KR20120045101A - Eco friendly and recyclable water soluble coating paper and manufacturing method thereof - Google Patents
Eco friendly and recyclable water soluble coating paper and manufacturing method thereof Download PDFInfo
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- KR20120045101A KR20120045101A KR1020100106427A KR20100106427A KR20120045101A KR 20120045101 A KR20120045101 A KR 20120045101A KR 1020100106427 A KR1020100106427 A KR 1020100106427A KR 20100106427 A KR20100106427 A KR 20100106427A KR 20120045101 A KR20120045101 A KR 20120045101A
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- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D127/00—Coating compositions 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 a halogen; Coating compositions based on derivatives of such polymers
- C09D127/02—Coating compositions 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 a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
- C09D127/04—Coating compositions 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 a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
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- C09D127/00—Coating compositions 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 a halogen; Coating compositions based on derivatives of such polymers
- C09D127/22—Coating compositions 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 a halogen; Coating compositions based on derivatives of such polymers modified by chemical after-treatment
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- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
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- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/20—Diluents or solvents
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- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
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- C09D7/42—Gloss-reducing agents
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- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
- C09D7/60—Additives non-macromolecular
- C09D7/61—Additives non-macromolecular inorganic
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- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
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- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/80—Processes for incorporating ingredients
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- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/10—Coatings without pigments
- D21H19/14—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
- D21H19/18—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising waxes
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Abstract
본 발명은 친환경적이며 재생 가능한 수용성 코팅지 및 그 제조방법에 관한 것으로서, 보다 상세하게는 사용후 폐기시 자연환경에서 생분해되어 환경에 부하를 주지 않고, 물 또는 알칼리 용액에 쉽게 해리되어 재활용이 용이하며, 형광증백제, 포름알데히드, 카드뮴, 납, 비소 등 유해중금속이 기구 및 용기 포장의 기준에 적합한 수용성 코팅지를 제공한다.
또한 우수한 내유성, 내수성 및 열실링성이 부여되어 일회용컵, 테이크아웃 용기, 햄버거 포장지, 치킨포장지, 아이스크림 용기 등 식품포장재 제조에 활용될 수 있다.The present invention relates to an eco-friendly and renewable water-soluble coating paper and a method for manufacturing the same, and more particularly, it is biodegradable in the natural environment upon disposal after use, and does not burden the environment, and is easily dissociated in water or alkaline solutions to facilitate recycling. Hazardous heavy metals such as fluorescent brighteners, formaldehyde, cadmium, lead and arsenic provide water-soluble coatings that meet the criteria for packaging equipment and containers.
In addition, it is endowed with excellent oil resistance, water resistance and heat sealing, and can be utilized for manufacturing food packaging materials such as disposable cups, takeout containers, hamburger wrappers, chicken wrappers and ice cream containers.
Description
본 발명은 사용 후 폐기시 자연환경에 부하를 주지 않고, 물 또는 알칼리 용액에 쉽게 해리되어 재활용이 용이한 친환경적이며 재생가능한 수용성 코팅지 및 그 제조방법에 관한 것이다.The present invention relates to an eco-friendly and renewable water-soluble coating paper and a method for manufacturing the same, which are easily dissociated into water or alkaline solution and do not put a load on the natural environment upon disposal after use.
현대 생활은 발달한 과학기술, 생활수준과 문화의 질적 향상 및 편리함 추구 등에 의하여 일회용품의 사용이 급격히 증가하면서 음료용으로 자동판매기의 컵, 음료수를 포장하는 용기, 컵라면 용기, 테이크아웃용 용기, 아이스크림용 용기, 햄버거 포장지, 치킨 포장지 등과 같이 다양한 일회용 용기 포장재가 개발되어 사용되고 있다.Modern life has rapidly increased the use of disposable products due to the development of scientific technology, quality improvement of living standards and culture, and the pursuit of convenience, and the cups of vending machines, beverage packaging containers, cup noodles containers, takeout containers, Various disposable container packaging materials have been developed and used, such as ice cream containers, hamburger wrappers, and chicken wrappers.
상기와 같은 일회용 용기 포장재는 종이를 사용하는 경우가 많으며, 종이의 경우 흡습성의 문제를 해결하기 위하여 방수성 재질로 내부를 코팅한다.Disposable container packaging material as described above is often used paper, in the case of paper to coat the inside with a waterproof material to solve the problem of hygroscopicity.
상기 종이 포장재의 코팅에 많이 사용되는 것이 폴리에틸렌(Polyethylene: PE)이다.Polyethylene (PE) is widely used for coating the paper packaging material.
일반적으로 폴리에틸렌은 플라스틱의 일종으로 가볍고, 녹슬지 않으며 썩지 않을 뿐만 아니라 화학적 안전성, 내수성, 유연성, 절연성, 성형성 등의 장점에 의하여 주변 생활용품에 많이 사용되는 화학물질이다.In general, polyethylene is a kind of plastic, which is light, rust and non-rotable, and is a chemical that is widely used in peripheral household goods due to its advantages such as chemical safety, water resistance, flexibility, insulation, and moldability.
상기 폴리에틸렌은 일반적으로 식품위생성이 우수하고, 유통가격이 비교적 저렴한 등의 이유에 의하여 다양한 식품 용기의 내부에 코팅되어 방수 등의 목적으로 사용되고 있으나 이를 사용한 코팅 용기 포장재는 사용 및 폐기과정에서 환경호르몬 방출 가능성이 있다. 또한 폴리에틸렌 코팅 용기 포장재는 사용후 재활용을 위해 해리하는 과정에서 물에 해리되지 않는 폴리에틸렌은 선별 과정을 거쳐야 하기 때문에 재활용 비용이 증가되는 단점이 있다.The polyethylene is generally used for the purpose of waterproofing and coating the inside of various food containers for reasons such as excellent food hygiene and distribution price is relatively low, but the coating container packaging material using the same releases environmental hormones during use and disposal. There is a possibility. In addition, the polyethylene coating container packaging material has a disadvantage in that the recycling cost is increased because polyethylene that is not dissociated in water in the process of dissociation for recycling after use has to undergo a screening process.
