KR100933242B1 - Biodegradable MDO Heat Shrink Film for Labels and Manufacturing Method Thereof - Google Patents
Biodegradable MDO Heat Shrink Film for Labels and Manufacturing Method Thereof Download PDFInfo
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- KR100933242B1 KR100933242B1 KR1020070041943A KR20070041943A KR100933242B1 KR 100933242 B1 KR100933242 B1 KR 100933242B1 KR 1020070041943 A KR1020070041943 A KR 1020070041943A KR 20070041943 A KR20070041943 A KR 20070041943A KR 100933242 B1 KR100933242 B1 KR 100933242B1
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- 229920006300 shrink film Polymers 0.000 title claims abstract description 44
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 229920000747 poly(lactic acid) Polymers 0.000 claims abstract description 16
- -1 polybutylene succinate adipate Polymers 0.000 claims abstract description 14
- 229920003232 aliphatic polyester Polymers 0.000 claims abstract description 12
- 229920009537 polybutylene succinate adipate Polymers 0.000 claims abstract description 9
- 239000004630 polybutylene succinate adipate Substances 0.000 claims abstract description 9
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 239000004744 fabric Substances 0.000 claims description 23
- 238000002844 melting Methods 0.000 claims description 18
- 230000008018 melting Effects 0.000 claims description 18
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 12
- 239000010954 inorganic particle Substances 0.000 claims description 8
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 6
- 239000008116 calcium stearate Substances 0.000 claims description 6
- 235000013539 calcium stearate Nutrition 0.000 claims description 6
- LYRFLYHAGKPMFH-UHFFFAOYSA-N octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(N)=O LYRFLYHAGKPMFH-UHFFFAOYSA-N 0.000 claims description 6
- FATBGEAMYMYZAF-KTKRTIGZSA-N oleamide Chemical compound CCCCCCCC\C=C/CCCCCCCC(N)=O FATBGEAMYMYZAF-KTKRTIGZSA-N 0.000 claims description 6
- 239000000377 silicon dioxide Substances 0.000 claims description 6
- 239000000454 talc Substances 0.000 claims description 6
- 229910052623 talc Inorganic materials 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 238000000137 annealing Methods 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims 1
- 239000002253 acid Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 14
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- 238000004806 packaging method and process Methods 0.000 description 5
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- 230000008569 process Effects 0.000 description 5
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- 238000002372 labelling Methods 0.000 description 4
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 3
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- 238000012858 packaging process Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000010998 test method Methods 0.000 description 3
- 239000004793 Polystyrene Substances 0.000 description 2
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- 238000005520 cutting process Methods 0.000 description 2
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- 239000002689 soil Substances 0.000 description 2
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- 238000004804 winding Methods 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229920006257 Heat-shrinkable film Polymers 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
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- 229920000704 biodegradable plastic Polymers 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
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- 238000002485 combustion reaction Methods 0.000 description 1
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- 235000005822 corn Nutrition 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
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- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
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- 230000003287 optical effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920002961 polybutylene succinate Polymers 0.000 description 1
- 239000004631 polybutylene succinate Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
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- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/022—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
- C08K3/36—Silica
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
- C08K5/098—Metal salts of carboxylic acids
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- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
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- C08K5/20—Carboxylic acid amides
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
- C08L67/03—Polyesters derived from dicarboxylic acids and dihydroxy compounds the dicarboxylic acids and dihydroxy compounds having the carboxyl- and the hydroxy groups directly linked to aromatic rings
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones
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- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/04—Polyesters derived from hydroxy carboxylic acids, e.g. lactones
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2467/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2467/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
- C08J2467/03—Polyesters derived from dicarboxylic acids and dihydroxy compounds the dicarboxylic acids and dihydroxy compounds having the hydroxy and the carboxyl groups directly linked to aromatic rings
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Abstract
본 발명은 용기의 수축 라벨용으로 인쇄성, 시일성, 투명성 및 우수한 기계적 특성을 갖으며 자연환경 속에서 분해되는 MDO 열수축 필름에 관한 것이다. The present invention relates to an MDO heat shrink film that has printability, sealability, transparency and excellent mechanical properties for shrink labels of containers and decomposes in a natural environment.
본 발명은 생분해성 원료인 폴리락트산계 중합체, 폴리부틸렌 숙시네이트 아디페이트 및 지방족 폴리에스테르를 90:1:9∼90:9:1의 중량비율로 혼합한 생분해성 MDO 열수축 필름을 제공하는 것을 특징으로 한다. The present invention provides a biodegradable MDO heat shrink film obtained by mixing a biolactic acid-based polylactic acid polymer, polybutylene succinate adipate and an aliphatic polyester in a weight ratio of 90: 1: 9 to 90: 9: 1. It features.
