KR100394365B1 - A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it - Google Patents

A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it Download PDF

Info

Publication number
KR100394365B1
KR100394365B1 KR10-2000-0061149A KR20000061149A KR100394365B1 KR 100394365 B1 KR100394365 B1 KR 100394365B1 KR 20000061149 A KR20000061149 A KR 20000061149A KR 100394365 B1 KR100394365 B1 KR 100394365B1
Authority
KR
South Korea
Prior art keywords
weight
polymerization
pressure
sensitive adhesive
added
Prior art date
Application number
KR10-2000-0061149A
Other languages
Korean (ko)
Other versions
KR20010007889A (en
Inventor
구용공
Original Assignee
(주) 고려물산
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by (주) 고려물산 filed Critical (주) 고려물산
Priority to KR10-2000-0061149A priority Critical patent/KR100394365B1/en
Publication of KR20010007889A publication Critical patent/KR20010007889A/en
Application granted granted Critical
Publication of KR100394365B1 publication Critical patent/KR100394365B1/en

Links

Classifications

    • 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
    • C09J4/00Adhesives based on organic non-macromolecular compounds having at least one polymerisable carbon-to-carbon unsaturated bond ; adhesives, based on monomers of macromolecular compounds of groups C09J183/00 - C09J183/16
    • 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
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C09J133/062Copolymers with monomers not covered by C09J133/06
    • C09J133/064Copolymers with monomers not covered by C09J133/06 containing anhydride, COOH or COOM groups, with M being metal or onium-cation
    • 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
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C09J133/062Copolymers with monomers not covered by C09J133/06
    • C09J133/066Copolymers with monomers not covered by C09J133/06 containing -OH groups
    • 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
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C09J133/08Homopolymers or copolymers of acrylic acid esters
    • 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
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C09J133/10Homopolymers or copolymers of methacrylic acid esters
    • C09J133/12Homopolymers or copolymers of methyl methacrylate
    • 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
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/18Homopolymers or copolymers of nitriles

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

본 발명은 유화제가 첨가되지 않는 점착제 및 그 제조방법에 관한 것으로서, 더욱 상세하게는 점착제를 구성하는 필수적인 유성의 조성물을 인체에 무해하며 환경 친화적인 에틸알코올 또는 에틸알코올 및 이소프로필알코올로 이루어진 모스타놀과 물을 용매로서 수용화시켜 알코올중합을 유도함으로써 용액중합으로 제조된 점착제의 점착력과 내수성 등의 물성을 그대로 유지하면서 인체 및 환경에는 무해할 뿐만 아니라 유기용매에 비해 저가의 모스타놀과 물을 병용함에 따른 폭발성의 배제 및 점착제의 제조원가 절감이 가능하게 되어 생산성 및 수익성을 증대할 수 있도록 한 유화제가 첨가되지 않는 점착제 및 그 제조방법에 관한 것이다.The present invention relates to a pressure-sensitive adhesive that is not added to the emulsifier and to a method for manufacturing the same, and more particularly, the essential oil composition constituting the pressure-sensitive adhesive harmless to the human body and made of environmentally friendly ethyl alcohol or ethyl alcohol and isopropyl alcohol. Soluble sol and water as a solvent to induce alcohol polymerization, it is harmless to human body and environment while maintaining the adhesiveness and water resistance of adhesive prepared by solution polymerization. The present invention relates to a pressure-sensitive adhesive and a method of manufacturing the same, wherein the emulsifier is not added so that the explosive exclusion and the production cost of the pressure-sensitive adhesive can be reduced and the productivity and profitability can be increased.

본 발명의 유화제가 첨가되지 않는 점착제는 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴의 조성물을, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀과 물을 용매로 사용하여 알코올 중합반응에 의해 제조한 것에 특징이 있다.The pressure-sensitive adhesive without addition of the emulsifier of the present invention is a composition of 2-ethyl hexyl acrylate, butyl acrylate, methyl methacrylate, vinyl acrylate, acrylic acid, azobisisobutyronitrile, 65% ethyl alcohol and isopropyl alcohol It is characterized in that it is prepared by alcohol polymerization using 35% mostolol and water as a solvent.

Description

유화제가 첨가되지 않는 점착제 및 그 제조방법{A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it}A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it}

본 발명은 유화제가 첨가되지 않는 점착제 및 그 제조방법에 관한 것으로서, 더욱 상세하게는 점착제를 구성하는 필수적인 유성의 조성물을 인체에 무해하며 환경 친화적인 에틸알코올 또는 에틸알코올 및 이소프로필알코올로 이루어진 모스타놀과 물을 용매로서 수용화시켜 알코올중합을 유도함으로써 용액중합으로 제조된 점착제의 점착력과 내수성 등의 물성을 그대로 유지하면서 인체 및 환경에는 무해할 뿐만 아니라 유기용매에 비해 저가의 모스타놀과 물을 병용함에 따른 폭발성의 배제 및 점착제의 제조원가 절감이 가능하게 되어 생산성 및 수익성을 증대할 수있도록 한 유화제가 첨가되지 않는 점착제 및 그 제조방법에 관한 것이다.The present invention relates to a pressure-sensitive adhesive that is not added to the emulsifier and to a method for manufacturing the same, and more particularly, the essential oil composition constituting the pressure-sensitive adhesive harmless to the human body and made of environmentally friendly ethyl alcohol or ethyl alcohol and isopropyl alcohol. Soluble sol and water as a solvent to induce alcohol polymerization, it is harmless to human body and environment while maintaining the adhesiveness and water resistance of adhesive prepared by solution polymerization. The present invention relates to a pressure-sensitive adhesive and a method for manufacturing the same, in which an emulsifier is added so that explosive exclusion and cost reduction of the pressure-sensitive adhesive can be reduced and the productivity and profitability can be increased.

일반적으로 점착제(粘着劑)는 특정 물질간에 일시적으로 점착시키고, 점착된 두 물질을 쉽게 분리할 수 있는 조성물을 의미하며, 산업상 많은 부분에 이용되고 있다. 그 일예로서 신발 제조공정의 경우 신발갑피와 인솔을 재봉하기전에 떨어지지 않게 하기 위하여 사전에 스티커 작업을 할 때 점착제가 사용된다.In general, the pressure-sensitive adhesive (粘着 劑) refers to a composition that can temporarily adhere between a specific material, and can easily separate the two adhered materials, it is used in many parts of the industry. As an example, in the shoe manufacturing process, an adhesive is used when the sticker work is performed in advance so that the shoe upper and the insole do not fall off before sewing.

또한, 점착제를 테이프의 한쪽면에 도포하여 서류나 장부 등의 수리.보강외에 포장이나 전기절연을 위한 공업용과, 점착제를 메모가 가능한 종이의 일면에 도포하여 사용하는 스티커 및 즉석 코팅지 등의 문구류에도 사용되며, 자동차 내장제에도 사용되고 있는 등 점착제의 적용범위는 매우 광범위하다.In addition, the adhesive is applied to one side of the tape to repair documents, books, etc.In addition to reinforcement, for industrial use for packaging and electrical insulation, as well as for stickers and instant coated paper used for applying the adhesive to one side of paper for memo It is also used in automobile interiors, such as the scope of application of the adhesive is very wide.

이러한 점착제는 통상적으로 톨루엔(C7H8), 메탄올(CH3OH), 초산에틸 등의 인체에 유해한 유기용제를 주원료로 사용하여 단량체와 촉매를 반응시키는 방법으로 생산되고 있다.Such pressure sensitive adhesives are typically produced by reacting monomers and catalysts using organic solvents harmful to the human body, such as toluene (C 7 H 8 ), methanol (CH 3 OH), and ethyl acetate, as main raw materials.

