KR20040005448A - A method for preparing ethyl alcohol type polyurethane adhesive - Google Patents

A method for preparing ethyl alcohol type polyurethane adhesive Download PDF

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KR20040005448A
KR20040005448A KR1020020040017A KR20020040017A KR20040005448A KR 20040005448 A KR20040005448 A KR 20040005448A KR 1020020040017 A KR1020020040017 A KR 1020020040017A KR 20020040017 A KR20020040017 A KR 20020040017A KR 20040005448 A KR20040005448 A KR 20040005448A
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water
ethanol
polyurethane
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유종선
최경만
최명진
신수
김동호
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한국신발피혁연구소
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J175/00Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
    • C09J175/04Polyurethanes

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  • Organic Chemistry (AREA)
  • Adhesives Or Adhesive Processes (AREA)
  • Polyurethanes Or Polyureas (AREA)

Abstract

PURPOSE: Provided is a process for producing an ethylalcohol type polyurethane adhesive by dispersing a polyurethane adhesive in water and ethanol, which shortens drying time and improves adhesive force. CONSTITUTION: The process comprises the steps of: reacting 100pts.wt. of a polyol component comprising polyester and polyether polyol with 20-25pts.wt. of a diisocyanate component in a low boiling point polymerization solvent in the presence of a catalyst to prepare a prepolymer; neutralizing the prepolymer and then adding 2-5pts.wt. of a chain extender; dispersing it by using 50-150pts.wt. of the water and dropping 100-200pts.wt. of the ethanol and then performing a vacuum distillation to remove the polymerization solvent, wherein the weight ratio of the water and the ethanol is 20-70:30-80.

Description

에틸알코올형 폴리우레탄 접착제의 제조방법{A method for preparing ethyl alcohol type polyurethane adhesive}A method for preparing ethyl alcohol type polyurethane adhesive

본 발명은 폴리우레탄 접착제의 제조방법에 관한 것으로서, 더욱 상세하게는 폴리올 성분과 디이소시아네이트를 반응시켜 폴리우레탄 프리폴리머를 제조하고 중화반응과 쇄연장반응 후 물과 에탄올로 분산시킴으로써 종래의 물로만 분산시킨 폴리우레탄 수분산체에 비하여 건조시간을 단축하고 접착력을 향상시킨 폴리우레탄 접착제의 제조방법에 관한 것이다.The present invention relates to a method for preparing a polyurethane adhesive, and more particularly, to prepare a polyurethane prepolymer by reacting a polyol component and a diisocyanate, and to disperse only with conventional water by dispersing with water and ethanol after neutralization and chain extension reaction. The present invention relates to a method for producing a polyurethane adhesive having a shorter drying time and improved adhesion as compared to a polyurethane water dispersion.

지금까지 신발 및 여러 산업분야에서 사용해온 거의 대부분의 접착제는 인체에 유해한 유기용제로서 용제형 타입의 1액형 또는 2액형으로 이용되어 왔으며, 에틸 아세테이트(ethyl acetate, EA), 톨루엔, 메틸 에틸 케톤(methyl ethyl ketone, MEK) 등의 용제를 사용한 폴리클로로프렌(polychloroprene, CR) 또는 폴리우레탄 접착제 등을 사용하였다.Up to now, almost all adhesives used in footwear and various industries have been used as one- or two-component solvent-type organic solvents that are harmful to humans. Ethyl acetate (EA), toluene, methyl ethyl ketone ( Polychloroprene (CR) or a polyurethane adhesive using a solvent such as methyl ethyl ketone (MEK) or the like was used.

그러나 점차 작업환경 개선에 대한 작업자의 욕구의 증가와 인체에 대한 유해성을 개선하기 위한 방법의 일환으로서 수용성화 또는 무용제화로 전환되어 가는추세이다.However, as a part of increasing the worker's desire to improve the working environment and a method for improving the harmfulness to the human body, the trend is shifting to water solubilization or solvent-free.