라벨 label
Description
도 1은 필름을 연신 하는데 사용되는 연신 장치를 개략적으로 나타낸 도면1 schematically shows a drawing device used to draw a film;
<도면의 주요 부분에 대한 부호의 설명><Explanation of symbols for the main parts of the drawings>
R1, R2 : 예열 로울러,R1, R2: preheat roller,
R3 : 저속 로울러,R3: low speed roller,
R4 : 고속 로울러,R4: high speed roller,
R5 : 어닐링 로울러,R5: annealing roller,
R6 : 냉각 로울러R6: Cooling Roller
본 발명은 생분해성 MDO 열수축 필름 및 그 제조방법에 관한 것으로, 자연환경 속에서 자연분해되고 압출·연신공정 상의 가공성이 우수하며, 투명성, 인쇄성, 용제에 대한 접착성 및 수축특성이 뛰어난 생분해성 MDO 열수축 필름 및 그 제조방법에 관한 것이다.The present invention relates to a biodegradable MDO heat shrink film and a method for manufacturing the same, which is naturally decomposed in a natural environment, has excellent processability in the extrusion and stretching process, and has excellent transparency, printability, adhesion to solvents, and shrinkage characteristics. An MDO heat-shrink film and a method of manufacturing the same.
MDO 열수축 필름은 유리병, 플라스틱, 건전지, 식용유, 식품, 세제류의 라벨 용으로 다양하게 사용되고 있으며, 라벨용으로 사용되기 위해서는 내용제성, 내열성, 내후성 등의 물성이 요구되고 특히 MD방향(길이방향= 기계방향)으로의 수축균일성이 우수하여야 한다. MDO heat shrink film is widely used for labeling of glass bottles, plastics, batteries, cooking oil, food, detergents, etc.In order to be used for labels, physical properties such as solvent resistance, heat resistance and weather resistance are required. Excellent shrinkage uniformity in the machine direction).
종래의 TDO 열수축 필름으로 사용되고 있는 폴리스티렌, 폴리에틸렌 테레프탈레이트, 폴리염화비닐의 열수축 필름의 경우에는 여러 가지 문제점이 있었다.There have been various problems in the case of heat shrink films of polystyrene, polyethylene terephthalate, and polyvinyl chloride, which are used as conventional TDO heat shrink films.
폴리스티렌 필름은 인쇄성에 문제가 있어 일반 플라스틱용 잉크의 사용이 어렵기 때문에 특수잉크를 사용하여야 하는 불편이 있었고, 특히 자연수축율이 커서 운송 및 보관상의 세심한 주의가 요구되었다.Polystyrene film has a problem in printability, so it is difficult to use a general ink for plastics, so it is inconvenient to use a special ink, and in particular, a large shrinkage rate requires great care in transportation and storage.
폴리에틸렌 테레프탈레이트 필름의 경우는 내열성, 내약품성, 내후성이 우수하나, 수축응력이 크고 수축속도가 빨라서 용기에 라벨링할 때 여러 가지 문제점이 발생하였다. 수축응력이 클 경우 플라스틱의 용기의 체적이 줄어들기 때문에 내용물의 수용이 적어지는 문제점이 있으며, 수축속도가 빠른 경우는 수축 불균일로 인한 상품의 가치를 떨어뜨리는 결과를 초래한다. The polyethylene terephthalate film has excellent heat resistance, chemical resistance, and weather resistance, but various problems have occurred when labeling a container because of high shrinkage stress and high shrinkage speed. If the shrinkage stress is large, the volume of the container of the plastic is reduced, there is a problem that the content of the content is reduced, the rapid shrinkage rate results in a drop in the value of the product due to shrinkage nonuniformity.
특히 폴리염화비닐 필름의 경우에는 염소성분을 함유하고 있기 때문에 소각 폐기시에 염화수소 및 다이옥신과 같은 유해물질을 다량 배출한다는 문제점이 있어서 환경친화적이지 못하다.In particular, the polyvinyl chloride film contains a chlorine component, which causes a large amount of harmful substances such as hydrogen chloride and dioxins to be emitted during incineration, which is not environmentally friendly.
이러한 문제점으로 인하여 상기 필름의 폐플라스틱을 매립지에 매립하고 있으나, 폐플라스틱의 난분해성에 따른 매립지의 안정화 저해, 이용기간 단축, 토질의 황폐화 등을 유발하고, 특히 바다, 강, 호수 등에 투기된 폐플라스틱은 자연생태계의 심각한 위해가 되고 있다. Due to this problem, the waste plastics of the film are buried in landfills, but the waste plastics are impaired in stabilization of landfills due to the degradability of waste plastics, shorten the use period, and degrade the soil. Plastics are a serious hazard to natural ecosystems.
