KR100314827B1 - Oxygen barrier resin composition and product containing the same - Google Patents
Oxygen barrier resin composition and product containing the same Download PDFInfo
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- KR100314827B1 KR100314827B1 KR1019990032122A KR19990032122A KR100314827B1 KR 100314827 B1 KR100314827 B1 KR 100314827B1 KR 1019990032122 A KR1019990032122 A KR 1019990032122A KR 19990032122 A KR19990032122 A KR 19990032122A KR 100314827 B1 KR100314827 B1 KR 100314827B1
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- ethylene
- copolymer
- resin composition
- meth
- polyamide
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- 230000004888 barrier function Effects 0.000 title claims abstract description 33
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 239000001301 oxygen Substances 0.000 title claims abstract description 26
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 26
- 239000011342 resin composition Substances 0.000 title claims abstract description 17
- 229920000219 Ethylene vinyl alcohol Polymers 0.000 claims abstract description 31
- 239000000203 mixture Substances 0.000 claims abstract description 31
- 239000004952 Polyamide Substances 0.000 claims abstract description 20
- 229920002647 polyamide Polymers 0.000 claims abstract description 20
- 229920001038 ethylene copolymer Polymers 0.000 claims abstract description 17
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 claims abstract description 16
- 229920005604 random copolymer Polymers 0.000 claims abstract description 12
- 239000000376 reactant Substances 0.000 claims abstract description 9
- 229920001577 copolymer Polymers 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 229920000092 linear low density polyethylene Polymers 0.000 claims description 10
- 239000004707 linear low-density polyethylene Substances 0.000 claims description 10
- 229920005989 resin Polymers 0.000 claims description 10
- 239000011347 resin Substances 0.000 claims description 10
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 9
- 239000005977 Ethylene Substances 0.000 claims description 9
- 125000000217 alkyl group Chemical group 0.000 claims description 9
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 6
- 229920000098 polyolefin Polymers 0.000 claims description 6
- 229920002292 Nylon 6 Polymers 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 5
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 5
- 239000004711 α-olefin Substances 0.000 claims description 5
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 229920001903 high density polyethylene Polymers 0.000 claims description 3
- 239000004700 high-density polyethylene Substances 0.000 claims description 3
- 229920001684 low density polyethylene Polymers 0.000 claims description 3
- 239000004702 low-density polyethylene Substances 0.000 claims description 3
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 claims description 2
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 claims description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 2
- 229920000299 Nylon 12 Polymers 0.000 claims description 2
- 229920002302 Nylon 6,6 Polymers 0.000 claims description 2
- 229920000572 Nylon 6/12 Polymers 0.000 claims description 2
- 150000001252 acrylic acid derivatives Chemical class 0.000 claims description 2
- 150000001408 amides Chemical class 0.000 claims 1
- 239000004715 ethylene vinyl alcohol Substances 0.000 description 27
- UFRKOOWSQGXVKV-UHFFFAOYSA-N ethene;ethenol Chemical compound C=C.OC=C UFRKOOWSQGXVKV-UHFFFAOYSA-N 0.000 description 26
- 239000010410 layer Substances 0.000 description 24
- 230000000052 comparative effect Effects 0.000 description 17
- -1 polyethylene Polymers 0.000 description 14
- 239000004698 Polyethylene Substances 0.000 description 12
- 229920000573 polyethylene Polymers 0.000 description 12
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical group O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 9
- 238000002156 mixing Methods 0.000 description 7
- 239000007789 gas Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000008188 pellet Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 4
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 230000035699 permeability Effects 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 3
- 239000012790 adhesive layer Substances 0.000 description 3
- 239000004840 adhesive resin Substances 0.000 description 3
- 229920006223 adhesive resin Polymers 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 229920005672 polyolefin resin Polymers 0.000 description 3
- 229920001155 polypropylene Polymers 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000002834 transmittance Methods 0.000 description 3
- 229920010126 Linear Low Density Polyethylene (LLDPE) Polymers 0.000 description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- 125000003277 amino group Chemical group 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 2
- 239000011976 maleic acid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 238000007127 saponification reaction Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229920005992 thermoplastic resin Polymers 0.000 description 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 2
- 229940117958 vinyl acetate Drugs 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000006057 Non-nutritive feed additive Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000008064 anhydrides Chemical group 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- JRBPAEWTRLWTQC-UHFFFAOYSA-N dodecylamine Chemical compound CCCCCCCCCCCCN JRBPAEWTRLWTQC-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- RZXDTJIXPSCHCI-UHFFFAOYSA-N hexa-1,5-diene-2,5-diol Chemical compound OC(=C)CCC(O)=C RZXDTJIXPSCHCI-UHFFFAOYSA-N 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000004611 light stabiliser Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229920006280 packaging film Polymers 0.000 description 1
- 239000012785 packaging film Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 150000003141 primary amines Chemical group 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000002076 thermal analysis method Methods 0.000 description 1
- LMYRWZFENFIFIT-UHFFFAOYSA-N toluene-4-sulfonamide Chemical class CC1=CC=C(S(N)(=O)=O)C=C1 LMYRWZFENFIFIT-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L29/00—Compositions of 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 an alcohol, ether, aldehydo, ketonic, acetal or ketal radical; Compositions of hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Compositions of derivatives of such polymers
- C08L29/02—Homopolymers or copolymers of unsaturated alcohols
- C08L29/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
- C08L23/0853—Vinylacetate
- C08L23/0861—Saponified vinylacetate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/14—Gas barrier composition
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2203/00—Applications
- C08L2203/16—Applications used for films
- C08L2203/162—Applications used for films sealable films
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Laminated Bodies (AREA)
Abstract
본 발명은 산소차단성 수지 조성물 및 이를 함유하는 제품에 관한 것으로, 좀 더 상세하게는 a) 에틸렌-비닐알코올 공중합체 20∼80중량, b) 에틸렌 공중합체 5∼79중량및 c) 에틸렌-무수말레익산-알킬(메타)아크릴레이트의 랜덤 공중합체와 분자량이 1,000∼5,000정도의 폴리아미드 올리고머의 반응물 1∼30중량로 이루어진 산소차단성 수지 조성물에 관한 것이다. 본 발명에 따른 조성물은 용융성형성 및 상용성(compatibility)이 동시에 우수하므로 상기 조성물을 차단층으로 사용한 제품은 외관 (투명성 등)과 기계적 강도 및 산소차단성이 우수하다.The present invention relates to an oxygen-blocking resin composition and a product containing the same, and more particularly, a) 20 to 80 weight of ethylene-vinyl alcohol copolymer, b) 5 to 79 weight of ethylene copolymer and c) ethylene-anhydride An oxygen-blocking resin composition comprising a random copolymer of maleic acid-alkyl (meth) acrylate and a reactant of 1 to 30% by weight of a polyamide oligomer having a molecular weight of about 1,000 to 5,000. Since the composition according to the present invention has excellent meltability and compatibility at the same time, the product using the composition as a barrier layer has excellent appearance (transparency, etc.), mechanical strength and oxygen barrier property.