따라서, 최근 신발용 접착제는 수분산형 폴리우레탄으로 대체되기 시작하였으며, 향후 급속하게 무독성 용매 타입으로 변화가 예상되지만 현재 사용되고 있는 수성 타입의 접착제는 웨팅성(wetting)이 좋지 못하며, 접착제 사용시 건조시간이 길게 소요되는 문제점이 있다.Therefore, in recent years, adhesives for footwear have been replaced by water-dispersed polyurethane, and it is expected to rapidly change to a non-toxic solvent type in the future, but the aqueous type adhesives currently used are not good in wetting, and the drying time when the adhesive is used There is a problem that takes a long time.

이에 본 발명의 발명자들은 상기와 같은 문제점를 해결하기 위하여 연구 노력한 결과, 통상의 폴리우레탄 접착제 조성물을 사용하여 폴리우레탄 접착제를 제조하되 쇄연장반응을 거친 후 분산반응시에 인체에 무해한 물과 에탄올을 특정 비율로 사용하면 웨팅성이 우수하고 건조시간이 짧은 폴리우레탄 접착제를 제조할 수 있음을 알게되어 본 발명을 완성하였다.Accordingly, the inventors of the present invention have made efforts to solve the problems described above, but the polyurethane adhesive is prepared using a conventional polyurethane adhesive composition, but after the chain extension reaction, specific water and ethanol that is harmless to the human body during the dispersion reaction. By using the ratio, it was found that a polyurethane adhesive having excellent wettability and a short drying time was completed, thereby completing the present invention.

따라서 본 발명은 에탄올을 분산제로 사용한 수분산성 폴리우레탄 접착제의 제조방법을 제공하는데 그 목적이 있다.Accordingly, an object of the present invention is to provide a method for producing a water dispersible polyurethane adhesive using ethanol as a dispersant.

본 발명은 폴리올 성분과 디이소시아네이트 성분, 쇄연장제, 촉매 및 중합용매를 사용하여 폴리우레탄계 접착제 조성물을 제조함에 있어서, 전체 고형분에 대하여 폴리에스테르 및 폴리에테르 폴리올의 혼합물로서 폴리올 성분 100 중량부에 대하여, 디이소시아네이트 성분 20 ∼ 25 중량부를 저비점 중합용매를 사용하여 촉매 존재하에 반응시켜서 프리폴리머를 제조하는 과정과, 상기 제조한 프리폴리머를 중화시킨 후 쇄연장제 2 ∼ 5 중량부를 첨가하여 쇄연장반응 시키는 과정과, 상기 쇄연장반응 후 분산제로서 물 50 ∼ 150 중량부를 사용하여 분산시킨 후 에탄올 100 ∼ 200 중량부를 적하하면서 분산시킨 다음 감압증류하여 중합용매를 제거하는 과정을 포함하여 이루어지는 폴리우레탄 접착제 제조방법을 특징으로 한다.The present invention provides a polyurethane-based adhesive composition using a polyol component, a diisocyanate component, a chain extender, a catalyst, and a polymerization solvent, based on 100 parts by weight of the polyol component as a mixture of polyester and polyether polyol based on the total solids. 20-25 parts by weight of the diisocyanate component is reacted in the presence of a catalyst using a low boiling point polymerization solvent to prepare a prepolymer, and neutralizing the prepared prepolymer, followed by chain extension reaction by adding 2 to 5 parts by weight of a chain extender. And, after the chain extension reaction is dispersed using 50 to 150 parts by weight of water as a dispersant and dispersed while dropping 100 to 200 parts by weight of ethanol and distilled under reduced pressure to remove the polymerization solvent comprising a process for producing a polyurethane adhesive It features.

이와 같은 본 발명을 상세하게 설명하면 다음과 같다.The present invention will be described in detail as follows.