이와 같은 폐플라스틱과 관련된 환경오염의 제반문제를 해결하기 위하여 환경보전의 필요성 및 방법 등에 대한 관심이 증대되고 있다.In order to solve such problems of environmental pollution related to waste plastics, there is increasing interest in the necessity and method of environmental conservation.
따라서 보통 플라스틱처럼 간편하게 사용할 수 있고, 사용 후에는 자연환경 속에서 자연분해되는 환경친화적이고 무해한 생분해성 플라스틱의 연구개발이 활발히 진행되고 있다.Therefore, research and development of environmentally friendly and harmless biodegradable plastics that can be used simply like ordinary plastics and decomposes in a natural environment after use are being actively conducted.
그 일례로 폴리락트산(polylactic acid)이 대표적이다. 폴리락트산은 흙 속에서 가수분해되고 미생물에 의해 무해한 분해물로 전환된다. One example is polylactic acid. Polylactic acid is hydrolyzed in soil and converted into harmless decomposition products by microorganisms.
본 발명의 목적은 플라스틱용기나 유리용기에 부착된 스티커 라벨을 용이하게 분리할 수 있는 생분해성 MDO 열수축 필름을 제공하는 데 있다.
본 발명의 또 다른 목적은 용기의 폐기에 따른 매립시에 생분해성이 뛰어난 MDO 열수축 필름을 제공하는 데 있다.SUMMARY OF THE INVENTION An object of the present invention is to provide a biodegradable MDO heat shrink film that can easily separate a sticker label attached to a plastic container or a glass container.
It is still another object of the present invention to provide a biodegradable MDO heat shrink film at the time of landfill due to the disposal of the container.
삭제delete
본 발명에 의하면, 상기의 목적은 생분해성 원료인 폴리락트산계 중합체 기재에 폴리부틸렌 숙시네이트 아디페이트(polybutylene succinate co-adipate; PBSA)와 지방족 폴리에스테르를 혼합한 것을 특징으로 하는 생분해성 MDO 열수축 필름에 의해 달성된다.According to the present invention, the above object is a biodegradable MDO heat shrink characterized in that a polybutylene succinate co-adipate (PBSA) and an aliphatic polyester are mixed on a polylactic acid polymer substrate which is a biodegradable raw material. Achieved by a film.
본 발명에 의하면 폴리락트산계 중합체와 폴리부틸렌 숙시네이트 아디페이트 및 지방족 폴리에스테르의 바람직한 중량비는 90:1:9∼90:9:1이다. According to the present invention, the preferred weight ratio of the polylactic acid polymer, polybutylene succinate adipate and aliphatic polyester is 90: 1: 9 to 90: 9: 1.
생분해성 MDO 열수축 필름을 플라스틱, 병 등의 용기에 라벨로 사용하는 것 은 TDO 수축라벨 필름보다 효과적으로 사용될 수 있으며, 미개발되어있는 생분해성 MDO 수축 라벨 시장에 새로운 전환기가 될 것으로 생각된다.The use of biodegradable MDO heat shrink films as labels in containers such as plastics, bottles, etc. can be used more effectively than TDO shrink label films and is expected to be a new turning point in the market of undeveloped biodegradable MDO shrink labels.
생분해성 MDO 열수축 필름은 자원절약 및 공해문제에 있어서 한걸음 진보된 대안으로 제시할 수 있고, 사용후 용기 및 재료의 재활용이 효과적이어서 친환경적이라 할 수 있다.Biodegradable MDO heat shrink film can be suggested as an advanced alternative to resource conservation and pollution problems, and it can be said to be environmentally friendly because the recycling of containers and materials after use is effective.
현재 열수축 라벨에 의한 용기의 포장방법으로 TDO 열수축 라벨 포장방법이 널리 알려져 있다. TDO 열수축 라벨 포장방법은 열수축 필름으로 라벨을 만든 다음, 라벨 포장기계에서 수축 라벨을 용기의 상하방향으로 투입하여 부착한 후 열수축 터널을 통과시켜서 부착하는 방법이다.Currently, the TDO heat shrink label packaging method is widely known as a method of packaging a container by a heat shrink label. TDO heat shrink label packaging method is a method of making a label with heat shrink film, and then attaching the shrink label in the up and down direction of the container in a label packaging machine and then attaching it through a heat shrink tunnel.
통상적으로 TDO 열수축 필름 라벨의 포장공정은 인쇄, 재단, 시일링 및 라벨링의 4단계로 구성되어 있다.Typically, the packaging process of TDO heat shrink film labels consists of four steps: printing, cutting, sealing and labeling.