즉, 종래 점착제의 제조는 크게 용액중합과 유화중합의 방법으로 이루어지며, 용액중합의 경우 톨루엔 35중량%와, 메탄올 20중량%와, 부틸 아크릴레이트 (butyl acrylate:CH2=CHCOOC4H9) 30중량%와, 메틸 메타 아크릴레이트(Butly methacrylate:CH2=C(CH3)COOCH3) 5중량%와, 비닐 아세테이트(vinyl acetate monomer:CH2=CHOCOCH3) 5중량%와, 아크릴산(acrylicacid:CHCOOH) 3중량%와, 아크릴아마이드(acrylamide: CH2=CHCONH2) 2중량%의 조성물로 이루어져 있고, 또한 유화중합의 경우 부틸 아크릴레이트 28중량%와, 메틸 메타 아크릴레이트 5중량%와, 비닐아세테이트 5중량%와, 아크릴산 5중량%와, 아크릴아마이드 1.8중량%와, 암모니움 퍼설페이트(Ammunium persulfate :(NH4)2S2O8) 0.2중량%와, 기타 유기용제 3중량%와, 후첨가제 2중량%와, 물 50중량%의 조성물로 각각 이루어져 있다.That is, the conventional pressure-sensitive adhesive is prepared by the method of solution polymerization and emulsion polymerization, in the case of solution polymerization, 35% by weight of toluene, 20% by weight of methanol, and butyl acrylate (butyl acrylate: CH 2 = CHCOOC 4 H 9 ) 30% by weight, methyl methacrylate (CH 2 = C (CH 3 ) COOCH 3 ) 5% by weight, vinyl acetate (CH 2 = CHOCOCH 3 ) 5% by weight, acrylic acid (acrylicacid) : 3% by weight of CHCOOH, 2% by weight of acrylamide (CH 2 = CHCONH 2 ), and in the case of emulsion polymerization, 28% by weight of butyl acrylate, 5% by weight of methyl methacrylate, 5% by weight of vinyl acetate, 5% by weight of acrylic acid, 1.8% by weight of acrylamide, 0.2% by weight of ammonium persulfate (NH 4 ) 2 S 2 O 8 ), and 3% by weight of other organic solvents , 2 wt% post-additive, and 50 wt% water.

이와 같이 종래 용액중합으로 제조되는 점착제는 증발성과 휘발성이 강한 유독성의 유기용제인 톨루엔과 메탄올 및 초산에틸 등이 50중량% 이상의 비중을 차지하게 되어 중합반응시 과발열로 인한 폭발의 위험성을 내재하고 있으며, 함유되어 있는 유기용제의 독성으로 인해서 환경을 오염시킴은 물론, 작업자의 인체에 유해한 작용을 일으키게 되는 문제점이 있는 것이다.Thus, the pressure-sensitive adhesive prepared by conventional solution polymerization has a specific gravity of 50% by weight or more of toluene, methanol and ethyl acetate, which are toxic and highly volatile organic solvents. And, due to the toxicity of the organic solvent contained there is a problem that not only pollute the environment, but also cause harmful effects on the human body of the worker.

또한, 유화중합으로 제조되는 점착제는 용매를 물을 사용하고 유기용제와 단량체 그리고 촉매를 반응시키는 수성 점착제(대한민국 특허공개 1997-42907, 1993- 13374)로서 인체 및 환경의 오염을 어느 정도 해소할 수 있는 이점은 지니고 있으나, 다량의 수분이 포함되어 있어서 이 수분을 건조시키는 별도의 접착장치인 기계설비가 있어야 할 뿐만 아니라 접착 종류에 따라 현저한 점착력 차이가 발생되어 수성만을 사용하는데 한계점이 있으며, 인체에 해로운 유기용제, 소포제 등을 소량 포함하고 있는 문제점이 있는 것이다.In addition, the pressure-sensitive adhesive prepared by emulsion polymerization is an aqueous pressure-sensitive adhesive (Republic of Korea Patent Publication No. 1997-42907, 1993-13374) that uses a solvent as water, and reacts an organic solvent with a monomer and a catalyst. It has the advantage, but because it contains a large amount of moisture, not only has to be a separate adhesive device for drying this moisture, but also a significant difference in adhesive strength occurs depending on the type of adhesion, there is a limit to using only aqueous, There is a problem that contains a small amount of harmful organic solvents, defoamers.

즉, 용액중합의 경우 유성의 유기용제의 증발에 따라서 균일한 용액에서 연속한 피막이 형성되는 것에 대해, 유화중합은 수성용매(물)의 건조에 의해서 피막이 형성됨으로써 제조시에 계면활성제나 소포제, 점도조성제라는 접착성능에 도움이 되지 않는 저분자량 성분이 함유되어 있으며, 이들 현상은 피막의 형성방법과 형성과정에 의해 다소 차이가 나지만 용액중합과 비교할 경우 내습.내수성이 떨어진다는 것이 유화중합의 큰 단점으로 지적되고 있다.That is, in the case of solution polymerization, the continuous film is formed in a uniform solution according to the evaporation of the oily organic solvent, whereas the emulsion polymerization is formed by the drying of an aqueous solvent (water). The composition contains a low molecular weight component that does not help the adhesive performance, and these phenomena are somewhat different depending on the method of forming and forming the coating, but the moisture and water resistance is poor when compared to solution polymerization. It is pointed out.

따라서 점착제를 신발 제품을 제조하는 생산공장에서 사용할 경우 신발 갑피의 원단 종류에 따라 점착력이 현저하게 차이가 발생됨으로써 유화중합으로 제조된 수성 점착제를 사용하는데 한계가 있음으로 인해 용액중합 및 유화중합으로 제조된 점착제를 동시에 사용하여야 한다.Therefore, when the pressure-sensitive adhesive is used in a production factory that manufactures shoe products, the adhesive force is remarkably different depending on the type of fabric of the shoe upper, so that the aqueous pressure-sensitive adhesive prepared by emulsion polymerization has a limitation. Used adhesives should be used simultaneously.

이럴 경우 용액중합 및 유화중합으로 제조된 점착제를 동시에 사용하는 기계설비를 구비하여야 하므로 본래의 환경문제 개선의 목적을 이루어지지 못하고 있는 실정이며, 특히 유화중합시 반응후 숙성과 포장단계를 거치면서 다음 반응의 준비단계를 만들기 위해서는 반응기 내벽에 붙어있는 반응물을 세척해 내어야하고, 이 과정에서 다량의 폐수가 발생함으로써 환경을 오염시키는 결과를 초래할 뿐만 아니라 유기용제와 후첨가제의 영향으로 인해서 점착력의 저하를 초래하여 원하는 물성에 얻을 수 없는 문제점이 있는 것이다.In this case, since the mechanical equipment using the pressure-sensitive adhesive prepared by solution polymerization and emulsion polymerization must be provided at the same time, the purpose of improving the original environmental problems cannot be achieved. In order to prepare the reaction, it is necessary to wash off the reactants attached to the inner wall of the reactor, and in this process, a large amount of waste water is generated to contaminate the environment, and the effect of the organic solvent and the post-additive on the lowering of the adhesive force is reduced. There is a problem that can not be obtained to the desired physical properties.

특히 최근에 들어 각 국가별로 인체에 유해한 유기용제를 사용한 점착제의 사용을 규제할 뿐만 아니라 수입에 제한을 두고 있는 실정이며, 이에 따라 점착제가 환경오염에 영향을 주지 않으며, 인체에 무해하고, 접착 강도 및 내수성이 용액중합 이상의 것으로 대체할 수 있는 점착제의 개발이 절실히 요구되는 것이다.In particular, in recent years, countries have restricted the use of pressure-sensitive adhesives using organic solvents that are harmful to humans, and have restrictions on imports. Therefore, the pressure-sensitive adhesives do not affect environmental pollution, are harmless to humans, and adhesive strength. And the development of pressure-sensitive adhesive that can be replaced by water resistance or more than solution polymerization is urgently required.

본 발명은 상기의 요구에 부응하기 위한 것으로서 점착제를 구성하는 필수적인 유성의 조성물인 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴 등의 조성물을 인체에 무해하며 환경 친화적인 에틸알코올 또는 에틸알코올 및 이소프로필알코올로 이루어져 있는 모스타놀과 물을 용매로 사용함에 따라 상기의 점착제 조성물을 수용화시켜 알코올중합을 유도함으로써 용액중합으로 제조된 점착제의 점착력과 내수성 등의 물성을 그대로 유지하면서 인체 및 환경에는 무해할 뿐만 아니라 유기용매에 비해 저가의 모스타놀과 물을 병용함에 따른 폭발성의 배제와 제조원가 절감이 가능하게 되어 생산성 및 수익성을 증대할 수 있도록 한 것을 기술적 과제로 한다.The present invention is to meet the above requirements, such as 2-ethyl hexyl acrylate, butyl acrylate, methyl methacrylate, vinyl acrylate, acrylic acid, azobisisobutyronitrile, etc. The composition is prepared by solution polymerization by inducing alcohol polymerization by accommodating the pressure-sensitive adhesive composition according to the use of a composition which is harmless to the human body and is environmentally friendly with ethyl alcohol or ethyl alcohol and isopropyl alcohol. It is harmless to human body and environment while maintaining physical properties such as adhesive strength and water resistance, and it is possible to eliminate explosiveness and reduce manufacturing cost by using inexpensive mosthanol and water compared to organic solvent, thereby increasing productivity and profitability. It is technical problem to make it possible.