본 발명에서는 폴리우레탄을 합성하기 위해서 폴리올과 이온성 모노머를 디이소시아네이트와 반응시키고 디이소시아네이트(NCO)기를 수산화기(OH)보다 과량 사용하여 폴리우레탄 프리폴리머를 제조한 후 쇄연장제를 첨가하여 쇄연장반응시켜서 폴리우레탄을 합성한다. 그리고 물을 사용해서 분산을 돕고 알코올을 첨가해서 물과 알코올에 분산된 폴리우레탄 접착제를 합성하였다.In the present invention, in order to synthesize the polyurethane, the polyol and ionic monomer is reacted with diisocyanate, and the polyisocyanate (NCO) group is used in excess of the hydroxyl group (OH) to prepare the polyurethane prepolymer, followed by the chain extension reaction by adding a chain extender. To synthesize polyurethane. Water was used to aid dispersion and alcohol was added to synthesize polyurethane adhesives dispersed in water and alcohol.

본 발명에 사용되는 폴리올성분으로는 폴리에스테르 폴리올과 폴리에테르 폴리올 등의 폴리올 성분을 사용하며, 디이소시아네이트 성분으로서는 1,6-헥사메틸렌 디이소시아네이트(HDI), 4,4'-디사이클로 헥실 메탄 디이소시아네이트 (H12MDI) 등을 사용한다.As the polyol component used in the present invention, polyol components such as polyester polyol and polyether polyol are used. As the diisocyanate component, 1,6-hexamethylene diisocyanate (HDI) and 4,4'-dicyclohexyl methane di Isocyanate (H 12 MDI) and the like.

OH 기가 도입된 프리폴리머를 고분자량화하기 위해 사용되는 쇄연장제는 말단에 2개 이상의 반응기를 갖는 화합물을 사용할 수 있으며, 구체적으로 예를 들면 에틸렌 글리콜, 2,2-디메칠-1,3-프로판디올, 1,6-헥산디올, 피페라진, 1,6-헥사메틸렌디아민 등을 사용한다.The chain extender used for high molecular weight of the prepolymer in which the OH group is introduced may be used a compound having two or more reactors at its end, and specifically, for example, ethylene glycol, 2,2-dimethyl-1,3- Propanediol, 1,6-hexanediol, piperazine, 1,6-hexamethylenediamine and the like are used.

폴리올 성분은 100 ∼ 110 ℃ 에서 감압 증류하여 정제해서 사용하며, 교반기와 냉각기가 장착된 5구 분리형 플라스크에 상기 폴리올을 넣고 80 ∼ 85 ℃로 온도를 높여서 약 30 분간 교반 하면서 혼합한다. 그 다음 촉매(DBTDL: Dibutyl tin dilaurate)를 0.02 중량부 투입하고 10분간 더 교반해 준 다음 정해진 양의 이소시아네이트를 가해주고 반응을 진행한다. 반응이 종결된 후 온도를 상온으로 낮추어 이소시아네이트가 양 말단에 있는 폴리우레탄 프리폴리머를 합성한다. 합성의 전 과정에서 점도를 조절하기 위해 용매인 아세톤을 일정량 첨가하였다.The polyol component is purified by distillation under reduced pressure at 100 to 110 ° C., and the polyol is added to a five-necked separate flask equipped with a stirrer and a cooler, and the mixture is stirred while heating at 80 to 85 ° C. for about 30 minutes. Next, 0.02 parts by weight of a catalyst (DBTDL: Dibutyl tin dilaurate) is added and stirred for 10 minutes, and then a predetermined amount of isocyanate is added to proceed with the reaction. After the reaction is completed, the temperature is lowered to room temperature to synthesize a polyurethane prepolymer having isocyanates at both ends. A certain amount of acetone, a solvent, was added to adjust the viscosity throughout the synthesis.

