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JP7110422B2 - Molded article containing gas barrier layer, packaging container containing the same, and method for producing molded article - Google Patents
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JP7110422B2 - Molded article containing gas barrier layer, packaging container containing the same, and method for producing molded article - Google Patents

Molded article containing gas barrier layer, packaging container containing the same, and method for producing molded article Download PDF

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JP7110422B2
JP7110422B2 JP2021019866A JP2021019866A JP7110422B2 JP 7110422 B2 JP7110422 B2 JP 7110422B2 JP 2021019866 A JP2021019866 A JP 2021019866A JP 2021019866 A JP2021019866 A JP 2021019866A JP 7110422 B2 JP7110422 B2 JP 7110422B2
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molded article
foam sheet
barrier layer
gas barrier
sheet
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JP2021079703A (en
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チェ・ジョンハン
ハム・ジンス
イ・グァンヒ
ホ・ミ
キム・ウジン
ハ・サンフン
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Huvis Corp
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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

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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)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Laminated Bodies (AREA)
  • Containers Having Bodies Formed In One Piece (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)
  • Packages (AREA)
  • Wrappers (AREA)

Description

本発明はガスバリアー層を含む成形体、これを含む包装容器および成形体の製造方法に関するものである。 TECHNICAL FIELD The present invention relates to a molded article containing a gas barrier layer, a packaging container including the same, and a method for producing the molded article.

通常の食品包装容器として使われている製品は発泡式と非発泡式に分かれる。発泡式の食品包装容器はポリスチレンを発泡ガスと混合させて押出させた製品が使われているが、これは厚さを比較的厚く維持することができるため形態の維持、断熱性、価格競争力が高い長所がある。その反面、このような発泡式製品は高温で有害物質が検出される短所がある。 Products used as ordinary food packaging containers are divided into foaming and non-foaming types. Foam-type food packaging containers are made by extruding polystyrene mixed with foaming gas, which can keep its thickness relatively thick, so it maintains its shape, is heat-insulating, and is price-competitive. has a high advantage. On the other hand, such foaming products have the disadvantage that harmful substances are detected at high temperatures.

非発泡式の食品包装容器の場合、熱に安定したポリプロピレンをフィルム形態に製作した製品が使われている。一方、このような非発泡式の食品包装容器は高温で形態の変化率が小さく、有害物質が検出されない長所がある。しかし、値段が高く断熱が悪い短所がある。 In the case of non-foaming food packaging containers, heat-stable polypropylene films are used. On the other hand, such a non-foaming type food packaging container has an advantage that the change rate of shape is small at high temperature and harmful substances are not detected. However, it has the disadvantages of high cost and poor insulation.

一方、現代社会において、次第に生活が便利になるにつれて使い捨て用品の使用が増加し、単身世帯の増加による出前料理および簡便料理製品の需要が次第に増えている。これに伴い、食品包装容器の需要も増加していて、有害物質から安全かつ用途による機能が付与された新しい容器の素材に対する消費者のニーズがますます大きくなってきている。 On the other hand, in modern society, as life becomes more convenient, the use of disposable items is increasing, and demand for food delivery and simple cooking products is gradually increasing due to the increase in single-person households. Along with this, the demand for food packaging containers is also increasing, and consumer needs for new container materials that are safe from harmful substances and given functions depending on the application are becoming more and more important.

これと関連して、食品包装容器関連業者では便利さ、安全性、環境に優しい性能および価格競争力をすべて備えた食品包装容器を製造するために多くの努力がなされている。 In this regard, food packaging manufacturers are making great efforts to manufacture food packaging containers that are convenient, safe, environmentally friendly, and competitively priced.

その例として、環境に優しい耐熱材およびこれを含む包装容器(大韓民国登録特許第10-1778629号)に対する技術が提案されてある。具体的には、前記登録特許にはポリエチレンテレフタレート(Polyethylene terephthalate、PET)発泡体の少なくとも一面にエチレンビニルアルコール(ethylene vinyl alcohol、EVOH)ガスバリアー層を含む2層構造の耐熱材を有する包装容器が開示されている。 As an example, technology has been proposed for environmentally friendly heat-resistant materials and packaging containers containing the same (Korea Registered Patent No. 10-1778629). Specifically, the registered patent discloses a packaging container having a two-layer heat-resistant material including an ethylene vinyl alcohol (EVOH) gas barrier layer on at least one surface of a polyethylene terephthalate (PET) foam. disclosed.