Description
본 발명은 산소차단성 수지 조성물 및 이를 함유하는 제품에 관한 것으로, 좀 더 상세하게는 에틸렌-비닐알코올 공중합체 (이하 'EVOH'라 함)와 에틸렌 공중합체의 혼합물을 이용하여, 기체차단성, 기계적물성 및 외관이 우수한 필름, 시트, 용기를 제조할 수 있는 수지 조성물 및 상기 조성물로 이루어진 하나 이상의 층을 포함하는 제품에 관한 것이다.The present invention relates to an oxygen barrier resin composition and a product containing the same, and more particularly, using a mixture of an ethylene-vinyl alcohol copolymer (hereinafter referred to as 'EVOH') and an ethylene copolymer, The present invention relates to a resin composition capable of producing a film, a sheet, a container having excellent mechanical properties and appearance, and an article including at least one layer composed of the composition.
폴리에틸렌, 폴리프로필렌과 같은 폴리올레핀계 수지는 우수한 성형성, 기계적 물성 및 습기에 대한 차단성능 때문에 여러 가지 용도로 널리 사용되고 있으나, 기체 투과도가 높으므로 산소를 비롯한 기체의 차단성능이 요구되는 식품 포장용과 같은 용도에는 그 사용이 제한되고 있다. 이러한 이유로 폴리올레핀계 수지는 산소차단성이 우수한 고분자인 EVOH와 함께 공압출, 라미네이션 (lamination) 또는 코팅 (coating)에 의하여 다층 구조를 갖는 식품 포장용 필름, 시트 또는 용기로 제조되고 있다.Polyolefin resins such as polyethylene and polypropylene are widely used for various purposes because of their excellent moldability, mechanical properties, and moisture barrier properties.However, due to their high gas permeability, such as those for food packaging requiring oxygen and gas barrier properties. The use is limited to the use. For this reason, polyolefin resins are manufactured as food packaging films, sheets or containers having a multilayer structure by coextrusion, lamination or coating with EVOH, which is a polymer having excellent oxygen barrier property.
한편, EVOH는 기체차단성, 투명성의 면에서 우수한 수지로서 다층 성형품 제조시 기체차단층의 수지로서 널리 사용되고 있으나, 가격이 폴리올레핀에 비하여 월등히 비싸므로 그 사용이 제한되고 있다. 이러한 면에서 EVOH 층의 두께를 최대한 얇게 함으로써 다층 성형품의 가격을 낮출 수 있으나, 일정한 두께 이하로 EVOH 층을 얇게 하는데는 성형품의 품질균일도를 유지하기에 큰 제약이 따른다.On the other hand, EVOH is a resin excellent in gas barrier properties and transparency, and is widely used as a resin for gas barrier layers when manufacturing multilayer molded articles, but its use is limited because the price is much higher than that of polyolefin. In this regard, the thickness of the multilayer molded article can be lowered by making the thickness of the EVOH layer as thin as possible. However, the thinning of the EVOH layer below a certain thickness has a great restriction in maintaining the uniformity of the molded article.
이러한 이유로 기체차단층의 가격을 낮추는 방법으로서 EVOH를 가격이 낮은 폴리에틸렌과 혼합시키는 방법이 공지되어 있다. 그러나, 이러한 목적으로 조성물을 제조할 때, EVOH와 폴리에틸렌간의 상용성 (compatibility)이 부족하여 두 혼합물의 제조가 어렵고, 이들 혼합물을 차단층으로 사용한 필름이나 시트의 외관이 불균일하며, 기계적 강도도 낮은 문제점이 있다. 따라서, 상기 혼합물을 제조할 때는 EVOH와 폴리에틸렌의 상용성을 높이기 위해 제 3의 성분으로서 상용화제 성분을 함께 혼합시키는 것이 일반적이며, 성형품의 기계적 강도와 외관이 우수한 조성물을 만들기 위한 상용화제의 선정이 주요한 기술적인 과제가 되어왔다.For this reason, a method of mixing EVOH with low-cost polyethylene is known as a method of lowering the price of the gas barrier layer. However, when preparing the composition for this purpose, it is difficult to prepare the two mixtures due to the lack of compatibility between EVOH and polyethylene, uneven appearance of the film or sheet using these mixtures as a barrier layer, and low mechanical strength. There is a problem. Therefore, when preparing the mixture, it is common to mix the compatibilizer components together as a third component in order to increase the compatibility of the EVOH and polyethylene, and the selection of the compatibilizer for making a composition having excellent mechanical strength and appearance of the molded article is difficult. It has been a major technical challenge.
