WO2020004744A1 - Molded article including gas barrier layer, packing container including same, and method for preparing molded article - Google Patents

Molded article including gas barrier layer, packing container including same, and method for preparing molded article Download PDF

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Publication number
WO2020004744A1
WO2020004744A1 PCT/KR2018/016023 KR2018016023W WO2020004744A1 WO 2020004744 A1 WO2020004744 A1 WO 2020004744A1 KR 2018016023 W KR2018016023 W KR 2018016023W WO 2020004744 A1 WO2020004744 A1 WO 2020004744A1
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WO
WIPO (PCT)
Prior art keywords
molded body
molded article
foam sheet
barrier layer
gas barrier
Prior art date
Application number
PCT/KR2018/016023
Other languages
French (fr)
Korean (ko)
Inventor
최종한
함진수
이광희
허미
김우진
하상훈
Original Assignee
주식회사 휴비스
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by 주식회사 휴비스 filed Critical 주식회사 휴비스
Priority to CN201880023564.3A priority Critical patent/CN112203835B/en
Priority to JP2019517938A priority patent/JP6838145B2/en
Publication of WO2020004744A1 publication Critical patent/WO2020004744A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D22/00Producing hollow articles
    • B29D22/003Containers for packaging, storing or transporting, e.g. bottles, jars, cans, barrels, tanks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/02Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D22/00Producing hollow articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/065Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of foam
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/18Layered products comprising a layer of synthetic resin characterised by the use of special additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B5/00Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
    • B32B5/18Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2067/00Use of polyesters or derivatives thereof, as moulding material
    • B29K2067/003PET, i.e. poylethylene terephthalate
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2266/00Composition of foam
    • B32B2266/02Organic
    • B32B2266/0214Materials belonging to B32B27/00
    • B32B2266/0264Polyester
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/724Permeability to gases, adsorption
    • B32B2307/7242Non-permeable
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2439/00Containers; Receptacles
    • B32B2439/70Food packaging

Definitions

  • the present invention relates to a molded article comprising a gas barrier layer, a packaging container including the same, and a manufacturing method of the molded article.
  • the food packaging container of the foam type is a product extruded by mixing polystyrene with the foaming gas, which can maintain the thickness relatively thick, has the advantages of maintaining the shape, insulation, and price competitiveness.
  • foamed foams have the disadvantage that harmful substances are detected at high temperatures.
  • non-foamable food packaging device a product made of polypropylene which is thermally stable in the form of a film is used.
  • a non-foamable food packaging container has the advantage of low form change rate at high temperature, harmful substances are not detected.
  • the price is expensive and the heat insulation is not good.
  • a technology for an eco-friendly heat-resistant material and a packaging container including the same has been proposed.
  • the registered patent discloses a packaging container having a heat resistant material having a two-layer structure including an ethylene vinyl alcohol (EVOH) gas barrier layer on at least one surface of a polyethylene terephthalate (PET) foam. It is.
  • EVOH ethylene vinyl alcohol
  • PET polyethylene terephthalate
  • the ethylene vinyl alcohol has excellent barrier properties
  • molding is difficult due to a large melting point difference with polyethylene terephthalate.
  • high temperature heat treatment is required to improve the heat resistance of polyethylene terephthalate.
  • the composition state of the food packaging container is such that the ethylene vinyl alcohol is fused to form a gas barrier layer on the entire area of the food packaging container. There is a problem that becomes poor.
  • the present invention is to solve the above-mentioned problems, to provide a molded body, a packaging container including the same and a manufacturing method thereof that can prevent damage to the gas barrier layer when forming the container.
  • the first foam sheet, the gas barrier layer and the second foam sheet is a laminated structure sequentially, a molded body that satisfies the following equation 1,
  • the first foam sheet and the second foam sheet is a foam of a polyester resin
  • the average thickness of the molded body is in the range of 1 to 5 mm
  • a molded article is characterized in that the oxygen permeability according to ASTM F 3985 is not more than 20 cc / m 2 ⁇ day under conditions of 23 ° C .:
  • H represents the depth of the receptacle and is 1 to 10 cm
  • D represents the diameter of the opening.
  • the present invention provides a packaging container including the molded body.
  • the first foam sheet and the second foam sheet provides a method for producing a molded body, characterized in that the foam of the polyester resin.
  • the molded article according to the present invention can minimize oxygen and moisture permeability by including first and second foam sheets on both sides of the gas barrier layer, respectively.
  • it may be easy to preserve the food by preventing the decay of the food due to oxygen and moisture.
  • FIG. 1 is a cross-sectional view of a molded article according to the present invention.
  • FIG. 2 is a view sequentially showing a method for producing a molded article according to the present invention.
  • the present invention relates to a molded article comprising a gas barrier layer, a packaging container including the same, and a manufacturing method of the molded article.
  • the molded article according to the present invention includes the first and second foam sheets on both sides of the gas barrier layer, thereby minimizing oxygen and moisture permeability.
  • it may be easy to preserve the food by preventing the decay of the food due to oxygen and moisture.
  • FIGS. 1 and 2 are cross-sectional views of a molded article according to the present invention
  • Figure 2 is a view showing a manufacturing method of the molded article according to the present invention in sequence.
  • the molded article according to the present invention will be described in detail with reference to FIGS. 1 and 2.
  • the first foam sheet 101, the gas barrier layer 102 and the second foam sheet (101 ') is a laminated structure sequentially, as a molded body 10 that satisfies the following equation 1,
  • the first foam sheet 101 and the second foam sheet 101 ' is a foam of polyester resin
  • the average thickness of the molded body 10 is in the range of 1 mm to 5 mm,
  • a molded article is characterized in that the oxygen permeability according to ASTM F 3985 is not more than 20 cc / m 2 ⁇ day under conditions of 23 ° C .:
  • H represents the depth of the receptacle and is 1 cm to 10 cm
  • D represents the diameter of the opening.
  • the molded article according to the present invention may have an oxygen permeability of 0.1 to 20 cc / m 2 ⁇ day measured according to ASTM D3985. More specifically, in the case of measuring the oxygen permeability for 30 minutes at (23 ⁇ 1) ° C.
  • the oxygen permeability of the molded article was 0.1 20 cc / m 2 ⁇ day, 0.1 to 15 cc / m 2 ⁇ day, 0.1 to 13 cc / m 2 ⁇ day, 0.1 to 10 cc / m 2 ⁇ day, 0.1 to 7 cc / m 2 ⁇ day, 0.1 to 5 cc / m 2 ⁇ day, or 0.1 to 3 cc / m 2 ⁇ day.
  • the first and second foam sheets 101 and 101 'of the polyester resin are formed in the cross-sectional outer layers of the molded body 10, respectively, and the first and second foam sheets 101 and 101' are formed.
  • the gas barrier layer 102 between it is possible to satisfy the above oxygen permeability. That is, the molded body 10 according to the present invention has an oxygen permeability within the above range, and has an advantage of excellent oxygen shielding performance to extend the shelf life of food.
  • the molded body 10 according to the present invention may form the first and second foam sheets 101 and 101 'on both sides of the gas barrier layer 102 to control oxygen permeability within the above range. .
  • the water vapor transmission rate according to ASTM F 1249 is characterized in that less than 50 g / m 2 ⁇ day under 37 °C, 100% relative humidity conditions.
  • the water vapor transmission rate is 0.1 to 50 g / m 2 ⁇ day, 0.1 to 40 g / m 2 ⁇ day, 0.1 to 30 g / m 2 ⁇ day, 0.1 to 20 g / m 2 ⁇ day, 0.1 to 10 g / m 2 ⁇ day, 0.1 to 7 g / m 2 ⁇ day, 0.1 to 5 g / m 2 ⁇ day or 0.1 to 3 g / m 2 ⁇ day.
  • the molded body 10 according to the present invention may have a water vapor permeability, and thus may be widely used in a product requiring gas barrier properties.
  • a product requiring gas barrier properties For example, when used as a food packaging container, since it is possible to prevent the food from reacting with water vapor to rot, it may be easy to store the food.
  • the polyester resin may include repeating units derived from an acid component and a diol component.
  • the polyester resin may be at least one selected from the group consisting of aromatic and aliphatic polyester resins synthesized from a dicarboxylic acid component and a glycol component or hydroxycarboxylic acid.
  • the polyester resin may be, for example, polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polylactic acid (PLA), polyglycolic acid (PGA) At least one selected from the group consisting of polyethylene adipate (PEA), polyhydroxyalkanoate (PHA), polytrimethylene terephthalate (PTT) and polyethylene naphthalate (PEN) have.
  • PET polyethylene terephthalate
  • PBT polybutylene terephthalate
  • PBT polylactic acid
  • PGA polyglycolic acid
  • PAT polyethylene adipate
  • PHA polyhydroxyalkanoate
  • PTT polytrimethylene terephthalate
  • PEN polyethylene naphthalate
  • PET polyethylene terephthalate
  • PET polyethylene terephthalate
  • the gas barrier layer 102 may include one or more of ethylene vinyl alcohol (EVOH), polyvinylidene chloride (PVDC), and polyethylene terephthalate (PET). have.
  • EVOH ethylene vinyl alcohol
  • PVDC polyvinylidene chloride
  • PET polyethylene terephthalate
  • the barrier layer 102 may be formed using ethylene vinyl alcohol.
  • the gas generated from the food inside the packaging can be discharged out, and at the same time the oxygen supply from the outside can be blocked.
  • the molded body 10 according to the present invention has a multilayer structure, and the average thickness of the multilayer structure forming the molded body 10 may range from 1 mm to 5 mm.
  • the molded body 10 may have a three-layer structure.
  • the total thickness of the three-layer structure may be an average of 1.2 to 4 mm, 1.5 to 3.5 mm, 1.8 to 3 mm, or 2 mm.
  • the average thickness of the gas barrier layer 102 may be 0.01 to 2 mm, 0.05 to 2 mm, 0.1 to 1.9 mm, 0.2 to 1.85 mm, 0.3 to 1.8 mm, 0.5 to 1.6 mm, 0.7 to 1.4 mm , 0.9 to 1.2 mm, or 1 mm.
  • the average thickness of the first foam sheet 101 and the second foam sheet 101 ' may be 0.5 to 1.5 mm, respectively, 0.6 to 1.3 mm, 0.7 to 1.2 mm, 0.8 to 1.0 mm, 0.9 to 0.95 mm Can be.
  • the molded body 10 of the present invention is composed of the foam sheet (101, 101 ') and the gas barrier layer 102 having a thickness in the above range, thereby satisfying the above-described oxygen permeability and water vapor permeability, and at the same time compressive strength While improving, it is possible to satisfy light weight and the like at the same time.
  • the melting point (T m ) of the first and second foam sheets (101, 101 ') may be an average of 240 to 260 °C.
  • the average melting points of the first and second foam sheets 101 and 101 ' may be 242 ° C to 257 ° C, 245 ° C to 255 ° C, 247 ° C to 253 ° C, or 248 ° C to 251 ° C.
  • the melting points of the first and second foam sheets 101 and 101 'including the polyethylene terephthalate resin may be 248 ° C to 251 ° C on average.
  • the melting point (T m ) of the gas barrier layer 102 may be an average of 150 °C to 190 °C.
  • the melting point of the gas barrier layer 102 may be an average of 150 °C to 190 °C, 155 °C to 185 °C, 160 °C to 180 °C, 165 °C to 175 °C or 169 °C to 171 °C.
  • the melting point of the gas barrier layer made of ethylene vinyl alcohol may be 170 ⁇ 0.5 ° C. on average.
  • polyethylene terephthalate and ethylene vinyl alcohol has a large melting point difference, and when the two-layer structure (foam sheet / gas barrier layer) molded body is formed, ethylene vinyl alcohol is peeled or melted, so that the barrier layer 102 is applied to the entire area of the molded body. Although there was a problem such that it cannot be formed evenly, the gas barrier layer 102 is melted away by laminating the foam sheets 101 and 101 'on both sides of the gas barrier layer 102, or the foam sheets 101 and 101 are laminated. Problems such as peeling off from ') can be solved.
  • the molded body 10 according to the present invention includes a bottom portion 11 and a wall portion 12 having an open top along a circumference of the bottom portion 11, and in the equation (1), H /
  • the D value may be 0.01 to 1.3, 0.05 to 1.2, 0.1 to 1.1, 0.3 to 1.0, 0.4 to 0.9, 0.5 to 0.8, 0.55 to 0.7 or 0.6 to 0.65.
  • the H value may be 1 to 10 cm.
  • the diameter of the opening of the molded body 10 may be 10 cm
  • the depth of the receiving portion may be 3 cm.
  • the molded body 10 according to the present invention may have a container shape, and may have a cylindrical container shape or a rectangular container shape.
  • the molded body 10 forms the first and second foam sheets 101 and 101 'on both surfaces of the gas barrier layer 102, thereby satisfying the following equation (2).
