KR20040005448A - A method for preparing ethyl alcohol type polyurethane adhesive - Google Patents
A method for preparing ethyl alcohol type polyurethane adhesive Download PDFInfo
- Publication number
- 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
- Authority
- KR
- South Korea
- Prior art keywords
- weight
- parts
- water
- ethanol
- polyurethane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 64
- 239000000853 adhesive Substances 0.000 title claims abstract description 43
- 230000001070 adhesive effect Effects 0.000 title claims abstract description 43
- 229920002635 polyurethane Polymers 0.000 title claims abstract description 32
- 239000004814 polyurethane Substances 0.000 title claims abstract description 32
- 238000000034 method Methods 0.000 title claims abstract description 10
- 235000019441 ethanol Nutrition 0.000 title abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 229920005862 polyol Polymers 0.000 claims abstract description 17
- 150000003077 polyols Chemical class 0.000 claims abstract description 17
- 239000002904 solvent Substances 0.000 claims abstract description 14
- 125000005442 diisocyanate group Chemical group 0.000 claims abstract description 10
- 239000004970 Chain extender Substances 0.000 claims abstract description 9
- 239000003054 catalyst Substances 0.000 claims abstract description 9
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 8
- 239000004721 Polyphenylene oxide Substances 0.000 claims abstract description 4
- 230000003472 neutralizing effect Effects 0.000 claims abstract description 4
- 229920000570 polyether Polymers 0.000 claims abstract description 4
- 238000009835 boiling Methods 0.000 claims abstract description 3
- 229920000728 polyester Polymers 0.000 claims abstract description 3
- 238000006243 chemical reaction Methods 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 7
- 239000002270 dispersing agent Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 238000001035 drying Methods 0.000 abstract description 12
- 238000005292 vacuum distillation Methods 0.000 abstract 1
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 15
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 14
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 9
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 6
- 229920001730 Moisture cure polyurethane Polymers 0.000 description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 239000006260 foam Substances 0.000 description 6
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 description 5
- 229920003009 polyurethane dispersion Polymers 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- 239000012153 distilled water Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 229920001971 elastomer Polymers 0.000 description 4
- 239000012948 isocyanate Substances 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 229920005906 polyester polyol Polymers 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000012936 correction and preventive action Methods 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 150000002513 isocyanates Chemical class 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- GLUUGHFHXGJENI-UHFFFAOYSA-N Piperazine Chemical compound C1CNCCN1 GLUUGHFHXGJENI-UHFFFAOYSA-N 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000009931 harmful effect Effects 0.000 description 2
- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 238000009736 wetting Methods 0.000 description 2
- 229940008841 1,6-hexamethylene diisocyanate Drugs 0.000 description 1
- 239000005057 Hexamethylene diisocyanate Substances 0.000 description 1
- 241000282412 Homo Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012975 dibutyltin dilaurate Substances 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 229920001084 poly(chloroprene) Polymers 0.000 description 1
- 229920001610 polycaprolactone Polymers 0.000 description 1
- 239000004632 polycaprolactone Substances 0.000 description 1
- 239000005056 polyisocyanate Substances 0.000 description 1
- 229920001228 polyisocyanate Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J175/00—Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
- C09J175/04—Polyurethanes
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
Description
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%.
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. .
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)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020020040017A KR20040005448A (en) | 2002-07-10 | 2002-07-10 | A method for preparing ethyl alcohol type polyurethane adhesive |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020020040017A KR20040005448A (en) | 2002-07-10 | 2002-07-10 | A method for preparing ethyl alcohol type polyurethane adhesive |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| KR20040005448A true KR20040005448A (en) | 2004-01-16 |
Family
ID=37315766
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR1020020040017A Ceased KR20040005448A (en) | 2002-07-10 | 2002-07-10 | A method for preparing ethyl alcohol type polyurethane adhesive |
Country Status (1)
| Country | Link |
|---|---|
| KR (1) | KR20040005448A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US607998A (en) * | 1898-07-26 | Heinrich kurtzig | ||
| US5043381A (en) * | 1987-09-14 | 1991-08-27 | Ici Americas, Inc. | Aqueous dispersions of a nonionic, water dispersible polyurethane having pendent polyoxyethylene chains |