반응물이 25 ∼ 30 ℃가 되면 중화제로서 아세톤에 희석된 정량의 TEA (Triethylamine)를 이용하여 중화를 시키고 약 40 분간 더 교반한다. 중화가 완료된 폴리우레탄 프리폴리머에 쇄연장제를 넣고 2시간에 걸쳐 쇄연장 반응을 한다. 그 후에 증류수를 천천히 적하하면서 유화시킨 후 알코올을 사용하여 완전한 폴리우레탄 분산체를 제조한다. 사용되는 물의 양은 50 ∼ 150 중량부이며 이때, 50 중량부 미만이면 폴리우레탄 접착제의 안정성이 떨어지고, 150 중량부를 초과하면 에탄올에 의한 빠른 건조효과를 기대할 수 없다. 사용되는 에탄올의 양은 100 ∼ 200 중량부이며, 이때 에탄올 사용량이 100 중량부 미만이면 에탄올에 의한 빠른 건조효과와 웨팅성을 기대할 수 없고, 200 중량부를 초과하면 폴리우레탄 접착제의 안정성이 결여된다. 즉, 최종 접착제에 포함된 용매 중에 물의 양이 20 ∼ 70%가 되도록 조절하여 증류수를 첨가한다. 물의 양이 20% 이하인 경우 안정성이 떨어지고, 70% 이상인 경우 알코올에 의한 빠른 건조와 웨팅성을 기대하기 힘들다. 그 후에 감압상태 또는 상압상태, 40 ∼ 45 ℃에서 용제를 추출하여 물과 알코올에 분산된 폴리우레탄 접착제를 얻는다. 최종 제조된 폴리우레탄 접착제의 농도를 50%로 조정하고 기타 첨가제 등을 이용하여 점도를 조정한다.When the reactant reaches 25 to 30 ° C., neutralize using a fixed amount of TEA (Triethylamine) diluted in acetone as a neutralizing agent and stir for about 40 minutes. The chain extender is added to the neutralized polyurethane prepolymer and subjected to chain extension reaction for 2 hours. Thereafter, distilled water is slowly added dropwise to emulsify, and then alcohol is used to prepare a complete polyurethane dispersion. The amount of water used is 50 to 150 parts by weight, at which time the stability of the polyurethane adhesive is lowered if it is less than 50 parts by weight, and if it exceeds 150 parts by weight, rapid drying effect by ethanol cannot be expected. The amount of ethanol to be used is 100 to 200 parts by weight, wherein when the amount of ethanol used is less than 100 parts by weight, the rapid drying effect and the wettability by ethanol cannot be expected, and when it exceeds 200 parts by weight, the polyurethane adhesive lacks stability. That is, distilled water is added to adjust the amount of water to be 20 to 70% in the solvent contained in the final adhesive. If the amount of water is less than 20%, the stability is poor, if more than 70% it is difficult to expect fast drying and wetting by alcohol. Thereafter, the solvent is extracted at 40 to 45 ° C. under reduced pressure or normal pressure to obtain a polyurethane adhesive dispersed in water and alcohol. The concentration of the finally prepared polyurethane adhesive is adjusted to 50% and the viscosity is adjusted using other additives and the like.

이하 본 발명을 실시예에 의거하여 구체적으로 설명하겠는바, 본 발명이 다음 실시예에 의해 한정되는 것은 아니다.Hereinafter, the present invention will be described in detail with reference to Examples, but the present invention is not limited by the following Examples.

