KR20220047410A - Water Soluble Coating Materials For Paper Coating And Manufacturing Method Thereof - Google Patents

Water Soluble Coating Materials For Paper Coating And Manufacturing Method Thereof Download PDF

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KR20220047410A
KR20220047410A KR1020200129770A KR20200129770A KR20220047410A KR 20220047410 A KR20220047410 A KR 20220047410A KR 1020200129770 A KR1020200129770 A KR 1020200129770A KR 20200129770 A KR20200129770 A KR 20200129770A KR 20220047410 A KR20220047410 A KR 20220047410A
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weight
parts
cellulose
water
coating composition
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장하다
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장하다
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/34Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising cellulose or derivatives thereof
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/09Sulfur-containing compounds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24Polysaccharides
    • D21H17/25Cellulose
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
    • D21H17/57Polyureas; Polyurethanes
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/60Waxes
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63Inorganic compounds
    • D21H17/67Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/675Oxides, hydroxides or carbonates
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/18Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising waxes
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/20Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/24Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H19/00Coated paper; Coating material
    • D21H19/36Coatings with pigments
    • D21H19/44Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
    • D21H19/52Cellulose; Derivatives thereof
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/16Sizing or water-repelling agents

Abstract

The present invention relates to an eco-friendly water-soluble paper coating composition and a manufacturing method thereof. More specifically, the eco-friendly water-soluble paper coating composition comprises, with respect to 100 parts by weight of an organic solvent, 10 to 30 parts by weight of a cellulose derivative, 1 to 10 parts by weight of a plasticizer, 3 to 30 parts by weight of a slip agent, and 0.5 to 50 parts by weight of a dispersing agent. According to the present invention, the eco-friendly water-soluble paper coating composition is easily coated on paper, provides excellent water resistance, oil resistance, and heat-sealing properties, and is made of cellulose so that it is harmless to the human body. In addition, a water-soluble coating film coated on paper is formed of a cellulose material like paper and is easily dissociated in water or alkaline solution, thereby facilitating recycling and being biodegradable in the natural environment to be returned to nature.

Description

친환경 수용성 종이 코팅제 제조방법 {Water Soluble Coating Materials For Paper Coating And Manufacturing Method Thereof}Eco-friendly Water Soluble Coating Material Manufacturing Method {Water Soluble Coating Materials For Paper Coating And Manufacturing Method Thereof}

본 발명은 가소화된 셀룰로오스 유도체를 포함하는 종이 코팅용 수용성 코팅조성 및 이의 제조방법에 관한 것이다.The present invention relates to a water-soluble coating composition for paper coating comprising a plasticized cellulose derivative and a method for preparing the same.

현대의 사회생활은 활동시간과 이동거리와 습득하여야 할 정보 등이 늘어나는 동시에 제한된 시간을 최대한 효율적으로 사용하여야 한다.In modern social life, active time, moving distance, and information to be acquired are increasing, and at the same time, limited time must be used as efficiently as possible.

인간의 활동 중에서 제외할 수 없는 것이 에너지를 제공하는 음식물 섭취이며, 바쁜 현대 사회생활 속에서도 한정된 시간 속에서 필요한 음식물을 빠른 시간에 간편하게 섭취할 필요가 있어 다양한 용기가 사용되고 있다.Food intake that provides energy is one of human activities that cannot be excluded, and various containers are used because it is necessary to quickly and conveniently consume necessary food in a limited time even in busy modern social life.

특히, 현대 생활은 발달한 과학기술, 생활수준과 문화의 질적 향상 및 편리함 추구 등에 의하여 일회용품의 사용이 급격히 중가하면서 음료용으로 자동판매기의 컵, 음료수를 포장하는 용기, 컵라면 용기, 테이크아웃용 용기, 아이스크림용 용기 등과 같이 다양한 일회용 용기가 개발되어 사용되고 있다.In particular, in modern life, the use of disposable products is rapidly increasing due to the development of science and technology, quality improvement in living standards and culture, and the pursuit of convenience. Various disposable containers such as containers and containers for ice cream have been developed and used.

상기와 같은 일회용 용기는 종이를 사용하는 경우가 많으며, 종이의 경우 흡습성의 문제를 해결하기 위하여 방수성 재질로 내부를 코팅한다.Disposable containers as described above often use paper, and in the case of paper, the inside is coated with a waterproof material to solve the problem of hygroscopicity.

상기 종이용기의 코팅에 많이 사용되는 것이 폴리에틸렌(POLYETHYLENE: PE)이다.Polyethylene (POLYETHYLENE: PE) is widely used for coating the paper container.

일반적으로 폴리에틸렌은 플라스틱으로 알려져 있으며 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 known as a plastic and is a chemical substance widely used in surrounding household products due to its advantages such as light, rust, and non-corrosion, as well as chemical safety, water resistance, flexibility, insulation, and moldability.

상기 폴리에틸렌은 일반적으로 식품위생성이 우수하고, 유통가격이 비교적 저렴한 등의 이유에 의하여 다양한식품 용기의 내부에 코팅되어 방수 등의 목적으로 사용되고 있으나 이를 이용한 코팅용기는 사용 및 폐기과정에서 환경호르몬이 방출될 수 있다. 또한, 폴리에틸렌 코팅용기는 사용 후 재활용을 위해 해리하는 과정에서 물에해리되지 않으므로 선별 과정을 거쳐야 하기 때문에 재활용 비용이 증가된다.The polyethylene is generally used for the purpose of waterproofing by being coated inside various food containers for reasons such as excellent food hygiene and relatively inexpensive distribution, but the coated container using the same releases environmental hormones during use and disposal. can be In addition, the polyethylene-coated container does not dissociate in water in the process of dissociation for recycling after use, so recycling costs increase because it has to go through a screening process.

이에 따라 종이용기 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 분해가되기까지 수백 년이 걸리기 때문에 토양 오염의 주범이 된다. 더욱이, 폴리에틸렌 코팅공정은 원천적으로 요구As a result, pulp is continuously imported for the manufacture of paper containers, and there are limitations in terms of resource recycling and environmental destruction. Because it takes hundreds of years to grow, it is the main culprit of soil pollution. Moreover, the polyethylene coating process is fundamentally required

되는 200 ℃ 가량의 폴리에틸렌 칩의 용해공정 및 이에 대한 휘발성유기용제(VOCs)로 인하여 고비용 및 작업환경 저하/대기오염으로 인한 환경문제를 유발한다.Due to the dissolution process of polyethylene chips at about 200 °C and volatile organic solvents (VOCs), it causes environmental problems due to high cost and deterioration of the working environment/air pollution.