이에 따라 종이 용기 포장재 제조에 계속적인 펄프의 수입이 이루어지며, 이에 대한 자원의 재활용 관점 및 환경파괴에서 그 한계점이 있을 뿐만 아니라, 소각 시 발생하는 매연은 대기오염을 유발하고, 매립을 하여도 자연 분해가 되기까지 수백 년이 걸리기 때문에 토양 오염의 주범이 된다. 더욱이, 폴리에틸렌 코팅공정은 원천적으로 요구되는 200 ℃ 가량의 폴리에틸렌 칩의 용해공정 및 이에 대한 휘발성 유기용제(VOCs)로 인하여 고비용 및 작업환경 저하/대기오염으로 인한 환경문제를 유발한다.As a result, pulp is continuously imported in the manufacture of packaging materials for paper containers, and there are limitations in terms of recycling resources and environmental destruction.In addition, soot generated during incineration causes air pollution, It takes hundreds of years for decomposition to become a major contributor to soil contamination. In addition, the polyethylene coating process causes environmental problems due to high cost and lowering of working environment / air pollution due to the dissolution process of polyethylene chips of about 200 ° C. and volatile organic solvents (VOCs).
또한, 폴리에틸렌 코팅은 사용조건에 따라 환경호르몬의 방출과 발암물질에 노출될 위험이 매우 높으며, 장기간 인체에 노출시 그 독성을 유발하기 때문에 식품위생 및 안전성 측면에서 문제가 제기되고 있다.In addition, polyethylene coating has a high risk of exposure to environmental hormones and carcinogens depending on the conditions of use, and poses problems in terms of food hygiene and safety because it causes toxicity to humans for a long time.
이를 극복하기 위한 종래 기술로는 아크릴 에멀젼으로 이루어진 수용성 수지, 슬립제 및 분산제로 이루어진 수용성 포장지가 개시되어 있다. 이 기술은 친환경적이며 재생 가능할 뿐만 아니라 환경호르몬이 방출되지 않는 식품포장용 수지이지만, 점도가 높아 코팅작업이 어려우며 물의 함량이 많으므로 코팅 작업시 물이 휘발되는 속도가 느려 작업성이 떨어진다. 또한, 아크릴 에멀젼은 딱딱한 특성으로 인하여 종이가 빳빳해져 경첩부분의 코팅막이 손상되어 물과 기름 등이 쉽게 종이에 스며들 뿐만 아니라 재활용시 물에 해리되는 시간이 많이 소요되는 문제가 있다.The prior art for overcoming this is disclosed a water-soluble wrapper consisting of a water-soluble resin, a slip agent and a dispersant made of an acrylic emulsion. This technology is not only eco-friendly and renewable, but also a food packaging resin that does not release environmental hormones, but due to its high viscosity, the coating is difficult and the water content is high. In addition, acrylic emulsion has a problem that takes a long time to dissociate in water during recycling, as well as water and oil easily penetrates the paper due to the hardened properties of the paper is damaged the coating film of the hinge portion.
본 발명은 사용후 폐기시 물 또는 알칼리에 의해 해리가 용이하여 재활용이 용이하며, 자연환경에서 분해되어 자연환경에 부하는 주지 않는 친환경적이며 재생가능한 수용성 코팅지의 제조방법을 제공하는 것을 목적으로 한다.It is an object of the present invention to provide a method for producing an eco-friendly and renewable water-soluble coating paper that is easily dissociated by water or alkali when disposed of after use, and is easily recycled and does not decompose in the natural environment and load on the natural environment.
또한, 본 발명은 수용성 코팅지를 제공하는 것을 다른 목적으로 한다.Another object of the present invention is to provide a water-soluble coated paper.
본 발명의 목적을 달성하기 위하여, (A) 30 내지 60℃로 유기용제를 가온시키는 단계; (B) 가온된 유기용제 100 중량부에 대하여 폴리염화비닐리덴 10 내지 40중량부를 첨가하고 30 내지 60℃에서 30 내지 150분 동안 교반하는 단계; (C) 상기 교반된 혼합물에 지방산을 유기용제 100 중량부에 대하여 0.005 내지 0.1 중량부 첨가하고 30 내지 60℃에서 10 내지 30분 동안 교반하는 단계; (D) 상기 혼합물에 말레산 무수물(maleic anhydride)를 유기용제 100 중량부에 대하여 0.01 내지 0.5 중량부 첨가하고 30 내지 60℃에서 10 내지 30분 동안 교반하는 단계; (E) 상기 말레산 무수물이 포함된 혼합물에 슬립제를 유기용제 100 중량부에 대하여 0.2 내지 2.0 중량부 첨가하고 30 내지 60℃에서 15 내지 60분 동안 교반하는 단계; (F) 상기 혼합물을 20 내지 80℃에서 2 내지 10시간 동안 숙성시켜 코팅액을 제조하는 코팅액 제조단계; (G) 상기 코팅액을 코터와 같은 코팅장치를 이용하여 종이에 코팅한 다음 건조, 냉각하여 코팅지를 제조하는 코팅지 제조단계;를 포함하는 것을 특징으로 하는 친환경적이며 재생가능한 수용성 코팅지의 제조 방법을 제시한다.In order to achieve the object of the present invention, (A) warming the organic solvent to 30 to 60 ℃; (B) adding 10 to 40 parts by weight of polyvinylidene chloride based on 100 parts by weight of the heated organic solvent and stirring at 30 to 60 ° C. for 30 to 150 minutes; (C) adding 0.005 to 0.1 parts by weight of fatty acid to 100 parts by weight of the organic solvent to the stirred mixture and stirring at 30 to 60 ℃ for 10 to 30 minutes; (D) adding 0.01 to 0.5 parts by weight of maleic anhydride to the mixture with respect to 100 parts by weight of an organic solvent and stirring at 30 to 60 ° C. for 10 to 30 minutes; (E) 0.2 to 2.0 parts by weight of a slip agent is added to the mixture containing maleic anhydride with respect to 100 parts by weight of an organic solvent and stirred at 30 to 60 ° C. for 15 to 60 minutes; (F) a coating solution preparation step of preparing a coating solution by aging the mixture at 20 to 80 ℃ for 2 to 10 hours; (G) coating the coating solution on a paper using a coating device such as a coater, and then dried and cooled to produce a coated paper to produce a coated paper; proposes an environmentally friendly and renewable water-soluble coating paper manufacturing method comprising a. .
(E) 단계와 (F) 단계 사이에, 분산제를 추가 투입하는 것인 것이며, 상기 분산제는 유기용제 100 중량부에 대하여 0.01 내지 1.0 중량부를 투입하고 (E) 단계와 동일 조건에서 20 내지 60분 교반하는 것이 바람직하다.Between step (E) and step (F), a dispersant is additionally added, and the dispersant is added in an amount of 0.01 to 1.0 parts by weight based on 100 parts by weight of an organic solvent, and 20 to 60 minutes under the same conditions as in step (E). It is preferable to stir.
본 발명의 다른 목적은 상기의 제조방법으로 제조되는 종이코팅용 수용성 코팅조성물을 제공한다.Another object of the present invention to provide a water-soluble coating composition for paper coating prepared by the above production method.