예를 들어, 유럽특허 제 15,556호 (1980)와 제 210,725호 (1987), 미국특허 제 4,971,864호 (1990) 및 미국특허 제 5,356,990호 (1994)에는 무수말레익산과 같은 극성기를 갖는 화합물이 폴리에틸렌에 그라프트 (graft) 중합된 상용화제를 사용함으로써 산소차단성과 기계적 물성을 향상시킨 필름을 제조할 수 있음이 개시되어 있다. 그러나, 상기의 방법들에 의한 차단성 수지 조성물은 여전히 성형품의 투명성 및 두께편차와 같은 외관이 불량하며, 상용성을 보다 높이기 위해 상용화제의 함량을 증가시킬 경우 용융성형성이 저하되고 산소차단성도 나빠지는 문제점이 있어 상업화하기에는 많은 어려움이 있었다.For example, European Patent Nos. 15,556 (1980) and 210,725 (1987), US Pat. No. 4,971,864 (1990) and US Pat. No. 5,356,990 (1994) include compounds having polar groups such as maleic anhydride in polyethylene. It is disclosed that a film having improved oxygen barrier properties and mechanical properties can be prepared by using a graft polymerized compatibilizer. However, the barrier resin composition according to the above methods still has poor appearance such as transparency and thickness deviation of the molded article, and when the content of the compatibilizer is increased to increase the compatibility, the meltability is lowered and the oxygen barrier property is also increased. There are many problems that make it difficult to commercialize.
따라서, 본 발명의 목적은 EVOH와 에틸렌 공중합체를 혼합함에 있어서, 두 수지간의 상용성이 우수할 뿐만 아니라, 용융성형성도 우수하여 성형품의 외관과 기계적 강도가 우수한 산소차단성 수지 조성물을 제공하는데 있다.Accordingly, an object of the present invention is to provide an oxygen-blocking resin composition having excellent compatibility between the two resins in mixing EVOH and an ethylene copolymer, as well as excellent melt formability and excellent appearance and mechanical strength of the molded article. .
본 발명의 또다른 목적은 상기 수지 조성물을 적어도 한 층 이상 포함하는 제품을 제공하는데 있다.Another object of the present invention to provide a product comprising at least one layer of the resin composition.
상기 목적을 달성하기 위한 본 발명의 수지 조성물은 EVOH 20∼80중량, 에틸렌 공중합체 5∼79중량및 에틸렌-무수말레익산-알킬(메타)아크릴레이트의 랜덤 공중합체와 분자량이 1,000∼5,000정도의 폴리아미드 올리고머 (polyamide oligomer)의 반응물 1∼30중량로 이루어진다.The resin composition of the present invention for achieving the above object is a random copolymer of 20 to 80 weight of EVOH, 5 to 79 weight of ethylene copolymer and ethylene-maleic anhydride-alkyl (meth) acrylate and molecular weight of about 1,000 to 5,000 It consists of 1-30 weights of reactants of polyamide oligomer.
상기 다른 목적을 달성하기 위한 본 발명의 제품은 상기 조성물을 적어도 한 층 이상으로 포함하는 산소차단성 필름 또는 시트이다.The product of the present invention for achieving the above another object is an oxygen barrier film or sheet comprising at least one layer of the composition.
이하 본 발명을 좀 더 구체적으로 살펴보면 다음과 같다.Looking at the present invention in more detail as follows.
전술한 바와 같이, 본 발명은 a) EVOH 20∼80중량, b) 에틸렌 공중합체 5∼79중량, 및 c) 에틸렌-무수말레익산-알킬(메타)아크릴레이트의 랜덤 공중합체와 분자량이 1,000∼5,000 정도의 폴리아미드 올리고머의 반응물 1∼30중량로 이루어진다.As described above, the present invention comprises a) a random copolymer of 20 to 80 weights of EVOH, b) 5 to 79 weights of ethylene copolymer, and c) ethylene-maleic anhydride-alkyl (meth) acrylate and a molecular weight of 1,000 to It consists of 1-30 weight of reactants of about 5,000 polyamide oligomer.
본 발명에 있어서, 상기 EVOH는 에틸렌과 비닐아세테이트의 공중합에 의하여 생성된 에틸렌-비닐아세테이트를 검화시킨 에틸렌-비닐알코올의 공중합체가 단독또는 혼합되어 사용된다. 이때, 상기 EVOH의 검화도가 90미만일 때는 산소차단성이 충분하지 않으며, 검화도가 높을수록 산소차단성이 우수하다. 또한, EVOH의 에틸렌 함유율이 10몰미만일 때는 가공성이 나빠 용융성형이 어려우며 50몰를 초과하면 산소차단성이 충분하지 않다.In the present invention, the EVOH is used alone or mixed with a copolymer of ethylene-vinyl alcohol obtained by saponifying ethylene-vinylacetate produced by copolymerization of ethylene and vinyl acetate. At this time, when the degree of saponification of the EVOH is less than 90, oxygen barrier property is not sufficient, and the higher the degree of saponification, the better the oxygen barrier property. In addition, when the ethylene content of EVOH is less than 10 moles, the workability is poor and melt molding is difficult, and when it exceeds 50 moles, the oxygen barrier property is not sufficient.