  • T 1 is the outer surface temperature of the molded body measured when 1 minute has elapsed by containing 100 ° C water in the molded body at 20 ° C and 1 atm conditions
  • T 2 is the temperature of the water inside the molded body measured when 1 minute has elapsed after 100 minutes of water is contained in the molded body at 20 ° C. and 1 atm conditions.
  • the molded article 10 according to the present invention includes the first and second foam sheets 101 and 101 ', indicating excellent thermal barrier properties. Specifically, at room temperature (20 ° C.) and 1 atm, the temperature difference between the water temperature inside the molded body and the outer surface of the molded body is 1 minute after 100 minutes of water at 100 ° C. (v / v) is contained in the molded body. May be greater than or equal to 10 ° C. This indicates that the molded body 10 according to the present invention has excellent thermal barrier properties. Specifically, when the molded product 10 has passed 70 minutes (v / v) of water at 100 ° C. in one minute, the molded body 10 is formed. It is the temperature difference between the temperature of the water contained therein and the outer surface of the molded body 10.
  • the molded body 10 according to the present invention contains 70% (v / v) of water at 100 ° C.
  • the external temperature of the molded body when the external temperature of the molded body is 40 ° C. at 1 minute, the molded body 10 is inside.
  • the temperature of the water accommodated in may be 95 ° C.
  • the molded body 10 according to the present invention can be seen that the thermal barrier property is excellent by maintaining a relatively high temperature difference between the temperature of the water accommodated inside the molded body 10 and the outer surface of the molded body 10 under the above conditions, thereby keeping food warm The effect is to effectively improve.
  • first and second foam sheets 101 and 101 ′ of the present invention may each include 0.5 to 9 wt% of calcium carbonate (CaCO 3 ).
  • the calcium carbonate (CaCO 3 ) is an inorganic particle, by including the inorganic particles as described above, the first and second foam sheets (101, 101 ') of the present invention is uniform sheet surface and excellent thermoformability Can be represented.
  • the thermal conductivity of the calcium carbonate may be 1.0 kcal / mh °C to 3.0 kcal / mh °C. Specifically, the thermal conductivity of calcium carbonate may be 1.2 kcal / mh ° C. to 2.5 kcal / mh ° C., 1.5 kcal / mh ° C. to 2.2 kcal / mh ° C. or 1.8 kcal / mh ° C. to 2.0 kcal / mh ° C.
  • the thermal conductivity of calcium carbonate may be 1.5 kcal / mh °C to 2.5 kcal / mh °C or 1.8 kcal / mh °C to 2.3 kcal / mh °C.
  • the first and second foam sheets 101 and 101 'including calcium carbonate exhibit excellent thermal conductivity and thus have a uniform surface, and may exhibit excellent thermoformability.
  • the content of calcium carbonate may be 0.5 to 9% by weight.
  • the calcium carbonate content is 0.5 to 8% by weight, 0.6 to 7% by weight, 0.7 to 6% by weight, 0.8 to 5% by weight, 0.9 to 4% by weight, 1.0 to 3.0% by weight, 2 to 3.5% by weight
  • it may be 1.0% by weight or 3% by weight.
  • the density of the foam sheets 101 and 101 '(KS M ISO 845) may be on average 300 to 700 kg / m 3 .
  • the density of the foam sheet (101, 101 ') is an average of 325 to 650 kg / m 3 , 350 to 600 kg / m 3 , 375 to 550 kg / m 3 , 400 to 500 kg / m 3 or 425 to 450 kg / m may be 3 days.
  • the foam sheets 101 and 101 'according to the present invention may have a high temperature elongation of 325 to 375% at 200 ° C for 10 seconds.
  • the high temperature elongation of the foam sheet (101, 101 ') for 10 seconds at 200 °C may be 330 to 360%, 345 to 370% or 335 to 360%.
  • the foam sheets 101 and 101 ' may have a high temperature elongation of 345 to 355% at 200 ° C for 10 seconds.
  • the foam sheet (101, 101 ') according to the present invention can exhibit excellent workability.
  • the first and second foam sheets 101 and 101 'of the molded body 10 according to the present invention are foams of a polyester resin, and the polyester resin of the first and second foam sheets 101 and 101' is polyethylene. It may be a terephthalate (polyethylene terephthalate, PET) resin. By using the PET resin, it may be environmentally friendly and easy to reuse.
  • PET resin polyethylene terephthalate
  • total elution amount is 30ppm or less, antimony germanium, terephthalic acid, isophthalic acid and acetaldehyde are not detected when measuring elution standard. Volatile substances are not detected.
  • the molded article 10 according to the present invention by using the polyester resin which is an environmentally friendly material as described above, the standards and specifications of the Agency and container packaging issued by the Ministry of Food and Drug Safety Republic of Korea Notice No. 2015-7
  • the substances of concern described in the above can be adjusted within the allowable range.
  • the molded body 10 may have a barrier performance, a hydrophilization function or a waterproof function, and may include a surfactant, a hydrophilizing agent, a heat stabilizer, a waterproofing agent, a cell size expander, and an infrared attenuation. It may further comprise one or more functional additives selected from the group consisting of plasticizers, fire protection chemicals, pigments, elastomers, extrusion aids, antioxidants, anti-static agents and UV absorbers.
  • the resin foam sheet of the present invention may include a thickener, a heat stabilizer and a foaming agent.
  • the thickener is not particularly limited, but for example, pyromellitic dianhydride (PMDA) may be used in the present invention.
  • PMDA pyromellitic dianhydride
  • the heat stabilizer may be an organic or inorganic phosphorus compound.
  • the organic or inorganic phosphorus compound may be, for example, phosphoric acid and its organic ester, phosphorous acid and its organic ester.
  • the thermal stabilizer is a commercially available material and may be phosphoric acid, alkyl phosphate or aryl phosphate.
  • the thermal stabilizer may be triphenyl phosphate, but is not limited thereto. If the thermal stabilizer is capable of improving the thermal stability of the resin foam sheet, the thermal stabilizer may be used without limitation.
  • blowing agent may include physical blowing agents such as N 2 , CO 2 , freon, butane, pentane, neopentane, hexane, isohexane, heptane, isoheptane, methyl chloride, or azodicarbonamide compounds, P, P'-oxybis (benzenesulfonylhydrazide) [P, P'-oxy bis (benzene sulfonyl hydrazide)] compound, N, N'-dinitrosopentamethylenetetraamine (N, N'-dinitroso pentamethylene chemical blowing agents such as tetramine-based compounds, and specifically, CO 2 may be used in the present invention.
  • physical blowing agents such as N 2 , CO 2 , freon, butane, pentane, neopentane, hexane, isohexane, heptane, isoheptane, methyl chlor
  • this invention provides the manufacturing method of a molded object.
  • FIG. 2 is a view sequentially showing a method for producing a molded article according to the present invention. 2, the present invention,
  • the first foam sheet and the second foam sheet provides a method for producing a molded body, characterized in that the foam of the polyester resin.
  • the manufacturing method for the first and second foam sheet is not specifically limited, for example, the first and second foam sheet can be produced by extrusion foaming the polyester resin.
  • the type of foaming method includes bead foaming or extrusion foaming.
  • the bead foaming is a method of forming a product by heating a resin bead and primary foaming, aging it for a suitable time, and then filling the mold in a plate or cylindrical shape and then heating it to be fused and molded by secondary foaming.
  • Extrusion foam heats and melts the resin and continuously extrudes and foams the resin melt, thereby simplifying the process steps, enabling mass production, and cracking and granular fracture between beads during bead foaming. Etc. can be prevented.
  • the sheet 1 disposed between the female mold 21 and the male mold 22 may be molded into the molded body 10 by thermoforming.
  • thermoforming include vacuum forming, pressure forming, or vacuum press forming a combination of vacuum forming and pressure forming, using a male mold (plug), or using the male mold 22, followed by vacuum and / or press forming. Can be thermoformed.
  • FIG. 2 (a) of FIG. 2 shows an arrangement step in which the sheet 1 is disposed between the female mold 21 and the male mold 22 of the molding apparatus before the sheet 1 is molded.
  • FIG. 2 (b) is a drawing showing the stretching process and the thermal process. As shown in FIG. 2 (b), the male mold 22 is lowered to stretch the sheet 1, and vacuum suction from the female mold 21 is performed. It shapes by the shape of the cavity of the female die 21, and heat is applied.
  • Fig. 2 (c) shows the molded body 10 which is a final molded product by shaping the sheet 1 being formed into the shape of the male mold 22 by pressurization of the male mold 22 and compressed air from the female mold 21. Indicates that is molded. Next, the molded body 10 may be taken out by raising the male mold 22 after cooling.
  • the sheet surface temperature is 140 to 160 ° C
  • the surface temperature of the female mold 21 and the male mold 22 is set to 60 ° C to 200 ° C to form the molded body 10. It can be molded.
  • the surface of the male mold 22 and the cavity surface temperature of the female mold 21 may be different from each other.
  • the surface temperature of the male mold 22 may be 250 to 280 ° C, 255 to 275 ° C, 260 to 270 ° C or 265 ° C, respectively
  • the cavity surface temperature of the female mold 21 may be 200 to 250 ° C or 210 ° C. To 240 ° C., 215 to 235 ° C., 220 to 230 ° C., or 225 ⁇ 3 ° C.
  • the surface temperature of the male mold 22 may be 265 ⁇ 1 ° C.
  • the surface temperature of the female mold 21 may be 225 ° C.
  • the male mold 22 may be female for 0.5 to 15 seconds. It is preferable to contact the mold 22.
  • the female mold 21 may have a structure in which a decompression hole 23 for depressurizing a cavity, which is an internal space, is formed at one side.
  • the container-shaped molded article or the packaging container including the molded article, in which the first foam sheet of the polyester resin, the gas barrier layer, and the second foam sheet of the polyester resin are sequentially laminated by the method of manufacturing the molded article described above. Can be prepared.
  • PET resin 100 parts by weight was dried at 130 ° C. to remove moisture, and 100 parts by weight of the PET resin from which the water was removed in the first extruder, 1 part by weight of pyromellitic dianhydride (PMDA), 1 part by weight of calcium carbonate (CaCO 3 ), Irganox (IRG 1010) 0.1 part by weight was mixed and heated to 280 ° C. to prepare a resin melt. Then, butane gas was mixed as a blowing agent in the first extruder, and the resin melt was sent to the second extruder and cooled to 220 ° C. The cooled resin melt passed through a die to form a foam sheet.
  • PMDA pyromellitic dianhydride
  • CaCO 3 calcium carbonate
  • Irganox IRG 1010
  • the density of the prepared polyester resin foam sheet was 380 kg / m 3 , the thickness was 1 mm.
  • a molded article was prepared in the same manner as in Example 1, except that the barrier layer was composed of an EVOH 0.02 mm film and a PET 0.03 mm film 2 layer.
  • a molded article was prepared in the same manner as in Example 1 except that the value of H / D was 0.5.
  • a sheet of a two-layer structure was prepared by laminating a 0.05 mm EVOH film with a barrier layer on one surface of the foam sheet prepared in the same manner as in Preparation Example 1. And the laminated 2-layered sheet was shape
  • molded to container shape, and the molded object (H: depth D: diameter of an opening part) with H / D 0.3 was manufactured.
  • the opening diameter of the molded body was 10 cm.
  • the surface temperature of the male mold was 60 degreeC, and the surface temperature of the female mold was 120 degreeC.
  • a container having the same structure as in Example 1 of H / D 0.3 was molded, and the temperature of the mold was maintained at 20 ° C. when molding.
  • the molded article was manufactured by changing sheet types and molding conditions of the molded article as shown in Table 1 below.
  • Example 1 Example 2 Example 3 Comparative Example 1 Comparative Example 2 Layer Layer PET Form PET Form PET Form PET Form PP EVOH EVOH + PET EVOH EVOH EVOH PET Form PET Form PET Form PP Thickness of gas barrier layer (mm) EVOH 0.05 EVOH 0.02 + PET 0.03 EVOH 0.05 EVOH 0.05 EVOH 0.05 Molding condition (H / D) 0.3 0.3 0.5 0.3 0.3
  • Oxygen permeability was measured with respect to the molded object produced by the Example and the comparative example under the temperature of 23 degreeC, and the relative humidity conditions of 50%.
  • the specimens of the molded body were randomly cut and measured. The results are shown in Table 2 below.
  • Tester OX-TRAN 702 (MOCON, USA)
  • Measuring range 0.1 to 2000 cc / m 2 day
  • Example 1 Example 2 Example 3 Comparative Example 1 Comparative Example 2 Oxygen Permeability (cc / m 2 Day) 2 3 7 15 2
  • the molded article oxygen permeability according to the present invention is low, thereby can be almost prevented from permeation of oxygen. This means that the gas barrier layer is evenly distributed over the entire area of the molded body. On the other hand, it was confirmed that the molded article of Comparative Example 1 had high oxygen permeability. It is determined that the gas barrier layer is damaged during molding of the molded body. In addition, in the case of Comparative Example 2 which is a non-foaming product, the oxygen permeability is low, but it can be confirmed that the thermal barrier property is not excellent in the thermal barrier test described later.