본 발명의 유화제가 첨가되지 않는 점착제는 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 비닐 아크릴레이트, 메틸 메타 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴을 포함하는 점착제에 있어서, 상기 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴의 조성물을, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀과 물을 용매로 사용하여 알코올 중합반응에 의해 제조한 것에 특징이 있다.In the pressure-sensitive adhesive to which the emulsifier of the present invention is not added, in the pressure-sensitive adhesive containing 2-ethyl hexyl acrylate, butyl acrylate, vinyl acrylate, methyl methacrylate, acrylic acid, azobisisobutyronitrile, the 2-ethyl hexyl Using a composition of acrylate, butyl acrylate, methyl methacrylate, vinyl acrylate, acrylic acid, azobisisobutyronitrile, using a mosstanol and water consisting of 65% ethyl alcohol and 35% isopropyl alcohol as solvents It is characterized by what is manufactured by alcohol polymerization.

또한, 본 발명의 유화제가 첨가되지 않는 점착제 제조방법은 2-에틸 헥실 아크릴레이트 28~36중량%와, 부틸 아크릴레이트 17~6중량%와, 메틸 메타 아크릴레이트 1.5~2.8중량%와, 비닐 아크릴레이트 0.05~1.7중량%와, 아크릴산 1.4~2.2중량%와, 아조비스이소부티로니트릴 0.05~0.3중량%와, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 30~5중량%를 교반기에 투입.혼합하여 중합반응물을 얻는 제 1 중합 반응공정과, 상기 제 1 중합과정에서 얻어진 중합반응물의 ⅓을 반응조에 투입하고, 상기 반응조의 온도를 약 80℃로 승온하여 1시간 동안 초기 반응시키고, 나머지 중합반응물의 ⅔를 상기 반응조에 약 3시간 동안에 걸쳐 적하 및 혼합하여 반응물 간에 재차 중합반응이 이루어지도록 하는 제 2 중합 반응공정과, 상기 제 2 중합 반응공정을 통해 반응조에 중합 반응물이 모두 투입된 상태에서 반응조의 온도를 83~87℃ 범위로 일정하게 유지시켜 2~4시간 동안 숙성시키는 숙성공정과, 상기 숙성과정을 통해 숙성된 중합 반응물에 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 10~5중량%와, 수용화제 2~1중량%를 투입.혼합하여 친유성물질과 친수성물질의 결합을 유도하는 알코올중합 반응공정과, 상기 알코올중합 반응공정을 거친 중합반응물에 물 10~40중량%를 투입.혼합하여 점도를 20,000 ~25,000 CPS/25℃로 조절하는 점도조절공정으로 제조되는 것에 특징이 있다.Moreover, the adhesive manufacturing method to which the emulsifier of this invention is not added is 28-36 weight% of 2-ethylhexyl acrylate, 17-6 weight% of butyl acrylate, 1.5-2.8 weight% of methyl methacrylate, and vinyl acrylic 30 to 5% by weight of mosstanol consisting of 0.05 to 1.7% by weight, 1.4 to 2.2% by weight of acrylic acid, 0.05 to 0.3% by weight of azobisisobutyronitrile, 65% of ethyl alcohol and 35% of isopropyl alcohol Into the stirrer, the first polymerization reaction step of mixing and obtaining a polymerization reaction product, and the reaction product of the polymerization reaction product obtained in the first polymerization process is introduced into the reaction tank, the temperature of the reaction tank is raised to about 80 ℃ and the initial reaction for 1 hour And a second polymerization reaction step of dropping and mixing the remaining polymerization reactant into the reaction vessel for about 3 hours so that the polymerization reaction is performed again between the reactants and the second polymerization reaction step. Aging process of maintaining the temperature of the reaction tank in a state in which all the reaction mixture is added in the range of 83 ~ 87 ℃ constant for 2 to 4 hours, 65% ethyl alcohol and isopropyl alcohol in the polymerization reaction aged through the aging process 10 to 5% by weight of moistol comprising 35% and 2 to 1% by weight of a solubilizer are added and mixed with each other to induce the coupling of the lipophilic and hydrophilic substances, and the alcohol polymerization reaction process. 10 to 40% by weight of water is added to the polymerization reaction. The mixture is characterized in that it is prepared by a viscosity control process to adjust the viscosity to 20,000 ~ 25,000 CPS / 25 ℃.

도 1은 본 발명에 따른 유화제가 첨가되지 않는 점착제의 제조공정도.1 is a manufacturing process of the pressure-sensitive adhesive is not added according to the present invention.

<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>

1 : 제 1 중합 반응공정 2 : 제 2 중합 반응공정1: first polymerization reaction step 2: second polymerization reaction step

3 : 숙성공정 4 : 알코올중합 반응공정3: aging step 4: alcohol polymerization reaction step

5 : 점도조절공정5: viscosity control process

이하 본 발명의 구성 및 작용을 첨부한 도면을 참조하여 상세히 설명하면 다음과 같다.Hereinafter, the configuration and operation of the present invention will be described in detail with reference to the accompanying drawings.

도 1은 본 발명에 따른 유화제가 첨가되지 않는 점착제의 제조공정도로서, 인체에 독성이 없으며 환경 오염을 유발시키지 않는 에틸알코올(CH2CH2OH) 또는 에틸알코올 및 이소프로필알코올(isopropylalcohol:(CH3)2CHOH)이 혼합된 모스타놀 "L"(MOSSTANOL "L")을 물과 함께 용매로 사용함에 따라 물에 녹지 않는 유성인 점착제 조성물을 수용화시켜 중합을 유도함으로써 인체 및 환경에 무해한 유화제가 첨가되지 않는 점착제를 제조한 것이다.1 is a manufacturing process chart of the pressure-sensitive adhesive according to the present invention, which is not toxic to humans and does not cause environmental pollution ethyl alcohol (CH 2 CH 2 OH) or ethyl alcohol and isopropyl alcohol (isopropylalcohol: (CH 3 ) Emulsifier that is harmless to human body and environment by inducing polymerization by accommodating oily adhesive composition which is insoluble in water by using mosthanol "L" (MOSSTANOL "L") mixed with 2 CHOH) as a solvent The pressure-sensitive adhesive is not prepared.

즉, 도 1에서와 같이 접착 성질을 갖는 2-에틸 헥실 아크릴레이트(2-hexyl ethyl acrylate) 28~36중량%와, 접착 성질을 갖는 부틸 아크릴레이트 17~6중량%와, 메틸 메타 아크릴레이트 1.5~2.8중량%와, 접착 성질을 갖는 비닐 아크릴레이트 0.05~1.7중량%와, 접착성질 및 반응활성화 기능을 갖는 아크릴산 1.4~2.2중량%와, 반응개시 기능(촉매)을 갖는 아조비스이소부티로니트릴(Azobisisobutyronitrile: C8H12N4) 0.05~0.3중량%와, 반응유도 기능을 가지며 지방족 포화알코올류의 하나인 이소프로필알코올 35중량% 및 에틸알코올 65중량%로 이루어져 있는 모스타놀 30~5중량%를 반응조에 투입하여 고르게 혼합함으로써 중합반응을 일으켜 중합반응물을 얻는 제 1 중합 반응공정(1)을 실행한다.That is, as shown in Fig. 1, 28 to 36% by weight of 2-hexyl ethyl acrylate having adhesive properties, 17 to 6% by weight of butyl acrylate having adhesive properties, and methyl methacrylate 1.5 ~ 2.8% by weight, 0.05-1.7% by weight of vinyl acrylate having adhesive properties, 1.4-2.2% by weight of acrylic acid having adhesive properties and reaction activating functions, and azobisisobutyronitrile having a reaction initiating function (catalyst) (Azobisisobutyronitrile: C 8 H 12 N 4 ) 0.05 ~ 0.3% by weight, mosthanol 30 ~ 5 consisting of 35% by weight of isopropyl alcohol and 65% by weight of ethyl alcohol having a reaction inducing function and one of aliphatic saturated alcohols The first polymerization reaction step (1) is carried out in which a weight% is added to the reaction tank and mixed evenly to cause a polymerization reaction to obtain a polymerization reaction product.