상기 에틸렌 공중합체로는 선형저밀도 폴리에틸렌, 바람직하게는 에틸렌과 α-올레핀과 공중합체 (LLDPE), 저밀도 폴리에틸렌 (LDPE), 고밀도 폴리에틸렌 (HDPE), 에틸렌-비닐아세테이트 공중합체 및 에틸렌-불포화산 유도체의 공중합체로 이루어진 군으로부터 선택된 하나 또는 그 이상의 혼합물이 사용된다. 상기 α-올레핀은 탄소수 4∼8개의 α-올레핀으로서, 부텐-1, 헥센-1, 4-메틸펜텐-1 및 옥텐-1으로 이루어진 군으로부터 하나 또는 그 이상이 선택되며, 불포화산 유도체는 (메타)아크릴산 및 알킬(메타)아크릴레이트로 이루어진 군으로부터 하나 또는 그 이상이 선택된다.The ethylene copolymer is a linear low density polyethylene, preferably air of ethylene and α-olefin and copolymer (LLDPE), low density polyethylene (LDPE), high density polyethylene (HDPE), ethylene-vinylacetate copolymer and ethylene-unsaturated acid derivative. One or more mixtures selected from the group consisting of coalescing are used. The α-olefin is an α-olefin having 4 to 8 carbon atoms, at least one selected from the group consisting of butene-1, hexene-1, 4-methylpentene-1, and octene-1, and the unsaturated acid derivative is ( One or more are selected from the group consisting of methacrylic acid and alkyl (meth) acrylates.
상기 c) 성분은 EVOH와 에틸렌 공중합체의 상용성을 증가시키기 위한 상용화제 성분으로 사용되며, 에틸렌-무수말레익산-알킬(메타)아크릴레이트의 랜덤 공중합체 50∼98 중량부에 폴리아미드 올리고머 2∼50 중량부를 혼합하여 용융압출함으로써 제조될 수 있다. 이때, 상기 에틸렌-무수말레익산-알킬(메타)아크릴레이트의 랜덤 공중합체의 양이 50 중량부 미만이면, 반응하지 않은 폴리아미드 올리고머가 과량 존재하게 되어 본 조성물의 모폴로지 (morphology)와 용융성형성에 영향을 미치므로 산소투과율이 오히려 저하되며, 98 중량부를 초과하면, 폴리아미드 올리고머와의 반응이 충분히 일어나지 못하므로 본 발명의 효과가 크게 나타나지 않는다. 여기서, 반응이 진행되는 부분은 주로 폴리아미드 올리고머의 말단기인 아민기와 에틸렌-무수말레익산-알킬(메타)아크릴레이트 랜덤 공중합체의 무수산기인 것으로 판단되며, 이 반응에 의하여 본 발명에 있어서의 우수한 상용화제가 제조되는 것으로 판단된다. 이렇게 하여 제조된 상용화제는 무수말레익산 대신에 폴리아미드의 주사슬이 그라프트 되어 있는 에틸렌-알킬(메타)아크릴레이트의 공중합체 형태로서, 본 발명의 조성물을 제조시에 폴리아미드의 주사슬이 EVOH의 상 (phase)에 침투되고, 에틸렌-알킬(메타)아크릴레이트의 주사슬이 에틸렌 공중합체 상에 침투함으로써 상용화제로서의 역할을 수행하는 것으로 판단된다. 또한, 이러한 방법은 EVOH와 직접 반응이 가능한 무수말레익산기를 변형시킴에 의하여 상용화제와 EVOH와의 직접적인 반응을 최소화시킴으로써 조성물 내에서의 가교반응을 최대한 억제하여 용융성형성, 성형물의 외관 및 기계적 물성을 우수하게 할 수 있는 것으로 보인다.The c) component is used as a compatibilizer component to increase the compatibility of the EVOH and the ethylene copolymer, polyamide oligomer 2 to 50 to 98 parts by weight of a random copolymer of ethylene-maleic anhydride-alkyl (meth) acrylate It can be prepared by melting and extruding by mixing -50 parts by weight. At this time, if the amount of the random copolymer of ethylene-maleic anhydride-alkyl (meth) acrylate is less than 50 parts by weight, an excessive amount of unreacted polyamide oligomer is present in the morphology and meltability of the composition. Oxygen permeability is rather lowered as it affects, and when it exceeds 98 parts by weight, the reaction with the polyamide oligomer does not sufficiently occur, so the effect of the present invention is not large. Here, it is judged that the part where the reaction proceeds is mainly an amine group which is an end group of the polyamide oligomer and an anhydride group of the ethylene-maleic anhydride-alkyl (meth) acrylate random copolymer, and the reaction is excellent in the present invention. It is believed that a compatibilizer is prepared. The compatibilizer thus prepared is in the form of a copolymer of ethylene-alkyl (meth) acrylate in which the main chain of polyamide is grafted instead of maleic anhydride. It is judged that it penetrates into the phase of EVOH and the main chain of ethylene-alkyl (meth) acrylate plays a role as a compatibilizer by penetrating onto the ethylene copolymer. In addition, this method minimizes the direct reaction between the compatibilizer and EVOH by modifying the maleic anhydride group which can react directly with EVOH, thereby inhibiting crosslinking reaction in the composition to the maximum, thereby forming meltability, appearance and mechanical properties of the molding. It seems to be excellent.