しかし、前記エチレンビニルアルコールはバリアー性は優秀であるものの、ポリエチレンテレフタレートとの融点差が大きいため成形が難しい短所がある。具体的には、ポリエチレンテレフタレートの耐熱性を向上させるために高温の熱処理が必要であるが、このような場合、前記エチレンビニルアルコールが融解して食品包装容器の全体面積にガスバリアー層を形成できないなど、食品包装容器の構成状態が不良となる問題点がある。 However, although ethylene vinyl alcohol has excellent barrier properties, it is difficult to mold due to a large difference in melting point from that of polyethylene terephthalate. Specifically, high-temperature heat treatment is required to improve the heat resistance of polyethylene terephthalate, but in such a case, the ethylene vinyl alcohol melts and the gas barrier layer cannot be formed over the entire area of the food packaging container. For example, there is a problem that the configuration state of the food packaging container is defective.

本発明は前述した問題点を解決するためのものであって、容器の成形時にガスバリアー層の損傷を防止できる成形体、これを含む包装容器およびその製造方法を提供する。 SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a molded article that can prevent the gas barrier layer from being damaged during molding of the container, a packaging container including the molded article, and a method for manufacturing the same.

本発明は、第1発泡シート、ガスバリアー層および第2発泡シートが順次積層された構造であり、下記の数学式1を満足する成形体であって、前記第1発泡シートおよび第2発泡シートはポリエステル樹脂の発泡体であり、前記成形体の平均厚さは1~5mm範囲であり、ASTM 3985による酸素透過度が23℃の条件下で、20cc/m・day以下であることを特徴とする成形体を提供する: The present invention has a structure in which a first foam sheet, a gas barrier layer and a second foam sheet are laminated in order, and is a molded article satisfying the following mathematical formula 1, wherein the first foam sheet and the second foam sheet is a polyester resin foam, the average thickness of the molded product is in the range of 1 to 5 mm, and the oxygen permeability according to ASTM D 3985 is 20 cc/m 2 ·day or less at 23 ° C. Provide compacts characterized by:

[数学式1]
H/D≧0.01
[Mathematical formula 1]
H/D≧0.01

数学式1において、収容部および開口部を含む容器構造の成形体を形成するものの、Hは収容部の深さを示し、1~10cmであり、Dは開口部の直径を示したものである。 In Mathematical Formula 1, forming a molded body of a container structure including a container and an opening, H represents the depth of the container and ranges from 1 to 10 cm, and D represents the diameter of the opening. .

また、本発明は前記成形体を含む包装容器を提供する。 The present invention also provides a packaging container containing the molded article.

さらに、本発明は、第1発泡シート、ガスバリアー層および第2発泡シートが順次積層された構造のシートを、成形装置の雌型金型と雄型金型の間に配置させる段階;および雄型金型を加圧して成形体を成形する段階;を含み、前記第1発泡シートおよび第2発泡シートはポリエステル樹脂の発泡体であることを特徴とする成形体の製造方法を提供する。 Furthermore, the present invention provides a step of placing a sheet having a structure in which a first foam sheet, a gas barrier layer and a second foam sheet are sequentially laminated between a female mold and a male mold of a molding device; The first foam sheet and the second foam sheet are polyester resin foams.

本発明に係る成形体は、ガスバリアー層の両面にそれぞれ第1および第2発泡シートを含むことによって、酸素および水分透過度を最小化することができる。併せて、前記成形体を食品包装容器に使う場合、酸素および水分による食品の腐敗などを防止するため食品の保存が容易である。 The molding 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 product is used as a food packaging container, the food can be easily preserved because the food is prevented from spoiling due to oxygen and moisture.

本発明に係る成形体の断面図。Sectional drawing of the molded object which concerns on this invention. 本発明に係る成形体の製造方法を順に図示した図面。3A to 3D are drawings sequentially illustrating the method for manufacturing a molded body according to the present invention;

本発明はガスバリアー層を含む成形体、これを含む包装容器および成形体の製造方法に関するものである。特に、本発明に係る成形体はガスバリアー層の両面に第1および第2発泡シートを含むことによって、酸素および水分透過度を最小化することができる。併せて、前記成形体を食品包装容器に使う場合、酸素および水分による食品の腐敗などを防止するため食品の保存が容易である。 TECHNICAL FIELD The present invention relates to a molded article containing a gas barrier layer, a packaging container including the same, and a method for producing the molded article. In particular, the molding 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. In addition, when the molded product is used as a food packaging container, the food can be easily preserved because the food is prevented from spoiling due to oxygen and moisture.