  • Comparative Example 1 had high oxygen permeability. It is determined that the gas barrier layer is damaged during molding of the molded body. In addition, in the case of Comparative Example 2 which is a non-foaming product, the oxygen permeability is low, but it can be confirmed that the thermal barrier property is not excellent in the thermal barrier test described later.
  • Example 1 Example 2 Example 3 Comparative Example 1 Comparative Example 2 Water vapor transmission rate (g / m 2 day) 8.5 17 18 19 3
  • T 1 is the outer surface temperature of the molded body measured when 1 minute has elapsed by containing 100 ° C water in the molded body at 20 ° C and 1 atm conditions
  • T 2 is the temperature of the water inside the molded body measured when 1 minute has elapsed after 100 minutes of water is contained in the molded body at 20 ° C. and 1 atm conditions.
  • Example 1 Example 2 Example 3 Comparative Example 1 Comparative Example 2 T 1 40 38 40 75 80 T 2 95 92 90 84 80 T 2 -T 1
  • the molded article according to the embodiment can be seen that the temperature difference between the temperature of the water contained in the molded body and the surface of the molded body is 10 ° C or more showing excellent heat shielding properties.
  • the molded articles according to Comparative Examples 1 and 2 were
  • the molded article according to the present invention has low water vapor permeability and oxygen permeability, and is excellent in thermal barrier property.
  • the molded article according to the present invention includes the first and second foam sheets respectively on both sides of the gas barrier layer, oxygen and moisture permeability can be minimized, and when used in a food packaging container, decay of food due to oxygen and moisture It may be easy to preserve the food by preventing such.

Abstract

The present invention relates to a molded article including a gas barrier layer, a packing container including same, and a method for preparing the molded article. The molded article according to the present invention includes first and second foam sheets on both sides of the gas barrier layer, respectively, so that the permeability of oxygen and moisture can be minimized. When the molded article is used in a food packing container, food spoilage or the like caused by oxygen or moisture are prevented, and thus food can be easily preserved.

Description

가스 베리어층을 포함하는 성형체, 이를 포함하는 포장용기 및 성형체의 제조방법Molded body comprising a gas barrier layer, a packaging container including the same and a method of manufacturing the molded body
본 발명은 가스 베리어층을 포함하는 성형체, 이를 포함하는 포장용기 및 성형체의 제조방법에 관한 것이다.The present invention relates to a molded article comprising a gas barrier layer, a packaging container including the same, and a manufacturing method of the molded article.
통상의 식품 포장용기로 사용되고 있는 제품은 발포식과 비발포식으로 나뉜다. 발포식의 식품 포장용기는 폴리스타이렌을 발포 가스와 혼합시켜 압출시킨 제품이 사용되고 있는데, 이는 두께를 비교적 두껍게 유지할 수 있어 형태유지, 단열성, 가격 경쟁력이 높은 장점이 있다. 반면, 이러한 발포식 제폼은 고온에서 유해물질이 검출되는 단점이 있다.Products used in general food packaging containers are divided into foamed and non-foamed. The food packaging container of the foam type is a product extruded by mixing polystyrene with the foaming gas, which can maintain the thickness relatively thick, has the advantages of maintaining the shape, insulation, and price competitiveness. On the other hand, such foamed foams have the disadvantage that harmful substances are detected at high temperatures.
비발포식의 식품 포장용기기 경우, 열에 안정한 폴리프로필렌을 필름형태로 제작된 제품이 사용되고 있다. 한편, 이러한 비발포식의 식품 포장용기는 고온에서 형태변화율이 적고, 유해물질이 검출되지 않는 장점이 있다. 그러나, 가격이 비싸고 단열이 잘 되지 않는 단점이 있다.In the case of a non-foamable food packaging device, a product made of polypropylene which is thermally stable in the form of a film is used. On the other hand, such a non-foamable food packaging container has the advantage of low form change rate at high temperature, harmful substances are not detected. However, there is a disadvantage that the price is expensive and the heat insulation is not good.
한편, 현대사회에서 점차 생활이 편리해 지면서 일회용품 사용이 증가하고, 1인 가구 증가에 따른 배달음식 및 간편요리 제품의 수요가 점차 늘어나고 있다. 이에 따라, 식품 포장용기의 수요도 증가하고 있으며, 유해물질로부터 안전하고 용도에 따른 기능이 부여된 새로운 용기 소재에 대한 소비자 니즈가 점점 커지고 있다.On the other hand, as life becomes more convenient in modern society, the use of disposable products is increasing, and the demand for delivery food and convenience food products is gradually increasing due to the increase of single households. Accordingly, the demand for food packaging containers is also increasing, and consumer needs for new container materials which are safe from harmful substances and given functions according to their use are increasing.
이와 관련하여, 식품 포장용기 관련 업체에서는 편리함, 안전성, 친환경 성능 및 가격경쟁력을 모두 갖춘 식품 포장용기를 제조하기 위하여 많은 노력이 이루어지고 있다.In this regard, a lot of efforts have been made in the food packaging container-related companies to manufacture a food packaging container with all the convenience, safety, eco-friendly performance and price competitiveness.
그 예로써, 친환경 내열재 및 이를 포함하는 포장용기(대한민국 등록특허 제10-1778629호)에 대한 기술이 제안된 바 있다. 구체적으로, 상기 등록특허에는 폴리에틸렌 테레프탈레이트(Polyethylene terephthalate, PET) 발포체의 적어도 일면에 에틸렌비닐알코올(ethylene vinyl alcohol, EVOH) 가스 베리어층을 포함하는 2층 구조의 내열재를 갖는 포장용기에 대해서 개시되어 있다. As an example, a technology for an eco-friendly heat-resistant material and a packaging container (Korean Patent No. 10-1778629) including the same has been proposed. Specifically, the registered patent discloses a packaging container having a heat resistant material having a two-layer structure including an ethylene vinyl alcohol (EVOH) gas barrier layer on at least one surface of a polyethylene terephthalate (PET) foam. It is.
그러나, 상기 에틸렌비닐알코올은 배리어성이 우수하나, 폴리에틸렌 테레프탈레이트와의 큰 융점 차이로 인하여 성형이 어려운 단점이 있다. 구체적으로, 폴리에틸렌테레프탈레이트의 내열성을 향상시키기 위해 고온의 열처리가 필요한데, 이러한 경우 상기 에틸렌비닐알코올이 융해되어 식품 포장용기의 전체 면적에 가스 베리어층을 형성할 수 없는 등 식품 포장용기의 구성상태가 불량해지는 문제점이 있다.However, although the ethylene vinyl alcohol has excellent barrier properties, molding is difficult due to a large melting point difference with polyethylene terephthalate. Specifically, high temperature heat treatment is required to improve the heat resistance of polyethylene terephthalate. In this case, the composition state of the food packaging container is such that the ethylene vinyl alcohol is fused to form a gas barrier layer on the entire area of the food packaging container. There is a problem that becomes poor.
본 발명은 전술한 문제점을 해결하기 위한 것으로, 용기의 성형시 가스 베리어층의 손상을 방지할 수 있는 성형체, 이를 포함하는 포장용기 및 이의 제조방법을 제공하고자 한다.The present invention is to solve the above-mentioned problems, to provide a molded body, a packaging container including the same and a manufacturing method thereof that can prevent damage to the gas barrier layer when forming the container.
본 발명은,The present invention,
제1 발포시트, 가스 베리어층 및 제2 발포시트가 순차적으로 적층된 구조이며, 하기 수학식 1을 만족하는 성형체로써,The first foam sheet, the gas barrier layer and the second foam sheet is a laminated structure sequentially, a molded body that satisfies the following equation 1,
상기 제1 발포시트 및 제2 발포시트는 폴리에스테르 수지의 발포체이며,The first foam sheet and the second foam sheet is a foam of a polyester resin,
상기 성형체의 평균 두께는 1 내지 5 mm 범위이고, The average thickness of the molded body is in the range of 1 to 5 mm,
ASTM F 3985 에 따른 산소 투과도가 23℃ 의 조건 하에서, 20 cc/m2·day 이하인 것을 특징으로 하는 성형체를 제공한다:A molded article is characterized in that the oxygen permeability according to ASTM F 3985 is not more than 20 cc / m 2 · day under conditions of 23 ° C .:
[수학식 1][Equation 1]
H/D ≥ 0.01H / D ≥ 0.01
수학식 1에서,In Equation 1,
수용부 및 개구부를 포함하는 용기 구조의 성형체를 형성하되,Forming a shaped body of the container structure including the receiving portion and the opening,
H는 수용부의 깊이를 나타내고, 1 내지 10 cm이며,H represents the depth of the receptacle and is 1 to 10 cm,
D는 개구부의 직경을 나타낸 것이다.D represents the diameter of the opening.
또한, 본 발명은 상기 성형체를 포함하는 포장용기를 제공한다.In addition, the present invention provides a packaging container including the molded body.
나아가, 본 발명은,Furthermore, the present invention,
제1 발포시트, 가스 베리어층 및 제2 발포시트가 순차적으로 적층된 구조의 시트를 성형장치의 암형 금형과 수형 금형 사이에 배치하는 단계; 및Disposing a sheet having a structure in which the first foam sheet, the gas barrier layer and the second foam sheet are sequentially stacked between the female mold and the male mold of the molding apparatus; And
수형 금형을 가압하여 성형체를 성형하는 단계;를 포함하며,And pressing the male mold to mold the molded body.
상기 제1 발포시트 및 제2 발포시트는 폴리에스테르 수지의 발포체인 것을 특징으로 하는 성형체의 제조방법을 제공한다.The first foam sheet and the second foam sheet provides a method for producing a molded body, characterized in that the foam of the polyester resin.
본 발명에 따른 성형체는 가스 베리어층의 양면에 각각 제1 및 제2 발포시트를 포함함으로써, 산소 및 수분 투과도를 최소화할 수 있다. 아울러, 상기 성형체를 식품 포장용기에 사용할 경우, 산소 및 수분으로 인한 식품의 부패 등을 방지하여 식품의 보존에 용이할 수 있다.The molded article according to the present invention can minimize oxygen and moisture permeability by including first and second foam sheets on both sides of the gas barrier layer, respectively. In addition, when the molded article is used in a food packaging container, it may be easy to preserve the food by preventing the decay of the food due to oxygen and moisture.
도 1은 본 발명에 따른 성형체의 단면도이다.1 is a cross-sectional view of a molded article according to the present invention.
도 2는 본 발명에 따른 성형체의 제조방법을 순차대로 도시한 도면이다.2 is a view sequentially showing a method for producing a molded article according to the present invention.
본 발명은 가스 베리어층을 포함하는 성형체, 이를 포함하는 포장용기 및 성형체의 제조방법에 관한 것이다. 특히, 본 발명에 따른 성형체는 가스 베리어층의 양면에 제1 및 제2 발포시트를 포함함으로써, 산소 및 수분 투과도를 최소화할 수 있다. 아울러, 상기 성형체를 식품 포장용기에 사용할 경우, 산소 및 수분으로 인한 식품의 부패 등을 방지하여 식품의 보존에 용이할 수 있다.The present invention relates to a molded article comprising a gas barrier layer, a packaging container including the same, and a manufacturing method of the molded article. In particular, the molded article according to the present invention includes the first and second foam sheets on both sides of the gas barrier layer, thereby minimizing oxygen and moisture permeability. In addition, when the molded article is used in a food packaging container, it may be easy to preserve the food by preventing the decay of the food due to oxygen and moisture.
도 1은 본 발명에 따른 성형체의 단면도, 도 2는 본 발명에 따른 성형체의 제조방법을 순차대로 도시한 도면이다. 이하, 도 1 및 도 2를 참조하여, 본 발명에 따른 성형체에 대해 상세하게 설명하도록 한다.1 is a cross-sectional view of a molded article according to the present invention, Figure 2 is a view showing a manufacturing method of the molded article according to the present invention in sequence. Hereinafter, the molded article according to the present invention will be described in detail with reference to FIGS. 1 and 2.