[0010] 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. 이를 극복하기 위한 종래기술로는 아크릴에멀젼으로 이루어진 수용성 수지, 슬립제 및 분산제로 이루어진 포장In addition, the polyethylene coating has a very high risk of exposure to carcinogens and the release of environmental hormones depending on the conditions of use, and since it induces toxicity when exposed to the human body for a long period of time, problems are raised in terms of food hygiene and safety. As a prior art for overcoming this, packaging made of a water-soluble resin made of an acrylic emulsion, a slip agent, and a dispersant.

용 수지가 개시되어 있다. 이 기술은 친환경적이며 재생 가능할 뿐만 아니라 환경호르몬이 방출되지 않는 식품 포장용 수지이지만, 점도가 높아 코팅작업이 어려우며 물의 함량이 많으므로 코팅 작업시 물이 휘발되는 속도가 느려 작업성이 떨어진다. 또한, 아크릴에멀젼은 딱딱한 특성으로 인하여 종이가 뻣뻣해져 경첩부분의 코팅막이 손상되어 물과 기름 등이 쉽게 종이에 스며들 뿐만 아니라 재활용 시 물에 해리되는 시간이 많이 소요되는 문제가 있다.A resin for use is disclosed. Although this technology is eco-friendly, renewable, and food packaging resin that does not release environmental hormones, it is difficult to coat because of its high viscosity, and because of the high water content, the rate at which water volatilizes during coating is slow and workability is poor. In addition, the acrylic emulsion has a problem in that the paper becomes stiff due to its hard nature and the coating film of the hinge part is damaged, so that water and oil easily permeate into the paper and it takes a lot of time to dissociate into water during recycling.

본 발명은 가소화된 셀룰로오스 유도체를 포함함으로써 친환경적이며, 재생가능한 종이 코팅용 수용성 코팅조성물을 제공하는 것을 목적으로 한다. 또한, 본 발명은 수용성 코팅조성물의 제조방법을 제공하는 것을 다른 목적으로 한다.An object of the present invention is to provide a water-soluble coating composition for paper coating that is environmentally friendly and recyclable by including a plasticized cellulose derivative. Another object of the present invention is to provide a method for preparing a water-soluble coating composition.

상기한 목적을 달성하기 위하여 본 발명의 수용성 코팅조성물은 유기용제 100 중량부에 대하여 셀룰로오스 유도체 10 내지 30 중량부, 가소제 1 내지 10 중량부 및 슬립제 3 내지 30 중량부를 포함한다.In order to achieve the above object, the water-soluble coating composition of the present invention contains 10 to 30 parts by weight of a cellulose derivative, 1 to 10 parts by weight of a plasticizer, and 3 to 30 parts by weight of a slip agent based on 100 parts by weight of the organic solvent.

상기 수용성 코팅조성물은 유기용제 100 중량부에 대하여 분산제 05 내지 50 중량부를 더 포함한다.The water-soluble coating composition further comprises 05 to 50 parts by weight of a dispersant based on 100 parts by weight of the organic solvent.

상기 유기용제는 메틸벤젠(Methyl benzene), 에틸아세테이트(Ethyl acetate), 메틸아세테이트(Methylacetate), 프로필아세테이트(Propyl acetate), 벤젠(Benzene), 클로로벤젠(Chloro Benzene), 에탄올(Ethanol) 및 이소프로판올(Isopropanol)로 이루어진 군에서 선택된 1종 이상이다.The organic solvent is methyl benzene, ethyl acetate, methyl acetate, propyl acetate, benzene, chlorobenzene, ethanol, and isopropanol. Isopropanol) is at least one selected from the group consisting of.

상기 셀룰로오스 유도체는 메틸셀룰로오스(Methyl cellulose)에틸셀룰로오스(Ethyl cellulose), 하이드록시프로필메틸셀룰로오스(Hydroxypropylmethyl cellulose), 셀룰로오스아세테이트(Cellulose acetate) 및 니트로셀룰로오스(Nitro cellulose)로 이루어진 군에서 선택된 1종 이상이다.The cellulose derivative is at least one selected from the group consisting of methyl cellulose, ethyl cellulose, hydroxypropylmethyl cellulose, cellulose acetate, and nitro cellulose.

상기 가소제는 트리아세틴(Triacetine), 트리에틸시트레이트(Triethylcitrate), 디사이클로헥실프탈레이트(Dicyclohexyl phthalate), 이에스오(ESO, Epoxidized soybean oil) 및 글리세롤(Glycerol)로 이루어진 군에서선택된 1종 이상이다.The plasticizer is at least one selected from the group consisting of triacetine, triethylcitrate, dicyclohexyl phthalate, ESO (Epoxidized soybean oil) and glycerol.

상기 슬립제는 파라핀 왁스 에멀젼(Paraffin wax emulsion), 리코왁스 에멀젼(Lico wax emulsion), 폴리에틸렌 왁스 에멀젼(Polyethylene wax emulsion), 실리콘 에멀젼(Silicone emulsion), 스테아르산 모노머(Stearicacid monomer)로 이루어진 군에서 선택된 1종 이상이다.The slip agent is selected from the group consisting of paraffin wax emulsion, Lico wax emulsion, polyethylene wax emulsion, silicone emulsion, and stearic acid monomer. more than one

상기 분산제는 친수성 실리카(Hydrophilic silica), 아크릴 에멀젼(Acrylic Emulsion), 디에스테르 설포석시네이트(Diester sulfosuccinate) 및 우레탄 에멀젼(Urethane Emulsion)로 이루어진 군에서 선택된 1종 이상이다.The dispersant is at least one selected from the group consisting of hydrophilic silica, acrylic emulsion, diester sulfosuccinate, and urethane emulsion.

상기한 다른 목적을 달성하기 위하여 본 발명의 수용성 코팅조성물의 제조방법은 30 내지 60℃로 유기용제를 가온시키는 단계; 가온된 유기용제 100 중량부에 대하여 셀룰로오스 유도체 10 내지 30 중량부를 첨가하고 30 내지 60℃에서 60 내지 200분 동안 교반하는 단계; 가소화 반응을 위하여 상기 교반된 혼합물에 가소제를 유기용제 100 중량부에 대하여 1 내지 10 중량부를 첨가하고 30 내지 60℃에서 10 내지 80분 동안 교반하는 단계; 상기 가소제가 포함된 혼합물에 슬립제를 유기용제 100 중량부에 대하여 3 내지 30 중량부를 첨가하고 교반하는 단계; 및 상기 슬립제가 포함된 혼합물을 30 내지 80℃에서 2 내지 10시간 동안 숙성시키는 단계를 포함한다.In order to achieve the above other object, the method for preparing a water-soluble coating composition of the present invention includes heating an organic solvent to 30 to 60°C; adding 10 to 30 parts by weight of a cellulose derivative based on 100 parts by weight of the heated organic solvent and stirring at 30 to 60° C. for 60 to 200 minutes; adding 1 to 10 parts by weight of a plasticizer to the stirred mixture based on 100 parts by weight of an organic solvent for a plasticization reaction and stirring at 30 to 60° C. for 10 to 80 minutes; adding 3 to 30 parts by weight of a slip agent to the mixture containing the plasticizer based on 100 parts by weight of an organic solvent and stirring; and aging the mixture containing the slip agent at 30 to 80° C. for 2 to 10 hours.