図1は本発明に係る成形体の断面図、図2は本発明に係る成形体の製造方法を順に図示した図面である。以下、図1および図2を参照して、本発明に係る成形体について詳細に説明する。 FIG. 1 is a cross-sectional view of a molded body according to the present invention, and FIG. 2 is a drawing sequentially illustrating a method for manufacturing a molded body according to the present invention. Hereinafter, the molded article according to the present invention will be described in detail with reference to FIGS. 1 and 2. FIG.

本発明は、第1発泡シート101、ガスバリアー層102および第2発泡シート101’が順次積層された構造であり、下記の数学式1を満足する成形体10であって、前記第1発泡シート101および第2発泡シート101’はポリエステル樹脂の発泡体であり、前記成形体10の平均厚さは1mm~5mm範囲であり、ASTM 3985による酸素透過度が23℃の条件下で、20cc/m・day以下であることを特徴とする成形体を提供する:
The present invention has a structure in which a first foam sheet 101, a gas barrier layer 102, and a second foam sheet 101' are sequentially laminated, and is a molded body 10 satisfying the following mathematical formula 1, wherein the first foam sheet 101 and the second foam sheet 101′ are polyester resin foams, the average thickness of the molded body 10 is in the range of 1 mm to 5 mm, and the oxygen permeability according to ASTM D 3985 is 20 cc/ Provide a compact characterized by m 2 · day or less:

[数学式1]
H/D≧0.01
[Mathematical formula 1]
H/D≧0.01

数学式1において、収容部および開口部を含む容器構造の成形体を形成するものの、Hは収容部の深さを示し、1cm~10cmであり、Dは開口部の直径を示したものである。 In Mathematical Formula 1, forming a molded body of a container structure including a container and an opening, H represents the depth of the container and ranges from 1 cm to 10 cm, and D represents the diameter of the opening. .

具体的には、本発明に係る成形体はASTM D3985に基づいて測定した酸素透過度が0.1~20cc/m・dayであり得る。より具体的には、製造された成形体の試片(横×縦×高さ40mm×40mm×3mm)を(23±1)℃条件で30分の間酸素透過度を測定する場合、成形体の酸素透過度は0.1~20cc/m・day、0.1~15cc/m・day、0.1~13cc/m・day、0.1~10cc/m・day、0.1~7cc/m・day、0.1~5cc/m・day、または0.1~3cc/m・dayであり得る。 Specifically, the molded article according to the present invention may have an oxygen permeability measured according to ASTM D3985 of 0.1 to 20 cc/m 2 ·day. More specifically, when measuring the oxygen permeability of a test piece (width x length x height 40 mm x 40 mm x 3 mm) of the manufactured compact at (23 ± 1) ° C for 30 minutes, the compact The oxygen permeability of the .1-7 cc/m 2 ·day, 0.1-5 cc/m 2 ·day, or 0.1-3 cc/m 2 ·day.

これは、前述した通り、ポリエステル樹脂の第1および第2発泡シート101、101’をそれぞれ成形体10の断面外層に形成し、前記第1および第2発泡シート101、101’の間にガスバリアー層102を形成することによって、前記のような酸素透過度を満足させることができる。すなわち、本発明に係る成形体10は、前記範囲内の酸素透過度を有することによって酸素を遮蔽する性能が優秀であるため、食品の保存期限を延長させることができる利点がある。 As described above, the first and second foam sheets 101 and 101' made of polyester resin are formed on the cross-sectional outer layers of the molded body 10, respectively, and a gas barrier is formed between the first and second foam sheets 101 and 101'. By forming layer 102, oxygen permeability as described above can be met. That is, the molded article 10 according to the present invention has an excellent oxygen shielding performance due to the oxygen permeability within the above range, and thus has the advantage of being able to extend the shelf life of food.