에틸렌-무수말레익산-알킬(메타)아크릴레이트 랜덤 공중합체에 있어서, 상기 알킬기는 탄소수 1∼12의 탄화수소 화합물을 의미하며, 1종 또는 그 이상이 혼합되어 사용될 수 있다. 이들 공중합체는 에틸렌과 공단량체 (comonomer)인 무수말레익산과 알킬(메타)아크릴레이트와의 라디칼 공중합에 의하여 생성될 수 있다.In the ethylene-maleic anhydride-alkyl (meth) acrylate random copolymer, the alkyl group means a hydrocarbon compound having 1 to 12 carbon atoms, and one or more thereof may be mixed and used. These copolymers can be produced by radical copolymerization of ethylene with maleic anhydride, which is a comonomer, and an alkyl (meth) acrylate.
이때, 에틸렌과 공단량체와의 중합비는 조절이 가능하며, 본 발명에서 사용하기에 적당한 공중합체에 있어서, 공단량체의 중량비는 무수말레익산이 0.1∼10 중량부, 알킬(메타)아크리렐이트가 3∼30 중량부 정도가 적당하다. 무수말레익산은 본 발명에서 폴리아미드 올리고머와의 반응을 일으키는데 있어서 중요한 관능기이며, 상기 공중합체 내에서 0.1 중량부 이하일 경우는 본 발명의 효과가 나타나기 어려우며, 10 중량부를 초과할 경우는 본 발명의 조성물을 제조시에 가교반응이 일어나기 쉬워 용융성형성이 나빠지므로 성형물의 외관이 나빠지게 된다. 한편, 알킬(메타)아크릴레이트는 상기 공중합체의 결정화도를 감소시킴에 의하여 투명성의 향상뿐만 아니라, 보다 낮은 용융온도를 가지게 함으로써, 제조된 상용화제가 조성물 내에서 용융시 흐름성이 좋으므로 우수한 상용성을 나타내게 한다. 본 발명에 있어서, 알킬(메타)아크릴레이트의 함량이 3 중량부 미만이면 이러한 효과를 얻기가 어려우며, 30중량부를 초과하면 제조된 상용화제가 에틸렌 공중합체와의 상용성이 나빠지므로 상용화제로서의 효과가 매우 낮아지게 된다. (현재 상업적으로 이용할 수 있는 상기 공중합체의 대표적인 예로는 Elf Atochem 사의 LotaderR또는 Japan Polyolefin 사의 AdtexR등이 있다.)At this time, the polymerization ratio of ethylene and the comonomer can be controlled, and in the copolymer suitable for use in the present invention, the weight ratio of the comonomer is 0.1 to 10 parts by weight of maleic anhydride, alkyl (meth) acrylrel About 3-30 weight part of wits are suitable. Maleic anhydride is an important functional group for causing a reaction with the polyamide oligomer in the present invention, when the content is less than 0.1 part by weight in the copolymer, the effect of the present invention is less likely to occur, and when it exceeds 10 parts by weight, the composition of the present invention. The crosslinking reaction tends to occur at the time of preparation, so that the meltability is deteriorated, so that the appearance of the molded product is deteriorated. On the other hand, alkyl (meth) acrylate not only improves the transparency by reducing the degree of crystallinity of the copolymer, but also has a lower melting temperature, so that the prepared compatibilizer has good flowability when melting in the composition excellent compatibility To indicate. In the present invention, when the content of the alkyl (meth) acrylate is less than 3 parts by weight, it is difficult to obtain such an effect, and when it exceeds 30 parts by weight, the prepared compatibilizer becomes poor in compatibility with the ethylene copolymer, and thus the effect as a compatibilizer Very low. (Illustrative examples of the copolymers that can be used currently for commercial may include Elf Atochem's Lotader R or Japan Polyolefin Corporation Adtex R.)
상기 폴리아미드는 폴리아미드-6, 폴리아미드-6/66, 폴리아미드-12, 및 폴리아미드-6/12로 이루어진 군으로부터 선택될 수 있으며, 폴리아미드 올리고머는 폴리아미드를 제조하는 과정에서 일차아민과 같은 분자량 조절제를 첨가함으로서 제조될 수 있다. 본 발명에서는 주로 분자량이 1,000∼5,000 정도의 폴리아미드 올리고머가 사용된다. 이때, 폴리아미드의 분자량이 5,000을 초과할 경우는 말단에 아민기가 적게 존재하고 용융압출시 흐름성이 나쁘므로 무수말레익산을 포함하는 상기의 공중합체들과의 반응이 일어날 확률이 적어지므로 본 발명에서와 같은 효과가 미미하다. 또한, 폴리아미드의 분자량이 1,000 미만으로 너무 작으면,에틸렌-무수말레익산-알킬(메타)아크릴레이트 공중합체와의 용융시 혼합이 잘 되지 않기 때문에 두 성분간의 반응이 잘 일어나지 않는다.The polyamide may be selected from the group consisting of polyamide-6, polyamide-6 / 66, polyamide-12, and polyamide-6 / 12, wherein the polyamide oligomer is a primary amine in the process of preparing polyamide. It can be prepared by adding a molecular weight regulator such as. In the present invention, polyamide oligomers having a molecular weight of about 1,000 to 5,000 are mainly used. In this case, when the molecular weight of the polyamide exceeds 5,000, since there are less amine groups at the terminal and the flowability is poor during melt extrusion, the reaction with the copolymers containing maleic anhydride is less likely to occur. Same effect as in In addition, if the molecular weight of the polyamide is too small, less than 1,000, the reaction between the two components is less likely to occur when mixing with the ethylene-maleic anhydride-alkyl (meth) acrylate copolymer is not well mixed.