상기 가소제가 포함된 혼합물에 슬립제를 첨가하여 교반하는 단계와 혼합물을 숙성시키는 단계 사이에, 분산제를 유기용제 100 중량부에 대하여 05 내지 50 중량부를 첨가하고 교반하는 단계를 더 포함한다.Between the step of adding a slip agent to the mixture containing the plasticizer and stirring the mixture and the step of aging the mixture, the method further includes adding and stirring 05 to 50 parts by weight of a dispersant based on 100 parts by weight of the organic solvent.

본 발명의 수용성 코팅조성물은 작업성이 우수하여 얇은 코팅막으로 종이에 용이하게 코팅되며, 코팅막이 얇게도포됨에도 우수한 내수성, 내유성 및 열실링성이 부여된다.The water-soluble coating composition of the present invention is easily coated on paper with a thin coating film due to excellent workability, and excellent water resistance, oil resistance and heat sealing properties are imparted even when the coating film is applied thinly.

또한, 본 발명의 수용성 코팅조성물은 열처리 건조 상태에서는 3~4일 동안 내수성 및 내유성을 유지하지만, 수용성 코팅조성물이 코팅된 종이를 재활용 시 이를 물 또는 알칼리 용액에 교반하면 기계적 교반처리에 의해 코팅막과 종이가 신속하게 해리되므로 용이하게 재활용할 수 있다.In addition, the water-soluble coating composition of the present invention maintains water resistance and oil resistance for 3-4 days in a heat-dried state, but when recycled paper coated with a water-soluble coating composition is stirred in water or alkaline solution, the coating film and the coating film by mechanical stirring treatment The paper dissociates quickly, making it easy to recycle.

또한, 본 발명의 수용성 코팅조성물은 종이와 같은 재질의 셀룰로오스 유도체를 사용하므로 인체에 무해하며,수용성 코팅조성물이 코팅된 종이는 자연환경에서 생분해되어 자연으로 돌아가며, 퇴비화되어 자연상태에서 선순환되는 친환경적인 조성물이다.In addition, the water-soluble coating composition of the present invention is harmless to the human body because it uses a cellulose derivative of the same material as paper, and the paper coated with the water-soluble coating composition is biodegradable in a natural environment and returns to nature. composition.

도 1은 본 발명의 코팅조성물을 일실시예에 따라 [0026] 제조하는 방법을 도시한 흐름도이다.1 is a flow chart showing a method for manufacturing the coating composition of the present invention according to an embodiment.

본 발명은 유기용제 100 중량부에 대하여 셀룰로오스 유도체 10 내지 30 중량부, 가소제 1 내지 10 중량부 및 슬립제 3 내지 30 중량부를 포함함으로써 종이에 용이하게 코팅되며 우수한 내수성, 내유성 및 열실링성이 부여될 수 있을 뿐만 아니라 인체에 무해한 수용성 코팅조성물 및 이의 제조방법에 관한 것이다. 이때, 수용성 코팅조성물은 분산제 05 내지 50 중량부를 더 포함할 수 있다.The present invention is easily coated on paper by including 10 to 30 parts by weight of a cellulose derivative, 1 to 10 parts by weight of a plasticizer, and 3 to 30 parts by weight of a slip agent with respect to 100 parts by weight of an organic solvent, and excellent water resistance, oil resistance and heat sealing properties are provided. It relates to a water-soluble coating composition that is harmless to the human body as well as a method for manufacturing the same. In this case, the water-soluble coating composition may further include 05 to 50 parts by weight of a dispersant.

이하, 본 발명을 상세하게 설명한다.Hereinafter, the present invention will be described in detail.

본 발명의 수용성 코팅조성물은 가소화된 셀룰로오스 유도체를 포함함으로써 종이에 얇게 도포되더라도 우수한내수성, 내유성 및 열실링성이 부여될 수 있다.Since the water-soluble coating composition of the present invention contains a plasticized cellulose derivative, excellent water resistance, oil resistance and heat sealing properties can be imparted even when applied thinly to paper.

셀룰로오스는 일반적으로 물에 불용성이지만 셀룰로오스를 구성하고 있는 글루코스환의 수산기를 메틸기, 에틸기, 하이드록시기 등으로 치환하면 치환정도에 따라 수용성이 된다.Cellulose is generally insoluble in water, but if the hydroxyl group of the glucose ring constituting cellulose is substituted with a methyl group, an ethyl group, or a hydroxyl group, it becomes water-soluble depending on the degree of substitution.

본 발명의 셀룰로오스 유도체는 셀룰로오스의 수산기(Hydroxyl group, -OH)를 니트로화, 아세틸화 또는 에테르화 반응에 의해 치환하여 수소결합을 현저히 감소시킨 것으로서 친수성의 수산기가 소수성의 다른 기로 변화된다.The cellulose derivative of the present invention significantly reduces hydrogen bonding by substituting a hydroxyl group (-OH) of cellulose by nitration, acetylation or etherification, and the hydrophilic hydroxyl group is changed to another hydrophobic group.

셀룰로오스 유도체의 예로는 메틸셀룰로오스(Methyl cellulose)에틸셀룰로오스(Ethyl cellulose), 하이드록시Examples of the cellulose derivative include methyl cellulose, ethyl cellulose, hydroxy

프로필메틸셀룰로오스(Hydroxypropylmethyl cellulose),셀룰로오스아세테이트(Cellulose acetate) 및 니트로셀룰로오스(Nitro cellulose)로 이루어진 군에서 선택된 1종 또는 2종 이상을 들 수 있다.and one or two or more selected from the group consisting of propylmethyl cellulose, cellulose acetate, and nitro cellulose.

상기 셀룰로오스 유도체는 유기용제 100 중량부에 대하여 10 내지 30 중량부, 바람직하게는 10 내지 20 중량부로 사용된다. 셀룰로오스 유도체의 함량이 10 중량부 미만인 경우에는 종이에 내수성 및 내유성을 부여할 수 없으며, 함량이 30 중량부 초과인 경우에는 코팅액의 점도가 높아 코팅작업 시 덩어리지는 현상에 의해 코팅이 불량해지며, 신속하게 건조가 되지 않아 코팅액끼리 붙는 브로킹 현상이 발생된다.The cellulose derivative is used in an amount of 10 to 30 parts by weight, preferably 10 to 20 parts by weight, based on 100 parts by weight of the organic solvent. When the content of the cellulose derivative is less than 10 parts by weight, water resistance and oil resistance cannot be imparted to the paper. It does not dry quickly, causing the coating solution to stick to each other.