具体的には、本発明に係る成形体10は前記ガスバリアー層102の両面にそれぞれ第1および第2発泡シート101、101’を形成し、酸素透過度を前記範囲内に制御することができる。 Specifically, in the molded article 10 according to the present invention, the first and second foam sheets 101 and 101' are formed on both sides of the gas barrier layer 102, respectively, and the oxygen permeability can be controlled within the above range. .

併せて、ASTM F 1249による水蒸気透過度が37℃、100%の相対湿度条件下で、50g/m・day以下であることを特徴とする。例えば、前記水蒸気透過度は0.1~50g/m・day、0.1~40g/m・day、0.1~30g/m・day、0.1~20g/m・day、0.1~10g/m・day、0.1~7g/m・day、0.1~5g/m・dayまたは0.1~3g/m・day範囲であり得る。本発明に係る成形体10は前記水蒸気透過度を有することによって、ガスバリアー特性が要求される製品に広く使用され得る。例えば、食品包装容器として使う場合、食品が水蒸気と反応して腐敗することを防止できるため、食品の保管が容易であり得る。 In addition, it is characterized by having a water vapor permeability of 50 g/m 2 ·day or less under conditions of 37° C. and 100% relative humidity according to ASTM F 1249. For example, the water vapor permeability 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. Since the molded article 10 according to the present invention has the water vapor permeability, it can be widely used for products requiring gas barrier properties. For example, when used as a food packaging container, food can be easily stored because it can prevent food from reacting with water vapor and spoiling.

ポリエステル樹脂は酸成分とジオール成分から誘導される繰り返し単位を含むことができる。具体的には、ポリエステル樹脂は、ジカルボン酸成分とグリコール成分またはヒドロキシカルボン酸から合成された芳香族および脂肪族ポリエステル樹脂からなる群から選択された1種以上であり得る。 The polyester resin can contain repeating units derived from acid and diol components. Specifically, the polyester resin may be one or more selected from the group consisting of aromatic and aliphatic polyester resins synthesized from dicarboxylic acid components and glycol components or hydroxycarboxylic acids.

前記ポリエステル樹脂は例えば、ポリエチレンテレフタレート(Polyethylene Terephthalate、PET)、ポリブチレンテレフタレート(Polybutylene Terephthalate、PBT)、ポリ乳酸(Poly Lactic acid、PLA)、ポリグリコール酸(Polyglycolic acid、PGA)、ポリエチレンアジペート(Polyehtylene adipate、PEA)、ポリヒドロキシアルカノエート(Polyhydroxyalkanoate、PHA)、ポリトリメチレンテレフタレート(Polytrimethylene Terephthalate、PTT)およびポリエチレンナフタレン(Polyethylene naphthalate、PEN)からなる群から選択された一つ以上であり得る。一例として、本発明ではポリエチレンテレフタレート(Polyethylene Terephthalate、PET)が使用され得る。 Examples of the polyester resin include polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polylactic acid (PLA), polyglycolic acid (PGA), and polyethylene adipate. , PEA), Polyhydroxyalkanoate (PHA), Polytrimethylene terephthalate (PTT) and Polyethylene naphthalate (PEN). As an example, Polyethylene Terephthalate (PET) may be used in the present invention.

併せて、前記ガスバリアー層102は、エチレンビニルアルコール(ethylene vinyl alcohol、EVOH)、ポリビニリデンクロライド(polyvinylidene chloride、PVdC)およびポリエチレンテレフタレート(polyethylene terephthalate、PET)のうち1種以上を含むことができる。 In addition, the gas barrier layer 102 may include at least one of ethylene vinyl alcohol (EVOH), polyvinylidene chloride (PVdC) and polyethylene terephthalate (PET).

具体的には、前記バリアー層102はエチレンビニルアルコールを利用して形成することができる。この場合、包装容器の内部にある食品で発生するガスは、外部への排出は可能であるとともに外部からの酸素の供給は遮断することができる。 Specifically, the barrier layer 102 may be formed using ethylene vinyl alcohol. In this case, the gas generated by the food inside the packaging container can be discharged to the outside, and the supply of oxygen from the outside can be cut off.

本発明に係る成形体10は多層構造であり、成形体10を形成する多層構造の平均厚さは1mm~5mm範囲であり得る。 The molded body 10 according to the present invention is a multilayer structure, and the average thickness of the multilayer structure forming the molded body 10 can be in the range of 1 mm to 5 mm.