상기 제 1 중합 반응공정(1)에서 얻어진 중합 반응물의 ⅓을 반응조에 투입하고, 상기 반응조의 온도를 약 80℃로 승온시킨 상태에서 1시간 동안 초기 반응을 시킨 다음, 나머지 접착 혼합물의 ⅔를 상기 반응조에 약 3시간 동안에 걸쳐 적하(Droping)하면서 고르게 혼합하여 반응물 간에 재차 중합반응이 이루어지도록 하는 제 2 중합 반응공정(2)을 실행한다.The reaction mixture of the polymerization reactant obtained in the first polymerization reaction step (1) was introduced into the reaction tank, and the reaction was performed for one hour while the temperature of the reaction vessel was raised to about 80 ° C. A second polymerization reaction step (2) is performed in which the reaction mixture is mixed evenly while dropping for about 3 hours so that the polymerization reaction is performed again between the reactants.

이 후, 상기 제 2 중합 반응공정(2)을 통해 반응조에 중합 반응물이 모두 투입된 상태에서 반응조의 온도를 83~87℃ 범위로 일정하게 유지시켜 2~4시간 동안 숙성시키는 숙성공정(3)을 진행한다.Thereafter, in the state where all the polymerization reactants are added to the reaction tank through the second polymerization reaction step (2), the temperature of the reaction tank is kept constant in the range of 83 to 87 ° C., and the aging step (3) is aged for 2 to 4 hours. Proceed.

상기 숙성과정(3)을 통해 숙성된 중합 반응물에 반응유도 기능을 가지며 지방족 포화알코올류의 하나인 이소프로필알코올 35중량%과 에틸알코올 65중량%로 이루어져 있는 모스타놀 10~5중량%와, 암모니아(NH3)의 수소원자를 탄화수소잔기 알킬기로 치환한 아민(amine)계의 수용화제 2~1중량%를 투입 및 고르게 혼합하여 친유성물질과 친수성물질의 결합을 유도함으로써 두 물질간에 분리가 이루어지지 않도록 하는 알코올중합 반응공정(4)을 실행한다.And 10 ~ 5% by weight of moistol consisting of 35% by weight of isopropyl alcohol and 65% by weight of ethyl alcohol having a reaction-inducing function to the polymerization reactants aged through the aging process (3), Separation between two substances is induced by incorporating 2 ~ 1% by weight of an amine-based solubilizer in which the hydrogen atom of ammonia (NH 3 ) is substituted with a hydrocarbon residue alkyl group and evenly mixing to induce the binding of the lipophilic and hydrophilic substances. The alcohol polymerization reaction step (4) is carried out so as not to occur.

상기 알코올중합 반응공정(4)을 통해 점착제로서 기능을 수행할 수 있는 중합 반응물에 물 10~40중량%를 투입 및 고르게 혼합하여 최적의 상태로 사용할 수 있도록 점도를 20,000~25,000 CPS/25℃로 조절하는 점도조절공정(5)을 거침으로써 유화제가 첨가되지 않는 점착제의 제조를 완료하게 되는 것이다.The viscosity of 20,000 to 25,000 CPS / 25 ℃ to be used in an optimal state by adding and mixing evenly 10 ~ 40% by weight of water to the polymerization reactant that can function as an adhesive through the alcohol polymerization reaction step (4) By going through the viscosity control step (5) to adjust the production of the pressure-sensitive adhesive is not added.

상기와 같은 과정에 의해 제조되는 본 발명에 따른 점착제는 상기의 제 1 중합 반응공정(1) 및 알코올중합 반응공정(4)에서 투입되는 인체에 무해하고 환경친화적인 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀과 물을 용매로 사용함에 따라 상기 모스타놀 및 물의 분자가 화학적 상호 반응에 의해 물에 녹지 않는 친유성 물질인 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴 등의 점착제 조성물을 수용화시켜 알코올중합이 이루어지게 되는 것이다.The pressure-sensitive adhesive according to the present invention prepared by the above process is harmless and environmentally friendly 65% of ethyl alcohol and isopropyl alcohol introduced in the first polymerization reaction step (1) and the alcohol polymerization reaction step (4). The use of 35% mostolol and water as a solvent makes the 2-ethanhexyl acrylate, butyl acrylate and methyl methacrylate lipophilic substances insoluble in water due to chemical interactions. The polymerization of the pressure-sensitive adhesive composition, such as the rate, vinyl acrylate, acrylic acid, azobisisobutyronitrile is to be made of alcohol polymerization.

여기에서 접착성질 및 반응 활성화 기능을 갖는 아크릴산을 1.4중량%이하로 투입하였을 경우 점착력이 저하되고 반응성이 약하여 미반응 잔존 모노머의 발생을 초래하게 되며, 아크릴산을 2.2중량%이상 투입하였을 경우 과중합으로 과대한 접착력을 가지게 됨으로써 1.4~2.2중량% 범위내에서 투입하는 것이 가장 바람직하다.In this case, when the acrylic acid having the adhesive property and the reaction activating function is added at 1.4 wt% or less, the adhesive strength is lowered and the reactivity is weak, resulting in the generation of unreacted residual monomer. It is most preferable to add in the range of 1.4 to 2.2 wt% by having excessive adhesive strength.

그리고 친유성물질과 친수성물질의 결합을 유도하는 수용화제를 1중량%이하로 투입하였을 경우는 친유성분과 친수성분이 분리되는 현상을 나타내고, 수용화제를 2중량% 이상 투입되었을 경우에는 내수성(耐水性)이 떨어져서 접착성 저하가 초래됨으로써 2~1중량% 범위내에서 투입하는 것이 가장 바람직하다.In addition, when a soluble agent that induces the binding of a lipophilic substance and a hydrophilic substance is added at 1 wt% or less, the lipophilic component is separated from the hydrophilic component. When 2 wt% or more of the soluble agent is added, it is water resistant. It is most preferable to inject | pour within 2 to 1 weight% because) drop off and adhesive fall occurs.

또한, 접착 성질을 갖는 2-에틸 헥실 아크릴레이트 및 부틸 아크릴레이트, 그리고 메틸 메타 아크릴레이트의 함량을 각각 28중량%, 6중량%, 1.5중량% 이하로 투입하여 스티커 작업을 할 경우 재질이 딱딱해지고 36중량%, 17중량%, 2.8중량% 이상 투입될 경우 점착력이 떨어지게 되어 28~36중량%, 17~6중량%, 1.5~2.8중량% 범위내에서 투입하는 것이 가장 바람직하다.In addition, when the content of 2-ethylhexyl acrylate, butyl acrylate, and methyl methacrylate having an adhesive property in an amount of 28% by weight, 6% by weight, or 1.5% by weight or less, respectively, the material becomes hard when the sticker work is performed. When more than 36% by weight, 17% by weight, 2.8% by weight is more than the adhesive strength is lowered 28 to 36% by weight, 17 to 6% by weight, it is most preferably added within the range of 1.5 to 2.8% by weight.

그리고 접착 성질을 갖는 비닐 아크릴레이트를 0.05중량%이하로 투입할 경우 중합도가 낮고 점도가 낮으며, 1.7%중량 이상일 경우 중합도가 너무 높아 점착제의 겔(GEL)현상이 일어나게 되어 0.05~1.7중량% 범위내에서 투입하는 것이 가장 바람직하다.And when the vinyl acrylate having an adhesive property is less than 0.05% by weight, the polymerization degree is low and the viscosity is low, and when it is 1.7% or more, the degree of polymerization is too high and the gel (GEL) phenomenon of the adhesive occurs, which ranges from 0.05 to 1.7% by weight. It is most preferable to inject | pour in.