본 발명을 활용하면 우수한 내수성, 내유성 및 열실링성이 부여된 수용성 코팅지를 제조할 수 있다.By utilizing the present invention it is possible to produce a water-soluble coating paper given excellent water resistance, oil resistance and heat sealing.
또한, 본 발명의 수용성 코팅지는 인쇄성이 우수하여 외관이 미려하고, 열처리 건조 상태에서는 3~4일 동안 내수 및 내유성을 유지하지만, 재활용시 물 또는 알칼리 용액중에서 교반하면서 해리할 경우, 기계적 교반처리에 신속하게 해리되므로 용이하게 재활용할 수 있다.In addition, the water-soluble coated paper of the present invention is excellent in printability and beautiful in appearance, and maintains water and oil resistance for 3 to 4 days in a heat-treated dry state, but when dissociated with stirring in water or alkaline solution during recycling, mechanical stirring treatment It dissociates quickly and can be easily recycled.
도 1은 본 발명의 코팅조성물을 일실시예에 따라 제조하는 방법을 도시한 흐름도이다.1 is a flowchart illustrating a method of preparing a coating composition of the present invention according to one embodiment.
이하, 도면을 참고하면서 더욱 상세하게 설명한다.It will be described below in more detail with reference to the drawings.
도 1은 본 발명의 친환경적이며 재생 가능한 수용성 코팅지의 제조 방법에 대한 일 실시예적 흐름도이다.1 is an exemplary flow chart of a method for producing an eco-friendly and renewable water-soluble coated paper of the present invention.
먼저, (A)단계는 교반기에 유기용제를 투입하고 30 내지 60℃로 가온하는 단계이다.First, step (A) is a step of adding an organic solvent to the stirrer and warming to 30 to 60 ℃.
상기 유기용매의 예로는 메틸벤젠(Methyl benzene), 에틸아세테이트(Ethyl acetate), 메틸아세테이트(Methyl acetate), 프로필아세테이트(Propyl acetate), 벤젠(Benzene), 클로로벤젠(Chloro Benzene), 테트라히드로퓨란(Tetrahydrofuran), 에탄올(Ethanol) 및 이소프로판올(Isopropanol)로 이루어진 군에서 선택된 1종 또는 2종 이상을 들 수 있다. Examples of the organic solvent include methyl benzene, ethyl acetate, methyl acetate, methyl acetate, propyl acetate, benzene, benzene, chlorobenzene, and tetrahydrofuran. Tetrahydrofuran), ethanol (Ethanol) and isopropanol (Isopropanol) is selected from the group consisting of one or two or more.
(B) 단계에서는 가온된 유기용제에 폴리염화비닐리덴을 첨가하고 30 내지 60℃를 유지하면서 30 내지 150분 동안 1,000 내지 2,000 RPM의 속도로 교반한다. 교반시간이 30분 미만인 경우에는 충분한 혼합이 이루어지지 않고, 교반시간이 150분 초과인 경우에는 유기용제가 휘발되어 이후에 계속되는 공정을 진행할 수 없다. 또한, 교반속도가 1,000 RPM미만인 경우에는 충분한 혼합이 이루어지지 않아 추후에 균일하게 용해시키기 어려우며, 교반속도가 2,000 RPM초과인 경우에는 기포가 발생되고 용액이 넘쳐 이후에 계속되는 공정을 진행할 수 없다. In step (B), polyvinylidene chloride is added to the heated organic solvent and stirred at a rate of 1,000 to 2,000 RPM for 30 to 150 minutes while maintaining 30 to 60 ° C. When the stirring time is less than 30 minutes, sufficient mixing is not made, and when the stirring time is more than 150 minutes, the organic solvent is volatilized and the subsequent process cannot proceed. In addition, when the stirring speed is less than 1,000 RPM, it is difficult to uniformly dissolve later, since sufficient mixing is not made, and when the stirring speed is more than 2,000 RPM, bubbles are generated and the solution cannot overflow to continue the process.
코팅액이 상기 폴리염화비닐리덴을 포함함으로써 종이에 얇게 도포되더라도 우수한 내수성, 내유성 및 열실링성이 부여될 수 있다.By including the polyvinylidene chloride in the coating solution, even if thinly applied to paper, excellent water resistance, oil resistance and heat sealing property can be imparted.
(C) 단계에서는 균일하게 용해가 될 수 있도록 상기 단계에서 제조된 혼합물에 지방산을 첨가하고 30 내지 60 ℃를 유지하면서 10 내지 30분 동안 1,000 내지 2,000 RPM의 속도로 교반한다. 온도가 30 ℃미만인 경우에는 균일하게 용해가 되지 않으며, 온도가 60 ℃초과인 경우에는 유기용제가 휘발되어 계속되는 공정을 진행할 수 없다. 폴리염화비닐리덴을 균일하게 용해시키기 위해서는 (A)단계 내지 (C)단계에서 상기 온도를 유지하여야 한다.In step (C), the fatty acid is added to the mixture prepared in the above step so as to dissolve uniformly, and stirred at a speed of 1,000 to 2,000 RPM for 10 to 30 minutes while maintaining 30 to 60 ° C. If the temperature is less than 30 ℃ do not dissolve uniformly, if the temperature is over 60 ℃ organic solvent is volatilized to continue the process. In order to uniformly dissolve polyvinylidene chloride, the temperature must be maintained in steps (A) to (C).
교반시간이 10분 미만인 경우에는 폴리염화비닐리덴이 균일하게 용해되지 못하며, 교반시간이 30분 초과인 경우에는 유기용제가 휘발될 수 있고 또한 용해에 따른 혼합물의 점도 상승의 문제가 있다.If the stirring time is less than 10 minutes, polyvinylidene chloride is not uniformly dissolved, if the stirring time is more than 30 minutes, the organic solvent may be volatilized and there is a problem of viscosity increase of the mixture due to dissolution.
상기 지방산은 폴리염화비닐리덴을 균일하게 융해시켜주는 역할을 하는 것으로써, 예로는 탄소수 C12~C24의 포화지방산으로서 라우르산(Lauric acid), 팔미트산(Palmitic acid), 스테아르산(stearic acid), 베헨산(Behenic acid), 리그노세르산(lignoceric acid) 중에서 선택된 1종 또는 2종 이상을 들 수 있다. The fatty acid serves to uniformly melt polyvinylidene chloride, for example, lauric acid, palmitic acid and stearic acid as saturated fatty acids having C 12 to C 24 carbon atoms. ), Behenic acid, and one or two or more selected from lignoceric acid.