본 발명은,The present invention,
제1 발포시트(101), 가스 베리어층(102) 및 제2 발포시트(101')가 순차적으로 적층된 구조이며, 하기 수학식 1을 만족하는 성형체(10)로써,The first foam sheet 101, the gas barrier layer 102 and the second foam sheet (101 ') is a laminated structure sequentially, as a molded body 10 that satisfies the following equation 1,
상기 제1 발포시트(101) 및 제2 발포시트(101')는 폴리에스테르 수지의 발포체이며,The first foam sheet 101 and the second foam sheet 101 'is a foam of polyester resin,
상기 성형체(10)의 평균 두께는 1 mm 내지 5 mm 범위이고, The average thickness of the molded body 10 is in the range of 1 mm to 5 mm,
ASTM F 3985 에 따른 산소 투과도가 23℃ 의 조건 하에서, 20 cc/m2·day 이하인 것을 특징으로 하는 성형체를 제공한다:A molded article is characterized in that the oxygen permeability according to ASTM F 3985 is not more than 20 cc / m 2 · day under conditions of 23 ° C .:
[수학식 1][Equation 1]
H/D ≥ 0.01H / D ≥ 0.01
수학식 1에서,In Equation 1,
수용부 및 개구부를 포함하는 용기 구조의 성형체를 형성하되,Forming a shaped body of the container structure including the receiving portion and the opening,
H는 수용부의 깊이를 나타내고, 1 cm 내지 10 cm이며,H represents the depth of the receptacle and is 1 cm to 10 cm,
D는 개구부의 직경을 나타낸 것이다.D represents the diameter of the opening.
구체적으로, 본 발명에 따른 성형체는 ASTM D3985 에 의거하여 측정한 산소 투과도가 0.1 내지 20 cc/m2·day 일 수 있다. 보다 구체적으로, 제조된 성형체의 시편(가로×세로×높이 40㎜×40㎜×3㎜)을 (23±1)℃ 조건에서 30 분 동안 산소 투과도를 측정하는 경우, 성형체의 산소 투과도는 0.1 내지 20 cc/m2·day, 0.1 내지 15 cc/m2·day, 0.1 내지 13 cc/m2·day, 0.1 내지 10 cc/m2·day, 0.1 내지 7 cc/m2·day, 0.1 내지 5 cc/m2·day, 또는 0.1 내지 3 cc/m2·day 일 수 있다. Specifically, the molded article according to the present invention may have an oxygen permeability of 0.1 to 20 cc / m 2 · day measured according to ASTM D3985. More specifically, in the case of measuring the oxygen permeability for 30 minutes at (23 ± 1) ° C. of the specimens (width × length × height 40mm × 40mm × 3mm) of the manufactured molded article, the oxygen permeability of the molded article was 0.1 20 cc / m 2 · day, 0.1 to 15 cc / m 2 · day, 0.1 to 13 cc / m 2 · day, 0.1 to 10 cc / m 2 · day, 0.1 to 7 cc / m 2 · day, 0.1 to 5 cc / m 2 · day, or 0.1 to 3 cc / m 2 · day.
이는, 상술한 바와 같이, 폴리에스테르 수지의 제1 및 제2 발포시트(101, 101')를 각각 성형체(10)의 단면 외층에 형성하고, 상기 제1 및 제2 발포시트(101, 101') 사이에 가스 베리어층(102)을 형성함으로써, 상기와 같은 산소 투과도를 만족시킬 수 있다. 즉, 본 발명에 따른 성형체(10)는 상기 범위 내의 산소 투과도를 가짐으로써, 산소를 차폐하는 성능이 우수하여 식품의 보존기한을 연장시킬 수 있는 이점이 있다.As described above, the first and second foam sheets 101 and 101 'of the polyester resin are formed in the cross-sectional outer layers of the molded body 10, respectively, and the first and second foam sheets 101 and 101' are formed. By forming the gas barrier layer 102 between), it is possible to satisfy the above oxygen permeability. That is, the molded body 10 according to the present invention has an oxygen permeability within the above range, and has an advantage of excellent oxygen shielding performance to extend the shelf life of food.
구체적으로, 본 발명에 따른 성형체(10)는 상기 가스 베리어층(102)의 양면에 각각 제1 및 제2 발포시트(101, 101')를 형성하여, 산소 투과도를 상기 범위 내로 제어할 수 있다.Specifically, the molded body 10 according to the present invention may form the first and second foam sheets 101 and 101 'on both sides of the gas barrier layer 102 to control oxygen permeability within the above range. .
아울러, ASTM F 1249에 따른 수증기 투과도가 37℃, 100 %의 상대습도 조건하에서, 50 g/m2·day 이하인 것을 특징으로 한다. 예를 들어, 상기 수증기 투과도는 0.1 내지 50 g/m2·day, 0.1 내지 40 g/m2·day, 0.1 내지 30 g/m2·day, 0.1 내지 20 g/m2·day, 0.1 내지 10 g/m2·day, 0.1 내지 7 g/m2·day, 0.1 내지 5 g/m2·day 또는 0.1 내지 3 g/m2·day 범위일 수 있다. 본 발명에 따른 성형체(10)는 상기 수증기 투과도를 가짐으로써, 가스 베리어 특성을 요구하는 제품에 널리 사용될 수 있다. 예를 들어, 식품 포장용기로 사용할 경우, 식품이 수증기와 반응하여 부패하는 것을 방지할 수 있으므로, 식품의 보관에 용이할 수 있다.In addition, the water vapor transmission rate according to ASTM F 1249 is characterized in that less than 50 g / m 2 · day under 37 ℃, 100% relative humidity conditions. For example, the water vapor transmission rate is 0.1 to 50 g / m 2 · day, 0.1 to 40 g / m 2 · day, 0.1 to 30 g / m 2 · day, 0.1 to 20 g / m 2 · day, 0.1 to 10 g / m 2 · day, 0.1 to 7 g / m 2 · day, 0.1 to 5 g / m 2 · day or 0.1 to 3 g / m 2 · day. The molded body 10 according to the present invention may have a water vapor permeability, and thus may be widely used in a product requiring gas barrier properties. For example, when used as a food packaging container, since it is possible to prevent the food from reacting with water vapor to rot, it may be easy to store the food.
폴리에스테르 수지는 산 성분과 디올 성분으로부터 유도되는 반복단위를 포함할 수 있다. 구체적으로, 폴리에스테르 수지는 디카복실산 성분과 글리콜 성분 또는 히드록시카복실산으로부터 합성된 방향족 및 지방족 폴리에스테르 수지로부터 이루어진 군으로부터 선택된 1종 이상일 수 있다. The polyester resin may include repeating units derived from an acid component and a diol component. Specifically, the polyester resin may be at least one selected from the group consisting of aromatic and aliphatic polyester resins synthesized from a dicarboxylic acid component and a glycol component or hydroxycarboxylic acid.
상기 폴리에스테르 수지는 예를 들어, 폴리에틸렌 테레프탈레이트(Polyethylene Terephthalate, PET), 폴리부틸렌 테레프탈레이트(Polybutylene Terephthalate, PBT), 폴리락트산(Poly Lactic acid, PLA), 폴리글리코르산(Polyglycolic acid, PGA), 폴리에틸렌 아디파트(Polyehtylene adipate, PEA), 폴리하이드로시알카노에이트(Polyhydroxyalkanoate, PHA), 폴리트리메틸렌 테레프탈레이트(Polytrimethylene Terephthalate, PTT) 및 폴리에틸렌 나프탈렌(Polyethylene naphthalate, PEN)로 이루어진 군으로부터 선택된 하나 이상일 수 있다. 일 예로, 본 발명에서는 폴리에틸렌 테레프탈레이트(Polyethylene Terephthalate, PET)가 사용될 수 있다.The polyester resin may be, for example, polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polylactic acid (PLA), polyglycolic acid (PGA) At least one selected from the group consisting of polyethylene adipate (PEA), polyhydroxyalkanoate (PHA), polytrimethylene terephthalate (PTT) and polyethylene naphthalate (PEN) have. For example, polyethylene terephthalate (PET) may be used in the present invention.
아울러, 상기 가스 베리어층(102)은, 에틸렌비닐알코올(ethylene vinyl alcohol, EVOH), 폴리비닐리덴클로라이드(polyvinylidene chloride, PVdC) 및 폴리에틸렌테레프탈레이트(polyethylene terephthalate, PET) 중 1 종 이상을 포함할 수 있다. In addition, the gas barrier layer 102 may include one or more of ethylene vinyl alcohol (EVOH), polyvinylidene chloride (PVDC), and polyethylene terephthalate (PET). have.
구체적으로, 상기 베리어층(102)은 에틸렌비닐알코올을 이용하여 형성할 수 있다. 이 경우, 포장용기 내부에 있는 식품에서 발생하는 가스는 밖으로 배출이 가능하며, 동시에 외부에서의 산소 공급은 차단할 수 있다.Specifically, the barrier layer 102 may be formed using ethylene vinyl alcohol. In this case, the gas generated from the food inside the packaging can be discharged out, and at the same time the oxygen supply from the outside can be blocked.
본 발명에 따른 성형체(10)는 다층 구조이며, 성형체(10)를 형성하는 다층 구조의 평균 두께는 1 mm 내지 5 mm 범위일 수 있다.The molded body 10 according to the present invention has a multilayer structure, and the average thickness of the multilayer structure forming the molded body 10 may range from 1 mm to 5 mm.
예를 들어, 성형체(10)는 3층 구조일 수 있으며, 이 경우, 3층 구조의 전체 두께는 평균 1.2 내지 4 mm, 1.5 내지 3.5 mm, 1.8 내지 3 mm 혹은 2 mm일 수 있다. 또한, 상기 가스 베리어층(102)의 평균 두께는 0.01 내지 2 mm일 수 있으며, 0.05 내지 2 mm, 0.1 내지 1.9 mm, 0.2 내지 1.85 mm, 0.3 내지 1.8 mm, 0.5 내지 1.6 mm, 0.7 내지 1.4 mm, 0.9 내지 1.2 mm, 또는 1 mm일 수 있다. For example, the molded body 10 may have a three-layer structure. In this case, the total thickness of the three-layer structure may be an average of 1.2 to 4 mm, 1.5 to 3.5 mm, 1.8 to 3 mm, or 2 mm. In addition, the average thickness of the gas barrier layer 102 may be 0.01 to 2 mm, 0.05 to 2 mm, 0.1 to 1.9 mm, 0.2 to 1.85 mm, 0.3 to 1.8 mm, 0.5 to 1.6 mm, 0.7 to 1.4 mm , 0.9 to 1.2 mm, or 1 mm.
아울러, 제1 발포시트(101) 및 제2 발포시트(101')의 평균 두께는 각각 0.5 내지 1.5 mm 일 수 있으며, 0.6 내지 1.3 mm, 0.7 내지 1.2 mm, 0.8 내지 1.0 mm, 0.9 내지 0.95 mm 일 수 있다. 본 발명의 성형체(10)는 상기 범위의 두께를 갖는 발포시트(101, 101') 및 가스 베리어층(102)으로 구성됨으로써, 상술된 산소 투과도 및 수증기 투과도를 만족시킬 수 있으며, 동시에 압축강도를 향상시키면서 경량성 등을 동시에 만족시킬 수 있다.In addition, the average thickness of the first foam sheet 101 and the second foam sheet 101 'may be 0.5 to 1.5 mm, respectively, 0.6 to 1.3 mm, 0.7 to 1.2 mm, 0.8 to 1.0 mm, 0.9 to 0.95 mm Can be. The molded body 10 of the present invention is composed of the foam sheet (101, 101 ') and the gas barrier layer 102 having a thickness in the above range, thereby satisfying the above-described oxygen permeability and water vapor permeability, and at the same time compressive strength While improving, it is possible to satisfy light weight and the like at the same time.
하나의 예시에서, 상기 제1 및 제2 발포시트(101, 101')의 융점(Tm) 은 평균 240 내지 260℃ 일 수 있다. 구체적으로, 제1 및 제2 발포시트(101, 101')의 평균 융점은 242℃ 내지 257℃, 245℃ 내지 255℃, 247℃ 내지 253℃, 또는 248℃ 내지 251℃ 일 수 있다. 일 예로, 폴리에틸렌 테레프탈레이트(polyethylene terephthalate) 수지를 포함하는 제1 및 제2 발포시트(101, 101')의 융점은 평균 248℃ 내지 251℃일 수 있다.In one example, the melting point (T m ) of the first and second foam sheets (101, 101 ') may be an average of 240 to 260 ℃. Specifically, the average melting points of the first and second foam sheets 101 and 101 'may be 242 ° C to 257 ° C, 245 ° C to 255 ° C, 247 ° C to 253 ° C, or 248 ° C to 251 ° C. For example, the melting points of the first and second foam sheets 101 and 101 'including the polyethylene terephthalate resin may be 248 ° C to 251 ° C on average.
아울러, 상기 가스 베리어층(102)의 융점(Tm) 은 평균 150℃ 내지 190℃ 일 수 있다. 구체적으로, 가스 베리어층(102)의 융점은 평균 150℃ 내지 190℃, 155℃ 내지 185℃, 160℃ 내지 180℃, 165℃ 내지 175℃ 또는 169℃ 내지 171℃ 일 수 있다. 일 예로, 에틸렌비닐알코올로 이루어진 가스 베리어층의 융점은 평균 170±0.5℃ 일 수 있다.In addition, the melting point (T m ) of the gas barrier layer 102 may be an average of 150 ℃ to 190 ℃. Specifically, the melting point of the gas barrier layer 102 may be an average of 150 ℃ to 190 ℃, 155 ℃ to 185 ℃, 160 ℃ to 180 ℃, 165 ℃ to 175 ℃ or 169 ℃ to 171 ℃. For example, the melting point of the gas barrier layer made of ethylene vinyl alcohol may be 170 ± 0.5 ° C. on average.