또한, 반응 촉매제인 아조비스이소부티로니트릴을 0.05중량% 이하로 투입될 경우 반응성이 약하며 잔존 모너머가 발생하여 점도 안정성이 떨어지고 0.3중량% 이상 투입될 경우 과중합으로 인한 점착력 저하를 나타냄으로써 0.05~0.3중량% 범위내에서 투입하는 것이 가장 바람직하다.In addition, when azobisisobutyronitrile, which is a reaction catalyst, is added in an amount of 0.05 wt% or less, the reactivity is weak and residual monomer is generated, resulting in a decrease in viscosity stability. When 0.3 wt% or more is added, a decrease in adhesion due to overpolymerization is shown. Most preferably, it is added within the range of 0.3 wt%.

그리고 알코올중합을 일으키는 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀을 10중량% 이하로 투입할 경우 알코올 중합반응이 일어나지 않으며, 40중량% 이상을 투입할 경우 과중합으로 인한 점착력의 저하를 초래함으로써 10~40중량% 범위내에서 투입하는 것이 가장 바람직하다.And when the amount of mosthanol consisting of 65% of ethyl alcohol and 35% of isopropyl alcohol that causes alcohol polymerization is added below 10% by weight, the polymerization of alcohol does not occur. It is most preferable to add in 10 to 40weight% of a range by causing a fall.

또한, 점도조절 및 모스타놀과 함께 알코올 중합반응을 일으키는 물을 40중량% 이상을 투입할 경우 점착력을 상실하게 되며, 10중량% 이하로 투입할 경우 알코올 중합반응이 일어나지 않으로써 40~10중량% 범위내에서 투입하는 것이 가장 바람직하다.In addition, when 40 wt% or more of water causing alcohol polymerization reaction with viscosity control and mosthanol is added, the adhesive force is lost, and when 10 wt% or less is added, 40 ~ 10 wt% of alcohol polymerization does not occur. Most preferably, it is added in the range of%.

상기의 조성물로 이루어진 본 발명에 따른 유화제가 첨가되지 않는 점착제의 실시예에 대하여 상세히 설명하면 다음과 같다.When explaining the embodiment of the pressure-sensitive adhesive is not added according to the present invention made of the above composition as follows.

(실시예 1)(Example 1)

2-에틸 헥실 아크릴레이트 35중량%와, 부틸 아크릴레이트 6중량%와, 메틸 메타 아크릴레이트 2.5중량와%, 비닐 아크릴레이트 1.5중량%와, 아크릴산 2.2중량%와, 반응개시 기능(촉매)을 갖는 아조비스이소부티로니트릴 0.25중량%와, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 30중량%를 교반기에 투입.혼합하여 중합반응을 일으켜 반응물을 수득한다.Azo having 35% by weight of 2-ethylhexyl acrylate, 6% by weight of butyl acrylate, 2.5% by weight of methyl methacrylate, 1.5% by weight of vinyl acrylate, 2.2% by weight of acrylic acid, and a reaction initiating function (catalyst) 0.25% by weight of bisisobutyronitrile and 30% by weight of mostolol consisting of 65% of ethyl alcohol and 35% of isopropyl alcohol are added to a stirrer and mixed to cause a polymerization reaction to obtain a reaction product.

상기 과정에서 수득한 반응물의 ⅓을 반응조에 투입하되, 상기 반응조의 온도를 약 80℃로 승온시킨 상태에서 1시간 동안 초기 반응을 시킨 다음, 나머지 반응물의 ⅔를 상기 반응조에 약 3시간 동안에 걸쳐 적하(Droping)하면서 고르게 혼합하여 반응물 간에 재차 중합반응이 이루어지도록 한다.The reaction product obtained in the above process was added to a reaction tank, and the reaction was initially performed for 1 hour while the temperature of the reaction temperature was raised to about 80 ° C., and the reaction product was added dropwise to the reaction vessel for about 3 hours. The mixture is mixed evenly while dropping to allow polymerization to occur again between the reactants.

상기 공정을 통해 수득한 반응물이 모두 투입된 상태에서 반응조의 온도를 83~87℃ 범위로 일정하게 유지시켜 2~4시간 동안 숙성시킨 다음, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 10중량%와, 수용화제 0.55중량%를 투입.혼합하여 친유성물질과 친수성물질의 결합을 유도하고, 물 12중량%를 투입하여 최적의 상태로 사용할 수 있도록 점도를 22,000 CPS/25℃로 조절함으로써 점착제의 제조를 완료하게 되는 것이다.In the state where all the reactants obtained through the above process were added, the temperature of the reaction tank was kept constant in the range of 83 to 87 ° C., and aged for 2 to 4 hours, followed by mosstanol consisting of 65% ethyl alcohol and 35% isopropyl alcohol. 10% by weight and 0.55% by weight of a solubilizer are added and mixed to induce binding of the lipophilic and hydrophilic materials, and 12% by weight of water is adjusted to adjust the viscosity to 22,000 CPS / 25 ° C for optimum use. This completes the manufacture of the pressure-sensitive adhesive.

(실시예 2)(Example 2)

하기의 실시예 2는 상기 실시예 1에 있어 조성물의 혼합비율을 달리한 것이다. 즉, 2-에틸 헥실 아크릴레이트 33중량%와, 부틸 아크릴레이트 17중량%와, 메틸 메타 아크릴레이트 1.7중량%와, 비닐 아크릴레이트 1.5중량%와, 아크릴산 1.7중량%와, 반응개시 기능(촉매)을 갖는 아조비스이소부티로니트릴 0.1중량%와, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 14중량%를 교반기에 투입.혼합하여 중합반응을 일으켜 반응물을 수득한다.Example 2 below is to vary the mixing ratio of the composition in Example 1. That is, 33 wt% of 2-ethylhexyl acrylate, 17 wt% of butyl acrylate, 1.7 wt% of methyl methacrylate, 1.5 wt% of vinyl acrylate, 1.7 wt% of acrylic acid, and a reaction start function (catalyst) 0.1% by weight of azobisisobutyronitrile having 14% by weight of moistol consisting of 65% of ethyl alcohol and 35% of isopropyl alcohol was added to the stirrer. The polymerization reaction was carried out to obtain a reaction product.

상기 과정에서 수득한 반응물의 ⅓을 반응조에 투입하되, 상기 반응조의 온도를 약 80℃로 승온시킨 상태에서 1시간 동안 초기 반응을 시킨 다음, 나머지 반응물의 ⅔를 상기 반응조에 약 3시간 동안에 걸쳐 적하(Droping)하면서 고르게 혼합하여 반응물 간에 재차 중합반응이 이루어지도록 한다.The reaction product obtained in the above process was added to a reaction tank, and the reaction was initially performed for 1 hour while the temperature of the reaction temperature was raised to about 80 ° C., and the reaction product was added dropwise to the reaction vessel for about 3 hours. The mixture is mixed evenly while dropping to allow polymerization to occur again between the reactants.

상기 공정을 통해 수득한 반응물이 모두 투입된 상태에서 반응조의 온도를 83~87℃ 범위로 일정하게 유지시켜 2~4시간 동안 숙성시킨 다음, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 10중량%와, 수용화제 1중량%를 투입.혼합하여 친유성물질과 친수성물질의 결합을 유도하고, 물 20중량%를 투입하여 최적의 상태로 사용할 수 있도록 점도를 22,000 CPS/25℃로 조절함으로써 점착제의 제조를 완료하게 되는 것이다.In the state where all the reactants obtained through the above process were added, the temperature of the reaction tank was kept constant in the range of 83 to 87 ° C., and aged for 2 to 4 hours, followed by mosstanol consisting of 65% ethyl alcohol and 35% isopropyl alcohol. 10% by weight and 1% by weight of a solubilizer are added and mixed to induce binding of lipophilic and hydrophilic materials, and 20% by weight of water is added to adjust the viscosity to 22,000 CPS / 25 ° C for optimum use. This completes the manufacture of the pressure-sensitive adhesive.

(실시예 3)(Example 3)

하기의 실시예 3은 상기 실시예 1에 있어 접착 및 응집성분을 갖는 비닐 아크릴레이트 대신에 방향족탄화수소의 하나인 스틸렌(styrene:C8H8)으로 치환한 것이다.Example 3 below is substituted with styrene (styrene: C 8 H 8 ) which is one of aromatic hydrocarbons in place of the vinyl acrylate having an adhesive and cohesive component in Example 1.