상기 가소제는 셀룰로오스 유도체를 가소화시키는 것으로서, 예로는 트리아세틴(Triacetine), 트리에틸시트레이트(Triethylcitrate), 디사이클로헥실프탈레이트(Dicyclohexyl phthalate), 이에스오(ESO, Epoxidized soybeanThe plasticizer is to plasticize the cellulose derivative, for example, triacetine, triethylcitrate, dicyclohexyl phthalate, ESO (Epoxidized soybean)

oil) 및 글리세롤(Glycerol)로 이루어진 군에서 선택된 1종 또는 2종 이상을 들 수 있다.oil) and one or more selected from the group consisting of glycerol (Glycerol).

가소제는 유기용제 100 중량부에 대하여 1 내지 10 중량부, 바람직하게는 1 내지 6 중량부로 사용된다. 가소제의 함량이 1 중량부 미만인 경우에는 셀룰로오스가 용액화가 되지 않고 코팅막의 열실링성이 저하되며, 함량이3 중량부 초과인 경우에는 셀룰로오스 입자가 분해되어 가공온도 상승되며, 이에 따라 코팅작업 시 온도가 상승되어 종이의 탄화현상이 발생될 뿐만 아니라 셀룰로오스 입자의 결정성이 약화되어 내수성 및 내유성의 코팅막을 형성할 수 없다.The plasticizer is used in an amount of 1 to 10 parts by weight, preferably 1 to 6 parts by weight, based on 100 parts by weight of the organic solvent. When the content of the plasticizer is less than 1 part by weight, the cellulose does not become solution and the heat sealing property of the coating film is lowered. is increased, not only carbonization of the paper occurs, but also the crystallinity of the cellulose particles is weakened, making it impossible to form a water-resistant and oil-resistant coating film.

가소제로 셀룰로오스를 가소화함으로써 고체의 셀룰로오스를 용액화하고 이 용액의 점성을 유지시킴으로써 종이등이 용이하게 코팅이 되도록 한다.By plasticizing cellulose with a plasticizer, solid cellulose is made into solution and the viscosity of the solution is maintained so that paper, etc. can be easily coated.

상기 슬립제는 본 발명의 코팅조성물이 도포된 종이의 마찰계수를 저하시켜 윤활성 강화 및 표면강도 향상을 유발함으로써 후공정인 인쇄작업 시 발생될 수 있는 종이의 층간 접/점착현상을 방지하며, 코팅조성물에 슬립성을부여하여 코팅막의 건조도막 두께가 얇게 형성되도록 할 뿐만 아니라 우수한 내수성 및 내유성을 부여한다. 이러한 슬립제의 예로는 파라핀 왁스 에멀젼(Paraffin wax emulsion), 리코왁스 에멀젼(Lico wax emulsion), 폴리에틸렌 왁스 에멀젼(Polyethylene wax emulsion), 실리콘 에멀젼(Silicone emulsion), 스테아르산 모노머(Stearic acid monomer)로 이루어진 군에서 선택된 1종 또는 2종 이상을 들 수 있다.The slip agent lowers the coefficient of friction of the paper coated with the coating composition of the present invention, thereby enhancing lubricity and improving surface strength, thereby preventing the interlayer contact/adhesion phenomenon of paper that may occur during the printing operation, which is a post process, and coating By imparting slip properties to the composition, it not only makes the dry film thickness of the coating film thin, but also provides excellent water resistance and oil resistance. Examples of such slip agents include paraffin wax emulsion, Lico wax emulsion, polyethylene wax emulsion, silicone emulsion, and stearic acid monomer. 1 type or 2 or more types selected from the group can be mentioned.

슬립제는 유기용제 100 중량부에 대하여 3 내지 30 중량부, 바람직하게는 3 내지 20 중량부로 사용된다. 슬립제의 함량이 3 중량부 미만인 경우에는 윤활성이 저하되어 코팅막 사이에 브로킹 현상에 의해 서로 달라붙는 현상이 발생되며, 함량이 30 중량부 초과인 경우에는 윤활성이 우수해져 종이 등에 코팅하기가 어려우며 슬립제로왁스류가 사용되면 왁스가 기름을 흡수하여 내유성이 저하된다.The slip agent is used in an amount of 3 to 30 parts by weight, preferably 3 to 20 parts by weight, based on 100 parts by weight of the organic solvent. If the content of the slip agent is less than 3 parts by weight, the lubricity is lowered and sticking occurs due to the blocking phenomenon between the coating films. When slip-zero waxes are used, the wax absorbs oil and the oil resistance decreases.

상기 분산제는 셀룰로오스 유도체 등의 물질들을 분산시키고 현탁성을 증가시키며 저장 안정성을 향상시키는 것으로서, 예로는 친수성 실리카(Hydrophilic silica), 아크릴 에멀젼(Acrylic Emulsion), 디에스테르 설포석시네이트(Diester sulfosuccinate) 및 우레탄 에멀젼(Urethane Emulsion)로 이루어진 군에서 선택된 1종 또는 2종 이상을 들 수 있다.The dispersing agent disperses substances such as cellulose derivatives, increases suspendability, and improves storage stability, for example, hydrophilic silica, acrylic emulsion, diester sulfosuccinate, and One or two or more selected from the group consisting of urethane emulsion may be mentioned.

분산제는 유기용매 100 중량부에 대하여 05 내지 50 중량부, 바람직하게는 2 내지 30 중량부로 사용된다. 분산제의 함량이 05 중량부 미만인 경우에는 분산효과를 기대할 수 없으며, 함량이 50 중량부 초과인 경우에는 현탁성은 우수하나 경제적 측면에서 바람직하지 못하다.The dispersant is used in an amount of 05 to 50 parts by weight, preferably 2 to 30 parts by weight, based on 100 parts by weight of the organic solvent. When the content of the dispersant is less than 05 parts by weight, a dispersing effect cannot be expected, and when the content is more than 50 parts by weight, the suspendability is excellent, but it is not preferable from an economic point of view.

상기 유기용매의 예로는 메틸벤젠(Methyl benzene), 에틸아세테이트(Ethyl acetate), 메틸아세테이트(Methylacetate), 프로필아세테이트(Propyl acetate), 벤젠(Benzene), 클로로벤젠(Chloro Benzene), 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, propyl acetate, benzene, chlorobenzene, ethanol, and ethanol. One or two or more selected from the group consisting of isopropanol may be mentioned.