| US5371166A (en) * | 1993-12-22 | 1994-12-06 | The B. F. Goodrich Company | Polyurethane composition for use as a dispersing binder |
| JPH11228667A (en) * | 1997-07-24 | 1999-08-24 | Bayer Ag | Aqueous polyurethane dispersed material having improved water resistance and solvent resistance |
| KR20010093832A (en) * | 1999-10-15 | 2001-10-29 | 더블유. 에이치. 바스코비치, 선드롬 시워트 | Process for the preparation of an aqueous dispersion of an anionic polyurethane free of volatile tertiary amines |
| WO2002010243A1 (en) * | 2000-07-27 | 2002-02-07 | 3M Innovative Properties Company | Polyurethane dispersion in alcohol-water system |
-
2002
- 2002-07-10 KR KR1020020040017A patent/KR20040005448A/en not_active Ceased
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US607998A (en) * | 1898-07-26 | Heinrich kurtzig | ||
| US5043381A (en) * | 1987-09-14 | 1991-08-27 | Ici Americas, Inc. | Aqueous dispersions of a nonionic, water dispersible polyurethane having pendent polyoxyethylene chains |
| US5371166A (en) * | 1993-12-22 | 1994-12-06 | The B. F. Goodrich Company | Polyurethane composition for use as a dispersing binder |
| JPH11228667A (en) * | 1997-07-24 | 1999-08-24 | Bayer Ag | Aqueous polyurethane dispersed material having improved water resistance and solvent resistance |
| KR20010093832A (en) * | 1999-10-15 | 2001-10-29 | 더블유. 에이치. 바스코비치, 선드롬 시워트 | Process for the preparation of an aqueous dispersion of an anionic polyurethane free of volatile tertiary amines |
| WO2002010243A1 (en) * | 2000-07-27 | 2002-02-07 | 3M Innovative Properties Company | Polyurethane dispersion in alcohol-water system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104774307B (en) | Preparation method of modified polyurethane flexible macromolecule emulsion of the chain alkyl containing side and products thereof | |
| EP1558659B1 (en) | Polyurethane dispersion and articles prepared therefrom | |
| KR101124471B1 (en) | Synthesis and composition of solvent-free waterborne polyurethane emulsion | |
| KR101784727B1 (en) | Manufacturing method of water based polyurethane adhesive composition with excellent adhesion | |
| CN1470564A (en) | water dispersible polyisocyanate composition and use thereof | |
| CN109957091B (en) | Polyurethane polymer suitable for adjusting viscosity of aqueous high-solvent system and composition containing polyurethane polymer | |
| CN116888230B (en) | Coating composition for metal with improved oil resistance and adhesion, method for preparing the same, and metal article coated therewith | |
| JP4128785B2 (en) | Novel polyurethanes and their use in thickening aqueous systems | |
| EP4169965B1 (en) | Hydrophilic acryl-modified polyurethane and method for preparing the same, and waterborne coating composition prepared therefrom and method for preparing the same | |
| KR101861086B1 (en) | Polyureathane water dispersion composition having improved adhesion for artificial leather | |
| US20050049358A1 (en) | Water dispersible polyisocyanate composition bearing urea and/or biuret and its uses | |
| CN113072852B (en) | Preparation method of fluorine-silicon-containing waterborne polyurethane acrylate composite coating for wood lacquer | |
| KR20120118657A (en) | Polyurethane adhesive composition in improving bonding strength for nylon shoe material | |
| KR20040005448A (en) | A method for preparing ethyl alcohol type polyurethane adhesive | |
| CN108530603A (en) | Mica modified aqueous polyurethane emulsion, adhesive and preparation method thereof | |
| KR20230060252A (en) | Waterborne polyurethane acrylate hybrid containing sulfonic acid groups and manufacturing method thereof | |
| KR102116533B1 (en) | Manufacturing method of waterborne polyurethane-arcylate silane adhesive having shorter adhesive process and waterborne polyurethane-arcylate silane adhesive using the same | |
| KR100341870B1 (en) | Process for preparing aqueous polyurethane | |
| CN116082598B (en) | Water-based polyurethane resin with impact resistance, and preparation method and application thereof | |
| US7772307B2 (en) | Water dispersible polyisocyanate composition and its uses | |
| TW202045572A (en) | Preparation method of waterborne polyurethane dispersion composition and waterborne polyurethane coating being free of pungent smell, healthy and environment-friendly | |
| KR101804895B1 (en) | Polysiloxane-modified waterborne-polyurethane coating composition and method for producing same | |
| CN115785367A (en) | Preparation method and application of waterborne polyurethane resin emulsion without added organic solvent | |
| MXPA05000436A (en) | Low residual monomer ipdi-ppg prepolymer. | |
| KR20230105701A (en) | Method of manufacturing scratch-resistant coating agent for biaxially oriented polypropylene film |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A201 | Request for examination | ||
| PA0109 | Patent application |
Patent event code: PA01091R01D Comment text: Patent Application Patent event date: 20020710 |
|
| PA0201 | Request for examination | ||
| PG1501 | Laying open of application | ||
| E902 | Notification of reason for refusal | ||
| PE0902 | Notice of grounds for rejection |
Comment text: Notification of reason for refusal Patent event date: 20050315 Patent event code: PE09021S01D |
|
| E601 | Decision to refuse application | ||
| PE0601 | Decision on rejection of patent |
Patent event date: 20050907 Comment text: Decision to Refuse Application Patent event code: PE06012S01D Patent event date: 20050315 Comment text: Notification of reason for refusal Patent event code: PE06011S01I |