본 발명에 따른 조성물은 제품의 제조조건에 따라 건조혼합 (Dry Blending) 또는 용융혼합 (Melt Blending)된 후에 압출기로 혼입되어 성형물로 제조될 수 있다.The composition according to the present invention may be mixed into an extruder after dry blending or melt blending according to the manufacturing conditions of the product, and then manufactured into a molding.
본 발명의 조성물은 블로운 (blown), 캐스트 (Cast) 압출성형 등의 가공 기기를 사용하여 가공이 가능하며, 본 발명의 조성물을 A, 접착성 수지를 B, 열가소성 수지를 C라고 할 때, A층 단독 또는 A/B, A/B/C, B/A/B, C/B/A/B/C, C/A/C/B/C, C/B/C/A/C/B/C 등의 다양한 구조를 갖는 다층 필름, 시트 또는 용기로 제조될 수 있다. 대표적인 접착성 수지는 폴리에틸렌 또는 폴리프로필렌과 같은 폴리올레핀 수지를 말레익산과 같은 불포화산으로 그라프트시킨 수지가 사용될 수 있다. 상기의 다층 구조에 있어서, 대표적으로 사용되는 열가소성 수지로는 폴리에틸렌, 폴리프로필렌, 폴리스티렌, 폴리아미드 등을 그 예로서 들 수 있다.The composition of the present invention can be processed using processing equipment such as blown, cast extrusion molding, and when the composition of the present invention is A, the adhesive resin is B, the thermoplastic resin is C, A layer alone or A / B, A / B / C, B / A / B, C / B / A / B / C, C / A / C / B / C, C / B / C / A / C / It can be made into a multilayer film, sheet or container having various structures such as B / C. Representative adhesive resins may be used in which a polyolefin resin such as polyethylene or polypropylene is grafted with an unsaturated acid such as maleic acid. In the multilayer structure described above, typical thermoplastic resins include polyethylene, polypropylene, polystyrene, polyamide, and the like.
본 발명의 상기 조성물은 필요에 따라 가공조제, 염료, 산화방지제, 광안정제, 가소제와 같은 첨가제가 사용될 수도 있으며, 특히 글리세롤, p-톨루엔설폰아미드류와 같은 EVOH에 대한 가소제를 첨가할 경우 차단층의 유연성 (Flexibility)을 향상시킬 수 있다.The composition of the present invention may be used additives such as processing aids, dyes, antioxidants, light stabilizers, plasticizers, if necessary, in particular when adding a plasticizer for EVOH, such as glycerol, p-toluenesulfonamides It can improve flexibility.
이하, 실시예 및 비교예를 통하여 본 발명을 좀 더 상세히 설명하지만, 하기 실시예에 본 발명의 범주가 한정되는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples, but the scope of the present invention is not limited to the following Examples.
모든 샘플 (sample)의 산소차단성은, 1일동안 이들을 온도 23℃와 상대습도50의 습기조건에 방치한 후, 가스투과율 측정기 (모델명: Toyoseiki MC1, B-Type)를 사용하여 측정하였다. 산소투과도의 단위는 cc/㎡·일·기압이다. 흐림도 (Haze)는 흐림도 측정기 (Nippon Denshoku사 300A Turbidimeter)를 사용하여 측정하였으며, 단위는 이다.Oxygen barrier properties of all samples were measured using a gas permeability meter (Model name: Toyoseiki MC1, B-Type) after leaving them in a humid condition at a temperature of 23 ° C. and a relative humidity of 50 for 1 day. The unit of oxygen permeability is cc / m 2 · day · atm. Haze was measured using a haze meter (300A Turbidimeter by Nippon Denshoku) and the unit is.
각 수지의 용융지수는 ASTM D1238 법에 의하여 190℃ 또는 210℃에서 2,160g의 힘을 가하여 측정하였으며, 단위는 g/10분이다. 각 수지의 밀도는 ASTM D-1505 법에 의하여 측정하였으며, 단위는 g/㎤이다.The melt index of each resin was measured by applying a force of 2160 g at 190 ° C or 210 ° C by ASTM D1238, and the unit was g / 10 min. The density of each resin was measured by ASTM D-1505 method, and the unit is g / cm 3.
실험에 사용한 EVOH와 에틸렌 공중합체의 종류를 하기 표 1에 나타내었다.The types of EVOH and ethylene copolymers used in the experiment are shown in Table 1 below.
실험에 사용한 c) 성분의 종류를 하기 표 2에 나타내었다.The kind of c) component used for the experiment is shown in Table 2 below.
1) Japan Polyolefin 사의 AdtexRET 182.1) Adtex R ET 182 from Japan Polyolefin.
2) Japan Polyolefin 사의 AdtexRET 184M.2) Adtex R ET 184M from Japan Polyolefin.
3) Japan Polyolefin 사의 AdtexRER 615F.3) Adtex R ER 615F from Japan Polyolefin.
4) Elf Atochem 사의 LotaderR3410.4) Lotader R 3410 from Elf Atochem.