본 발명의 코팅조성물로 코팅막을 형성 시 코팅막의 도공량은 5 내지 20 g/㎡, 바람직하게는 7 내지 15 g/㎡이다. 코팅막의 도공량이 5 g/㎡ 미만인 경우에는 우수한 내유성, 내수성 및 열실링성을 얻지 못하며, 도공량이20 g/㎡ 초과인 경우에는 내수성, 내유성 및 열실링성이 더 우수해 지기는 하지만 이를 경제적인 측면과 고려하면 바람직하지 못한 정도이다.When forming a coating film with the coating composition of the present invention, the coating amount of the coating film is 5 to 20 g/m 2 , preferably 7 to 15 g/m 2 . If the coating amount of the coating film is less than 5 g/m2, excellent oil resistance, water resistance and heat sealing properties are not obtained. Considering the aspect, it is an undesirable degree.

또한, 도공량은 코팅조성물을 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 내지 3 g/㎡을 도포한 다음 2차 도포를 하는 것이 바람직하다.또한, 본 발명은 수용성 코팅조성물을 이용한 제조방법을 제공하며, 도 1을 참조하여 설명한다.In addition, the amount of coating can be formed by applying the coating composition at once, but it is preferable to apply it twice in order to obtain more excellent water resistance, oil resistance and heat sealing properties. In particular, when the surface of the paper is rough, it is preferable to apply 2 to 3 g/m 2 first and then apply the second application. Also, the present invention provides a manufacturing method using a water-soluble coating composition, see FIG. 1 . to explain

먼저, 교반기에 유기용제를 투입하고 30 내지 60℃로 가온한다(S110)First, an organic solvent is added to the stirrer and heated to 30 to 60° C. (S110)

S110단계에서 가온된 유기용제에 셀룰로오스 유도체를 첨가하고 30 내지 60℃를 유지하면서 60 내지 200분 동안1,000 내지 2,000 RPM의 속도로 교반한다(S120) 교반시간이 60분 미만인 경우에는 충분한 혼합이 이루어지지 않아 추후에 셀룰로오스를 가소화시키기 어려우며, 교반시간이 200분 초과인 경우에는 유기용제가 휘발되어 이후에 계속되는 공정을 진행할 수 없다. 또한, 교반속도가 1,000 RPM미만인 경우에는 충분한 혼합이 이루어지지 않아 추후에 셀룰로오스를 가소화시키기 어려우며, 교반속도가 2,000 RPM초과인 경우에는 기포가 발생되고 용액이 넘쳐 이후에 계속되는 공정을 진행할 수 없다.A cellulose derivative is added to the organic solvent heated in step S110 and stirred at a speed of 1,000 to 2,000 RPM for 60 to 200 minutes while maintaining 30 to 60 °C (S120) If the stirring time is less than 60 minutes, sufficient mixing is not made. Therefore, it is difficult to plasticize the cellulose later, and when the stirring time is more than 200 minutes, the organic solvent is volatilized and the subsequent process cannot be performed. In addition, when the stirring speed is less than 1,000 RPM, it is difficult to plasticize the cellulose later because sufficient mixing is not made.

가소화 반응이 일어나도록 상기 S120단계에서 제조된 혼합물에 가소제를 첨가하고 30 내지 60 ℃를 유지하면서10 내지 80분 동안 1,000 내지 2,000 RPM의 속도로 교반한다(S130) 온도가 30 ℃미만인 경우에는 셀룰로오스가 가소화되지 않으며, 온도가 60 ℃초과인 경우에는 유기용제가 휘발되어 계속되는 공정을 진행할 수 없다. 셀룰로오스를 가소화시키기 위해서는 S110 내지 S130단계에서 상기 온도를 유지하여야 한다.A plasticizer is added to the mixture prepared in step S120 to cause the plasticization reaction, and stirred at a speed of 1,000 to 2,000 RPM for 10 to 80 minutes while maintaining 30 to 60 ° C. (S130) When the temperature is less than 30 ° C., cellulose It is not plasticized, and when the temperature is higher than 60 ℃, the organic solvent is volatilized and the continuous process cannot be performed. In order to plasticize the cellulose, the temperature should be maintained in steps S110 to S130.

S130단계에서 교반시간이 10분 미만인 경우에는 셀룰로오스 유도체의 가소화가 충분하지 못하며, 교반시간이 80분 초과인 경우에는 과도한 가소화로 인하여 혼합물의 점도가 상승하게 된다.When the stirring time is less than 10 minutes in step S130, plasticization of the cellulose derivative is not sufficient, and when the stirring time is more than 80 minutes, the viscosity of the mixture increases due to excessive plasticization.

상기 S130단계에서 제조된 혼합물에 슬립제를 첨가하고 10 내지 80분 동안 1,000 내지 2,000 RPM의 속도로 교반(S140)한 후 이를 30 내지 80℃에서 2 내지 10시간동안 숙성시킨다(S150) S140단계에서 제조된 혼합물을 S150단계의 조건으로 숙성시키지 않으면 고분자간 결합이 안정화 되지 않으므로 용매와 용질간의 이형에 의해 용액이 분리된다.After adding a slip agent to the mixture prepared in step S130 and stirring at a speed of 1,000 to 2,000 RPM for 10 to 80 minutes (S140), it is aged at 30 to 80° C. for 2 to 10 hours (S150) in step S140 If the prepared mixture is not aged under the conditions of step S150, the interpolymer bond is not stabilized, so the solution is separated by release between the solvent and the solute.

또한 상기 S140단계 및 S150단계 사이에, S140단계에서 제조된 혼합물에 분산제를 첨가하여 10 내지 80분 동안1,000 내지 2,000 RPM의 속도로 교반하는 단계(S160)를 추가할 수 있다.Also, between steps S140 and S150, a step (S160) of stirring at a speed of 1,000 to 2,000 RPM for 10 to 80 minutes by adding a dispersing agent to the mixture prepared in step S140 may be added.

본 발명의 코팅조성물은 코팅장치를 이용하여 종이의 일측면에 코팅막을 형성한다. 코팅장치의 코터는 특별한 제한이 없으나, 2단 내지 6단 롤러 바브레이드코터, 콤마코터, 스프레이코터, 메쉬 또는 망점코터, 케스팅코터, 그라비아코터, 드라핑(dropping)코터, 에어나이프코터 등을 사용할 수 있다.The coating composition of the present invention forms a coating film on one side of the paper using a coating device. There is no particular limitation on the coater of the coating device, but 2 to 6 roller bar braid coaters, comma coaters, spray coaters, mesh or mesh coaters, casting coaters, gravure coaters, dropping coaters, air knife coaters, etc. can be used. can

또한, 수용성 코팅조성물이 종이(원지) 등에 코팅됨으로써 종이용기, 식품 포장지 등을 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 addition, by coating the water-soluble coating composition on paper (base paper) or the like, it is possible to manufacture paper containers, food packaging paper, and the like. Since the above paper has to meet various demands in the coating process, cutting process, printing process, molding process, etc., it is used that has excellent strength, long-term storage, moisture resistance, dimensional stability, processing aptitude, etc., and there are special restrictions on this However, it is preferable to use bleached chemical pulp as a raw material and to use paper excellent in folding resistance and moldability.