그러나 MDO 열수축 필름 라벨의 포장공정은 기존의 TDO 열수축 필름의 포장공정과는 다르게 인쇄, 재단 및 라벨링의 3단계로 이루어져 있기 때문에 TDO 열수축 포장공정보다 공정이 1단계 단축되므로 간편하다. 또한 라벨을 용기에 부착할 때 원형방법으로 권취하여 라벨을 접착하거나 부착하기 때문에 기존의 TDO 열수축 필름의 포장방법보다 간편하여 시간당 생산량이 많이 증가한다. However, the packaging process of MDO heat shrink film label is simpler than the TDO heat shrink film process because it consists of three steps of printing, cutting and labeling, unlike the conventional TDO heat shrink film packaging process. In addition, since the label is attached or adhered to the container by winding it in a circular method, it is simpler than the packaging method of the conventional TDO heat shrink film, thereby increasing the yield per hour.
또한 MDO 열수축 필름은 옥수수, 감자, 타피오카, 고구마, 밀, 쌀 등의 식물성 원료로 제조되기 때문에, 일반적으로 사용되고 있는 광유성 원료를 주재로 한 TDO 열수축 필름의 라벨보다 연소시에 유해가스가 발생하지 않아 환경친화적이다.In addition, since MDO heat shrink film is made of vegetable raw materials such as corn, potato, tapioca, sweet potato, wheat, and rice, no harmful gas is generated during combustion than the label of TDO heat shrink film mainly made of mineral oil. It is environmentally friendly.
이러한 장점으로 인하여 생분해성 MDO 열수축 필름은 종래의 광유성 원료로 제조된 TDO 열수축 필름으로는 달성할 수 없었던 친환경 분야로의 진출이 가능하게 되었다.These advantages enable the biodegradable MDO heat shrink film to enter the eco-friendly field that could not be achieved by the TDO heat shrink film made of a conventional mineral oil material.
본 발명에 의하면, 생분해성 원료인 폴리락트산계 중합체에, 1종 이상의 알킬글리콜과 1종 이상의 지방족 다관능성 산을 중합하여 제조된 폴리부틸렌 숙시네이트 아디페이트(PBSA)와 지방족 폴리에스테르를 혼합하여 가공성 및 인장강도가 개량된 생분해성 MDO 열수축필름을 제조한다.According to the present invention, a polybutylene succinate adipate (PBSA) prepared by polymerizing at least one alkyl glycol and at least one aliphatic polyfunctional acid is mixed with a polylactic acid polymer which is a biodegradable raw material, A biodegradable MDO heat shrink film with improved processability and tensile strength is prepared.
본 발명에 있어서, 일정량의 조성비로 혼합된 생분해성 MDO 필름원료를 직선형 T다이스의 개량형인 코우트행거(coat hanger) 방식의 T다이스를 통하여 압출한다. T다이스는 압출량의 변동이 없고 균일속도로 수지를 방출하며, 혼련분산이 양호하고 기포의 혼입을 배출할 수 있는 가열 용융 압출기를 통하여 생분해성 수지의 체류를 방지하도록 설계되어 있다. In the present invention, the biodegradable MDO film material mixed in a certain amount of composition ratio is extruded through a coat hanger type T dice, which is an improvement of the linear T dice. T-die is designed to prevent the retention of biodegradable resin through the hot melt extruder, which does not change the extrusion amount and releases the resin at a uniform speed, and has good kneading dispersion and discharge of bubble mixing.
생분해성 필름 원단을 압출하는 성형기는 수지송출 안정성 및 수지체류시간이 균일한 쌍축 압출기(동방향 및 역방향 회전) 보다는 폴리락트산계 중합체, PBSA 및 지방족 폴리에스테르의 혼합물을 균일한 조성물로 만들기 위하여 수지혼련이 양호한 단축 압출기를 사용한다. The molding machine for extruding the biodegradable film fabric is kneaded to make a mixture of polylactic acid polymer, PBSA and aliphatic polyester into a uniform composition, rather than twin screw extruder (coaxial and reverse rotation) with uniform resin delivery stability and resin residence time. This good single screw extruder is used.
T다이스를 통하여 용융압출된 생분해성 수지를 냉각기에서 냉각된 물이 저장되어 있는 냉각조에 저장한 다음, 순환펌프에 의하여 냉각되어 있는 냉각롤로 급랭한 후, 몇 번의 가이드롤을 통과시켜서 균일성 및 투명성이 우수한 필름을 제조한다. The biodegradable resin melt-extruded through the T dice is stored in a cooling tank in which water cooled in a cooler is stored, and then quenched by a cooling roll cooled by a circulation pump, and then passed through several guide rolls for uniformity and transparency. This excellent film is produced.