例えば、成形体10は3層構造であり得、この場合、3層構造の全体厚さは、平均1.2~4mm、1.5~3.5mm、1.8~3mmあるいは2mmであり得る。また、前記ガスバリアー層102の平均厚さは0.01~2mmであり得、0.05~2mm、0.1~1.9mm、0.2~1.85mm、0.3~1.8mm、0.5~1.6mm、0.7~1.4mm、0.9~1.2mm、または1mmであり得る。 For example, the molded body 10 can be a three-layer structure, in which case the overall thickness of the three-layer structure can be an average of 1.2-4 mm, 1.5-3.5 mm, 1.8-3 mm or 2 mm. . Also, the average thickness of the gas barrier layer 102 may be 0.01-2 mm, 0.05-2 mm, 0.1-1.9 mm, 0.2-1.85 mm, 0.3-1.8 mm. , 0.5-1.6 mm, 0.7-1.4 mm, 0.9-1.2 mm, or 1 mm.

併せて、第1発泡シート101および第2発泡シート101’の平均厚さはそれぞれ0.5~1.5mmであり得、0.6~1.3mm、0.7~1.2mm、0.8~1.0mm、0.9~0.95mmであり得る。本発明の成形体10は前記範囲の厚さを有する発泡シート101、101’およびガスバリアー層102で構成されることによって、前述した酸素透過度および水蒸気透過度を満足させることができるとともに圧縮強度を向上させて軽量性などを同時に満足させることができる。 Together, the average thickness of the first foam sheet 101 and the second foam sheet 101′ can be 0.5-1.5 mm, respectively, 0.6-1.3 mm, 0.7-1.2 mm, 0.6-1.3 mm, 0.7-1.2 mm. It can be 8-1.0 mm, 0.9-0.95 mm. By comprising the foamed sheets 101 and 101' and the gas barrier layer 102 having thicknesses within the above range, the molded article 10 of the present invention can satisfy the oxygen permeability and the water vapor permeability described above, and also has a compressive strength. can be improved, and lightness and the like can be satisfied at the same time.

一つの例示において、前記第1および第2発泡シート101、101’の融点Tは平均240~260℃であり得る。具体的には、第1および第2発泡シート101、101’の平均融点は242℃~257℃、245℃~255℃、247℃~253℃、または248℃~251℃であり得る。一例として、ポリエチレンテレフタレート(polyethylene terephthalate)樹脂を含む第1および第2発泡シート101、101’の融点は、平均248℃~251℃であり得る。 In one example, the melting point Tm of the first and second foam sheets 101, 101' can be 240-260°C on average. Specifically, the average melting point of the first and second foam sheets 101, 101' can be 242°C to 257°C, 245°C to 255°C, 247°C to 253°C, or 248°C to 251°C. As an example, the melting point of the first and second foam sheets 101, 101' comprising polyethylene terephthalate resin may average between 248°C and 251°C.

併せて、前記ガスバリアー層102の融点Tは、平均150℃~190℃であり得る。具体的には、ガスバリアー層102の融点は、平均150℃~190℃、155℃~185℃、160℃~180℃、165℃~175℃または169℃~171℃であり得る。一例として、エチレンビニルアルコールからなるガスバリアー層の融点は、平均170±0.5℃であり得る。 In addition, the melting point Tm of the gas barrier layer 102 may range from 150°C to 190°C on average. Specifically, the melting point of the gas barrier layer 102 can average 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. As an example, the melting point of the gas barrier layer made of ethylene vinyl alcohol can be 170±0.5° C. on average.

一方、ポリエチレンテレフタレートとエチレンビニルアルコールは融点の差が大きいため、2層構造(発泡シート/ガスバリアー層)成形体の成形時にエチレンビニルアルコールが剥離または融解して成形体の全体面積に前記バリアー層102を等しく形成できないなどの問題点があったが、前記発泡シート101、101’をガスバリアー層102の両面にそれぞれ積層させることによって、前記ガスバリアー層102が融解してなくなったり発泡シート101、101’から剥離されるなどの問題点を解決することができる。 On the other hand, since polyethylene terephthalate and ethylene vinyl alcohol have a large melting point difference, ethylene vinyl alcohol is peeled off or melted during molding of a two-layer structure (foamed sheet/gas barrier layer) molding, and the barrier layer covers the entire area of the molding. However, by laminating the foamed sheets 101 and 101′ on both sides of the gas barrier layer 102, the gas barrier layer 102 is melted away and the foamed sheet 101, Problems such as separation from 101' can be solved.