이하, 본 발명의 이해를 돕기 위하여 바람직한 실시예를 제시하나, 하기 실시예는 본 발명을 예시하는 것일 뿐 본 발명의 범주 및 기술사상 범위 내에서 다양한 변경 및 수정이 가능함은 당업자에게 있어서 명백한 것이며,이러한 변형 및 수정이 첨부된 특허청구범위에 속하는 것도 당연한 것이다.Hereinafter, preferred examples are presented to help the understanding of the present invention, but the following examples are merely illustrative of the present invention, and it will be apparent to those skilled in the art that various changes and modifications are possible within the scope and spirit of the present invention, It goes without saying that such variations and modifications fall within the scope of the appended claims.

실시예 1Example 1

메틸벤젠 400 중량부와 에탄올 600 중량부를 교반기에 넣은 다음 온수를 이용하여 40 ℃로 가열한 후 동일 온도하에서 니트로셀룰로오스 150 중량부를 첨가하여 80분 동안 교반하였다. 상기와 동일한 온도하에서 디사이클로헥실프탈레이트 20 중량부를 첨가하여 30분 동안 교반한 후 파라핀 왁스 에멀젼 60 중량부를 첨가하여 30분 동안 교반하였다. 이렇게 수득한 혼합물을 35 ℃에서 5시간 동안 숙성하여 수용성 코팅조성물을 제조하였다.400 parts by weight of methylbenzene and 600 parts by weight of ethanol were put into a stirrer, and then heated to 40° C. using hot water. Then, 150 parts by weight of nitrocellulose was added under the same temperature and stirred for 80 minutes. At the same temperature as above, 20 parts by weight of dicyclohexyl phthalate was added and stirred for 30 minutes, and then 60 parts by weight of the paraffin wax emulsion was added and stirred for 30 minutes. The mixture thus obtained was aged at 35° C. for 5 hours to prepare a water-soluble coating composition.

도공량이 10 g/㎡가 되도록 상기 제조된 코팅조성물을 식품지에 1차로 코팅한 후 120 ℃ 건조오븐에 5분 동안 건조하였다.The prepared coating composition was first coated on food paper so that the coating amount was 10 g/m 2 , and then dried in a drying oven at 120° C. for 5 minutes.

실시예 2Example 2

상기 실시예 1과 동일하게 실시하되, 실시예 1에서 제조된 코팅조성물을 식품지에 1차로 도공량이 3 g/㎡가 되도록 코팅한 후 건조시키고 2차로 도공량이 7 g/㎡가 되도록 코팅하여 120 ℃ 건조오븐에 3분 동안 건조하였다.The same procedure as in Example 1, except that the coating composition prepared in Example 1 was first coated on food paper so that the coating amount was 3 g/m2, dried, and secondarily coated so that the coating amount was 7 g/m2, at 120 ° C. It was dried in a drying oven for 3 minutes.

실시예 3Example 3

메틸벤젠 400 중량부와 에탄올 600 중량부를 교반기에 넣은 다음 온수를 이용하여 40 ℃로 가열한 후 동일 온도하에서 니트로셀룰로오스 150 중량부를 첨가하여 80분 동안 교반하였다. 상기와 동일한 온도하에서 트리아세틴20 중량부를 첨가하여 30분 동안 교반한 후 리코 왁스 에멀젼 60 중량부를 첨가하여 30분 동안 교반하였다. 이400 parts by weight of methylbenzene and 600 parts by weight of ethanol were put into a stirrer, and then heated to 40° C. using hot water. Then, 150 parts by weight of nitrocellulose was added under the same temperature and stirred for 80 minutes. At the same temperature as above, 20 parts by weight of triacetin was added and stirred for 30 minutes, and then 60 parts by weight of Ricoh wax emulsion was added and stirred for 30 minutes. this

후 친수성 실리카 20 중량부를 첨가하여 50분 동안 교반하였다. 이렇게 수득한 혼합물을 35 ℃에서 5시간 동안 숙성하여 수용성 코팅조성물을 제조하였다.Then, 20 parts by weight of hydrophilic silica was added and stirred for 50 minutes. The mixture thus obtained was aged at 35° C. for 5 hours to prepare a water-soluble coating composition.

도공량이 12 g/㎡가 되도록 상기 제조된 코팅조성물을 식품지에 1차로 코팅한 후 120 ℃건조오븐에 5분 동안 건조하였다.The prepared coating composition was first coated on food paper so that the coating amount was 12 g/m 2 , and then dried in a drying oven at 120° C. for 5 minutes.

실시예 4Example 4

상기 실시예 3과 동일하게 실시하되, 실시예 3에서 제조된 코팅조성물을 식품지에 1차로 도공량이 5 g/㎡가 되도록 코팅한 후 건조시키고 2차로 도공량이 7 g/㎡가 되도록 코팅하여 120 ℃건조오븐에 3분 동안 건조하였다.The same procedure as in Example 3, except that the coating composition prepared in Example 3 is first coated on food paper so that the coating amount is 5 g/m2, dried, and secondarily coated so that the coating amount is 7 g/m2, at 120 ° C. It was dried in a drying oven for 3 minutes.

실시예 5Example 5

상기 실시예 3과 동일하게 실시하되, 니트로셀룰로오스 대신에 메틸셀룰로오스를 사용하였다.It was carried out in the same manner as in Example 3, except that methyl cellulose was used instead of nitrocellulose.

실시예 6Example 6

상기 실시예 5와 동일하게 실시하되, 실시예 5에서 제조된 코팅조성물을 식품지에 1차로 도공량이 5 g/㎡가 되도록 코팅한 후 건조시키고 2차로 도공량이 7 g/㎡가 되도록 코팅하여 120 ℃건조오븐에 3분 동안 건조하였다.The same procedure as in Example 5, except that the coating composition prepared in Example 5 is first coated on food paper so that the coating amount is 5 g/m2, dried, and secondarily coated so that the coating amount is 7 g/m2, at 120 ° C. It was dried in a drying oven for 3 minutes.

비교예 1Comparative Example 1

상기 실시예 3과 동일하게 실시하되, 가소제(트리아세틴)를 사용하지 않았다.It was carried out in the same manner as in Example 3, but a plasticizer (triacetin) was not used.

비교예 2Comparative Example 2

상기 비교예 1과 동일하게 실시하되, 비교예 1에서 제조된 코팅조성물을 식품지에 1차로 도공량이 3 g/㎡가 되도록 코팅한 후 건조시키고 2차로 도공량이 7g/㎡가 되도록 코팅하여 120 ℃ 건조오븐에 3분 동안 건조하였다.The same procedure as in Comparative Example 1, except that the coating composition prepared in Comparative Example 1 was first coated on food paper so that the coating amount was 3 g/m2, dried, and secondarily coated so that the coating amount was 7g/m2, and dried at 120 ° C. Dry in the oven for 3 minutes.