즉, 2-에틸 헥실 아크릴레이트 35중량%와, 부틸 아크릴레이트 6중량%와, 메틸 메타 아크릴레이트 2.5중량%와, 스틸렌 1.5중량%와, 아크릴산 2.2중량%와, 반응개시 기능(촉매)을 갖는 아조비스이소부티로니트릴 0.25중량%와, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 30중량%를 교반기에 투입.혼합하여 중합반응을 일으켜 반응물을 수득한다.That is, it has 35 weight% of 2-ethylhexyl acrylate, 6 weight% of butyl acrylate, 2.5 weight% of methyl methacrylate, 1.5 weight% of styrene, 2.2 weight% of acrylic acid, and reaction start function (catalyst) 0.25% by weight of azobisisobutyronitrile and 30% by weight of mostanol consisting of 65% of ethyl alcohol and 35% of isopropyl alcohol are added to a stirrer and mixed to cause a polymerization reaction to obtain a reaction product.

상기 과정에서 수득한 반응물의 ⅓을 반응조에 투입하되, 상기 반응조의 온도를 약 80℃로 승온시킨 상태에서 1시간 동안 초기 반응을 시킨 다음, 나머지 반응물의 ⅔를 상기 반응조에 약 3시간 동안에 걸쳐 적하(Droping)하면서 고르게 혼합하여 반응물 간에 재차 중합반응이 이루어지도록 한다.The reaction product obtained in the above process was added to a reaction tank, and the reaction was initially performed for 1 hour while the temperature of the reaction temperature was raised to about 80 ° C., and the reaction product was added dropwise to the reaction vessel for about 3 hours. The mixture is mixed evenly while dropping to allow polymerization to occur again between the reactants.

상기 공정을 통해 수득한 반응물이 모두 투입된 상태에서 반응조의 온도를 83~87℃ 범위로 일정하게 유지시켜 2~4시간 동안 숙성시킨 다음, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 10중량%와, 수용화제 0.55중량%를 투입.혼합하여 친유성물질과 친수성물질의 결합을 유도하고, 물 12중량%를 투입하여 최적의 상태로 사용할 수 있도록 점도를 22,000 CPS/25℃로 조절함으로써 점착제의 제조를 완료하게 되는 것이다.In the state where all the reactants obtained through the above process were added, the temperature of the reaction tank was kept constant in the range of 83 to 87 ° C., and aged for 2 to 4 hours, followed by mosstanol consisting of 65% ethyl alcohol and 35% isopropyl alcohol. 10% by weight and 0.55% by weight of a solubilizer are added and mixed to induce binding of the lipophilic and hydrophilic materials, and 12% by weight of water is adjusted to adjust the viscosity to 22,000 CPS / 25 ° C for optimum use. This completes the manufacture of the pressure-sensitive adhesive.

(실시예 4)(Example 4)

하기의 실시예 4는 상기 실시예 1에서 에틸알코올 65% 및 이소프로필알코올35%로 이루어진 모스타놀 대신에 에틸알코올 만을 첨가한 것으로, 2-에틸 헥실 아크릴레이트 35중량%와, 부틸 아크릴레이트 6중량%와, 메틸 메타 아크릴레이트 2.5중량%와, 비닐 아크릴레이트 1.5중량%와, 아크릴산 2.2중량%와, 반응개시 기능(촉매)을 갖는 아조비스이소부티로니트릴 0.25중량%와, 에틸알코올 30중량%를 교반기에 투입.혼합하여 중합반응을 일으켜 반응물을 수득한다.In Example 4 below, only ethyl alcohol was added instead of mosstanol consisting of 65% ethyl alcohol and 35% isopropyl alcohol in Example 1, 35% by weight of 2-ethylhexyl acrylate, and butyl acrylate 6 Wt%, methyl methacrylate 2.5 wt%, vinyl acrylate 1.5 wt%, acrylic acid 2.2 wt%, azobisisobutyronitrile 0.25 wt% having a reaction initiation function (catalyst), ethyl alcohol 30 wt% % Is added to the stirrer and mixed to give a polymerization reaction to obtain a reaction product.

상기 과정에서 수득한 반응물의 ⅓을 반응조에 투입하되, 상기 반응조의 온도를 약 80℃로 승온시킨 상태에서 1시간 동안 초기 반응을 시킨 다음, 나머지 반응물의 ⅔를 상기 반응조에 약 3시간 동안에 걸쳐 적하(Droping)하면서 고르게 혼합하여 반응물 간에 재차 중합반응이 이루어지도록 한다.The reaction product obtained in the above process was added to a reaction tank, and the reaction was initially performed for 1 hour while the temperature of the reaction temperature was raised to about 80 ° C., and the reaction product was added dropwise to the reaction vessel for about 3 hours. The mixture is mixed evenly while dropping to allow polymerization to occur again between the reactants.

상기 공정을 통해 수득한 반응물이 모두 투입된 상태에서 반응조의 온도를 83~87℃ 범위로 일정하게 유지시켜 2~4시간 동안 숙성시킨 다음, 에틸알코올 10중량%와, 수용화제 0.55중량%를 투입.혼합하여 친유성물질과 친수성물질의 결합을 유도하고, 물 12중량%를 투입하여 최적의 상태로 사용할 수 있도록 점도를 22,000 CPS/25℃로 조절함으로써 점착제의 제조를 완료하게 되는 것이다.In the state where all of the reactants obtained through the above process was added, the temperature of the reaction tank was kept constant in the range of 83 to 87 ° C., and aged for 2 to 4 hours. Then, 10% by weight of ethyl alcohol and 0.55% by weight of a solubilizer were added. By mixing the lipophilic material and the hydrophilic material to induce a combination, and by adjusting the viscosity to 22,000 CPS / 25 ℃ to be used in an optimal state by adding 12% by weight of water to complete the preparation of the pressure-sensitive adhesive.

상기와 같은 본 발명의 실시예에 의해 제조된 알코올중합 점착제와, 종래 용액중합 점착제, 그리고 유화중합 점착제의 시편을 제작하여 40~50℃에서 3일 경과 후 대한민국 점착제 규격(KS A 1107)에 의거하여 시험하여 각 측정 항목에 대한 결과치를 표 1에 나타내었다.According to the Korean adhesive standard (KS A 1107) after three days at 40 ~ 50 ℃ by preparing a specimen of the alcohol polymerization adhesive prepared by the embodiment of the present invention, the conventional solution polymerization adhesive, and emulsion polymerization adhesive Test results are shown in Table 1 for each measurement item.

여기에서 접착력의 측정방법은 제품에 도포하여 상온에서 20분간 방치 후 25℃에서 측정하고 단위는 gf/25㎜이며, 유지력(내열) 측정방법은 25㎜×25㎜ 크기의제작 시험편을 상온에서 20분간 방치한 다음 1㎏, 80℃에서 1시간 방치시 접착 유지시간 및 1시간 후의 점착력(Creep)을 측정하고 단위는 Creep.㎜/hr(at80℃)이다.Here, the measuring method of adhesive force is applied to the product and left for 20 minutes at room temperature, and then measured at 25 ° C., and the unit is gf / 25 mm, and the holding force (heat resistance) measuring method is performed using a test specimen of 25 mm × 25 mm size at room temperature. After leaving for 1 minute, the adhesive holding time and creep after 1 hour were measured at 1 kg and 80 ° C. for 1 hour, and the unit was Creep. Mm / hr (at 80 ° C.).

그리고 볼 택(Ball Tack)은 NO.1(Ø:1/32inch) ~ No.32(Ø/32inch) at24℃, 경사각:26°, 톨루엔(Toluene) 세척 1시간 상온에서 방치하여 측정하고 단위는 J. DOW law로 나타내었다.And Ball Tack is measured at NO.1 (Ø: 1 / 32inch) ~ No.32 (Ø / 32inch) at24 ℃, inclination angle: 26 °, at room temperature for 1 hour of toluene washing. J. DOW law.