실시예 1Example 1

다음 표 1에 나타낸 바와 같이, 폴리 에스테르폴리올인 PBA 3791 47.6 중량부, 폴리카프로락톤다이올인 CAPA 240 40.3 중량부, 이온성 모노머인 P-205BA 12.1 중량부를 반응기에 주입하여 80 ∼ 85 ℃로 승온시킨 후, 0.02 중량부의 촉매(DBTDL)을 첨가하고, 10분간 더 교반해 준 다음 22 중량부의 4,4'-디사이클로 헥실 메탄 디이소시아네이트(H12MDI)를 가해주고 4시간 정도 반응을 진행시킨 후 온도를 낮추어 프리폴리머를 제조하였다. 합성의 전 과정에서 점도를 조절하기 위해 아세톤을 150 ∼ 200 중량부 첨가하였다.As shown in Table 1, 47.6 parts by weight of PBA 3791, which is a polyester polyol, 40.3 parts by weight of CAPA 240, which is a polycaprolactonediol, and 12.1 parts by weight of P-205BA, which is an ionic monomer, were heated to 80 to 85 ° C. Thereafter, 0.02 parts by weight of catalyst (DBTDL) was added, followed by stirring for 10 minutes, followed by addition of 22 parts by weight of 4,4'-dicyclohexyl methane diisocyanate (H 12 MDI), followed by reaction for about 4 hours. The prepolymer was prepared by lowering the temperature. Acetone was added in an amount of 150 to 200 parts by weight to adjust the viscosity throughout the synthesis.

반응물이 상온이 되면 아세톤에 10 % 농도로 희석된 TEA를 2.5 중량부 사용하여 중화시키고 약 40 분간 더 교반하여 중화를 완료시킨 후 제조된 폴리우레탄 프리폴리머에 쇄연장제인 1.6-HDA를 2.2 중량부 사용하여 2시간에 걸쳐 쇄연장 반응시켰다.When the reaction product is at room temperature, neutralize the mixture by using 2.5 parts by weight of TEA diluted to 10% in acetone, and stirring the solution for about 40 minutes to complete the neutralization. Then, 2.2 parts by weight of 1.6-HDA, a chain extender, is used in the prepared polyurethane prepolymer. Chain reaction was carried out over 2 hours.

쇄연장후에 알코올에 분산이 잘 이루어지도록 50 중량부의 증류수를 천천히적하하면서 유화시키고 어느 정도 유화가 진행되면 알코올을 200 중량부 첨가하여 물과 알코올에 분산된 폴리우레탄을 합성하고 감압증류로 아세톤을 제거하여 고형분양 50 %의 유백색의 폴리우레탄 분산체를 제조하였다.After chain extension, 50 parts by weight of distilled water is slowly dropped to emulsify the alcohol well, and after emulsification to some extent, 200 parts by weight of alcohol is added to synthesize polyurethane dispersed in water and alcohol, and acetone is removed by distillation under reduced pressure. To prepare a milky polyurethane dispersion of 50% solid content.

실시예 2Example 2

상기 실시예 1과 동일한 방법으로 폴리우레탄 분산체를 제조하되 쇄연장 반응 후 사용하는 물과 에탄올을 각각 100 중량부와 150 중량부를 사용하였으며, 각 조성성분은 다음 표 1에 나타내었다.To prepare a polyurethane dispersion in the same manner as in Example 1, 100 parts by weight and 150 parts by weight of water and ethanol, respectively, used after the chain extension reaction were used, and each component is shown in Table 1 below.

실시예 3Example 3

상기 실시예 1과 동일한 방법으로 폴리우레탄 분산체를 제조하되 쇄연장 반응 후 사용하는 물과 에탄올을 각각 150 중량부와 100 중량부를 사용하였으며, 각 조성성분은 다음 표 1에 나타내었다.The polyurethane dispersion was prepared in the same manner as in Example 1, but 150 parts by weight and 100 parts by weight of water and ethanol, respectively, used after the chain extension reaction, were shown in Table 1 below.