융점이 150∼160℃인 폴리락트산계 중합체를 압출하여 성형된 생분해성 원단 에 저분자 물질이 함유되어 있는 경우, 이들 물질이 필름 표면으로 확산되어 배어나오고 권취시 온도와 압력에 의하여 필름이 접착되어 일체화되는 현상이 생기게 된다. 이로 인하여 수축필름 제조의 생산성 및 가공성이 떨어지고, 필름의 외관을 크게 손상된다. When low-molecular substances are contained in the biodegradable fabric formed by extruding polylactic acid polymer having a melting point of 150 to 160 ° C., these substances diffuse to the surface of the film to be oozed out, and the film is adhered and integrated by the temperature and pressure at the time of winding. The phenomenon occurs. Because of this, the productivity and processability of the shrink film production is degraded, and the appearance of the film is largely damaged.
따라서 본 발명에서는 우수한 생분해성 MDO 열수축 필름을 제조하기 위해서 융점이 50∼100℃인 올레인산 아미드 300∼5000ppm, 스테아린산 칼슘 350∼6000ppm, 스테아릴 아미드 300∼5000ppm를 첨가한다. 또 블록킹을 방지하고, 결정화도와 결정화 속도를 조정하기 위하여 무기입자 SiO2(실리카) 50∼1500ppm 및 활석 200∼1500ppm을 첨가한다. 상기 무기입자는 압출시 마스터배치 방식으로 첨가될 수 있으며, 무기입자의 평균입경은 1∼5㎛, 바람직하게는 2∼3㎛이다. Therefore, in the present invention, in order to produce an excellent biodegradable MDO heat shrink film, 300 to 5000 ppm of oleic acid amide having a melting point of 50 to 100 ° C, 350 to 6000 ppm of calcium stearate and 300 to 5000 ppm of stearyl amide are added. In addition, in order to prevent blocking and to adjust the crystallinity and crystallization rate, 50 to 1500 ppm of inorganic particles SiO 2 (silica) and 200 to 1500 ppm of talc are added. The inorganic particles may be added in a master batch method during extrusion, the average particle diameter of the inorganic particles is 1 to 5㎛, preferably 2 to 3㎛.
폴리락트산계 중합체에 융점이 95∼125℃인 PBSA와 융점이 60∼125℃인 지방족 폴리에스테르를 혼합한 반결정성 폴리머를 위와 같은 방법에 의하여 용융압출한 후 바로 급냉하여 연신할 수 있는 비결정성 생분해성 원단으로 만든다. 이렇게 만들어진 생분해성 원단은 MDO 연신장치를 통과시킨다. MDO 연신장치를 통과하는 원단은 도 1에 나타난 바와 같이, 몇 개의 로울러를 조합하여 만든 로울러와 로울러 사이를 통과하게 된다. Amorphous biodegradation that can be quenched and stretched immediately after melt-extruding a semi-crystalline polymer in which a polylactic acid polymer is mixed with PBSA having a melting point of 95 to 125 ° C and an aliphatic polyester having a melting point of 60 to 125 ° C. Made of castle fabric. The biodegradable fabric thus made is passed through an MDO drawing machine. The fabric passing through the MDO stretching apparatus is passed between the roller and the roller made by combining several rollers, as shown in FIG.
MDO 연신장치로 연신하는 방법은 생분해성 원단이 제1 로울러(R1, 예열로울러)을 통과하여 제2 로울러(R2, 예열로울러)를 지난다. 제1 로울러(R1) 및 제2 로울러(R2)는 길이방향(MD)의 연신을 원할하게 하기 위하여 70℃∼80℃ 예열장치를 설치한다. 충분히 예열된 생분해성 원단은 길이 방향으로 연신하기 위한 장치인 제 3 로울러(R3, 저속로울러)와 제4 로울러(R4, 고속 로울러)를 통과한다. R3와 R4의 온도는 배합물의 융점 이하로 설정된다. In the stretching method using the MDO stretching apparatus, the biodegradable fabric passes through the first roller (R1, preheat roller) and passes through the second roller (R2, preheat roller). The 1st roller R1 and the 2nd roller R2 are equipped with 70 degreeC-80 degreeC preheating apparatus in order to make extending | stretching of longitudinal direction MD smooth. The sufficiently preheated biodegradable fabric passes through a third roller (R3, low speed roller) and a fourth roller (R4, high speed roller), which are devices for stretching in the longitudinal direction. The temperature of R3 and R4 is set below the melting point of the blend.