한편, 폴리에틸렌테레프탈레이트와 에틸렌비닐알코올은 큰 융점 차이로, 2층 구조(발포시트/가스 베리어층) 성형체의 성형시 에틸렌비닐알코올이 박리 또는 융해되어 성형체의 전체 면적에 상기 베리어층(102)을 고루 형성할 수 없는 등의 문제점이 있었으나, 상기 발포시트(101, 101')를 가스 베리어층(102) 양면에 각각 적층시킴으로써 상기 가스 베리어층(102)이 융해되어 없어지거나 발포시트(101, 101')로부터 박리되는 등의 문제점을 해결할 수 있다. On the other hand, polyethylene terephthalate and ethylene vinyl alcohol has a large melting point difference, and when the two-layer structure (foam sheet / gas barrier layer) molded body is formed, ethylene vinyl alcohol is peeled or melted, so that the barrier layer 102 is applied to the entire area of the molded body. Although there was a problem such that it cannot be formed evenly, the gas barrier layer 102 is melted away by laminating the foam sheets 101 and 101 'on both sides of the gas barrier layer 102, or the foam sheets 101 and 101 are laminated. Problems such as peeling off from ') can be solved.
하나의 예로서, 본 발명에 따른 성형체(10)는 바닥부(11) 및 바닥부(11)의 둘레를 따라 상단이 개방된 상태의 벽부(12)를 포함하고, 상기 수학식 1 에서 H/D 값은 0.01 내지 1.3, 0.05 내지 1.2, 0.1 내지 1.1, 0.3 내지 1.0, 0.4 내지 0.9, 0.5 내지 0.8, 0.55 내지 0.7 또는 0.6 내지 0.65 일 수 있다. 아울러, 상기 수학식 1에서 H 값은 1 내지 10 cm일 수 있다. 일 예로, 성형체(10)의 개구부의 직경이 10 cm 일 수 있으며, 수용부의 깊이가 3 cm 일 수 있다. 아울러, 본 발명에 따른 성형체(10)는 용기형상일 수 있으며, 원통형의 용기형상 또는 사각형의 용기형상일 수 있다.As an example, the molded body 10 according to the present invention includes a bottom portion 11 and a wall portion 12 having an open top along a circumference of the bottom portion 11, and in the equation (1), H / The D value may be 0.01 to 1.3, 0.05 to 1.2, 0.1 to 1.1, 0.3 to 1.0, 0.4 to 0.9, 0.5 to 0.8, 0.55 to 0.7 or 0.6 to 0.65. In addition, in Equation 1, the H value may be 1 to 10 cm. For example, the diameter of the opening of the molded body 10 may be 10 cm, the depth of the receiving portion may be 3 cm. In addition, the molded body 10 according to the present invention may have a container shape, and may have a cylindrical container shape or a rectangular container shape.
한편, 본 발명에 따른 성형체(10)는 상기 가스 베리어층(102)의 양면에 각각 제1 및 제2 발포시트(101, 101')를 형성함으로써, 하기 수학식 2를 만족하는 성형체(10)를 제공할 수 있다:Meanwhile, the molded body 10 according to the present invention forms the first and second foam sheets 101 and 101 'on both surfaces of the gas barrier layer 102, thereby satisfying the following equation (2). Can provide:
[수학식 2][Equation 2]
|T2 - T1| ≥ 10℃T 2 -T 1 | ≥ 10 ℃
상기 수학식 2에서,In Equation 2,
T1 는 20℃, 1 atm 조건에서, 성형체에 100℃의 물을 담고, 1분 경과 되었을 때 측정한 성형체의 외측 표면 온도이며,T 1 is the outer surface temperature of the molded body measured when 1 minute has elapsed by containing 100 ° C water in the molded body at 20 ° C and 1 atm conditions,
T2 은 20℃, 1 atm 조건에서, 성형체에 100℃의 물을 담고, 1분 경과 되었을 때 측정한 성형체 내부의 물의 온도이다.T 2 is the temperature of the water inside the molded body measured when 1 minute has elapsed after 100 minutes of water is contained in the molded body at 20 ° C. and 1 atm conditions.
본 발명에 따른 성형체(10)는 제 1, 2 발포시트(101, 101')를 포함함으로써, 열차단성이 우수함을 나타낸다. 구체적으로, 상온(20℃), 1 기압 조건에서, 성형체 내부에 100℃의 물을 70 %(v/v) 담은 상태에서, 1분 경과된 시점에서, 성형체 내부 물의 온도와 성형체 외부 표면의 온도차가 10℃ 이상일 수 있다. 이는 본 발명에 따른 성형체(10)가 열차단성이 우수함을 나타내는데, 구체적으로, 제조된 성형체에 100℃의 물을 70%(v/v) 담은 상태에서 1 분 경과된 시점에서, 성형체(10) 내부에 수용된 물의 온도와 성형체(10) 외부 표면의 온도차이다.The molded article 10 according to the present invention includes the first and second foam sheets 101 and 101 ', indicating excellent thermal barrier properties. Specifically, at room temperature (20 ° C.) and 1 atm, the temperature difference between the water temperature inside the molded body and the outer surface of the molded body is 1 minute after 100 minutes of water at 100 ° C. (v / v) is contained in the molded body. May be greater than or equal to 10 ° C. This indicates that the molded body 10 according to the present invention has excellent thermal barrier properties. Specifically, when the molded product 10 has passed 70 minutes (v / v) of water at 100 ° C. in one minute, the molded body 10 is formed. It is the temperature difference between the temperature of the water contained therein and the outer surface of the molded body 10.
하나의 예로써, 본 발명에 따른 성형체(10)에 100℃의 물을 70%(v/v) 담은 상태에서, 1분 경과된 시점에 성형체 외부 온도가 40℃ 인 경우, 성형체(10) 내부에 수용된 물의 온도는 95℃ 일 수 있다. 본 발명에 따른 성형체(10)는 상기 조건에서 성형체(10) 내부에 수용된 물의 온도와 성형체(10) 외부 표면의 온도차를 비교적 높게 유지함으로써, 열차단성이 우수함을 알 수 있으며, 이로 인해 식품의 보온을 효과적으로 향상시키는 효과를 나타낸다.As an example, in the state in which the molded body 10 according to the present invention contains 70% (v / v) of water at 100 ° C., when the external temperature of the molded body is 40 ° C. at 1 minute, the molded body 10 is inside. The temperature of the water accommodated in may be 95 ° C. The molded body 10 according to the present invention can be seen that the thermal barrier property is excellent by maintaining a relatively high temperature difference between the temperature of the water accommodated inside the molded body 10 and the outer surface of the molded body 10 under the above conditions, thereby keeping food warm The effect is to effectively improve.
한편, 본 발명의 제1 및 제2 발포시트(101, 101')는 각각 0.5 내지 9 중량% 의 탄산칼슘(CaCO3)을 포함할 수 있다.Meanwhile, the first and second foam sheets 101 and 101 ′ of the present invention may each include 0.5 to 9 wt% of calcium carbonate (CaCO 3 ).
구체적으로, 상기 탄산칼슘(CaCO3)은 무기입자로, 상기와 같은 무기입자를 포함함으로써, 본 발명의 제1 및 제2 발포시트(101, 101')는 시트표면이 균일하며 우수한 열 성형성을 나타낼 수 있다.Specifically, the calcium carbonate (CaCO 3 ) is an inorganic particle, by including the inorganic particles as described above, the first and second foam sheets (101, 101 ') of the present invention is uniform sheet surface and excellent thermoformability Can be represented.
상기 탄산칼슘의 열전도율은 1.0 kcal/mh℃ 내지 3.0 kcal/mh℃일 수 있다. 구체적으로, 탄산칼슘의 열전도율은 1.2 kcal/mh℃ 내지 2.5 kcal/mh℃, 1.5 kcal/mh℃ 내지 2.2 kcal/mh℃ 또는 1.8 kcal/mh℃ 내지 2.0 kcal/mh℃ 일 수 있다. 보다 구체적으로, 탄산칼슘의 열전도율은 1.5 kcal/mh℃ 내지 2.5 kcal/mh℃ 또는 1.8 kcal/mh℃ 내지 2.3 kcal/mh℃일 수 있다. 상기와 같이 탄산칼슘을 포함하는 제1 및 제2 발포시트(101, 101')는 우수한 열전도율을 나타냄으로써 균일한 표면을 가지고, 우수한 열 성형성을 나타낼 수 있다.The thermal conductivity of the calcium carbonate may be 1.0 kcal / mh ℃ to 3.0 kcal / mh ℃. Specifically, the thermal conductivity of calcium carbonate may be 1.2 kcal / mh ° C. to 2.5 kcal / mh ° C., 1.5 kcal / mh ° C. to 2.2 kcal / mh ° C. or 1.8 kcal / mh ° C. to 2.0 kcal / mh ° C. More specifically, the thermal conductivity of calcium carbonate may be 1.5 kcal / mh ℃ to 2.5 kcal / mh ℃ or 1.8 kcal / mh ℃ to 2.3 kcal / mh ℃. As described above, the first and second foam sheets 101 and 101 'including calcium carbonate exhibit excellent thermal conductivity and thus have a uniform surface, and may exhibit excellent thermoformability.
예를 들어, 상기 탄산칼슘의 함량은 0.5 내지 9 중량%일 수 있다. 구체적으로, 탄산칼슘의 함량은 0.5 내지 8 중량 %, 0.6 내지 7 중량 %, 0.7 내지 6 중량 %, 0.8 내지 5 중량 %, 0.9 내지 4 중량 %, 1.0 내지 3.0 중량 %, 2 중량% 내지 3.5 중량%일 수 있다 일 예로, 1.0 중량 % 또는 3 중량 % 일 수 있다.For example, the content of calcium carbonate may be 0.5 to 9% by weight. Specifically, the calcium carbonate content is 0.5 to 8% by weight, 0.6 to 7% by weight, 0.7 to 6% by weight, 0.8 to 5% by weight, 0.9 to 4% by weight, 1.0 to 3.0% by weight, 2 to 3.5% by weight For example, it may be 1.0% by weight or 3% by weight.
하나의 예시에서, 발포시트(101, 101')의 밀도(KS M ISO 845) 는 평균 300 내지 700 kg/m3 일 수 있다. 구체적으로, 발포시트(101, 101')의 밀도는 평균 325 내지 650 kg/m3, 350 내지 600 kg/m3, 375 내지 550 kg/m3, 400 내지 500 kg/m3 또는 425 내지 450 kg/m3일 수 있다. In one example, the density of the foam sheets 101 and 101 '(KS M ISO 845) may be on average 300 to 700 kg / m 3 . Specifically, the density of the foam sheet (101, 101 ') is an average of 325 to 650 kg / m 3 , 350 to 600 kg / m 3 , 375 to 550 kg / m 3 , 400 to 500 kg / m 3 or 425 to 450 kg / m may be 3 days.
다른 하나의 예시에서, 본 발명에 따른 발포시트(101, 101')는 200℃에서 10초의 조건에서 고온신율은 325 내지 375%일 수 있다. 구체적으로, 발포시트(101, 101')는 200℃에서 10초의 조건에서 고온신율은 330 내지 360%, 345 내지 370% 또는 335 내지 360%일 수 있다. 보다 구체적으로, 발포시트(101, 101')는 200℃에서 10초의 조건에서 고온신율은 345 내지 355%일 수 있다.In another example, the foam sheets 101 and 101 'according to the present invention may have a high temperature elongation of 325 to 375% at 200 ° C for 10 seconds. Specifically, the high temperature elongation of the foam sheet (101, 101 ') for 10 seconds at 200 ℃ may be 330 to 360%, 345 to 370% or 335 to 360%. More specifically, the foam sheets 101 and 101 'may have a high temperature elongation of 345 to 355% at 200 ° C for 10 seconds.
상기와 같은 폴리에스테르 및 탄산칼슘를 포함함으로써, 본 발명에 따른 발포시트(101, 101')는 우수한 가공성을 나타낼 수 있다. By including the polyester and calcium carbonate as described above, the foam sheet (101, 101 ') according to the present invention can exhibit excellent workability.
본 발명에 따른 성형체(10)의 제1 및 제2 발포시트(101, 101')는 폴리에스테르 수지의 발포체이며, 상기 제1 및 제2 발포시트(101, 101')의 폴리에스테르 수지는 폴리에틸렌 테레프탈레이트 (Polyethylene Terephthalate, PET) 수지일 수 있다. 상기 PET 수지를 사용함으로써, 친환경적이며, 재사용에 용이할 수 있다.The first and second foam sheets 101 and 101 'of the molded body 10 according to the present invention are foams of a polyester resin, and the polyester resin of the first and second foam sheets 101 and 101' is polyethylene. It may be a terephthalate (polyethylene terephthalate, PET) resin. By using the PET resin, it may be environmentally friendly and easy to reuse.