비교예Comparative example

다음 표 1에 나타낸 바와 같이, 폴리 에스테르폴리올인 PBA 3791(평균 분자량 : 3791) 47.6 중량부, 폴리카프로락톤다이올인 CAPA 240(평균 분자량 : 4000) 40.3 중량부, 이온성 모노머인 P-205BA(평균 분자량 : 500) 12.1 중량부를 반응기에 주입하여 80 ∼ 85 ℃로 승온시킨 후, 0.02 중량부의 촉매(DBTDL)을 첨가하고, 10분간 더 교반해 준 다음 22 중량부의 4,4'-디사이클로 헥실 메탄디이소시아네이트(H12MDI)를 가해주고 4시간 정도 반응을 진행시킨 후 온도를 낮추어 프리폴리머를 제조한다. 합성의 전 과정에서 점도 조절을 위해 이소시아네이트나 폴리올과 반응하지 않는 아세톤을 일정량 가해준다.As shown in Table 1, 47.6 parts by weight of PBA 3791 (average molecular weight: 3791), which is a polyester polyol, 40.3 parts by weight of CAPA 240 (average molecular weight: 4000), which is a polycaprolactonediol, and P-205BA (average, which is an ionic monomer) Molecular weight: 500) 12.1 parts by weight of the reactor was heated to 80 to 85 ° C., then 0.02 parts by weight of catalyst (DBTDL) was added and stirred for 10 minutes, followed by 22 parts by weight of 4,4′-dicyclohexyl methane. After adding a diisocyanate (H 12 MDI) and proceeding the reaction for about 4 hours to prepare a prepolymer by lowering the temperature. A certain amount of acetone, which does not react with isocyanates or polyols, is added to control the viscosity throughout the synthesis.

반응물이 상온이 되면 아세톤에 희석된 정량의 TEA를 2.5 중량부 사용하여 중화를 시키고 약 40분간 더 교반한다. 중화가 완료된 폴리우레탄 프리폴리머에 1.6-HDA를 2.2 중량부 사용하여 2시간에 걸쳐 쇄연장 반응을 한다. 쇄연장후에 250 중량부의 증류수를 천천히 적하하면서 유화시켜서 수분산된 폴리우레탄을 합성하고 감압증류로 용제를 제거하여 고형분양 50%의 유백색의 폴리우레탄 분산체를 제조한다.When the reactant is at room temperature, 2.5 parts by weight of TEA diluted in acetone is neutralized and stirred for about 40 minutes. The chain extension reaction was carried out over 2 hours using 1.6 parts by weight of 1.6-HDA in the neutralized polyurethane prepolymer. After chain extension, 250 parts by weight of distilled water is slowly added dropwise to emulsify the synthetic polyurethane, and the solvent is removed by distillation under reduced pressure to prepare a milky polyurethane dispersion having a solid content of 50%.

구성성분Ingredient 조성성분(중량부)Ingredients (parts by weight) 실시예1Example 1 실시예2Example 2 실시예3Example 3 비교예Comparative example 폴리올Polyol 폴리에스테르폴리올1) Polyester Polyol 1) 47.647.6 47.647.6 47.647.6 47.647.6 폴리카프로락톤다이올2) Polycaprolactone diol 2) 40.340.3 40.340.3 40.340.3 40.340.3 이온성 모노머3) Ionic monomer 3) 12.112.1 12.112.1 12.112.1 12.112.1 디이소시아네이트4) Diisocyanate 4) 2222 2222 2222 2222 중화제5) Neutralizer 5) 2.52.5 2.52.5 2.52.5 2.52.5 쇄연장제6) Chain extension agent 6) 2.22.2 2.22.2 2.22.2 2.22.2 촉매7) Catalyst 7) 0.020.02 0.020.02 0.020.02 0.020.02 분산제Dispersant water 5050 100100 150150 250250 에탄올8) Ethanol 8) 200200 150150 100100 -- 1)PBA 3791(평균분자량: 3791), 애경화학2)CAPA 240(평균분자량: 4000), Solvay3)P-205BA(평균분자량: 500), Daicel4)H12MDI, aldrich5)TEA, aldrich6)1,6-HDA, aldrich7)DBTDL, Fluka8)ethanol, aldrich1) PBA 3791 (average molecular weight: 3791), Aekyung Chemistry 2) CAPA 240 (average molecular weight: 4000), Solvay 3) P-205BA (average molecular weight: 500), Daicel4) H 12 MDI, aldrich5) TEA, aldrich6) 1, 6-HDA, aldrich 7) DBTDL, Fluka 8) ethanol, aldrich

실험예Experimental Example

상기 실시예 1 ∼ 3와 비교예에서 제조된 폴리우레탄 수분산체는 다음과 같은 방법에 의해 특성을 검토하였으며 그 결과는 다음 표 2에 나타내었다.The polyurethane water dispersions prepared in Examples 1 to 3 and Comparative Examples were characterized by the following method, and the results are shown in Table 2 below.