연신하기 위한 장치인 R3의 속도를 20∼80m/min로 조정하고, R4의 속도를 40∼160m/min로 작동하도록 조정한다. 이렇게 되면 로울러(R3)와 (R4)의 속도비는 2:1이 된다. 연신로울러 R3와 R4를 통과한 생분해성 원단은 초기 원단 면적보다 길어지고 두께도 1/2로 줄어든 얇은 생분해성 MDO 필름이 생산되며, MD방향(길이방향) 연신비는 2배가 된다. 본 발명에 의한 바람직한 연신배율은 2∼5이다. The speed of R3, the device for stretching, is adjusted to 20 to 80 m / min, and the speed of R4 is adjusted to operate at 40 to 160 m / min. In this case, the speed ratio of the rollers (R3) and (R4) is 2: 1. The biodegradable fabric passing through the drawing rollers R3 and R4 produces a thin biodegradable MDO film that is longer than the initial fabric area and is reduced in thickness by 1/2, and the draw ratio in the MD direction (length direction) is doubled. The draw ratio which is preferable by this invention is 2-5.
필름의 두께 및 수축율 특성에 따라 R1, R2의 온도와 R3, R4의 온도 및 속도를 조절하여 연신배율을 정할 수 있다. 본 발명에 의한 생분해성 MDO 필름의 두께는 5∼70㎛이다. The draw ratio may be determined by adjusting the temperature of R1 and R2 and the temperature and speed of R3 and R4 according to the thickness and shrinkage characteristics of the film. The thickness of the biodegradable MDO film according to the present invention is 5 to 70 µm.
연신배율을 조정하고, 생분해성 원단을 융점 이하의 적당한 온도로 설정함으로써 연신되는 생분해성 원단의 분자구조와 수지결정성에 배향을 주어서 생분해성 필름의 단점인 기계적 강도, 광학적 특성, 가스투과도 및 수축율 향상을 향상시킨다.By adjusting the draw ratio and setting the biodegradable fabric to a suitable temperature below the melting point, the orientation of the molecular structure and resin crystallinity of the stretched biodegradable fabric is improved, thereby improving the mechanical strength, optical properties, gas permeability and shrinkage, which are disadvantages of the biodegradable film. To improve.
생분해성 원료인 폴리락트산계 중합체, PBSA 및 지방족 폴리에스테르로 생산된 원단은 융점에 따라서 가공온도가 다르지만 예열처리 공정에서 온도분포가 일정하도록 R1, R2의 온도를 일정하게 조절한다. R1, R2의 온도는 70℃∼80℃이다. 연신과정에서 R1, R2의 온도가 일정하지 않으면 온도의 불균일로 인하여 연신된 생분해성 열수축 필름의 두께 및 수축율에 악영향을 주며, 연신로울러 R3와 R4의 속도비가 일정하지 않을 경우에는 연신방향으로 분자배향이 일정하지 않아 수축필름의 길이방향의 인장강도 및 수축율에 부분적으로 차이가 발생하게 된다. 바람직한 연신로울러 R3와 R4의 속도비는 2:1∼2:10이다. Fabrics made of biodegradable polylactic acid-based polymers, PBSA and aliphatic polyester have different processing temperatures depending on melting point, but the temperature of R1 and R2 is controlled to be constant in the preheating process. The temperature of R1 and R2 is 70 degreeC-80 degreeC. If the temperature of R1 and R2 is not constant in the stretching process, it will adversely affect the thickness and shrinkage rate of the stretched biodegradable heat-shrinkable film due to the temperature nonuniformity, and if the speed ratio of R3 and R4 is not constant, the molecular orientation will be in the stretching direction. This non-uniformity causes partial differences in tensile strength and shrinkage in the longitudinal direction of the shrink film. Preferred drawing rollers have a speed ratio of R3 to R4 of 2: 1 to 2:10.
연신공정 상의 R3와 R4를 통과한 원단이 불안정한 상태인 경우 이를 안정화시키기 위하여, 약 40∼50℃ 정도의 열로 가열되어 있는 어닐링(annealing) 로울러(R5)를 통과시켜서 연신원단을 안정화시킨다. 어닐링 로울러(R5)의 속도는 R4의 속도와 같거나 약간 빠르다. In order to stabilize the fabric having passed through R3 and R4 in the stretching process to stabilize it, the stretching fabric is stabilized by passing through an annealing roller (R5) heated by heat of about 40 to 50 ° C. The speed of the annealing roller R5 is equal to or slightly faster than the speed of R4.
안정화된 원단이 여러 개의 로울러를 통과하는 도중에 가열되어 연신된 원단이 변형될 수 있기 때문에 이러한 변형을 방지하기 위하여 약 30∼40℃ 정도의 냉각로울러(R6)를 통과시킨다. 이렇게 하여 제조된 생분해성 MDO 열수축 필름은 58℃ 90% RH 습도하에서 59일 경과시 93.9%가 생분해된다. Since the stabilized fabric is heated while passing through several rollers, the stretched fabric may be deformed, and then passed through a cooling roller R6 of about 30 to 40 ° C. to prevent such deformation. The biodegradable MDO heat-shrink film prepared in this way biodegraded 93.9% after 59 days under 58 ° C 90% RH humidity.