식품의약품안전처의 기구 및 용기포장과 그 원재료에 관한 규격을 기준으로, 용출규격 측정 시, 총 용출량이 30ppm 이하이고, 안티몬 게르마늄, 테레프탈산, 이소프탈산, 아세트 알데하이드 물질이 불검출되며, 잔류규격 측정 시, 휘발성 물질이 검출되지 않는 것을 특징으로 한다.Based on the standards of equipment and container packaging and raw materials of the Ministry of Food and Drug Safety and its raw materials, total elution amount is 30ppm or less, antimony germanium, terephthalic acid, isophthalic acid and acetaldehyde are not detected when measuring elution standard. Volatile substances are not detected.
구체적으로, 본 발명에 따른 성형체(10)는 상기와 같이 친환경 소재인 폴리에스테르 수지를 사용함으로써, 대한민국 식품의약품안전처에서 발행하고 있는 기구 및 용기포장의 기준 및 규격 고시전문고시 제2015-7호에 기재된 우려 물질들을 허용 범위 내로 조절할 수 있다.Specifically, the molded article 10 according to the present invention by using the polyester resin which is an environmentally friendly material as described above, the standards and specifications of the Agency and container packaging issued by the Ministry of Food and Drug Safety Republic of Korea Notice No. 2015-7 The substances of concern described in the above can be adjusted within the allowable range.
이와 같은 소재를 이용한 성형체(10)를 이용하여 식품 포장용기(10)를 제조함으로써, 친환경적인 식품 용기를 제공할 수 있다.By manufacturing the food packaging container 10 using the molded body 10 using such a material, it is possible to provide an environmentally friendly food container.
하나의 예로서, 본 발명에 따른 성형체(10)는, 배리어(Barrier) 성능, 친수화 기능 또는 방수 기능을 가질 수 있으며, 계면활성제, 친수화제, 열안정제, 방수제, 셀 크기 확대제, 적외선 감쇠제, 가소제, 방화 화학 약품, 안료, 탄성폴리머, 압출 보조제, 산화방지제, 공전 방지제 및 UV 흡수제로 이루어진 군으로부터 선택되는 하나 이상의 기능성 첨가제를 더 포함할 수 있다. 구체적으로, 본 발명의 수지 발포시트는 증점제, 열안정제 및 발포제를 포함할 수 있다.As an example, the molded body 10 according to the present invention may have a barrier performance, a hydrophilization function or a waterproof function, and may include a surfactant, a hydrophilizing agent, a heat stabilizer, a waterproofing agent, a cell size expander, and an infrared attenuation. It may further comprise one or more functional additives selected from the group consisting of plasticizers, fire protection chemicals, pigments, elastomers, extrusion aids, antioxidants, anti-static agents and UV absorbers. Specifically, the resin foam sheet of the present invention may include a thickener, a heat stabilizer and a foaming agent.
상기 증점제는 특별히 한정하지 않으나, 본 발명에서는 예를 들면 피로멜리트산 이무수물(PMDA)가 사용될 수 있다.The thickener is not particularly limited, but for example, pyromellitic dianhydride (PMDA) may be used in the present invention.
상기 열안정제는, 유기 또는 무기 인 화합물일 수 있다. 상기 유기 또는 무기 인 화합물은, 예를 들어, 인산 및 그 유기 에스테르, 아인산 및 그 유기 에스테르일 수 있다. 예를 들어, 상기 열안정제는 상업적으로 입수 가능한 물질로서, 인산, 알킬 포스페이트 또는 아릴 포스페이트일 수 있다. 구체적으로, 본 발명에서 열안정제는 트리페닐 포스페이트일 수 있으나, 이에 제한되는 것은 아니며, 상기 수지 발포시트의 열적 안정성을 향상시킬 수 있는 것이라면, 통상적인 범위 내에서 제한 없이 사용 가능하다.The heat stabilizer may be an organic or inorganic phosphorus compound. The organic or inorganic phosphorus compound may be, for example, phosphoric acid and its organic ester, phosphorous acid and its organic ester. For example, the thermal stabilizer is a commercially available material and may be phosphoric acid, alkyl phosphate or aryl phosphate. Specifically, in the present invention, the thermal stabilizer may be triphenyl phosphate, but is not limited thereto. If the thermal stabilizer is capable of improving the thermal stability of the resin foam sheet, the thermal stabilizer may be used without limitation.
상기 발포제의 예로는, N2, CO2, 프레온, 부탄, 펜탄, 네오펜탄, 헥산, 이소헥산, 헵탄, 이소헵탄, 메틸클로라이드 등의 물리적 발포제 또는 아조디카르본아마이드(azodicarbonamide)계 화합물, P,P'-옥시비스(벤젠술포닐하이드라지드)[P,P'-oxy bis (benzene sulfonyl hydrazide)]계 화합물, N,N'-디니트로소펜타메틸렌테트라아민(N,N'-dinitroso pentamethylene tetramine)계 화합물 등의 화학적 발포제가 있으며, 구체적으로 본 발명에서는 CO2가 사용될 수 있다.Examples of the blowing agent may include physical blowing agents such as N 2 , CO 2 , freon, butane, pentane, neopentane, hexane, isohexane, heptane, isoheptane, methyl chloride, or azodicarbonamide compounds, P, P'-oxybis (benzenesulfonylhydrazide) [P, P'-oxy bis (benzene sulfonyl hydrazide)] compound, N, N'-dinitrosopentamethylenetetraamine (N, N'-dinitroso pentamethylene chemical blowing agents such as tetramine-based compounds, and specifically, CO 2 may be used in the present invention.
또한, 본 발명은 성형체의 제조방법을 제공한다.Moreover, this invention provides the manufacturing method of a molded object.
도 2는 본 발명에 따른 성형체의 제조방법을 순차적으로 도시한 도면이다. 도 2를 참조하면, 본 발명은,2 is a view sequentially showing a method for producing a molded article according to the present invention. 2, the present invention,
제1 발포시트, 가스 베리어층 및 제2 발포시트가 순차적으로 적층된 구조의 시트(1)를 성형장치의 암형 금형(21)과 수형 금형(22) 사이에 배치하는 단계; 및Disposing a sheet 1 having a structure in which the first foam sheet, the gas barrier layer and the second foam sheet are sequentially stacked between the female mold 21 and the male mold 22 of the molding apparatus; And
수형 금형(22)을 가압하여 성형체(10)를 성형하는 단계를 포함하며,Pressing the male mold 22 to form the molded body 10,
상기 제1 발포시트 및 제2 발포시트는 폴리에스테르 수지의 발포체인 것을 특징으로 하는 성형체의 제조방법을 제공한다.The first foam sheet and the second foam sheet provides a method for producing a molded body, characterized in that the foam of the polyester resin.
한편, 제1 및 제2 발포시트에 대한 제조방법은 구체적으로 한정되지 않으나, 예를 들어, 제1 및 제2 발포시트는 폴리에스테르 수지를 압출 발포하여 제조할 수 있다. 구체적으로, 발포 방법의 종류에는 크게 비드 발포 또는 압출 발포가 있다. 상기 비드 발포는, 일반적으로, 수지 비드를 가열하여 1차 발포시키고 이것을 적당한 시간 숙성 시킨 후 판모양, 통모양의 금형에 채우고 다시 가열하여 2차 발포에 의해 융착, 성형하여 제품을 만드는 방법이다. 반면, 압출 발포는 수지를 가열하여 용융시키고, 상기 수지 용융물을 연속적으로 압출 및 발포시킴으로써, 공정 단계를 단순화할 수 있으며, 대량 생산이 가능하며, 비드 발포 시의 비드 사이에서 균열과, 입상 파괴 현상 등을 방지할 수 있다.On the other hand, the manufacturing method for the first and second foam sheet is not specifically limited, for example, the first and second foam sheet can be produced by extrusion foaming the polyester resin. Specifically, the type of foaming method includes bead foaming or extrusion foaming. In general, the bead foaming is a method of forming a product by heating a resin bead and primary foaming, aging it for a suitable time, and then filling the mold in a plate or cylindrical shape and then heating it to be fused and molded by secondary foaming. Extrusion foam, on the other hand, heats and melts the resin and continuously extrudes and foams the resin melt, thereby simplifying the process steps, enabling mass production, and cracking and granular fracture between beads during bead foaming. Etc. can be prevented.
다음으로, 가공하는 단계는 제1 발포시트, 가스 베리어층 및 제2 발포시트가 순차적으로 적층된 구조의 시트(1)를 성형체 성형장치(20)의 암형 금형(21)과 수형 금형(22) 사이에 배치하는 단계 및 수형 금형(22)을 가압하여 성형체 (10)를 성형하는 단계를 제공한다.Next, the step of processing the sheet 1 having a structure in which the first foam sheet, the gas barrier layer and the second foam sheet are sequentially stacked, the female mold 21 and the male mold 22 of the molded body molding apparatus 20. And forming the molded body 10 by pressing the male mold 22.
구체적으로, 암형 금형(21)과 수형 금형(22) 사이에 배치된 시트(1) 는 열 성형됨으로써 성형체(10)로 성형될 수 있다. 상기 열 성형으로는 진공 성형, 압공 성형 또는 진공 성형과 압공 성형을 조합한 진공 압공 성형, 수형 금형(플러그)을 사용하면서 또는 수형 금형(22)을 사용한 후, 진공 및/또는 압공 성형하는 등의 열 성형될 수 있다.Specifically, the sheet 1 disposed between the female mold 21 and the male mold 22 may be molded into the molded body 10 by thermoforming. Examples of the thermoforming include vacuum forming, pressure forming, or vacuum press forming a combination of vacuum forming and pressure forming, using a male mold (plug), or using the male mold 22, followed by vacuum and / or press forming. Can be thermoformed.
도 2를 참조하면, 도 2의 (a)는 시트(1)를 성형하기 전, 시트(1)를 성형장치의 암형 금형(21)과 수형 금형(22) 사이에 배치하는 배치단계를 나타낸다. 도 2(b)는 연신 공정 및 열 공정을 나타내는 도면으로, 도 2(b)와 같이, 수형 금형(22)을 하강하여 시트(1)를 연신하고, 암형 금형(21)으로부터의 진공 흡인에 의해 암형 금형(21)의 캐비티의 형상으로 부형되며, 열이 가해진다. 도 2(c)는 수형 금형(22)의 가압과 암형 금형(21)으로부터 압축 공기에 의해, 성형되고 있는 시트(1)를 수형 금형(22)의 형상으로 부형되어 최종 성형품인 성형체(10)가 성형되는 것을 나타낸다. 다음으로, 성형된 성형체 (10)는 냉각 후 수형 금형(22)을 상승시켜 취출될 수 있다.Referring to FIG. 2, (a) of FIG. 2 shows an arrangement step in which the sheet 1 is disposed between the female mold 21 and the male mold 22 of the molding apparatus before the sheet 1 is molded. FIG. 2 (b) is a drawing showing the stretching process and the thermal process. As shown in FIG. 2 (b), the male mold 22 is lowered to stretch the sheet 1, and vacuum suction from the female mold 21 is performed. It shapes by the shape of the cavity of the female die 21, and heat is applied. Fig. 2 (c) shows the molded body 10 which is a final molded product by shaping the sheet 1 being formed into the shape of the male mold 22 by pressurization of the male mold 22 and compressed air from the female mold 21. Indicates that is molded. Next, the molded body 10 may be taken out by raising the male mold 22 after cooling.
아울러, 성형하는 단계는, 시트 표면 온도가 140 내지 160℃ 되도록 열을 인가하고, 상기 암형 금형(21) 및 수형 금형(22)의 표면 온도를 60℃ 내지 200℃ 로 설정하여 성형체(10)를 성형할 수 있다.In addition, in the forming step, heat is applied such that the sheet surface temperature is 140 to 160 ° C, and the surface temperature of the female mold 21 and the male mold 22 is set to 60 ° C to 200 ° C to form the molded body 10. It can be molded.
한편, 성형단계에서 수형 금형(22)의 표면과 암형 금형(21)의 캐비티 표면 온도는 서로 다를 수 있다. 바람직하게는 수형 금형(22)의 표면 온도는 각각 250 내지 280℃, 255 내지 275℃, 260 내지 270℃ 또는 265℃ 일 수 있으며, 암형 금형(21)의 캐비티 표면 온도는 200 내지 250℃, 210 내지 240℃, 215 내지 235℃, 220 내지 230℃ 또는 225±3℃ 일 수 있다.Meanwhile, in the molding step, the surface of the male mold 22 and the cavity surface temperature of the female mold 21 may be different from each other. Preferably, the surface temperature of the male mold 22 may be 250 to 280 ° C, 255 to 275 ° C, 260 to 270 ° C or 265 ° C, respectively, and the cavity surface temperature of the female mold 21 may be 200 to 250 ° C or 210 ° C. To 240 ° C., 215 to 235 ° C., 220 to 230 ° C., or 225 ± 3 ° C.