<접착시편 제조><Adhesive specimen preparation>

본 실험에서 사용된 고무 피착재는 연마석으로 연마한 후 톨루엔으로 세척하여 사용하였다. 고무에 폴리우레탄 접착제용 전처리제인 D-PLY 007을 도포하고 60 ℃에서 5분간 건조시켰다. 접착제를 도포하고 60 ℃에서 4분간 건조시킨 후 압착하여 접착 시편을 제조하였으며, 폼(EVA 발포체, 비중 0.15 ∼ 0.3) 피착재는 D-PLY PC-3(동성NSC)로 세척하여 사용하였다. 완전히 건조 후 UV용 전처리제인 D-PLY P-5-2를 도포한 후 UV(200∼400nm)에 2회 통과시켰다. 그 후 상기 실시예 1 ∼ 3와 비교예에 따라 제조된 접착제를 도포하고 65 ℃에서 4 분간 건조시킨 후 압착하여 접착시편을 제조하였다.The rubber adherend used in this experiment was polished with abrasive stone and washed with toluene. D-PLY 007, a pretreatment agent for polyurethane adhesives, was applied to rubber and dried at 60 ° C. for 5 minutes. The adhesive was applied and dried at 60 ° C. for 4 minutes and then pressed to prepare an adhesive specimen. Foam (EVA foam, specific gravity 0.15 to 0.3) adherend was washed with D-PLY PC-3 (Dynamic NSC). After completely drying, D-PLY P-5-2, a UV pretreatment agent, was applied and then passed through UV (200-400 nm) twice. Thereafter, adhesives prepared according to Examples 1 to 3 and Comparative Examples were applied, dried at 65 ° C. for 4 minutes, and pressed to prepare an adhesive specimen.

<접착력 평가><Adhesion evaluation>

준비된 고무와 폼(EVA 발포체, 비중 0.15 ∼ 0.3) 피착재 위에 폴리우레탄 접착제를 도포하고 압착시킨 다음 5분후에 접착력평가를 해서 초기접착력을 측정하고, 24시간 후에 접착력평가를 해서 상태접착력을 측정하였다.Polyurethane adhesive was applied on the prepared rubber and foam (EVA foam, specific gravity 0.15 to 0.3) adherend and pressed, and after 5 minutes, the adhesive strength was evaluated and the initial adhesive strength was measured. After 24 hours, the adhesive strength was evaluated. .

구분division 실시예1Example 1 실시예2Example 2 실시예3Example 3 비교예Comparative example 물성Properties 초기접착력(kgf/cm)Initial Adhesion (kgf / cm) 3.53.5 3.03.0 2.72.7 2.52.5 접착개선효과(%)Adhesion Improvement Effect (%) 140140 120120 108108 100100 상태접착력(kgf/cm)Adhesive force (kgf / cm) 4.04.0 3.93.9 3.73.7 3.53.5 접착개선효과(%)Adhesion Improvement Effect (%) 114114 111111 106106 100100 건조시간* Drying time * 3분3 minutes 4분4 minutes 4분 30초4 minutes 30 seconds 8분8 minutes 피착재Substrate 고무/폼(EVA 발포체)Rubber / Foam (EVA Foam) * 건조는 60 ℃의 컨벡션 오븐에서 실시하였다.Drying was carried out in a convection oven at 60 ° C.