(실시예)(Example)
이하에 본 발명의 구체적인 실시예를 들어 보다 상세하게 설명하지만 이에 한정되는 것은 아니다.Specific examples of the present invention are described below in more detail, but the present invention is not limited thereto.
(실시예 1)(Example 1)
중량 평균분자량이 20만 이상인 폴리락트산계 중합체 90중량%에 폴리부틸렌 숙시네이트 아디페이트 4중량%와 지방족 폴리에스테르 6중량%를 혼합한 후 평균입경이 1∼2㎛인 무기입자 실리카 150ppm과 활석 350ppm을 첨가하였다.150 ppm of inorganic particle silica with an average particle diameter of 1 to 2 µm and talc after mixing 4 weight% of polybutylene succinate adipate and 6 weight% of aliphatic polyester to 90 weight% of polylactic acid polymer having a weight average molecular weight of 200,000 or more 350 ppm was added.
또한 생산성 및 가공성을 향상시키기 위하여, 용융점이 50∼100℃인 올레인산 아미드 300ppm, 스테아린산 칼슘 500ppm, 스테아릴 아미드 300ppm을 첨가하여 혼합하고 T다이 압출기를 이용하여 생분해성 원단을 제조하였다. In addition, in order to improve productivity and processability, 300 ppm of oleic acid amide having a melting point of 50 to 100 ° C., 500 ppm of calcium stearate, and 300 ppm of stearyl amide were added and mixed to prepare a biodegradable fabric using a T-die extruder.
제조된 생분해성 원단을 MDO 연신기계 장치를 사용하여 MD방향(길이방향)으로 2.5배 연신하여 25㎛의 생분해성 MDO 열수축 필름을 제조하였다. 제조된 수축필름의 수축 특성은 다음과 같다. The prepared biodegradable fabric was stretched 2.5 times in the MD direction (length direction) using an MDO drawing machine device to prepare a biodegradable MDO heat shrink film having a thickness of 25 μm. Shrinkage characteristics of the prepared shrink film is as follows.
* 열수축율 실험방법: 필름샘플을 가로방향, 세로방향으로 각각 120mm로 절단하여, 그사이에 가로, 세로 100mm의 표선을 넣고 각 온도의 온수조에 30초 동안 침적시킨후, 그 표선 간의 치수를 재고, 다음과 같은 식에 따라서 수축율을 계산하였다.* Thermal shrinkage test method: Cut the film sample into 120mm in the horizontal and vertical directions, insert the horizontal and vertical 100mm marks in between, immerse them in a hot water bath at each temperature for 30 seconds, and measure the dimensions between the marks. Shrinkage was calculated according to the following equation.
열수축율 (%) = (수축전치수 - 수축후치수) / (수축전 치수) × 100 Heat Shrinkage (%) = (Before Shrinkage-After Shrinkage) / (Before Shrinkage) × 100
(실시예 2)(Example 2)
중량 평균분자량이 20만 이상인 폴리락트산 90중량%에 폴리부틸렌 숙시네이트 아디페이트 3중량%와 지방족 폴리에스테르 7중량%를 혼합한 후 평균입경이 1∼2㎛인 무기입자 실리카 450ppm과 활석 550ppm을 첨가하였다.After mixing 3% by weight of polybutylene succinate adipate and 7% by weight of aliphatic polyester to 90% by weight of polylactic acid having a weight average molecular weight of 200,000 or more, 450 ppm of inorganic particle silica having an average particle diameter of 1 to 2 µm and 550 ppm of talc were obtained. Added.
또한 좋은 생분해성 열수축 필름을 제조생산 하기 위해서, 용융점이 50∼100 ℃인 올레인산 아미드 300ppm, 스테아린산 칼슘 500ppm, 스테아릴 아미드 300ppm을 첨가하여 혼합하고 T다이 압출기를 이용하여 생분해성 원단을 제조하였다. In addition, in order to manufacture and produce a good biodegradable heat shrink film, 300 ppm of oleic acid amide having a melting point of 50 to 100 ° C., 500 ppm of calcium stearate, and 300 ppm of stearyl amide were added and mixed, and a biodegradable fabric was manufactured using a T-die extruder.
제조된 생분해성 원단을 MDO 연신기계 장치를 이용하여 MD방향(길이방향)으로 3배 연신하여 40㎛의 생분해성 MDO 열수축 필름을 제조하였다. 제조된 수축필름의 수축 특성은 다음과 같다. The prepared biodegradable fabric was stretched three times in the MD direction (length direction) using an MDO drawing machine device to prepare a biodegradable MDO heat shrink film having a thickness of 40 μm. Shrinkage characteristics of the prepared shrink film is as follows.