(표 1)Table 1

종류Kinds 점도Viscosity 고형분Solid content 점착력adhesiveness 유지력(내열)Holding force (heat resistant) 볼 택(Ball tack)Ball tack 습도Humidity 유화중합점착제Emulsified Polymeric Adhesive 30,00030,000 60.1360.13 1.5001.500 20분20 minutes 25이상25 or more 77∼85%77-85% 용액중합점착제Solution Polymeric Adhesive 3,6003,600 46.2646.26 2,1502,150 0.1㎜ creep0.1mm creep 2121 알코올중합점착제Alcohol polymerization adhesive 10,00010,000 50.2850.28 2,0102,010 0.1㎜ creep0.1mm creep 2121 도포량Coating amount 60㎛(Dry)양면60㎛ (Dry) Double Side 사용기재Equipment used SUS 304 판, Art paper, PET film. L-75(00518)SUS 304 plate, Art paper, PET film. L-75 (00518)

상기의 표 1에서와 같이 물을 용매로 사용하는 유화중합 점착제는 점착력 자체가 낮은 반면, 본 발명에 의해 제조되는 알코올중합 점착제는 기존의 용액중합 점착제와 동일한 점착력과 유지력을 가지는 것을 알 수 있는 것이다.As shown in Table 1, the emulsion polymerization pressure-sensitive adhesive using water as a solvent has low adhesive strength, whereas the alcohol polymerization pressure-sensitive adhesive prepared by the present invention has the same adhesive strength and holding strength as the conventional solution polymerization pressure-sensitive adhesive. .

이상에서와 같이 본 발명은 점착제를 구성하는 필수적인 유성의 조성물인 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴 등의 점착제 조성물을 인체에 무해하며 환경 친화적인 에틸알코올 및 이소프로필알코올로 이루어지는 모스타놀과 물을 용매로 사용함에 따라 상기의 점착제 조성물을 수용화시켜 알코올중합을 유도함으로써 용액중합으로 제조된 점착제의 점착력과 내수성 등의 물성을 그대로 유지하면서 인체 및 환경에는 무해할 뿐만 아니라 유기용매에 비해 저가의 모스타놀과 물을 병용함에 따른 반응시 폭발성의 배제 및 제조원가 절감이 가능하게 되어 생산성 및 수익성을 증대할 수 있는 효과가 있는 것이다.As described above, the present invention uses a pressure-sensitive adhesive composition such as 2-ethyl hexyl acrylate, butyl acrylate, methyl methacrylate, vinyl acrylate, acrylic acid, azobisisobutyronitrile, etc., which are essential oil-based compositions constituting the pressure-sensitive adhesive. The adhesive and water resistance of the pressure-sensitive adhesive prepared by solution polymerization by inducing alcohol polymerization by accommodating the pressure-sensitive adhesive composition by using water as a solvent and using mosethanol and water, which are harmless and environmentally friendly, ethyl alcohol and isopropyl alcohol. It is harmless to human body and environment while maintaining physical properties, and it is possible to eliminate explosiveness and reduce manufacturing cost when reacting with low-cost mosthanol and water compared to organic solvent, which can increase productivity and profitability. It is.

Claims (5)

( 삭 제 )( delete ) 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴 조성물을 포함하는 점착제에 있어서,In the pressure-sensitive adhesive containing 2-ethyl hexyl acrylate, butyl acrylate, methyl methacrylate, vinyl acrylate, acrylic acid, azobisisobutyronitrile composition, 상기 2-에틸 헥실 아크릴레이트 28~36중량%와, 부틸 아크릴레이트 17~6중량%와, 메틸 메타 아크릴레이트 1.5~2.8중량%와, 비닐 아크릴레이트 0.05~1.7중량%와, 아크릴산 1.4~2.2중량%와, 아조비스이소부티로니트릴 0.05~0.3중량%와, 수용화제 2~1중량%와, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 40~10중량%와, 물 10~40중량%으로 이루어진 것을 특징으로 하는 유화제가 첨가되지 않는 점착제.28-36 weight% of said 2-ethylhexyl acrylates, 17-6 weight% of butyl acrylates, 1.5-2.8 weight% of methyl methacrylates, 0.05-1.7 weight% of vinyl acrylates, 1.4-2.2 weights of acrylic acid %, Azobisisobutyronitrile 0.05 to 0.3% by weight, 2 to 1% by weight solubilizer, 40 to 10% by weight of mosthanol consisting of 65% ethyl alcohol and 35% isopropyl alcohol, and 10 to water The pressure-sensitive adhesive is not added, characterized in that consisting of 40% by weight. ( 정 정 ) 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴 조성물을 포함하는 점착제에 있어서,In the pressure-sensitive adhesive containing 2-ethylhexyl acrylate, butyl acrylate, methyl methacrylate, vinyl acrylate, acrylic acid, azobisisobutyronitrile composition, 상기 2-에틸 헥실 아크릴레이트 28~36중량%와, 부틸 아크릴레이트 17~6중량%와, 메틸 메타 아크릴레이트 1.5~2.8중량%와, 비닐 아크릴레이트 0.05~1.7중량%와, 아크릴산 1.4~2.2중량%와, 아조비스이소부티로니트릴 0.05~0.3중량%와, 수용화제 2~1중량%와, 에틸알코올 40~10중량%와, 물 10~40중량%으로 이루어진 것을 특징으로 하는 유화제가 첨가되지 않는 점착제.28-36 weight% of said 2-ethylhexyl acrylates, 17-6 weight% of butyl acrylates, 1.5-2.8 weight% of methyl methacrylates, 0.05-1.7 weight% of vinyl acrylates, 1.4-2.2 weights of acrylic acid %, Azobisisobutyronitrile 0.05 to 0.3% by weight, 2 to 1% by weight solubilizer, 40 to 10% by weight ethyl alcohol, 10 to 40% by weight of water is not added Do not have adhesive. ( 정 정 ) 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴 조성물을 포함하는 점착제에 있어서,In the pressure-sensitive adhesive containing 2-ethylhexyl acrylate, butyl acrylate, methyl methacrylate, vinyl acrylate, acrylic acid, azobisisobutyronitrile composition, 상기 2-에틸 헥실 아크릴레이트 28~36중량%와, 부틸 아크릴레이트 17~6중량%와, 메틸 메타 아크릴레이트 1.5~2.8중량%와, 스틸렌 0.05~1.7중량%와, 아크릴산 1.4~2.2중량%와, 아조비스이소부티로니트릴 0.05~0.3중량%와, 수용화제 2~1중량%와, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 40~10중량%와, 물 10~40중량%으로 이루어진 것을 특징으로 하는 유화제가 첨가되지 않는 점착제.28-36 weight% of said 2-ethylhexyl acrylate, 17-6 weight% of butyl acrylate, 1.5-2.8 weight% of methyl methacrylate, 0.05-1.7 weight% of styrene, 1.4-2.2 weight% of acrylic acid, , 40 to 10% by weight of azobisisobutyronitrile, 0.05 to 0.3% by weight, 2 to 1% by weight of a solubilizer, 65% of ethyl alcohol and 35% of isopropyl alcohol, and 10 to 40% by weight of water Pressure-sensitive adhesive, characterized in that consisting of%. 2-에틸 헥실 아크릴레이트, 부틸 아크릴레이트, 메틸 메타 아크릴레이트, 비닐 아크릴레이트, 아크릴산, 아조비스이소부티로니트릴 조성물을 포함하는 점착제 제조방법에 있어서,In the pressure-sensitive adhesive production method comprising 2-ethyl hexyl acrylate, butyl acrylate, methyl methacrylate, vinyl acrylate, acrylic acid, azobisisobutyronitrile composition, 상기 2-에틸 헥실 아크릴레이트 28~36중량%와, 부틸 아크릴레이트 17~6중량%와, 메틸 메타 아크릴레이트 1.5~2.8중량%와, 비닐 아크릴레이트 0.05~1.7중량%와, 아크릴산 1.4~2.2중량%와, 아조비스이소부티로니트릴 0.05~0.3중량%와, 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 30~5중량%를 교반기에 투입.혼합하여 중합반응물을 얻는 제 1 중합 반응공정(1)과,28-36 weight% of said 2-ethylhexyl acrylates, 17-6 weight% of butyl acrylates, 1.5-2.8 weight% of methyl methacrylates, 0.05-1.7 weight% of vinyl acrylates, 1.4-2.2 weights of acrylic acid %, 30 to 5% by weight of azobisisobutyronitrile and 0.05 to 0.3% by weight of mostolol comprising 65% of ethyl alcohol and 35% of isopropyl alcohol are mixed in a stirrer to obtain a polymerization reaction. Reaction step (1), 상기 제 1 중합과정(1)에서 얻어진 중합반응물의 ⅓을 반응조에 투입하고, 상기 반응조의 온도를 약 80℃로 승온하여 1시간 동안 초기 반응시키고, 나머지 중합반응물의 ⅔를 상기 반응조에 약 3시간 동안에 걸쳐 적하 및 혼합하여 반응물 간에 재차 중합반응이 이루어지도록 하는 제 2 중합 반응공정(2)과,⅓ of the polymerization reactant obtained in the first polymerization process (1) was added to the reaction tank, the temperature of the reaction tank was raised to about 80 ° C. for initial reaction for 1 hour, and ⅔ of the remaining polymerization reactant was reacted in the reaction tank for about 3 hours. A second polymerization reaction step (2), in which the polymerization reaction is performed again between the reactants by dropping and mixing over a period of time; 상기 제 2 중합 반응공정(2)을 통해 반응조에 중합 반응물이 모두 투입된 상태에서 반응조의 온도를 83~87℃ 범위로 일정하게 유지시켜 2~4시간 동안 숙성시키는 숙성공정(3)과,Aging step (3) to maintain a constant temperature of the reaction tank in the range 83 ~ 87 ℃ in the state in which all the polymerization reactants are added to the reaction tank through the second polymerization reaction step (2) for 2 to 4 hours, and 상기 숙성과정(3)을 통해 숙성된 중합 반응물에 에틸알코올 65% 및 이소프로필알코올 35%로 이루어진 모스타놀 10~5중량%와, 수용화제 2~1중량%를 투입.혼합하여 친유성물질과 친수성물질의 결합을 유도하는 알코올중합 반응공정(4)과,10-5% by weight of moistol consisting of 65% ethyl alcohol and 35% isopropyl alcohol and 2-1% by weight of a solubilizer are added to the polymerization reaction aged through the aging process (3). Alcohol polymerization reaction process (4) to induce the binding of the hydrophilic substance, 상기 알코올중합 반응공정(4)을 거친 중합반응물에 물 10~40중량%를 투입.혼합하여 점도를 20,000~25,000 CPS/25℃로 조절하는 점도조절공정(5)으로 제조되는 것을 특징으로 하는 유화제가 첨가되지 않는 점착제 제조방법.Emulsifier, characterized in that prepared by the viscosity control step (5) to adjust the viscosity to 20,000 ~ 25,000 CPS / 25 ℃ by mixing 10 ~ 40% by weight of water to the polymerization reaction product after the alcohol polymerization reaction step (4). The pressure-sensitive adhesive manufacturing method is not added.
KR10-2000-0061149A 2000-10-18 2000-10-18 A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it KR100394365B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR10-2000-0061149A KR100394365B1 (en) 2000-10-18 2000-10-18 A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR10-2000-0061149A KR100394365B1 (en) 2000-10-18 2000-10-18 A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it