지방산은 유기용제 100 중량부에 대하여 0.005 내지 0.1 중량부, 바람직하게는 0.01 내지 0.8 중량부로 사용된다. 지방산이 0.005 중량부 미만이면 폴리염화비닐리덴 등 고분자의 균일한 용해가 어렵고, 0.1 중량부 이상이면 고분자 응집에 의해 균일한 용해가 저해된다.The fatty acid is used in 0.005 to 0.1 parts by weight, preferably 0.01 to 0.8 parts by weight based on 100 parts by weight of the organic solvent. If the fatty acid is less than 0.005 parts by weight, it is difficult to uniformly dissolve polymers such as polyvinylidene chloride, and if it is 0.1 parts by weight or more, uniform dissolution is inhibited by polymer aggregation.
(D) 단계에서는 제조된 혼합물에 말레산 무수물을 첨가하고 30 내지 60 ℃를 유지하면서 10 내지 30분 동안 1,000 내지 2,000 RPM의 속도로 교반하여 더욱 혼합한 다음, In step (D), maleic anhydride is added to the prepared mixture, the mixture is further stirred and stirred at a speed of 1,000 to 2,000 RPM for 10 to 30 minutes while maintaining 30 to 60 ° C,
상기 말레산 무수물은 지방산과 함께 폴리염화비닐리덴을 더욱 균일하게 용해시켜 주는 역할을 하여 코팅 조성물이 종이 등에 용이하게 코팅이 되도록 한다.The maleic anhydride serves to more uniformly dissolve the polyvinylidene chloride together with the fatty acid so that the coating composition is easily coated on paper.
말레산 무수물 유기용제 100 중량부에 대하여 0.01 내지 0.5 중량부, 바람직하게는 0.02 내지 0.4 중량부로 사용된다. 0.01 중량부 미만이면 고분자의 균일한 용해가 어렵고, 0.5 중량부 이상이면 경제성이 나빠진다.0.01 to 0.5 parts by weight, preferably 0.02 to 0.4 parts by weight, based on 100 parts by weight of maleic anhydride organic solvent. If it is less than 0.01 weight part, uniform dissolution of a polymer will be difficult, and if it is 0.5 weight part or more, economic efficiency will worsen.
(E) 단계로 슬립제를 첨가하고 동일 조건에서 15 내지 60분 동안 1,000 내지 2,000 RPM의 속도로 교반한 다음, Add the slip agent in step (E) and stir at a speed of 1,000 to 2,000 RPM for 15 to 60 minutes under the same conditions,
상기 슬립제는 본 발명의 코팅조성물이 도포된 종이의 마찰계수를 저하시켜 윤활성 강화 및 표면강도 향상을 유발함으로써 후공정인 인쇄 작업시 발생될 수 있는 종이의 층간 접/점착현상을 방지하며, 코팅조성물에 슬립성을 부여하여 코팅막의 건조도막 두께가 얇게 형성되도록 할 뿐만 아니라 우수한 내수성 및 내유성을 부여한다. 이러한 슬립제의 예로는 파라핀 왁스(Paraffin wax), 리코 왁스(Lico wax), 폴리에틸렌 왁스(Polyethylene wax), 실리콘(Silicone), 스테아르산 모노머(Stearic acid monomer)로 이루어진 군에서 선택된 1종 또는 2종 이상을 들 수 있다.The slip agent lowers the friction coefficient of the paper coated with the coating composition of the present invention to induce lubrication enhancement and surface strength, thereby preventing interlayer adhesion / adhesion of paper, which may occur during post-process printing, and coating Slip property is imparted to the composition to allow the dry film thickness of the coating film to be formed thin, as well as to impart excellent water resistance and oil resistance. Examples of such slip agents include one or two selected from the group consisting of paraffin wax, rico wax, polyethylene wax, silicone, stearic acid monomer, and the like. The above is mentioned.
슬립제는 유기용제 100 중량부에 대하여 0.2 내지 2.0 중량부, 바람직하게는 0.2 내지 1.5 중량부로 사용된다. 슬립제의 함량이 0.2 중량부 미만인 경우에는 윤활성이 저하되어 코팅막 사이에 브로킹 현상에 의해 상호 달라붙는 현상이 발생되며, 함량이 2.0 중량부 초과인 경우에는 윤활성이 우수해져 종이 등에 코팅하기가 어려우며 슬립제로 왁스류가 사용되면 왁스가 기름을 흡수하여 내유성이 저하된다. The slip agent is used in an amount of 0.2 to 2.0 parts by weight, preferably 0.2 to 1.5 parts by weight, based on 100 parts by weight of the organic solvent. If the content of the slip agent is less than 0.2 parts by weight, the lubricity is lowered and sticking to each other due to the cracking phenomenon between the coating film occurs. If the content is more than 2.0 parts by weight, it is difficult to coat the paper, etc. If wax is used as a slip agent, the wax absorbs oil and oil resistance is lowered.
(F) 단계에서 20 내지 80℃에서 20 내지 200rpm으로 2 내지 10시간동안 숙성시켜 코팅액을 제조한다. (E) 단계에서 제조된 혼합물을 (F) 단계의 조건으로 숙성시키지 않으면 고분자간 결합이 안정화 되지 않아 용매와 용질간의 이형에 의해 용액이 분리된다.In the step (F) it is aged at 20 to 200rpm at 20 to 200rpm for 2 to 10 hours to prepare a coating solution. If the mixture prepared in step (E) is not aged under the conditions of step (F), the intermolecular bonds are not stabilized and the solution is separated by release between the solvent and the solute.