하나의 예시로, 수형 금형(22)의 표면 온도가 265±1℃일 수 있으며, 암형 금형(21)의 표면 온도가 225℃ 일 수 있으며, 수형 금형(22)은 0.5초 내지 15초 동안 암형 금형(22)에 접촉시키는 것이 바람직하다. 아울러, 암형 금형(21)은 일측에 내부 공간인 캐비티를 감압하기 위한 감압홀(23)이 형성된 구조일 수 있다.In one example, the surface temperature of the male mold 22 may be 265 ± 1 ° C., the surface temperature of the female mold 21 may be 225 ° C., and the male mold 22 may be female for 0.5 to 15 seconds. It is preferable to contact the mold 22. In addition, the female mold 21 may have a structure in which a decompression hole 23 for depressurizing a cavity, which is an internal space, is formed at one side.
이에 따라, 상술한 성형체의 제조방법에 의해서 폴리에스테르 수지의 제1 발포시트, 가스 베리어층, 및 폴리에스테르 수지의 제2 발포시트가 순차적으로 적층된 용기 형상의 성형체 또는 상기 성형체를 포함하는 포장용기를 제조할 수 있다. Accordingly, the container-shaped molded article or the packaging container including the molded article, in which the first foam sheet of the polyester resin, the gas barrier layer, and the second foam sheet of the polyester resin are sequentially laminated by the method of manufacturing the molded article described above. Can be prepared.
이하, 본 발명을 실시예 및 실험예에 의해 보다 상세히 설명한다.Hereinafter, the present invention will be described in more detail with reference to Examples and Experimental Examples.
단, 하기 실시예 및 실험예는 본 발명을 예시하는 것일 뿐, 본 발명의 내용이 하기 실시예 및 실험예에 한정되는 것은 아니다.However, the following Examples and Experimental Examples are only illustrative of the present invention, and the content of the present invention is not limited to the following Examples and Experimental Examples.
제조예 1.Preparation Example 1.
PET 수지 100 중량부를 130℃ 에서 건조하여 수분을 제거하였고, 제1 압출기에서 상기 수분이 제거된 PET 수지 100 중량부, PMDA(pyromellitic dianhydride) 1 중량부, 탄산칼슘(CaCO3) 1 중량부, Irganox (IRG 1010) 0.1 중량부를 혼합하고, 280℃로 가열하여 수지 용융물을 제조하였다. 그런 다음, 제1 압출기에 발포제로서 부탄 가스를 혼합하고, 수지 용융물을 제2 압출기로 보내 220℃ 로 냉각하였다. 냉각된 수지 용융물은 다이(Die) 를 통과하면서 발포시트를 형성하였다.100 parts by weight of PET resin was dried at 130 ° C. to remove moisture, and 100 parts by weight of the PET resin from which the water was removed in the first extruder, 1 part by weight of pyromellitic dianhydride (PMDA), 1 part by weight of calcium carbonate (CaCO 3 ), Irganox (IRG 1010) 0.1 part by weight was mixed and heated to 280 ° C. to prepare a resin melt. Then, butane gas was mixed as a blowing agent in the first extruder, and the resin melt was sent to the second extruder and cooled to 220 ° C. The cooled resin melt passed through a die to form a foam sheet.
이때, 제조된 폴리에스테르 수지 발포시트의 밀도는 380 kg/m3였으며, 두께는 1 mm이였다.At this time, the density of the prepared polyester resin foam sheet was 380 kg / m 3 , the thickness was 1 mm.
실시예 1Example 1
제조예 1에서 제조한 발포시트의 일면에 베리어층으로 0.05 mm의 EVOH 필름을 라미네이팅 하고, 그 위에 제조예 1에서 제조한 발포시트를 적층하였다. 그리고, 적층한 3층 구조의 시트를 용기 형상으로 성형하여, H/D = 0.3 인 성형체(H: 수용부의 깊이 D: 개구부의 직경)를 제조하였다. 상기 성형체의 개구부 직경은 10 cm 였다. 한편, 성형체의 성형시, 수형 금형의 표면온도는 60℃ 이며, 암형 금형의 표면온도는 120℃ 였다.Laminating a 0.05 mm EVOH film with a barrier layer on one surface of the foam sheet prepared in Preparation Example 1, and laminated on the foam sheet prepared in Preparation Example 1 thereon. And the laminated three-layered sheet was shape | molded to container shape, and the molded object (H: depth D: diameter of opening part) with H / D = 0.3 was manufactured. The opening diameter of the molded body was 10 cm. On the other hand, at the time of shaping | molding of a molded object, the surface temperature of the male mold was 60 degreeC, and the surface temperature of the female mold was 120 degreeC.
실시예 2. Example 2.
배리어층으로는 EVOH 0.02 mm 와 PET 0.03 mm 필름 2 Layer로 구성된 것을 제외하고, 실시예 1과 동일한 방법으로 성형체를 제조하였다. A molded article was prepared in the same manner as in Example 1, except that the barrier layer was composed of an EVOH 0.02 mm film and a PET 0.03 mm film 2 layer.
실시예 3. Example 3.
H/D 의 값이 0.5 인 것을 제외하곤 실시예 1과 동일한 방법으로 성형체를 제조하였다.A molded article was prepared in the same manner as in Example 1 except that the value of H / D was 0.5.
비교예 1Comparative Example 1
두께가 2mm인 것을 제외하고, 제조예 1과 동일한 방법으로 제조한 발포시트의 일면에 베리어층으로 0.05 mm의 EVOH 필름을 라미네이팅 하여 2 층 구조의 시트를 제조하였다. 그리고, 적층한 2 층 구조의 시트를 용기 형상으로 성형하여, H/D = 0.3인 성형체(H: 수용부의 깊이 D: 개구부의 직경)를 제조하였다. 상기 성형체의 개구부 직경은 10 cm 였다. 한편, 수형 금형의 표면온도는 60℃이며, 암형 금형의 표면온도는 120℃ 였다.Except that the thickness is 2mm, a sheet of a two-layer structure was prepared by laminating a 0.05 mm EVOH film with a barrier layer on one surface of the foam sheet prepared in the same manner as in Preparation Example 1. And the laminated 2-layered sheet was shape | molded to container shape, and the molded object (H: depth D: diameter of an opening part) with H / D = 0.3 was manufactured. The opening diameter of the molded body was 10 cm. In addition, the surface temperature of the male mold was 60 degreeC, and the surface temperature of the female mold was 120 degreeC.
비교예 2Comparative Example 2
PP 다층시트 (PP/EVOH/PP)를 사용하여 H/D 0.3의 실시예 1과 동일한 구조의 용기를 성형하였고, 성형할 때 금형의 온도는 20℃를 유지하였다.Using a PP multilayer sheet (PP / EVOH / PP), a container having the same structure as in Example 1 of H / D 0.3 was molded, and the temperature of the mold was maintained at 20 ° C. when molding.
실시예 및 비교예에서 성형체의 시트 종류 및 성형 조건을 아래의 표 1과 같이 달리하여 성형체를 제조하였다.In Examples and Comparative Examples, the molded article was manufactured by changing sheet types and molding conditions of the molded article as shown in Table 1 below.
실시예 1Example 1 실시예 2Example 2 실시예 3Example 3 비교예 1Comparative Example 1 비교예 2Comparative Example 2
Layer 층Layer Layer PET FormPET Form PET FormPET Form PET FormPET Form PET FormPET Form PPPP
EVOHEVOH EVOH+PETEVOH + PET EVOHEVOH EVOHEVOH EVOHEVOH
PET FormPET Form PET FormPET Form PET FormPET Form PPPP
가스 베리어층의 두께(mm)Thickness of gas barrier layer (mm) EVOH 0.05EVOH 0.05 EVOH 0.02+PET 0.03EVOH 0.02 + PET 0.03 EVOH 0.05EVOH 0.05 EVOH 0.05EVOH 0.05 EVOH 0.05EVOH 0.05
성형 조건 (H/D)Molding condition (H / D) 0.30.3 0.30.3 0.50.5 0.30.3 0.30.3
실험예 1. 산소 투과도 측정Experimental Example 1. Measurement of oxygen permeability
실시예와 비교예에서 제조한 성형체에 대하여, 23℃ 의 온도 및 50% 의 상대습도 조건 하에서 산소 투과도를 측정하였다. 한편, 가스 베리어층이 성형체 내에 고루 분포되었는지를 확인하기 위하여, 성형체의 시편을 랜덤하게 잘라서 측정하였다. 그리고, 그 결과는 하기 표 2에 나타내었다.Oxygen permeability was measured with respect to the molded object produced by the Example and the comparative example under the temperature of 23 degreeC, and the relative humidity conditions of 50%. On the other hand, in order to confirm whether the gas barrier layer was evenly distributed in the molded body, the specimens of the molded body were randomly cut and measured. The results are shown in Table 2 below.
<산소 투과도 시험>Oxygen Permeability Test
- 시험방법: ASTM D 3985Test Method: ASTM D 3985
- 시험기기: OX-TRAN 702 (MOCON 사, 미국)Tester: OX-TRAN 702 (MOCON, USA)
- 시험온도: 23℃-Test temperature: 23 ℃
- 시험시간: 30분-Exam time: 30 minutes
- 측정범위: 0.1 ~ 2000 cc/m2dayMeasuring range: 0.1 to 2000 cc / m 2 day
- 시편 크기: 가로×세로×높이 40㎜×40㎜×3㎜-Specimen size: width × length × height 40mm × 40mm × 3mm
실시예 1Example 1 실시예 2Example 2 실시예 3Example 3 비교예 1Comparative Example 1 비교예 2Comparative Example 2
산소 투과도(cc/m2day)Oxygen Permeability (cc / m 2 Day) 22 33 77 1515 22
상기 표 2를 참조하면, 본 발명에 따른 성형체 산소 투과도가 낮은 것을 확인할 수 있으며, 이에 따라 산소의 투과를 거의 방지할 수 있다는 것을 알 수 있다. 이는, 가스 베리어층이 성형체의 전체 면적에 고루 분포되어 있음을 의미한다. 반면, 비교예 1의 성형체는 산소 투과도가 높은 것을 확인할 수 있었다. 이는, 성형체의 성형시 가스 베리어층이 손상된 것으로 판단된다. 아울러, 비발포 제품인 비교예 2의 경우, 산소 투과도가 낮으나 후술하게 되는 열차단성 시험에서 열차단성이 우수하지 못한 것을 확인할 수 있다.Referring to Table 2, it can be seen that the molded article oxygen permeability according to the present invention is low, thereby can be almost prevented from permeation of oxygen. This means that the gas barrier layer is evenly distributed over the entire area of the molded body. On the other hand, it was confirmed that the molded article of Comparative Example 1 had high oxygen permeability. It is determined that the gas barrier layer is damaged during molding of the molded body. In addition, in the case of Comparative Example 2 which is a non-foaming product, the oxygen permeability is low, but it can be confirmed that the thermal barrier property is not excellent in the thermal barrier test described later.
반면, 비교예 1의 성형체는 산소 투과도가 높은 것을 확인할 수 있었다. 이는, 성형체의 성형시 가스 베리어층이 손상된 것으로 판단된다. 아울러, 비발포 제품인 비교예 2의 경우, 산소 투과도가 낮으나 후술하게 되는 열차단성 시험에서 열차단성이 우수하지 못한 것을 확인할 수 있다.On the other hand, it was confirmed that the molded article of Comparative Example 1 had high oxygen permeability. It is determined that the gas barrier layer is damaged during molding of the molded body. In addition, in the case of Comparative Example 2 which is a non-foaming product, the oxygen permeability is low, but it can be confirmed that the thermal barrier property is not excellent in the thermal barrier test described later.
실험예 2. 수증기 투과도 측정 Experimental Example 2. Water vapor permeability measurement
실시예와 비교예에서 제조한 성형체에 대하여, ASTM F 1249 를 기준으로, 37℃ 의 온도 및 100 % 의 상대습도 조건 하에서, 수증기 투과도를 측정하였다. 그리고, 그 결과를 하기 표 3에 나타내었다.Water vapor permeability was measured for the molded products prepared in Examples and Comparative Examples under a temperature of 37 ° C. and a relative humidity of 100% based on ASTM F 1249. The results are shown in Table 3 below.