一つの例として、本発明に係る成形体10は、底部11および底部11の周りに沿って上端が開放された状態の壁部12を含み、前記数学式1でH/D値は0.01~1.3、0.05~1.2、0.1~1.1、0.3~1.0、0.4~0.9、0.5~0.8、0.55~0.7または0.6~0.65であり得る。併せて、前記数学式1でH値は1~10cmであり得る。一例として、成形体10の開口部の直径は10cmであり得、収容部の深さが3cmであり得る。併せて、本発明に係る成形体10は容器の形状であり得、円筒形または四角形の容器の形状であり得る。 As an example, the molded body 10 according to the present invention includes a bottom portion 11 and a wall portion 12 with an open upper end along the circumference of the bottom portion 11, and the H/D value in Equation 1 is 0.01. ~1.3, 0.05-1.2, 0.1-1.1, 0.3-1.0, 0.4-0.9, 0.5-0.8, 0.55-0 .7 or 0.6 to 0.65. In addition, the H value in Equation 1 may range from 1 to 10 cm. As an example, the diameter of the opening of the molded body 10 may be 10 cm, and the depth of the receiving portion may be 3 cm. Together, the molded body 10 according to the present invention may be in the shape of a container, and may be in the shape of a cylindrical or square container.

一方、本発明に係る成形体10は前記ガスバリアー層102の両面にそれぞれ第1および第2発泡シート101、101’を形成することによって、下記の数学式2を満足する成形体10を提供することができる: On the other hand, the molded body 10 according to the present invention provides the molded body 10 that satisfies Equation 2 below by forming the first and second foam sheets 101 and 101' on both sides of the gas barrier layer 102, respectively. be able to:

[数学式2]
|T-T|≧10℃
[Mathematical formula 2]
|T 2 −T 1 |≧10° C.

前記数学式2において、Tは20℃、1atm条件で、成形体に100℃の水を入れて1分経過したときに測定した成形体の外側の表面温度であり、Tは20℃、1atm条件で、成形体に100℃の水を入れて1分経過したときに測定した成形体の内部の水の温度である。 In the above formula 2 , T1 is the outer surface temperature of the molded body measured after one minute has elapsed after the molded body is filled with water of 100°C under the conditions of 20°C and 1 atm, and T2 is 20°C. It is the temperature of the water inside the molded body measured when water of 100° C. is poured into the molded body under 1 atm condition and one minute has passed.

本発明に係る成形体10は第1、2発泡シート101、101’を含むことによって、優秀な熱遮断性を示す。具体的には、常温(20℃)、1気圧条件で、成形体の内部に100℃の水を70%(v/v)入れた状態で、1分経過した時点での成形体内部の水の温度と成形体外部の表面の温度差が10℃以上であり得る。これは本発明に係る成形体10の熱遮断性が優秀であることを示すものであるが、具体的には、製造された成形体に100℃の水を70%(v/v)入れた状態で、1分経過した時点での成形体10の内部に収容された水の温度と成形体10の外部表面の温度差である。 The molding 10 according to the present invention exhibits excellent heat insulation properties by including the first and second foam sheets 101, 101'. Specifically, at room temperature (20 ° C.) and 1 atmospheric pressure, 70% (v / v) of water at 100 ° C. was added to the inside of the compact, and after 1 minute, the water inside the compact The temperature difference between the temperature of and the surface of the outside of the molded body can be 10° C. or more. This indicates that the molded article 10 according to the present invention has excellent heat shielding properties. This is the temperature difference between the temperature of the water contained inside the molded body 10 and the temperature of the outer surface of the molded body 10 after one minute has passed.