* 열수축율 실험방법: 필름샘플을 가로방향, 세로방향으로 각각 120mm로 절단하여, 그사이에 가로, 세로 100mm의 표선을 넣고 각 온도의 온수조에 30초 동안 침적시킨 후, 그 표선 간의 치수를 재고, 다음과 같은 식에 따라서 수축율을 계산하였다.* Thermal shrinkage test method: cut the film sample into 120mm in the horizontal and vertical directions, insert the horizontal and vertical 100mm marks in between, immerse them in a hot water bath at each temperature for 30 seconds, and measure the dimensions between the marks. Shrinkage was calculated according to the following equation.
열수축율 (%) = (수축전치수 - 수축후치수) / (수축전 치수) × 100 Heat Shrinkage (%) = (Before Shrinkage-After Shrinkage) / (Before Shrinkage) × 100
(실시예 3)(Example 3)
중량 평균분자량이 20만 이상인 폴리락트산 90중량%에 폴리부틸렌 숙시네이트 아디페이트 2중량%와 지방족 폴리에스테르 8중량%를 혼합한 후 평균입경이 1∼2㎛인 무기입자 실리카 300ppm과 활석 700ppm을 첨가한다.After mixing 2% by weight of polybutylene succinate adipate and 8% by weight of aliphatic polyester to 90% by weight of polylactic acid having a weight average molecular weight of 200,000 or more, 300 ppm of inorganic particle silica having an average particle diameter of 1 to 2 µm and 700 ppm of talc are obtained. Add.
또한 좋은 생분해성 열수축 필름을 제조생산 하기 위해서, 용융점이 50∼100 ℃의 범위를 갖는 올레인산 아미드 300ppm, 스테아린산 칼슘 500ppm, 스테아릴 아미드 300ppm을 첨가하여 혼합하고 T다이 압출기를 이용하여 생분해성 원단을 제조하였다. In addition, in order to manufacture and produce a good biodegradable heat-shrink film, 300 ppm of oleic acid amide having a melting point in the range of 50 to 100 ° C., 500 ppm of calcium stearate, and 300 ppm of stearyl amide are added and mixed, and a biodegradable fabric is manufactured using a T-die extruder. It was.
제조된 생분해성 원단을 MDO 연신기계 장치를 이용하여 MD방향(길이방향)으로 2.5배 연신하여 30㎛의 생분해성 MDO 열수축 필름을 제조하였다. 제조된 수축필름의 수축 특성은 다음과 같다. The prepared biodegradable fabric was stretched 2.5 times in the MD direction (length direction) using an MDO drawing machine device to prepare a biodegradable MDO heat shrink film having a thickness of 30 μm. Shrinkage characteristics of the prepared shrink film is as follows.
* 열수축율 실험방법: 필름샘플을 가로방향, 세로방향으로 각각 120mm로 절단하여, 그사이에 가로, 세로 100mm의 표선을 넣고 각 온도의 온수조에 30초 동안 침적시킨 후, 그 표선 간의 치수를 재고, 다음과 같은 식에 따라서 수축율을 계산하였다.* Thermal shrinkage test method: cut the film sample into 120mm in the horizontal and vertical directions, insert the horizontal and vertical 100mm marks in between, immerse them in a hot water bath at each temperature for 30 seconds, and measure the dimensions between the marks. Shrinkage was calculated according to the following equation.
열수축율 (%) = (수축전치수 - 수축후치수) / (수축전 치수) × 100 Heat Shrinkage (%) = (Before Shrinkage-After Shrinkage) / (Before Shrinkage) × 100
상기의 실시예에서 본 바와 같이, 본 발명에 의한 수축 필름은 온도 80℃∼100℃에서 우수한 수축 특성을 갖는다. As seen in the above examples, the shrink film according to the present invention has excellent shrinkage characteristics at a temperature of 80 ° C to 100 ° C.
본 발명에 의한 수축 필름은 온도 80℃∼100℃에서 우수한 수축 특성을 갖기 때문에 플라스틱용기나 유리용기에서 부착된 스티커 라벨을 용이하게 분리할 수 있으며, 따라서 플라스틱용기나 유리용기를 재활용하는데 시간이 절약되며 생산성이 향상된다. Since the shrink film according to the present invention has excellent shrinkage characteristics at a temperature of 80 ° C. to 100 ° C., the sticker label attached to the plastic container or the glass container can be easily separated, thus saving time in recycling the plastic container or the glass container. And productivity is improved.
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