폴리아미드 올리고머 (PAO)의 제조:Preparation of Polyamide Oligomers (PAO):
500ml 용량의 가압반응기에 카프로락탐 (ε-Caprolactam) 170g, 도데실아민 (Dodecylamine) 10.9g 및 물 3.9g을 넣고 밀봉한 뒤, 260℃에서 2 시간동안 교반하면서 반응시켰다. 이때, 가압반응기의 압력이 4.5 kg/㎠까지 상승하였다. 압력 조절 밸브를 열어 상압으로 맞춘 후 다시 260℃에서 2 시간동안 반응시킨 후 상온으로 온도를 떨어뜨려 생성된 고체 성분을 얻었다. 이 고체성분들을 분쇄기에서 분쇄하여 파우더로 제조한 후 끓는 물에 넣고 2 시간동안 교반한 후, 여과하여 80℃의 진공오븐에서 8 시간동안 건조하였다. 열 분석 장비로 측정한 결과 얻어진폴리아미드 올리고머의 용융온도는 220℃이었다.170 g of caprolactam (ε-Caprolactam), 10.9 g of dodecylamine and 3.9 g of water were sealed in a 500 ml pressurized reactor, and reacted with stirring at 260 ° C. for 2 hours. At this time, the pressure of the pressure reactor increased to 4.5 kg / ㎠. The pressure control valve was opened to normal pressure, and then reacted at 260 ° C. for 2 hours, and then the temperature was lowered to room temperature to obtain a solid component. The solid components were pulverized in a pulverizer, made into a powder, put into boiling water, stirred for 2 hours, filtered, and dried in a vacuum oven at 80 ° C. for 8 hours. The melting temperature of the polyamide oligomer obtained as a result of the measurement by the thermal analysis equipment was 220 degreeC.
본 발명의 상용화제 C-5 ∼ C-9의 제조:Preparation of Compatibilizers C-5 to C-9 of the Invention:
상기 표 2에서 기재된 중량부로 각각 건조혼합 (Dry Blending)한 후, 이 혼합물을 직경 19㎜의 이축스크류 (twin screw) 압출기를 이용하여 130-180-210- 220-210℃에서 용융압출함으로써 펠렛 (pallet)으로 제조하였다.After dry blending with each weight part described in Table 2, pellets were melt-extruded at 130-180-210-220-210 ° C using a twin screw extruder having a diameter of 19 mm. pallet).
실시예 1∼5 및 비교예 1∼5Examples 1-5 and Comparative Examples 1-5
E-2 50중량, P-1 40중량, 및 상용화제 10중량를 각각 총량 2kg으로 텀블믹서를 사용하여 건조 혼합한 후, 이 혼합물을 직경 19mm의 이축스크류 압출기를 이용하여 190-200-210-210-210℃에서 용융압출함으로써 펠렛으로 제조하였다. 제조된 펠렛을 60℃에서 12시간 동안 건조한 후, 차단층으로 사용하여 5층 캐스팅 필름 장비를 이용하여 폴리에틸렌/접착층/차단층/접착층/폴리에틸렌의 구조를 갖는 5층필름을 제조하였다. 이때, 폴리에틸렌은 용융지수가 2.8 (190℃, 2.16㎏)인 선형저밀도 폴리에틸렌을, 접착층으로 용융지수가 3.5 (190℃, 2.16㎏)인 무수말레익산 변성 (그라프트) 선형저밀도 폴리에틸렌 (MAH-g-LLDPE)을 사용하였다. 각 층의 두께는 30/10/15/10/30㎛가 되도록 제조하였다. 하기 표 3에 그 결과를 나타내었다.E-2 50 weights, P-1 40 weights, and 10 weights of compatibilizers, respectively, in a total amount of 2 kg each dry mixed using a tumble mixer, and then the mixture was 190-200-210-210 using a twin screw extruder with a diameter of 19 mm. Pellets were prepared by melt extrusion at −210 ° C. FIG. After drying the prepared pellets at 60 ℃ for 12 hours, using a five-layer casting film equipment using a barrier film to prepare a five-layer film having a structure of polyethylene / adhesive layer / barrier layer / adhesive layer / polyethylene. In this case, the polyethylene is a linear low density polyethylene having a melt index of 2.8 (190 ° C., 2.16 kg) and a maleic anhydride modified (graft) linear low density polyethylene having a melt index of 3.5 (190 ° C., 2.16 kg) as an adhesive layer (MAH-g -LLDPE) was used. Each layer was prepared to have a thickness of 30/10/15/10/30 μm. The results are shown in Table 3 below.
*◎;±10이내, ○;±10∼15, △;±15∼20, ×;±20이상* ◎; Within ± 10, ○; ± 10-15, △; ± 15-20, ×; ± 20 or more
상기의 실시예와 비교예에서 나타난 바와 같이, 본 발명의 조성물은 용융성형성이 우수하여 두께편차와 투명성 (낮은 흐림도)이 우수한 필름을 제조할 수 있고, 산소차단성도 우수함을 알 수 있다.As shown in the above Examples and Comparative Examples, the composition of the present invention is excellent in the melt-molding can be produced a film excellent in thickness deviation and transparency (low haze), it can be seen that also excellent oxygen barrier properties.