Publications (2)

Publication Number Publication Date
KR20010007889A KR20010007889A (en) 2001-02-05
KR100394365B1 true KR100394365B1 (en) 2003-08-09

Family

ID=19694015

Family Applications (1)

Application Number Title Priority Date Filing Date
KR10-2000-0061149A KR100394365B1 (en) 2000-10-18 2000-10-18 A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it

Country Status (1)

Country Link
KR (1) KR100394365B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20160004844A (en) * 2014-07-04 2016-01-13 (주)시그마소재 Adhesives of coating plate for LCD Alignment layer and manufacturing process thereof

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20040097877A (en) * 2003-05-12 2004-11-18 함현식 Pressure sensitive adhesives compound and the manufacturing method
KR102176891B1 (en) * 2019-05-29 2020-11-11 주식회사 대양포리졸 Adhesive composition and method for producing the same
KR102088427B1 (en) * 2019-07-27 2020-03-12 박문도 Preparation method of adhesive

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR970009578A (en) * 1995-08-29 1997-03-27 다루이 시로 Egg yolk phospholipid composition
JPH1036801A (en) * 1996-07-18 1998-02-10 Daicel Chem Ind Ltd Water-based adhesive and its production
JPH1060402A (en) * 1996-06-18 1998-03-03 Hercules Inc Pressure sensitive adhesive
KR19990023423A (en) * 1997-08-06 1999-03-25 미우라 유이찌, 쓰지 가오루 glue
JPH11172216A (en) * 1997-12-12 1999-06-29 Shoei Kagaku Kogyo Kk Aqueous adhesive composition
KR19990072192A (en) * 1995-12-14 1999-09-27 스프레이그 로버트 월터 Bulk Radical Polymerization Process Using Batch Reactor

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR970009578A (en) * 1995-08-29 1997-03-27 다루이 시로 Egg yolk phospholipid composition
KR19990072192A (en) * 1995-12-14 1999-09-27 스프레이그 로버트 월터 Bulk Radical Polymerization Process Using Batch Reactor
JPH1060402A (en) * 1996-06-18 1998-03-03 Hercules Inc Pressure sensitive adhesive
JPH1036801A (en) * 1996-07-18 1998-02-10 Daicel Chem Ind Ltd Water-based adhesive and its production
KR19990023423A (en) * 1997-08-06 1999-03-25 미우라 유이찌, 쓰지 가오루 glue
JPH11172216A (en) * 1997-12-12 1999-06-29 Shoei Kagaku Kogyo Kk Aqueous adhesive composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20160004844A (en) * 2014-07-04 2016-01-13 (주)시그마소재 Adhesives of coating plate for LCD Alignment layer and manufacturing process thereof
KR101647619B1 (en) 2014-07-04 2016-08-11 (주)시그마소재 Adhesives of coating plate for LCD Alignment layer and manufacturing process thereof

Also Published As

Publication number Publication date
KR20010007889A (en) 2001-02-05

Similar Documents

Publication Publication Date Title
CA1141895A (en) Copolymers for pressure-sensitive adhesives based on acrylic esters, vinyl acetate and ethylene
Bunker et al. Miniemulsion polymerization of acrylated methyl oleate for pressure sensitive adhesives
KR930002404A (en) Polyurethane dispersion
CN101372607B (en) Emulsion pressure-sensitive adhesive for soft PVC electric adhesive tape and preparation thereof
KR100394365B1 (en) A pressure sensitive adhesives, that was not added emulsifer, and the manufacturing method of it
US4234467A (en) Binder for pressure sensitive adhesive
US5258479A (en) Self-adhesive acrylate copolymers, a process for their preparation and self-adhesive webs, which contain them
JPS61281112A (en) Perfluoroalkylvinyl polymer and use thereof
WO2009071506A1 (en) Cross-linkable vinylester-copolymers and use thereof as low-profile-additives
CN105238322A (en) Interpenetrated network structural type aqueous polyurethane for medicine packaging and preparation method thereof
JPH0354683B2 (en)
CN112126003A (en) Thermoplastic acrylate emulsion and preparation method and application thereof
US3835086A (en) Polymeric dispersions of pressure-sensitive adhesives and process
KR102354796B1 (en) Surfactant composition for adhesive and adhesive comprising the same
KR102338870B1 (en) Surfactant composition for adhesive and adhesive comprising the same
KR100394368B1 (en) An adhesives, that was not added emulsifer for making shoes and the manufacturing method of it
CN101709205A (en) Method for preparing degradable pressure-sensitive adhesive
JP2022122842A (en) Adhesion structure and method for manufacturing the same, adherend set, adherend, and activated alkyne group-containing polymer
CN109563391A (en) Acrylic adhesive composition, adhesive and bonding sheet
JP2016222741A (en) Adhesive composition and re-peelable adhesive double-sided tape
CN102911302A (en) Living polymerization method of vinyl acetate monomer emulsion
KR960705888A (en) Binders based on fatty chemical reaction products [BINDERS BASED ON FAT CHEMICAL REACTION PRODUCTS]
EP0409218B1 (en) Method for production of aqueous dispersion of long-chain alkyl graft polymer and aqueous release agent
KR20210031321A (en) Acrylic emulsion pressure snsitive adhesive composition
CN106497463B (en) A kind of water-borne pressure sensitive adhesive and preparation method thereof

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20110729

Year of fee payment: 9

LAPS Lapse due to unpaid annual fee