실시예 1Example 1 실시예 2Example 2 실시예 3Example 3 비교예 1Comparative Example 1 비교예 2Comparative Example 2
수증기 투과도(g/m2day)Water vapor transmission rate (g / m 2 day) 8.58.5 1717 1818 1919 33
표 3을 참조하면, 실시예 1-3에 따른 성형체의 경우, 각각 8.5 g/m2day, 17 g/m2day 및 18 g/m2day 으로 낮은 결과를 보였다. 이는, 가스 베리어층이 성형체의 전체 면적에 고루 분포되어 있음을 의미한다.아울러, 비교예 1의 경우, 19 g/m2day 로 실시예보다 높은 결과를 보였다. 이는 비교예 1 성형체의 성형시 가스 베리어층이 손상된 것으로 판단된다. 아울러, 비발포 제품인 비교예 2의 경우, 산소 투과도가 낮으나 후술하게 되는 열차단성 시험에서 열차단성이 우수하지 못한 것을 확인할 수 있다.Referring to Table 3, in the case of the molded article according to Example 1-3, the results were low as 8.5 g / m 2 day, 17 g / m 2 day and 18 g / m 2 day, respectively. This means that the gas barrier layer is evenly distributed over the entire area of the molded body. In addition, in the case of Comparative Example 1, 19 g / m 2 day was higher than the Example. It is judged that the gas barrier layer is damaged during molding of the molded article of Comparative Example 1. In addition, in the case of Comparative Example 2 which is a non-foaming product, the oxygen permeability is low, but it can be confirmed that the thermal barrier property is not excellent in the thermal barrier test described later.
실험예 3. 열차단성 측정Experimental Example 3. Thermal Insulation Measurement
실시예와 비교예에 따른 성형체의 열차단성을 평가하기 위하여, 성형체 내부에 100℃ 의 물을 70%(v/v) 담은 상태에서, 2분 경과된 시점에서, 성형체 내부 임의의 지점과 용기 외부 임의의 지점의 온도를 측정하였다. 그리고, 그 결과를 표 4와 표 5에 나타내었다:In order to evaluate the thermal barrier properties of the molded articles according to the Examples and Comparative Examples, at a point 2 minutes after 100% of water at 70 ℃ (v / v) contained in the molded body, any point inside the molded body and the outside of the container The temperature at any point was measured. The results are shown in Tables 4 and 5:
[수학식 2][Equation 2]
|T2 - T1| ≥ 10℃T 2 -T 1 | ≥ 10 ℃
상기 수학식 2에서,In Equation 2,
T1 는 20℃, 1 atm 조건에서, 성형체에 100℃의 물을 담고, 1 분 경과 되었을 때 측정한 성형체의 외측 표면 온도이며,T 1 is the outer surface temperature of the molded body measured when 1 minute has elapsed by containing 100 ° C water in the molded body at 20 ° C and 1 atm conditions,
T2 은 20℃, 1 atm 조건에서, 성형체에 100℃의 물을 담고, 1 분 경과 되었을 때 측정한 성형체 내부의 물의 온도이다.T 2 is the temperature of the water inside the molded body measured when 1 minute has elapsed after 100 minutes of water is contained in the molded body at 20 ° C. and 1 atm conditions.
실시예 1Example 1 실시예 2Example 2 실시예 3Example 3 비교예 1Comparative Example 1 비교예 2Comparative Example 2
T1 T 1 4040 3838 4040 7575 8080
T2 T 2 9595 9292 9090 8484 8080
|T2-T1|T 2 -T 1 | 5555 5454 5050 99 00
상기 표 4를 참조하면, 실시예에 따른 성형체는 성형체 내부에 수용된 물의 온도와 성형체 표면의 온도차가 10℃ 이상으로 나타나 뛰어나 열차단성을 보이는 것을 알 수 있다. 반면, 비교예 1 및 2에 따른 성형체는 |T2-T1| 가 각각 27℃ 와 0℃ 로, 열 차단성이 현저히 낮았다. 따라서, 본 발명에 따른 성형체는 PET 발포시트를 포함함으로써 우수한 열차단성을 가지며, 이로 인해 뛰어난 보온 특성 및 취급의 안전성을 구현할 수 있음을 확인하였다.Referring to Table 4, the molded article according to the embodiment can be seen that the temperature difference between the temperature of the water contained in the molded body and the surface of the molded body is 10 ° C or more showing excellent heat shielding properties. On the other hand, the molded articles according to Comparative Examples 1 and 2 were | T 2 -T 1 | Were 27 degreeC and 0 degreeC, respectively, and the thermal barrier property was remarkably low. Therefore, it was confirmed that the molded article according to the present invention has excellent thermal barrier properties by including a PET foam sheet, thereby realizing excellent thermal insulation properties and handling safety.
특히, 가스 베리어층의 양면에 각각 제1 및 제2 발포시트를 포함함으로써 우수한 열차단성을 가지는 것을 확인할 수 있었다.In particular, by including the first and second foam sheets on both sides of the gas barrier layer was confirmed to have excellent thermal barrier properties.
이를 통해서, 본 발명에 따른 성형체는 낮은 수증기 투과도 및 산소 투과도를 가지며, 열차단성이 우수한 것을 알 수 있다.Through this, it can be seen that the molded article according to the present invention has low water vapor permeability and oxygen permeability, and is excellent in thermal barrier property.
[부호의 설명][Description of the code]
1: 시트1: sheet
10: 성형체10: molded body
101: 제1 발포시트101: first foam sheet
101': 제2 발포시트101 ': second foam sheet
102: 가스 베리어층102: gas barrier layer
11: 바닥부11: bottom
12: 벽부12: wall
13: 플랜지13: flange
20: 금형20: mold
21: 암형 금형21: female mold
22: 수형 금형22: male mold
23: 감압홀23: decompression hole
본 발명에 따른 성형체는 가스 베리어층의 양면에 각각 제1 및 제2 발포시트를 포함함으로써, 산소 및 수분 투과도를 최소화할 수 있으므로, 이를 식품 포장용기에 사용할 경우, 산소 및 수분으로 인한 식품의 부패 등을 방지하여 식품의 보존에 용이할 수 있다.Since the molded article according to the present invention includes the first and second foam sheets respectively on both sides of the gas barrier layer, oxygen and moisture permeability can be minimized, and when used in a food packaging container, decay of food due to oxygen and moisture It may be easy to preserve the food by preventing such.

Claims (13)

  1. 제1 발포시트, 가스 베리어층 및 제2 발포시트가 순차적으로 적층된 구조이며, 하기 수학식 1을 만족하는 성형체로써,The first foam sheet, the gas barrier layer and the second foam sheet is a laminated structure sequentially, a molded body that satisfies the following equation 1,
    상기 제1 발포시트 및 제2 발포시트는 폴리에스테르 수지의 발포체이며,The first foam sheet and the second foam sheet is a foam of a polyester resin,
    상기 성형체의 평균 두께는 1 mm 내지 5 mm 범위이고, The average thickness of the molded body ranges from 1 mm to 5 mm,
    ASTM F 3985 에 따른 산소 투과도가 23℃ 의 조건 하에서, 20 cc/m2·day 이하인 것을 특징으로 하는 성형체:A molded article characterized in that the oxygen permeability according to ASTM F 3985 is 20 cc / m 2 · day or less, under conditions of 23 ° C .:
    [수학식 1][Equation 1]
    H/D ≥ 0.01H / D ≥ 0.01
    수학식 1에서,In Equation 1,
    수용부 및 개구부를 포함하는 용기 구조의 성형체를 형성하되,Forming a shaped body of the container structure including the receiving portion and the opening,
    H는 수용부의 깊이를 나타내고, 1 cm 내지 10 cm이며,H represents the depth of the receptacle and is 1 cm to 10 cm,
    D는 개구부의 직경을 나타낸 것이다.D represents the diameter of the opening.
  2. 제1항에 있어서,The method of claim 1,
    ASTM F 1249에 따른 수증기 투과도가 37℃, 100%의 상대습도 조건하에서, 50 g/m2·day 이하인 것을 특징으로 하는 성형체.A molded article characterized in that the water vapor transmission rate according to ASTM F 1249 is 50 g / m 2 · day or less under 37 ° C. and 100% relative humidity conditions.
  3. 제1항에 있어서,The method of claim 1,
    가스 베리어층의 평균 두께는 0.01 내지 2 mm이며,The average thickness of the gas barrier layer is 0.01 to 2 mm,
    제1 및 제2 발포시트의 평균 두께는 각각 0.5 내지 1.5 mm인 것을 특징으로 하는 성형체.Molded body, characterized in that the average thickness of the first and second foam sheet is 0.5 to 1.5 mm each.
  4. 제1항에 있어서,The method of claim 1,
    가스 베리어층은 에틸렌비닐알코올, 폴리비닐리덴클로라이드 및 폴리에틸렌테레프탈레이트 중 1 종 이상을 포함하는 것을 특징으로 하는 성형체.The gas barrier layer is a molded article comprising at least one of ethylene vinyl alcohol, polyvinylidene chloride and polyethylene terephthalate.
  5. 제1항에 있어서,The method of claim 1,
    가스 베리어층의 융점(Tm)은 평균 150℃ 내지 190℃이며,Melting point (T m ) of the gas barrier layer is an average of 150 ℃ to 190 ℃,
    제1 및 제2 발포시트의 융점(Tm)은 평균 240℃ 내지 260℃인 것을 특징으로 하는 성형체.Melting point (T m ) of the first and second foam sheet is characterized in that the average 240 ℃ to 260 ℃.
  6. 제1항에 있어서,The method of claim 1,
    폴리에스테르 수지는 폴리에틸렌 테레프탈레이트(polyethylene terephthalate) 수지인 것을 특징으로 하는 성형체.Polyester resin is a molded article characterized in that the polyethylene terephthalate (polyethylene terephthalate) resin.
  7. 제 1 항에 있어서,The method of claim 1,
    제1 및 제2 발포시트는 각각 0.5 내지 9.0 중량% 의 탄산칼슘을 포함하는 것을 특징으로 하는 성형체.The first and second foam sheet is a molded article, characterized in that each containing 0.5 to 9.0% by weight of calcium carbonate.
  8. 제1항에 있어서,The method of claim 1,
    하기 수학식 2를 만족하는 것을 특징으로 하는 성형체:A molded article characterized by satisfying the following Equation 2:
    [수학식 2][Equation 2]
    |T2 - T1| ≥ 10℃T 2 -T 1 | ≥ 10 ℃
    상기 수학식 2에서,In Equation 2,
    T1 는 20℃, 1 atm 조건에서, 성형체에 100℃의 물을 담고, 1 분 경과 되었을 때 측정한 성형체의 외측 표면 온도이며,T 1 is the outer surface temperature of the molded body measured when 1 minute has elapsed by containing 100 ° C water in the molded body at 20 ° C and 1 atm conditions,
    T2 은 20℃, 1 atm 조건에서, 성형체에 100℃의 물을 담고, 1 분 경과 되었을 때 측정한 성형체 내부의 물의 온도이다.T 2 is the temperature of the water inside the molded body measured when 1 minute has elapsed after 100 minutes of water is contained in the molded body at 20 ° C. and 1 atm conditions.
  9. 제1항 내지 제8항 중 어느 한 항에 따른 성형체를 포함하는 포장용기.A packaging container comprising the molded article according to any one of claims 1 to 8.
  10. 제9항에 있어서,The method of claim 9,
    포장용기는 식품 포장용기인 것을 특징으로 하는 포장용기.The packaging container is a packaging container, characterized in that the food packaging container.
  11. 제1 발포시트, 가스 베리어층 및 제2 발포시트가 순차적으로 적층된 구조의 시트를 성형장치의 암형 금형과 수형 금형 사이에 배치하는 단계; 및Disposing a sheet having a structure in which the first foam sheet, the gas barrier layer and the second foam sheet are sequentially stacked between the female mold and the male mold of the molding apparatus; And
    수형 금형을 가압하여 성형체를 성형하는 단계; 를 포함하며,Pressing the male mold to form a molded body; Including;
    상기 제1 발포시트 및 제2 발포시트는 폴리에스테르 수지의 발포체인 것을 특징으로 하는 성형체의 제조방법.The first foam sheet and the second foam sheet is a method for producing a molded body, characterized in that the foam of the polyester resin.
  12. 제11항에 있어서,The method of claim 11,
    성형하는 단계는, 시트 표면 온도가 140 내지 160℃ 되도록 열을 인가하고, 상기 암형 금형 및 수형 금형의 표면 온도를 60 내지 200℃ 로 설정하여 성형체를 성형하는 것을 특징으로 하는 성형체의 제조방법.The molding step includes applying heat so that the sheet surface temperature is 140 to 160 ° C, and molding the molded body by setting the surface temperatures of the female mold and the male mold to 60 to 200 ° C.
  13. 제11항에 있어서,The method of claim 11,
    암형 금형은, 일측에 내부 공간을 감압하는 감압홀이 형성된 구조인 것을 특징으로 하는 성형체의 제조방법.The female mold has a structure in which a pressure reducing hole for depressurizing an internal space is formed on one side.
PCT/KR2018/016023 2018-06-28 2018-12-17 Molded article including gas barrier layer, packing container including same, and method for preparing molded article WO2020004744A1 (en)

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