실시예 6∼9 및 비교예 5∼7Examples 6-9 and Comparative Examples 5-7
EVOH, 상용화제 및 에틸렌 공중합체를 하기 표 4에 기재된 무게비로 각각 총량 20kg으로 텀블 믹서를 사용하여 건조 혼합한 후, 이 혼합물을 3층 (3-Layer) 블로운 필름 머신 (제조회사: 독일 Kiefel사, 모델명: Rotex 40S/30S/40S)의 중간층 압출기 (Middle Layer Extruder)에 투입하고, 내부 (Inside)와 외부 (Outside) 압출기에는 접착성 수지인 무수말레익산-그라프트-폴리에틸렌을 투입하여 폭 500㎜, 두께 55㎛의 3층 필름을 제조하였다. 이때, 중간층 압출기의 스크류 압축비가 3.3:1인 스크류를 사용하였고, 중간층 압출기의 온도는 210℃로 유지하였다. 전자현미경 (Philips사 SEM 515)으로 측정한 결과 각층의 평균두께는 20/15/20㎛이었다.The EVOH, compatibilizer and ethylene copolymer were dry mixed using a tumble mixer in a total amount of 20 kg each in the weight ratios shown in Table 4 below, and then the mixture was mixed with a 3-layer blown film machine manufactured by Kiefel, Germany. Company name: Rotex 40S / 30S / 40S) into the middle layer extruder, and inside and outside extruder, the adhesive resin maleic anhydride-graft-polyethylene is added to the width A three-layer film of 500 mm and a thickness of 55 µm was prepared. In this case, a screw having a screw compression ratio of 3.3: 1 was used, and the temperature of the interlayer extruder was maintained at 210 ° C. The average thickness of each layer was 20/15/20 µm as measured by an electron microscope (Shimen 515 SEM).
상기 실시예 및 비교예에 나타난 바와 같이, 본 발명의 조성물을 차단층으로 하여 블로운 필름을 제조할 경우, 투명성이 우수할 뿐만 아니라, 산소차단성도 우수함을 알 수 있다.As shown in the above Examples and Comparative Examples, when the blown film is prepared using the composition of the present invention as a barrier layer, not only the transparency but also the oxygen barrier property is excellent.
실시예 10∼11 및 비교예 8∼9Examples 10-11 and Comparative Examples 8-9
EVOH, 에틸렌 공중합체 및 상용화제를 하기 표 5에 기재된 무게비로 각각 총량 50Kg으로 텀블믹서를 사용하여 건조 혼합한 후, 이 혼합물을 직경 40㎜의 이축스크류 압출기를 이용하여 190-200-210-210-210℃에서 용융압출함으로써 펠렛으로 제조하였다. 제조된 펠렛을 60℃에서 12시간 동안 건조한 후, 각각 직경이 각각 50/50/60/50/60㎜의 압출기 5개 (A/B/C/D/E)를 갖는 5중 공냉식 블로운 필름 압출기의 C-압출기에 투입하여 폭 1,200㎜의 필름을 제조하였다.EVOH, ethylene copolymer and compatibilizer were dry mixed using a tumble mixer in a total amount of 50 kg each at a weight ratio shown in Table 5 below, and then the mixture was 190-200-210-210 using a twin screw extruder having a diameter of 40 mm. Pellets were prepared by melt extrusion at −210 ° C. FIG. The prepared pellets were dried at 60 ° C. for 12 hours and then five air-cooled blown films with five extruders (A / B / C / D / E) each 50/50/60/50/60 mm in diameter. It was put in the C-extruder of the extruder to prepare a film having a width of 1,200 mm.
A층 및 E층 : 선형저밀도 폴리에틸렌 (용융지수 1.0, 밀도 0.919)Layers A and E: linear low density polyethylene (melt index 1.0, density 0.919)
B층 및 D층 : 말레익산 변성 선형저밀도 폴리에틸렌 (MI 1.2, 밀도 0.90)Layers B and D: Maleic Acid Modified Linear Low Density Polyethylene (MI 1.2, Density 0.90)
가공온도 ; - A,B,D,E 압출기 : 190-200-210-215℃Processing temperature; -A, B, D, E Extruder: 190-200-210-215 ℃
- C 압출기 : 200-210-215-220℃C extruder: 200-210-215-220 ℃
- 어뎁터 (Adapter) : 225℃Adapter: 225 ℃
- 다이 (Die) : 220℃-Die: 220 ℃
압출량 ; 200㎏/시간Extrusion amount; 200 kg / hour
필름두께는 A/B/C/D/E를 각각 15/10/12/10/15㎛로 하여 총 62㎛로 제조하였다.The film thickness was made into 62 micrometers with A / B / C / D / E being 15/10/12/10/15 micrometers, respectively.
상기 실시예와 비교예에 나타난 바와 같이, 본 발명의 상용화제를 사용한 경우, 필름의 외관, 산소차단성 및 기계적 강도가 우수한 필름의 산소차단층으로 사용 가능한 EVOH와 에틸렌 공중합체의 혼합 조성물을 제조할 수 있음을 알 수 있다.As shown in the above Examples and Comparative Examples, when the compatibilizer of the present invention is used, a mixed composition of EVOH and an ethylene copolymer which can be used as an oxygen barrier layer of a film excellent in appearance, oxygen barrier property and mechanical strength is prepared. It can be seen that.
이상에서 살펴본 바와 같이, 본 발명의 상용화제를 사용한 수지 조성물은 기존의 상용화제들을 사용한 것에 비하여, 조성물의 용융성형성 및 상용성이 동시에 우수하므로, 본 발명에 따른 조성물을 차단층으로 사용한 성형품의 외관 (투명성 등)과 기계적 강도 및 산소차단성이 우수한 필름이나 시트를 제조하는 것이 가능하다.As described above, since the resin composition using the compatibilizer of the present invention has excellent meltability and compatibility at the same time as the conventional compatibilizer, the molded article using the composition according to the present invention as a barrier layer. It is possible to produce a film or sheet excellent in appearance (transparency, etc.), mechanical strength and oxygen barrier property.
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