비교예 3Comparative Example 3

상기 비교예 1과 동일하게 실시하되, 비교예 1에서 제조된 코팅조성물을 식품지에 1차로 도공량이 17 g/㎡이 되도록 코팅한 후 건조시키고 2차로 도공량이 5 g/㎡가 되도록 코팅하여 120 ℃건조오븐에 3분 동안 건조하였다.The same procedure as in Comparative Example 1, except that the coating composition prepared in Comparative Example 1 was first coated on food paper so that the coating amount was 17 g/m2, dried, and secondarily coated so that the coating amount was 5 g/m2, at 120 ° C. It was dried in a drying oven for 3 minutes.

비교예 4Comparative Example 4

아크릴에멀젼 60 중량부, 에틸렌 비닐아세테이트에멀젼 29 중량부, 우레탄에멀젼 9 중량부, 슬립제로 광진 실리콘사의 SO-7920을 1 중량부, 소디움 디옥틸 설포석시네이트계 분산제인 CYTEC사의 OS-75를 1 중량부 첨가하여 반응용기에 넣고 상온에서 30분간 교반하는 방법으로 코팅액을 제조하였다.60 parts by weight of acrylic emulsion, 29 parts by weight of ethylene vinyl acetate emulsion, 9 parts by weight of urethane emulsion, 1 part by weight of SO-7920 from Kwangjin Silicone as a slip agent, and OS-75 from CYTEC, a sodium dioctyl sulfosuccinate-based dispersant, 1 A coating solution was prepared by adding parts by weight, putting it in a reaction vessel, and stirring at room temperature for 30 minutes.

도공량이 10 g/㎡가 되도록 상기 제조된 코팅조성물을 식품지에 1차로 코팅한 후 120 ℃ 건조오븐에 5분 동안 건조하였다.The prepared coating composition was first coated on food paper so that the coating amount was 10 g/m 2 , and then dried in a drying oven at 120° C. for 5 minutes.

비교예 5Comparative Example 5

상기 비교예 4와 동일하게 실시하되, 비교예 4에서 제조된 코팅조성물을 식품지에 1차로 도공량이 3 g/㎡가 되도록 코팅한 후 건조시키고 2차로 도공량이 7 g/㎡가 되도록 코팅하여 120 ℃ 건조오븐에 3분 동안 건조하였다.The same procedure as in Comparative Example 4, except that the coating composition prepared in Comparative Example 4 was first coated on food paper so that the coating amount was 3 g/m2, dried, and secondarily coated so that the coating amount was 7 g/m2, at 120 ° C. It was dried in a drying oven for 3 minutes.

비교예 6Comparative Example 6

상기 비교예 4와 동일하게 실시하되, 비교예 4에서 제조된 코팅조성물을 식품지에 1차로 도공량이 17 g/㎡가 되도록 코팅한 후 건조시키고 2차로 도공량이 5 g/㎡가 되도록 코팅하여 120 ℃건조오븐에 3분 동안 건조하였다.The same procedure as in Comparative Example 4, except that the coating composition prepared in Comparative Example 4 was first coated on food paper so that the coating amount was 17 g/m2, dried, and secondarily coated so that the coating amount was 5 g/m2, at 120 ° C. It was dried in a drying oven for 3 minutes.

비교예 7Comparative Example 7

상기 실시예 1과 동일하게 실시하되, 도공량이 3 g/㎡가 되도록 형성하였다.It was carried out in the same manner as in Example 1, but the coating amount was formed to be 3 g/m 2 .

시험예.test example.

1 내수성 및 내유성: 코팅조성물로 코팅된 식품지 일면에 물 및 식용유를 각각 5g씩 도포하여 상온에서 1시간 동안 방치한 후 식품지에 물 및 식용유가 젖은 정도를 육안으로 관찰하였다.1 Water resistance and oil resistance: 5 g each of water and cooking oil was applied to one side of the food paper coated with the coating composition, left at room temperature for 1 hour, 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 are wet to less than 5% on food paper)

□ : 보통(식품지에 물 및 식용유가 6~10% 젖음)□ : Normal (6~10% wet with water and cooking oil on food paper)

△ : 불량(식품지에 물 및 식용유가 11~20% 젖음)△: Bad (11-20% of water and cooking oil wet on food paper)

× : 아주불량(식품지에 물 및 식용유가 20%초과로 젖음)×: Very poor (food paper wet with water and cooking oil more than 20%)

2 열실링성: 코팅조성물로 코팅된 식품지를 열실링기(삼보테크, SK-310)를 사용하여 실링강도 5로 한 후 코팅층과 식품지가 떨어지는 정도를 육안으로 관찰하였다.2 Heat sealing property: After setting the sealing strength of the food paper coated with the coating composition to 5 using a heat sealing machine (Sambotech, SK-310), the degree of falling off of the coating layer and the food paper was visually observed.

◎ : 우수(코팅층과 식품지가 떨어지지 않음)◎: Excellent (coating layer and food paper do not fall off)

○ : 양호(코팅층과 식품지가 1%이하로 떨어짐)○: Good (coating layer and food paper fall below 1%)

□ : 보통([0093] 코팅층과 식품지가 2~5%로 떨어짐)□: Normal (coating layer and food paper fall to 2-5%)

△ : 불량(코팅층과 식품지가 6~10%로 떨어짐)△: defective (coating layer and food paper fall to 6~10%)

× : 아주불량(코팅층과 식품지가 10%이상으로 떨어짐)×: Very poor (coating layer and food paper fall to more than 10%)

표 1Table 1

Figure pat00001
Figure pat00001

위 표 1에 나타낸 바와 같이, 본 발명에 따른 실시예 1 내지 6의 코팅조성물은 내수성, 내유성 및 열실링성이 우수한 것을 확인하였다.As shown in Table 1 above, it was confirmed that the coating compositions of Examples 1 to 6 according to the present invention were excellent in water resistance, oil resistance and heat sealing properties.

반면, 가소제를 사용하지 않은 비교예 1 및 3은 내수성, 내유성 및 열실링성이 우수하지 못하였다.On the other hand, Comparative Examples 1 and 3 in which a plasticizer was not used did not have excellent water resistance, oil resistance, and heat sealing properties.

또한, 셀룰로오스 유도체 대신 아크릴에멀젼을 사용한 비교예 4 내지 7의 코팅조성물의 경우, 내수성, 내유성 및 열실링성 우수하지 못하다는 것을 확인하였다. 특히, 비교예 5 및 6은 1차 코팅막 위에 2차 코팅이 잘 되지 않아 열실링후 박리현상이 심하였다.In addition, in the case of the coating compositions of Comparative Examples 4 to 7 using an acrylic emulsion instead of a cellulose derivative, it was confirmed that the water resistance, oil resistance and heat sealing properties were not excellent. In particular, in Comparative Examples 5 and 6, the secondary coating did not work well on the primary coating film, so the peeling phenomenon after heat sealing was severe.