(G) 단계에서는 숙성시켜 얻은 코팅액을 코터와 같은 코팅장치를 이용하여 종이에 코팅한 다음 건조하여 내수, 내유 및 열실링성이 부여된 코팅지를 제조하는 단계이다. 건조는 통상적으로 사용되는 50 내지 200℃ 열풍으로 열풍 건조후, 50 내지 200℃의 히팅롤러를 통과하면서 2차 건조하였고, 최종적으로 0 내지 30℃ 냉각롤러를 통과시킨 후 롤타입으로 권취하였다. 건조방식은 코팅후 바로 히팅롤러 2 내지 3단계를 거쳐 건조후 냉각롤러로 냉각하는 것이 더욱 바람직하다. 코팅장치는 특별한 제한이 없으나, 2단 내지 6단 롤러 바브레이드 코터, 콤마코터, 스프레이코터, 메쉬 또는 망점코터, 케스팅코터, 그라비아코터, 드라핑(dropping)코터, 에어나이프코터 등을 사용할 수 있다. 또한 수용성 코팅액이 종이 원지 등에 코팅되어 내수성, 내유성 및 열실링성이 부여된 수용성 코팅지를 제조할 수 있다. 상기 종이는 코팅공정, 재단공정, 인쇄공정, 성형공정 등의 과정에서 다양한 요구에 부응하여야 하므로 적정한 강도, 장기보존성, 내습성, 치수안정성, 가공적성 등이 우수한 것을 사용하며, 이에 대해 특별한 제약은 없으나, 표백 화학펄프를 원료로 하고 내절성 및 형부성(型付性)이 우수한 종이가 바람직하다.In the step (G), the coating liquid obtained by aging is coated on paper using a coating apparatus such as a coater, and then dried to prepare coated paper having water, oil and heat sealing properties. Drying was followed by hot air drying with 50 to 200 ° C. hot air, which is commonly used, and then secondary drying while passing through a heating roller of 50 to 200 ° C., and finally winding after passing through a 0 to 30 ° C. cooling roller. The drying method is more preferably cooled through a cooling roller after drying through the heating roller 2 to 3 steps immediately after coating. The coating apparatus is not particularly limited, but may be a two to six-speed roller barb coater, a comma coater, a spray coater, a mesh or dot coater, a casting coater, a gravure coater, a dropping coater, an air knife coater, or the like. . In addition, the water-soluble coating liquid may be coated on a paper base or the like to produce a water-soluble coating paper provided with water resistance, oil resistance and heat sealing. Since the paper has to meet various requirements in the process of coating, cutting, printing, molding, etc., it has excellent strength, long-term storage, moisture resistance, dimensional stability, processability, etc. However, a paper having bleaching chemical pulp as a raw material and excellent in cutting resistance and moldability is preferable.
또한 상기 (E)단계 및 (F)단계 사이에, (E)단계에서 제조된 혼합물에 분산제를 첨가하여 (E)단계와 동일 조건에서 20 내지 60분 동안 1,000 내지 2,000 RPM의 속도로 교반하는 단계를 추가할 수 있다.In addition, between the steps (E) and (F), adding a dispersant to the mixture prepared in step (E) and stirring at a rate of 1,000 to 2,000 RPM for 20 to 60 minutes under the same conditions as step (E) You can add
상기 분산제는 폴리염화비닐리덴 고분자 등의 물질들을 분산시키고 현탁성을 증가시키며 저장 안정성을 향상시키는 것으로서, 예로는 친수성 실리카, 디에스테르 설포석시네이트(Diester sulfosuccinate) 및 우레탄 에멀젼(Urethane Emulsion)로 이루어진 군에서 선택된 1종 또는 2종 이상을 들 수 있다.The dispersing agent is to disperse materials such as polyvinylidene chloride polymer, increase suspension, and improve storage stability. Examples of the dispersant include hydrophilic silica, diester sulfosuccinate, and urethane emulsion. 1 type, or 2 or more types selected from the group can be mentioned.
분산제는 유기용매 100 중량부에 대하여 0.01 내지 1.0 중량부, 바람직하게는 0.05 내지 0.4 중량부로 사용된다. 분산제의 함량이 0.05 중량부 미만인 경우에는 분산효과를 기대할 수 없으며, 함량이 0.5 중량부 초과인 경우에는 현탁성은 우수하나 경제적 측면에서 바람직하지 못하다.
The dispersant is used in an amount of 0.01 to 1.0 parts by weight, preferably 0.05 to 0.4 parts by weight, based on 100 parts by weight of the organic solvent. If the content of the dispersant is less than 0.05 parts by weight can not be expected dispersing effect, if the content is more than 0.5 parts by weight, the suspension is excellent, but it is not preferable economically.
본 발명의 코팅지의 코팅막 도공량은 5~20 g/㎡, 바람직하게는 7~15 g/㎡ 이다. 코팅막의 도공량이 5g/㎡ 미만인 경우에는 우수한 내유성, 내수성 및 열실링성을 얻지 못하며, 도공량이 20g/㎡ 초과인 경우에는 내수성, 내유성 및 열실링성이 더 우수해 지기는 하지만 이를 경제적인 측면과 고려하면 바람직하지 못한 정도이다.Coating film coating amount of the coated paper of this invention is 5-20 g / m <2>, Preferably it is 7-15 g / m <2>. If the coating amount of the coating film is less than 5g / ㎡ it does not obtain excellent oil resistance, water resistance and heat sealing, if the coating amount is more than 20g / ㎡ it is more excellent in water resistance, oil resistance and heat sealing, but it is economical and Considering this is undesirable.
또한, 도공량은 코팅 조성물을 한 번에 도포하여 형성할 수 있으나, 보다 우수한 내수성, 내유성 및 열실링성을 얻기 위해서는 두 번에 걸쳐 도포하는 것이 바람직하다. 특히 종이의 표면이 거친 경우에는 1차로 2~3g을 도포한 다음, 2차 도포를 하는 것이 더욱 바람직하다.In addition, the coating amount may be formed by applying the coating composition at once, but in order to obtain better water resistance, oil resistance and heat sealing, it is preferable to apply the coating twice. In particular, when the surface of the paper is rough, it is more preferable to apply 2 to 3 g first, and then apply the second coating.
상기 열풍이 50℃ 이하이면 건조가 잘 되지 않고, 200℃ 이상이면 코팅지 일부가 접힘 현상이 발생된다. When the hot air is 50 ° C. or less, the drying is not good, and when 200 ° C. or more, a part of the coated paper is folded.
상기 히팅롤러가 50℃ 이하이면 건조가 잘 되지 않고, 200℃ 이상이면 코팅액의 일부가 히팅롤러에 엉겨붙어 코팅지의 품질이 나빠진다. If the heating roller is 50 ° C. or less, the drying is not good. If the heating roller is 200 ° C. or more, a part of the coating liquid is entangled with the heating roller, thereby deteriorating the quality of the coated paper.
상기 냉각롤러 0℃ 이하이면 코팅지가 롤러에 엉겨붇는 현상이 발생되고, 30℃ 이상이면 냉각이 잘되지 않아 코팅지 붙어버리게 되어 이후에 계속되는 공정을 진행할 수 없다. If the cooling roller is 0 ℃ or less, the phenomenon that the coated paper is entangled in the roller is generated, if it is 30 ℃ or more, the cooling is not good, the coated paper is stuck, it can not proceed with the subsequent process.
이하, 본 발명의 이해를 돕기 위하여 바람직한 실시예를 제시하나, 하기 실시예는 본 발명을 설명하기 위한 것이며 본 발명이 그에 의해 한정되는 것은 아니다.
Hereinafter, preferred examples are provided to help understanding of the present invention, but the following examples are provided to illustrate the present invention and the present invention is not limited thereto.
