디졸버 믹서기에서 RPM 800의 속도로 균일하게 분산시켜 필러의 분산상태를 확인하여 제조한다. 이후, 제조된 주제 A액을 포장한다.9 parts by weight of TiO₂ (titanium dioxide) based on 100 parts by weight of diamine prepared by mixing 38 parts by weight of primary reactant diamine, 2 parts by weight of diethyltoluenediamine, and 60 parts by weight of polyoxypropylene diamine prepared through the above primary reactant diamine production step. 1 part by weight, 1 part by weight of iron black, 25 parts by weight of heavy carbon, 3 parts by weight of silica, 0.2 parts by weight of defoaming agent, 10 parts by weight of polyoxypropylene glycol, 0.5 parts by weight of dispersant, and 0.3 parts by weight of bismuth 9% solution and mixed in a dissolver mixer at RPM 800. It is manufactured by uniformly dispersing at a speed of and checking the dispersion state of the filler. Afterwards, the prepared main solution A is packaged.

이때, TiO₂(이산화타이타늄) 및 철흑은 안료, 중탄은 필러(filler), 실리카는 증점제, 폴리옥시프로필렌글리콜은 안정제, 비스무트 9% 용액은 촉진제로 사용된 것이다. At this time, TiO₂ (titanium dioxide) and iron black were used as pigments, bicarbonate as a filler, silica as a thickener, polyoxypropylene glycol as a stabilizer, and bismuth 9% solution as an accelerator.

다음, B액 제조단계이다.Next is the liquid B manufacturing step.

폴리옥시프로필렌글리콜 100중량부에 이소포린디이소시아네이트 100중량부를 반응기에 투입 후, 서서히 승온시켜 50~60℃를 유지하면서 반응으로 인해 90℃까지 자체 발열하는 것을 확인 후, 90~100℃에서 4시간 반응 후, NCO기의 함량이 14.5~15.5 중량%내에 포함되면 반응을 종결하여 제조완료 후, 포장한다.After adding 100 parts by weight of isophorine diisocyanate to 100 parts by weight of polyoxypropylene glycol into the reactor, gradually increase the temperature and maintain 50~60℃, confirm that self-heating occurs up to 90℃ due to the reaction, and then heat at 90~100℃ for 4 hours. After the reaction, when the NCO group content is within 14.5 to 15.5% by weight, the reaction is terminated and the product is packaged after completion of production.

다음, 혼합 및 시공단계이다.Next is the mixing and construction stage.

상기의 제조단계를 통해 제조된 A액과 B액을 시공 시, A액 100중량부에 B액 70중량부를 믹서기로 균일하게 혼합한 후, 시공표면에 균일하게 도포하여 시공한다.When applying Liquid A and Liquid B prepared through the above manufacturing steps, 100 parts by weight of Liquid A are mixed uniformly with 70 parts by weight of Liquid B using a mixer, and then applied evenly to the construction surface.

이와 같이, 본 발명에서는 주제인 A액과 경화제인 B액을 각각 제조 및 포장하여 시공 현장에서 A액과 B액을 혼합하여 사용 가능한 것으로, 주제인 A액의 제조 시, 디아민과 알데히드를 반응시켜 블록화한 것을 일부 사용함으로써, 폴리우레아의 경화시간을 늦춰 수작업이 가능하도록 한다.As such, in the present invention, Liquid A, the main liquid, and Liquid B, the hardener, are manufactured and packaged separately, and Liquid A and Liquid B can be mixed and used at the construction site. When producing Liquid A, the main liquid, diamine and aldehyde are reacted. By using some of the blocks, the curing time of polyurea is slowed down, making manual work possible.

Claims (4)