상기 표 2에 나타낸 바와 같이, 본 발명에 따라 제조된 폴리우레탄 접착제는물로만 분산시킨 비교예 보다 초기접착력과 상태접착력이 우수하며, 건조시간이 약 2배 단축됨을 알 수 있다.As shown in Table 2, the polyurethane adhesive prepared according to the present invention is superior to the initial adhesive strength and state adhesive strength than the comparative example dispersed only in water, it can be seen that the drying time is reduced by about 2 times.

상기한 바와 같이, 본 발명의 제조방법에 따르면 폴리우레탄 접착제를 물과 에탄올로서 분산시킴으로써 유기용제를 사용하지 않아서 인체에 대한 유해성을 제거하였으며, 그 결과 작업환경을 개선할 수 있고, 에탄올에 의한 웨팅성 개선으로 접착력이 향상되며 건조시간이 단축되어 접착공정에서 생산력을 높이는 폴리우레탄 접착제를 제조할 수 있다.As described above, according to the production method of the present invention, by dispersing the polyurethane adhesive as water and ethanol, organic solvents are not used to remove harmful effects to the human body, and as a result, the working environment can be improved, Improved adhesiveness improves the adhesive strength and can shorten the drying time to produce a polyurethane adhesive to increase the productivity in the bonding process.

Claims (3)

폴리올 성분과 디이소시아네이트 성분, 쇄연장제, 촉매 및 중합용매를 사용하여 폴리우레탄계 접착제 조성물을 제조함에 있어서,In preparing a polyurethane-based adhesive composition using a polyol component and a diisocyanate component, a chain extender, a catalyst and a polymerization solvent, 전체 고형분에 대하여 폴리에스테르 및 폴리에테르 폴리올의 혼합물로서 폴리올 성분 100 중량부에 대하여, 디이소시아네이트 성분 20 ∼ 25 중량부를 저비점중합용매를 사용하여 촉매 존재하에 반응시켜서 프리폴리머를 제조하는 과정과,Preparing a prepolymer by reacting 20 to 25 parts by weight of the diisocyanate component in the presence of a catalyst using a low boiling point polymerization solvent with respect to 100 parts by weight of the polyol component as a mixture of polyester and polyether polyol with respect to the total solids; 상기 제조한 프리폴리머를 중화시킨 후 쇄연장제 2 ∼ 5 중량부를 첨가하여 쇄연장반응 시키는 과정과,Neutralizing the prepared prepolymer and then adding 2 to 5 parts by weight of a chain extender to perform a chain extension reaction; 상기 쇄연장반응 후 분산제로서 물 50 ∼ 150 중량부를 사용하여 분산시킨 후 에탄올 100 ∼ 200 중량부를 적하하면서 분산시킨 다음 감압증류하여 중합용매를 제거하는 과정을 포함하는 것을 특징으로 하는 폴리우레탄 접착제 제조방법.After the chain extension reaction is dispersed using 50 to 150 parts by weight of water as a dispersant, and then dispersed while dropping 100 to 200 parts by weight of ethanol and distilled under reduced pressure to remove the polymerization solvent, characterized in that it comprises a polyurethane adhesive manufacturing method . 제 1 항에 있어서, 상기 물과 에탄올은 20 ∼ 70 : 30 ∼ 80 중량비의 범위로 이루어지는 것임을 특징으로 하는 폴리우레탄 접착제 제조방법.The method of claim 1, wherein the water and ethanol are in the range of 20 to 70:30 to 80 weight ratio. 상기 청구항 1 내지 2항의 방법으로 제조된 것을 특징으로 하는 폴리우레탄 접착제.Polyurethane adhesive, characterized in that produced by the method of claim 1 to 2.
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KR101222112B1 (en) * 2009-12-14 2013-01-15 한국신발피혁연구소 The composition of dismantlable polyurethane adhesives and its dismantlement method
KR102510617B1 (en) * 2022-10-05 2023-03-20 주식회사 세진에코텍 Chain break detection and tension apparatus

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KR102510617B1 (en) * 2022-10-05 2023-03-20 주식회사 세진에코텍 Chain break detection and tension apparatus

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