<< 실시예Example 1~4> 1-4>
수용성 코팅조성물의 제조Preparation of Water-soluble Coating Composition
<실시예 1>≪ Example 1 >
메틸벤젠 30 중량부와 테트라히드로퓨란 50 중량부를 교반기에 넣은 다음 온수를 이용하여 40 ℃로 가열한 후, 동일 온도하에서 폴리염화비닐리덴 15 중량부를 첨가하여 1,000rpm으로 80분 동안 교반하였다. 상기와 동일한 조건하에서 베헨산 0.02 중량부를 첨가하여 20분 동안 교반한 후, 말레산 무수물 0.05 중량부를 첨가하여 20분 동안 교반하였다. 또한 상기와 동일한 조건에서 리코왁스를 0.7 중량부를 첨가하여 20분 동안 교반한 다음, 잔부를 테트라히드로퓨란으로 하였다. 상기 혼합물을 30 ℃를 유지하면서 50rpm으로 5시간 동안 숙성하여 수용성 코팅조성물을 제조하였다.
30 parts by weight of methylbenzene and 50 parts by weight of tetrahydrofuran were added to a stirrer, heated to 40 ° C. using hot water, and 15 parts by weight of polyvinylidene chloride was added under the same temperature, followed by stirring at 1,000 rpm for 80 minutes. Under the same conditions as above, 0.02 parts by weight of behenic acid was added and stirred for 20 minutes, and then 0.05 parts by weight of maleic anhydride was added and stirred for 20 minutes. Further, 0.7 parts by weight of licowax was added and stirred for 20 minutes under the same conditions as above, and the remainder was tetrahydrofuran. The mixture was aged at 50 rpm for 5 hours while maintaining the 30 ℃ to prepare a water-soluble coating composition.
<실시예 2><Example 2>
상기 실시예 1과 동일하게 실시하되, 베헤닌산 대신에 리그노세르산을 사용하였고, 리코왁스 대신에 파라핀왁스를 사용하였다.
The same procedure as in Example 1 except that lignoseric acid was used instead of behenic acid, and paraffin wax was used instead of licowax.
<실시예 3><Example 3>
메틸벤젠 30 중량부와 테트라히드로퓨란 50 중량부를 교반기에 넣은 다음 온수를 이용하여 40 ℃로 가열한 후, 동일 온도하에서 폴리염화비닐리덴 15 중량부를 첨가하여 1,000rpm으로 80분 동안 교반하였다. 상기와 동일한 조건하에서 베헨산 0.02 중량부를 첨가하여 20분 동안 교반한 후, 말레산 무수물 0.05 중량부를 첨가하여 20분 동안 교반하였다. 또한 상기와 동일한 조건에서 리코왁스를 0.7 중량부를 첨가하여 20분 동안 교반하였고, 친수성 실리카 0.15 중량부를 첨가한 다음 30분간 교반한 다음, 잔부를 테트라히드로퓨란으로 하였다. 상기 혼합물을 30 ℃를 유지하면서 50rpm으로 5시간 동안 숙성하여 수용성 코팅조성물을 제조하였다.
30 parts by weight of methylbenzene and 50 parts by weight of tetrahydrofuran were added to a stirrer, heated to 40 ° C. using hot water, and 15 parts by weight of polyvinylidene chloride was added under the same temperature, followed by stirring at 1,000 rpm for 80 minutes. Under the same conditions as above, 0.02 parts by weight of behenic acid was added and stirred for 20 minutes, and then 0.05 parts by weight of maleic anhydride was added and stirred for 20 minutes. Also, 0.7 parts by weight of licowax was added and stirred for 20 minutes under the same conditions as above, 0.15 parts by weight of hydrophilic silica was added, followed by stirring for 30 minutes, and the remainder was tetrahydrofuran. The mixture was aged at 50 rpm for 5 hours while maintaining the 30 ℃ to prepare a water-soluble coating composition.
<실시예 4><Example 4>
상기 실시예 3과 동일하게 실시하되, 베헤닌산 대신에 리그노세르산을 사용하였고, 리코왁스 대신에 파라핀왁스를 사용하였다.
In the same manner as in Example 3, lignoseric acid was used instead of behenic acid, and paraffin wax was used instead of licowax.
<< 실시예Example 5~8> 5 ~ 8>
수용성 receptivity
코팅지의Coated paper
제조 Produce
<실시예 5>Example 5
상기 실시예 1에서 제조된 코팅액을 식품지에 120메시 롤러를 이용하여 12 g/㎡의 도공량으로 코팅한 후 100℃의 열풍 챔버 10m를 통과시키면서 1차 건조하였고, 80℃ 히팅 롤러를 통과시켜 추가 건조를 한 다음, 4℃의 냉각롤러를 통과하여 냉각후 권취하여 롤타입으로 권취된 코팅지를 제조하였다.
The coating liquid prepared in Example 1 was coated on food paper with a coating amount of 12 g / m 2 using a 120 mesh roller, and then firstly dried while passing through a 10 m hot air chamber at 100 ° C., and added by passing through a heating roller at 80 ° C. After drying, the resultant was passed through a cooling roller at 4 ° C., cooled and wound to prepare a coated paper wound in a roll type.
<실시예 6><Example 6>
상기 실시예 5와 동일하게 실시하되, 실시예 1의 수용성 코팅조성물 대신에 실시예 2의 수용성 코팅조성물을 사용하여 코팅지를 제조하였다.
The coating was carried out in the same manner as in Example 5, but using the water-soluble coating composition of Example 2 instead of the water-soluble coating composition of Example 1.
<실시예 7><Example 7>
상기 실시예 5와 동일하게 실시하되, 실시예 1의 수용성 코팅조성물 대신에 실시예 3의 수용성 코팅조성물을 사용하여 코팅지를 제조하였다.
In the same manner as in Example 5, but instead of the water-soluble coating composition of Example 1 to prepare a coated paper using the water-soluble coating composition of Example 3.
<실시예 8><Example 8>
상기 실시예 5와 동일하게 실시하되, 실시예 1의 수용성 코팅조성물 대신에 실시예 4의 수용성 코팅조성물을 사용하여 코팅지를 제조하였다.
In the same manner as in Example 5, but instead of the water-soluble coating composition of Example 1 to prepare a coated paper using the water-soluble coating composition of Example 4.