상온 경화형 폴리우레아 수지에 있어서,
상기 폴리우레아 수지는 디아민 100중량부에 대하여 글리콜류 5~10중량부, 안료 2~15중량부, 필러10~30중량부, 증점제 1~10중량부, 소포제 0.2~0.5중량부, 분산제 0.5~1.0중량부, 촉진제 0.2~1.0중량부를 혼합되는 주제 A액;
글리콜류 100중량부에 디이소시아네이트 100 중량부를 반응시켜 제조한 경화제 B액;으로 이루어지되,
상기 A액의 디아민 100중량부에는 디아민과 알데히드를 반응시켜 제조한 1차 반응물 디아민이 일부 포함되고,
상기 주제 A액의 디아민은 디에틸톨루엔디아민, 에틸렌디아민, 디메틸피오톨루엔디아민, 이소포론디아민, 폴리옥시프로필렌 디아민 중 어느 1종 또는 2종 이상이 사용되고,
상기 1차 반응물 디아민의 알데히드는 부틸알데히드, 이소부틸알데히드, 신남알데히드 중 어느 1종 또는 2종 이상이 사용되고,
상기 주제 A액과 경화제 B액의 글리콜류는 폴리옥시프로필렌 글리콜, 폴리에틸렌글리콜, 폴리테트라메틸렌에테르글리콜, 1.4부틸렌글리콜 중 어느 1종 또는 2종 이상 사용되며,
상기 경화제 B액의 디이소시아네이트는 TDI, MDI, IPDI, HDI, XMDI 중 어느 1종 또는 2종 이상 사용됨을 특징으로 하는 상온 경화형 폴리우레아 수지.
In the room temperature curing polyurea resin,
The polyurea resin contains 5 to 10 parts by weight of glycols, 2 to 15 parts by weight of pigment, 10 to 30 parts by weight of filler, 1 to 10 parts by weight of thickener, 0.2 to 0.5 parts by weight of antifoam, and 0.5 to 0.5 parts by weight of dispersant, based on 100 parts by weight of diamine. Main solution A mixed with 1.0 parts by weight and 0.2 to 1.0 parts by weight of accelerator;
It consists of a curing agent B solution prepared by reacting 100 parts by weight of diisocyanate with 100 parts by weight of glycols,
100 parts by weight of diamine in solution A includes some of the primary reactant diamine prepared by reacting diamine and aldehyde,
The diamine of the main solution A is any one or two or more of diethyltoluenediamine, ethylenediamine, dimethylpiotoluenediamine, isophorone diamine, and polyoxypropylene diamine,
The aldehyde of the primary reactant diamine is any one or two or more of butyraldehyde, isobutyraldehyde, and cinnamaldehyde,
The glycol of the main liquid A and the hardener liquid B is any one or two or more of polyoxypropylene glycol, polyethylene glycol, polytetramethylene ether glycol, and 1.4 butylene glycol,
A room temperature curable polyurea resin, characterized in that the diisocyanate of the curing agent B liquid is any one or two or more of TDI, MDI, IPDI, HDI, and XMDI.
삭제delete 디아민 100중량부에 대하여 글리콜류 5~10중량부, 안료 2~15중량부, 필러10~30중량부, 증점제 1~10중량부, 소포제 0.2~0.5중량부, 분산제 0.5~1.0중량부, 촉진제 0.2~1.0중량부를 혼합하여주제 A액을 제조하는 A액 제조단계;
글리콜류 100중량부에 디이소시아네이트 100 중량부를 반응시켜 NC0기의 함량이 14.5~15.5 중량%내에 포함되도록 경화제 B액을 제조하는 B액 제조단계;
상기 A액 제조단계 및 B액 제조단계에서 제조된 주제 A액과 경화제 B액을 A액 100중량부에 B액 70중량부를 혼합하여 시공표면에 도포하여 시공하는 혼합 및 시공단계;를 포함하며,
상기 A액 제조단계는 디아민을 반응기에 투입하고, 알데히드를 개량하여 드랍핑 탱크(dropping tank)에 투입한 후, 반응기 내부 온도를 서서히 승온하여 알데히드를 드랍핑(dropping)하여 반응시킨 후, 진공 탈수시켜 제조하는 1차 반응물 디아민 제조단계를 포함하는 것을 특징으로 하는 상온 경화형 폴리우레아 수지 제조방법.
For 100 parts by weight of diamine, 5 to 10 parts by weight of glycols, 2 to 15 parts by weight of pigment, 10 to 30 parts by weight of filler, 1 to 10 parts by weight of thickener, 0.2 to 0.5 parts by weight of antifoam, 0.5 to 1.0 parts by weight of dispersant, accelerator. Liquid A manufacturing step of mixing 0.2 to 1.0 parts by weight to prepare main liquid A;
Liquid B preparation step of reacting 100 parts by weight of diisocyanate with 100 parts by weight of glycol to prepare liquid B of curing agent so that the content of NC0 group is contained within 14.5 to 15.5% by weight;
It includes a mixing and construction step of mixing the main liquid A and the hardener liquid B prepared in the liquid A preparation step and the liquid B preparation step with 100 parts by weight of liquid A and 70 parts by weight of liquid B, and applying the mixture to the construction surface,
In the liquid A production step, diamine is added to the reactor, aldehyde is improved and added to a dropping tank, the temperature inside the reactor is gradually raised, the aldehyde is dropped to react, and then vacuum dehydration is performed. A method for producing a room temperature curable polyurea resin, characterized in that it includes the step of producing the first reactant diamine.
삭제delete
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Citations (7)

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JPH08193112A (en) * 1994-08-29 1996-07-30 Bayer Ag Polyisocyanate/polyamine mixture and its use in polyurea film production
KR20040012633A (en) * 2003-12-10 2004-02-11 김동규 Composition for floor material of concrete parking area, and construction method using thereof
JP2012121970A (en) * 2010-12-07 2012-06-28 Canon Chemicals Inc Polyurea resin composition and curing agent of aliphatic or alicyclic polyisocyanates
KR101372812B1 (en) 2013-06-04 2014-03-12 삼화페인트공업주식회사 Polyurea paint enable manual operation
KR102163364B1 (en) 2020-05-12 2020-10-08 김진영 Eco freindly hybrid polyurea resin-based composition and working method thereof
KR102209863B1 (en) * 2020-05-12 2021-01-28 김진영 Non-slip resin composition and non-slip packing materials using the same
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08193112A (en) * 1994-08-29 1996-07-30 Bayer Ag Polyisocyanate/polyamine mixture and its use in polyurea film production
KR20040012633A (en) * 2003-12-10 2004-02-11 김동규 Composition for floor material of concrete parking area, and construction method using thereof
JP2012121970A (en) * 2010-12-07 2012-06-28 Canon Chemicals Inc Polyurea resin composition and curing agent of aliphatic or alicyclic polyisocyanates
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