또한, 비교예 7은 도공량이 적어 내수성, 내유성 및 열실링성 우수하지 못하다는 것을 확인하였다.In addition, it was confirmed that Comparative Example 7 was not excellent in water resistance, oil resistance and heat sealing property due to a small amount of coating.

Claims (1)

청구항 1
유기용제 100 중량부에 대하여 셀룰로오스 유도체 10 내지 30 중량부, 가소제 1 내지 10 중량부, 슬립제 3 내지 30 중량부 및 분산제 05 내지 50 중량부를 더 포함하는 수용성 코팅조성물.
청구항 2
제1항에 있어서, 유기용제는 메틸벤젠(Methyl benzene), 에틸아세테이트(Ethyl acetate), 메틸아세테이트(Methyl acetate), 프로필아세테이트(Propyl acetate), 벤젠(Benzene), 클로로벤젠(Chloro Benzene), 에탄올(Ethanol) 및 이소프로판올(Isopropanol)로 이루어진 군에서 선택된 1종 이상인 수용성 코팅조성물.
청구항 3
제1항에 있어서, 셀룰로오스 유도체는 메틸셀룰로오스(Methyl cellulose), 에틸셀룰로오스(Ethyl cellulose),하이드록시프로필메틸셀룰로오스(Hydroxypropylmethyl cellulose), 셀룰로오스아세테이트(Cellulose acetate)및 니트로셀룰로오스(Nitro cellulose)로 이루어진 군에서 선택된 1종 이상인 수용성 코팅조성물.
청구항 4
제1항에 있어서, 가소제는 트리아세틴(Triacetine),트리에틸시트레이트(Triethylcitrate), 디사이클로헥실프탈레이트(Dicyclohexyl phthalate), 이에스오(ESO, Epoxidized soybean oil) 및 글리세롤(Glycerol)로 이루어진 군에서 선택된 1종 이상인 수용성 코팅조성물.
청구항 5
제1항에 있어서, 슬립제는 파라핀 왁스 에멀젼(Paraffin wax emulsion), 리코왁스 에멀젼(Lico wax emulsion),폴리에틸렌 왁스 에멀젼(Polyethylene wax emulsion), 실리콘 에멀젼(Silicone emulsion), 스테아르산 모노머(Stearic acid monomer)로 이루어진 군에서 선택된 1종 이상인 수용성 코팅조성물.
청구항 6
제1항에 있어서, 분산제는 친수성 실리카, 아크릴 에멀젼(Acrylic Emulsion), 디에스테르 설포석시네이트(Diester sulfosuccinate) 및 우레탄 에멀젼(Urethane Emulsion)로 이루어진 군에서 선택된 1종 이상인 수용성 코팅조성물.
청구항 7
30 내지 60℃로 유기용제를 가온시키는 단계;가온된 유기용제 100 중량부에 대하여 셀룰로오스 유도체 10 내지 30 중량부를 첨가하고 30 내지 60℃에서 60
내지 200분 동안 교반하는 단계;가소화 반응을 위하여 상기 교반된 혼합물에 가소제를 유기용제 100 중량부에 대하여 1 내지 10 중량부를 첨가하고 30 내지 60℃에서 10 내지 80분 동안 교반하는 단계;상기 가소제가 포함된 혼합물에 슬립제를 유기용제 100 중량부에 대하여 3 내지 30 중량부를 첨가하고 교반하는 단계;
분산제를 유기용제 100 중량부에 대하여 05 내지 50 중량부 첨가하고 교반하는 단계: 및 상기 슬립제가 포함된 혼합물을 30 내지 80℃에서 2 내지 10시간 동안 숙성시키는 단계를 포함하는 수용성 코팅 조성물의 제조방법.
claim 1
A water-soluble coating composition further comprising 10 to 30 parts by weight of a cellulose derivative, 1 to 10 parts by weight of a plasticizer, 3 to 30 parts by weight of a slip agent, and 05 to 50 parts by weight of a dispersant based on 100 parts by weight of the organic solvent.
claim 2
According to claim 1, wherein the organic solvent is methyl benzene (Methyl benzene), ethyl acetate (Ethyl acetate), methyl acetate (Methyl acetate), propyl acetate (Propyl acetate), benzene (Benzene), chlorobenzene (Chloro Benzene), ethanol (Ethanol) and isopropanol (Isopropanol) at least one water-soluble coating composition selected from the group consisting of.
claim 3
According to claim 1, wherein the cellulose derivative is methyl cellulose (Methyl cellulose), ethyl cellulose (Ethyl cellulose), hydroxypropylmethyl cellulose (Hydroxypropylmethyl cellulose), cellulose acetate (Cellulose acetate) and nitro cellulose (Nitro cellulose) from the group consisting of At least one selected water-soluble coating composition.
claim 4
According to claim 1, wherein the plasticizer is triacetine (Triacetine), triethyl citrate (Triethylcitrate), dicyclohexyl phthalate (Dicyclohexyl phthalate), ESO (Epoxidized soybean oil) and glycerol (Glycerol) selected from the group consisting of One or more water-soluble coating compositions.
claim 5
According to claim 1, wherein the slip agent is a paraffin wax emulsion (Paraffin wax emulsion), Lico wax emulsion (Lico wax emulsion), polyethylene wax emulsion (Polyethylene wax emulsion), silicone emulsion (Silicone emulsion), stearic acid monomer (Stearic acid monomer) ) at least one water-soluble coating composition selected from the group consisting of.
claim 6
The water-soluble coating composition of claim 1, wherein the dispersant is at least one selected from the group consisting of hydrophilic silica, acrylic emulsion, diester sulfosuccinate, and urethane emulsion.
claim 7
heating the organic solvent to 30 to 60° C.; adding 10 to 30 parts by weight of a cellulose derivative based on 100 parts by weight of the heated organic solvent and adding 60 parts by weight at 30 to 60° C.
Stirring for 200 minutes; Adding 1 to 10 parts by weight of a plasticizer based on 100 parts by weight of an organic solvent to the stirred mixture for a plasticization reaction and stirring at 30 to 60° C. for 10 to 80 minutes; The plasticizer adding 3 to 30 parts by weight of a slip agent to a mixture containing 100 parts by weight of an organic solvent and stirring;
A method for preparing a water-soluble coating composition comprising adding 05 to 50 parts by weight of a dispersant based on 100 parts by weight of an organic solvent and stirring the mixture: and aging the mixture containing the slip agent at 30 to 80° C. for 2 to 10 hours .
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