<실험예 1>Experimental Example 1
실시예 5~8에 따라 제조된 수용성 코팅지의 사용후 폐기시 재활용 용이성 및 폐기물 감소 특성을 확인하기 위하여 환경마크 인증기준인 EL606의 방법에 따라서 알칼리 해리성 및 알칼리 분산성을 확인하였다. EL606의 시험방법에 따라 (1) 2L 용량의 해리용기에 0.5% NaoH 용액 1L를 가한 다음, 친환경 점착식 에코타일 1㎠ 이하로 잘게 절단한 시료 20g을 넣었다. (2) 이어서 55±5도에서 1,500±100 RPM으로 10분간 해리시킨 다음, (3) 교반을 멈추고 용기벽에 부착된 물질을 50mL의 알칼리 용액으로 씻어내린 다음 교반기를 작동하여 1,500±100 RPM으로 다시 10분간 해리시켰다. (4) (3)의 과정을 3회 반복하고 시료액을 5분간 정치하고 150메시의 여과재인 금속망체로 여과하였다. 또한 여과재 위의 남아있는 펄프 슬러지를 알칼리용액으로 5회 세척한 다음 80±5도의 물로 여과재를 5회 세척하였다. (5) 여과재 위에 남아있는 펄프 슬러지는 여과재와 함께 상온에서 30분간 정치시킨 후, 잔류하는 수산화나트륨을 제거하기 위해 105±5도의 건조기에서 2시간 동안 건조시켰다. (6) 건조시킨 여과재를 꺼내 방랭한 다음 여과재 위에 남아있는 펄프를 취하여 알칼리 해리성 및 분산성을 평가한 결과를 표 1에 나타내었다.
Alkali dissociation and alkali dispersibility were confirmed in accordance with the method of EL606, which is an environmental mark certification standard, in order to confirm the ease of recycling and waste reduction characteristics of the water-soluble coated paper prepared according to Examples 5-8. According to the test method of EL606 (1) 1L of 0.5% NaoH solution was added to a 2L dissociation container, and 20 g of a sample chopped into 1 cm 2 or less of an eco-friendly adhesive eco-tile was added. (2) dissociate at 1,500 ± 100 RPM for 10 minutes at 55 ± 5 degrees, and then (3) stop the agitation and wash off the material attached to the vessel wall with 50 mL of alkaline solution and operate the stirrer to 1,500 ± 100 RPM. It was dissociated again for 10 minutes. (4) The process of (3) was repeated three times, and the sample solution was allowed to stand for 5 minutes and filtered through a metal mesh that is a 150 mesh filter medium. In addition, the remaining pulp sludge on the filter medium was washed five times with alkaline solution, and then the filter medium was washed five times with water of 80 ± 5 degrees. (5) The pulp sludge remaining on the filter medium was allowed to stand for 30 minutes at room temperature together with the filter medium, and then dried in a dryer of 105 ± 5 degrees for 2 hours to remove the remaining sodium hydroxide. (6) The dried filter medium was taken out and left to cool, and the pulp remaining on the filter medium was taken to evaluate alkali dissociation and dispersibility.
상기 표1의 결과에서 보아 실시예 4~8의 4종류 코팅지 모두 EL606 포장재 규격에 따른 “재활용이 쉬음, 폐기물 감소”에 대한 판단 기준인 펄프 이외에 불순물이 포함되어 있지 않고, 펄프 점착성이 나타나지 않아 알칼리 해리성 또는 알칼리 분산성인 것으로 평가되어 재활용이 용이하고, 폐기물 감소 기준에 적합한 것을 알 수 있었다.
From the results of Table 1, all four types of coated papers of Examples 4 to 8 do not contain impurities other than pulp, which is a criterion for “easy recycling, waste reduction,” according to EL606 packaging material standard, and does not show pulp stickiness. It was evaluated that it was dissociable or alkali dispersible, and it was found that it was easy to recycle and met waste reduction criteria.
<실험예 2>Experimental Example 2
실시예 7에 따라 제조된 수용성 코팅지의 중금속, 유해물질 함유 여부를 확인하기 위하여 “기구 및 용기포장의 기준규격” 따라 시험하였고, 그 결과를 표 2에 나타내었다.
In order to determine whether the water-soluble coated paper prepared according to Example 7 contained heavy metals and harmful substances, the test was carried out according to the "standard specification of packaging of utensils and containers", and the results are shown in Table 2.
상기 표 2의 결과에서 보아 기구 및 용기포장 기준규격에 적합하여 인체에 무해하고, 중금속 함량이 적합한 것을 알 수 있었다.
From the results of Table 2, it can be seen that the apparatus is suitable for the standard packaging standards and is harmless to humans, and the heavy metal content is suitable.
<실험예 3><Experimental Example 3>
1. 내수성 및 내유성: 실시예 5~8의 수용성 코팅지의 코팅면에 물 및 식용유를 각각 5g씩 도포하여 상온에서 24시간 동안 방치한 후 식품지에 물 및 식용유가 젖은 정도를 육안으로 관찰하였다.1. Water resistance and oil resistance: 5g each of water and cooking oil were coated on the coated surface of the water-soluble coated paper of Examples 5 to 8 and left at room temperature for 24 hours, and then the degree of wetness of water and cooking oil on the food paper was visually observed.
◎ : 우수(식품지에 물 및 식용유가 전혀 젖지 않음)◎: Excellent (water and cooking oil do not get wet at all)
○ : 양호(식품지에 물 및 식용유가 5% 이하로 젖음)○: Good (water and cooking oil wet 5% or less on food paper)
□ : 보통(식품지에 물 및 식용유가 6~10% 젖음)□: Normal (6 ~ 10% wet water and cooking oil on food paper)
△ : 불량(식품지에 물 및 식용유가 11~20도 젖음)(Triangle | delta): Poor (11-20 degrees of water and cooking oil wet on food paper)
× : 아주 불량 (식품지에 물 및 식용유가 20% 초과로 젖음)
×: Very poor (water and cooking oil wet more than 20% in food paper)
2. 열실링성: 실시예 5~8의 수용성 코팅지를 접어서 두 코팅면이 마주보도록 한 다음 열실링기(삼보테크, SK-310)를 사용하여 실링강도 5로 열실링하였다. 열실링한 수용성 코팅지를 물 속에 완전히 잠기게하였고, 48시간 경과후 열실링면이 떨어지는 정도를 육안으로 관찰하였다.2. Heat sealing property: Fold the water-soluble coating paper of Examples 5 to 8 so that the two coating surfaces faced each other, and then heat-sealed to a sealing strength of 5 using a heat sealing machine (Sambo Tech, SK-310). The heat-sealed water-soluble coated paper was completely submerged in water, and after 48 hours, the degree of heat-sealing surface drop was visually observed.
◎ : 우수(코팅층과 식품지가 떨어지지 않음)◎: Excellent (coating layer and food sheet do not fall)
○ : 양호(코팅층과 식품지가 1% 이하로 떨어짐)○: Good (coating layer and food sheet fell below 1%)
□ : 보통(코팅층과 식품지가 2~5% 로 떨어짐)□: Normal (coating layer and food sheet dropped to 2 ~ 5%)
△ : 불량(코팅층과 식품지가 6~10% 로 떨어짐)(Triangle | delta): Poor (coating layer and food paper fall to 6-10%)
× : 아주 불량 (코팅층과 식품지가 10% 이상으로 떨어짐)
×: Very poor (coating layer and food sheet dropped to more than 10%)
위 표 3에 나타낸 바와 같이, 본 발명에 따른 실시예 5 내지 8의 코팅지는 내수성 및 열실링성이 우수한 것을 확인하였다.As shown in Table 3 above, it was confirmed that the coated paper of Examples 5 to 8 according to the present invention is excellent in water resistance and heat sealing.
반면, 내유성은 실시예 5 및 실시예 7은 우수하였지만, 실시예 6은 양호한 수준, 실시예 8은 보통 수준이었다.On the other hand, oil resistance was excellent in Examples 5 and 7, but Example 6 was a good level, Example 8 was a moderate level.
본 발명의 친환경적이며 재생가능한 수용성 코팅지는 일회용컵, 테이크아웃 용기, 햄버거 포장지, 치킨포장지, 아이스크림 용기 등 식품포장재 제조에 활용될 수 있고, 사용후 폐기시 용이하게 재활용할 수 있다.
Eco-friendly and renewable water-soluble coating paper of the present invention can be utilized in the manufacture of food packaging materials, such as disposable cups, take-out containers, hamburger wrappers, chicken wrappers, ice cream containers, and can be easily recycled when disposed of after use.
Claims (7)
(B) 가온된 유기용제 100 중량부에 대하여 폴리염화비닐리덴 10 내지 40중량부를 첨가하고 30 내지 60℃, 1,000 내지 2,000RPM으로 30 내지 150분 동안 교반하는 단계;
(C) 상기 교반된 혼합물에 지방산을 유기용제 100 중량부에 대하여 0.005 내지 0.1 중량부 첨가하고 30 내지 60℃, 1,000 내지 2,000RPM으로 10 내지 30분 동안 교반하는 단계;
(D) 상기 혼합물에 말레산 무수물(maleic anhydride)를 유기용제 100 중량부에 대하여 0.01 내지 0.5 중량부 첨가하고 30 내지 60℃, 1,000 내지 2,000RPM으로 10 내지 30분 동안 교반하는 단계;
(E) 상기 말레산 무수물이 포함된 혼합물에 슬립제를 유기용제 100 중량부에 대하여 0.2 내지 2.0 중량부 첨가하고 30 내지 60℃, 1,000 내지 2,000RPM으로 15 내지 60분 동안 교반하는 단계;
(F) 상기 슬립제가 포함된 혼합물을 20 내지 80℃, 20 내지 200RPM으로 2 내지 10시간 동안 숙성시켜 코팅 조성물을 제조하는 단계
(G) 상기 코팅을 코터와 같은 코팅장치를 이용하여 종이에 코팅한 다음, 50 내지 200℃의 열풍으로 1차 건조, 50 내지 200℃의 히팅 롤러를 통과하면서 2차 건조한 다음, 0 내지 30℃ 냉각롤러를 통과시켜 코팅지를 제조하는 단계;를 포함하는 것을 특징으로 하는 수용성 코팅지의 제조 방법.(A) warming the organic solvent to 30 to 60 ℃;
(B) adding 10 to 40 parts by weight of polyvinylidene chloride based on 100 parts by weight of the heated organic solvent and stirring at 30 to 60 ° C. and 1,000 to 2,000 RPM for 30 to 150 minutes;
(C) adding 0.005 to 0.1 parts by weight of fatty acid to 100 parts by weight of the organic solvent to the stirred mixture and stirring for 10 to 30 minutes at 30 to 60 ℃, 1,000 to 2,000 RPM;
(D) adding 0.01 to 0.5 parts by weight of maleic anhydride to the mixture with respect to 100 parts by weight of an organic solvent and stirring at 30 to 60 ° C. and 1,000 to 2,000 RPM for 10 to 30 minutes;
(E) 0.2 to 2.0 parts by weight of a slip agent is added to the mixture containing maleic anhydride with respect to 100 parts by weight of an organic solvent and stirred at 30 to 60 ° C. and 1,000 to 2,000 RPM for 15 to 60 minutes;
(F) aging the mixture containing the slip agent at 20 to 80 ℃, 20 to 200 RPM for 2 to 10 hours to prepare a coating composition
(G) The coating is coated on paper using a coating apparatus such as a coater, and then firstly dried with hot air at 50 to 200 ° C., secondly while passing through a heating roller at 50 to 200 ° C., and then 0 to 30 ° C. Manufacturing a coated paper by passing through a cooling roller; Method of producing a water-soluble coated paper comprising a.
Water-soluble coated paper produced by the method of any one of claims 1 to 6.
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| CN108117661A (en) * | 2018-01-18 | 2018-06-05 | 常德金德新材料科技股份有限公司 | A kind of powder is to the method for modifying of surface modification film |
| KR102510005B1 (en) | 2022-08-16 | 2023-03-14 | 주식회사 이수 | Apparatus and method for manufacturing eco-friendly containers using fallen leaves, and eco-friendly container thereof |
| KR102860552B1 (en) * | 2024-09-30 | 2025-09-16 | 에이치비페이퍼 주식회사 | Method for producing adhesive composition having water resistance and oil resistance and adhesive composition according to the method |
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| KR102750420B1 (en) | 2024-05-10 | 2025-01-09 | 주진만 | Environmentally friendly sealing paper and manufacturing method thereof |
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| JP3060432B2 (en) * | 1990-07-06 | 2000-07-10 | 株式会社リコー | A rewritable barcode display, a method of processing the barcode display, a method of reading the barcode, and a processing device of the barcode display. |
| JP3350821B2 (en) * | 1991-06-07 | 2002-11-25 | 株式会社リコー | Reversible thermosensitive recording material |
| JPH06320860A (en) * | 1993-05-11 | 1994-11-22 | Nitto Denko Corp | Reversible thermosensitive recording medium |
| JPH09254337A (en) * | 1996-03-22 | 1997-09-30 | Kohjin Co Ltd | Polyvinylidene chloride copolymer resin coated heat-shrinkable polypropylene film |
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| CN108117661A (en) * | 2018-01-18 | 2018-06-05 | 常德金德新材料科技股份有限公司 | A kind of powder is to the method for modifying of surface modification film |
| KR102510005B1 (en) | 2022-08-16 | 2023-03-14 | 주식회사 이수 | Apparatus and method for manufacturing eco-friendly containers using fallen leaves, and eco-friendly container thereof |
| KR102860552B1 (en) * | 2024-09-30 | 2025-09-16 | 에이치비페이퍼 주식회사 | Method for producing adhesive composition having water resistance and oil resistance and adhesive composition according to the method |
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