一つの例として、本発明に係る成形体10に100℃の水を70%(v/v)入れた状態で、1分経過した時点での成形体の外部温度が40℃である場合、成形体10の内部に収容された水の温度は95℃であり得る。本発明に係る成形体10は、前記条件で成形体10の内部に収容された水の温度と成形体10の外部表面の温度差を比較的に高く維持することによって優秀な熱遮断性を示すことが分かり、これによって食品の保温を効果的に向上させることができる。 As an example, when 70% (v/v) of water at 100°C is added to the molded body 10 according to the present invention, and the external temperature of the molded body is 40°C after one minute has passed, molding The temperature of the water contained inside body 10 may be 95°C. The molded article 10 according to the present invention exhibits excellent heat shielding properties by maintaining a relatively high temperature difference between the temperature of the water contained inside the molded article 10 and the outer surface of the molded article 10 under the above conditions. It can be seen that this can effectively improve the heat retention of the food.

一方、本発明の第1および第2発泡シート101、101’はそれぞれ0.5~9重量%の炭酸カルシウム(CaCO)を含むことができる。 Meanwhile, the first and second foam sheets 101, 101' of the present invention may each contain 0.5-9% by weight of calcium carbonate (CaCO 3 ).

具体的には、前記炭酸カルシウム(CaCO)は無機粒子であり、前記のような無機粒子を含むことによって、本発明の第1および第2発泡シート101、101’はシートの表面が均一であり、優秀な熱成形性を示すことができる。 Specifically, the calcium carbonate (CaCO 3 ) is inorganic particles, and by including the inorganic particles, the surfaces of the first and second foam sheets 101 and 101′ of the present invention are uniform. It has excellent thermoformability.

前記炭酸カルシウムの熱伝導率は1.0kcal/mh℃~3.0kcal/mh℃であり得る。具体的には、炭酸カルシウムの熱伝導率は1.2kcal/mh℃~2.5kcal/mh℃、1.5kcal/mh℃~2.2kcal/mh℃または1.8kcal/mh℃~2.0kcal/mh℃であり得る。より具体的には、炭酸カルシウムの熱伝導率は1.5kcal/mh℃~2.5kcal/mh℃または1.8kcal/mh℃~2.3kcal/mh℃であり得る。前記のように炭酸カルシウムを含む第1および第2発泡シート101、101’は優秀な熱伝導率を示すことによって均一な表面を有し、優秀な熱成形性を示すことができる。 The thermal conductivity of the calcium carbonate may range from 1.0 kcal/mh°C to 3.0 kcal/mh°C. Specifically, the thermal conductivity of calcium carbonate is 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 can be from 1.5 kcal/mh°C to 2.5 kcal/mh°C or from 1.8 kcal/mh°C to 2.3 kcal/mh°C. As described above, the first and second foamed sheets 101 and 101' containing calcium carbonate exhibit excellent thermal conductivity, have a uniform surface, and exhibit excellent thermoformability.

例えば、前記炭酸カルシウムの含量は0.5~9重量%であり得る。具体的には、炭酸カルシウムの含量は0.5~8重量%、0.6~7重量%、0.7~6重量%、0.8~5重量%、0.9~4重量%、1.0~3.0重量%、2重量%~3.5重量%であり得る。一例として、1.0重量%または3重量%であり得る。 For example, the calcium carbonate content may be 0.5-9% by weight. Specifically, the content of calcium carbonate is 0.5-8 wt%, 0.6-7 wt%, 0.7-6 wt%, 0.8-5 wt%, 0.9-4 wt%, It can be 1.0-3.0% by weight, 2%-3.5% by weight. As an example, it can be 1.0 wt% or 3 wt%.

一つの例示において、発泡シート101、101’の密度(KS M ISO 845)は、平均300~700kg/mであり得る。具体的には、発泡シート101、101’の密度は、平均325~650kg/m、350~600kg/m、375~550kg/m、400~500kg/mまたは425~450kg/mであり得る。 In one example, the density (KS M ISO 845) of the foam sheets 101, 101' can average 300-700 kg/m3. Specifically, the density of the foam sheets 101, 101′ is 325-650 kg/m 3 , 350-600 kg/m 3 , 375-550 kg/m 3 , 400-500 kg/m 3 or 425-450 kg/m 3 on average. can be

他の一つの例示において、本発明に係る発泡シート101、101’は200℃で10秒の条件で高温伸び率は325~375%であり得る。具体的には、発泡シート101、101’は200℃で10秒の条件で高温伸び率は330~360%、345~370%または335~360%であり得る。より具体的には、発泡シート101、101’は200℃で10秒の条件で高温伸び率は345~355%であり得る。 In another example, the foam sheets 101, 101' according to the present invention may have a high temperature elongation of 325-375% at 200° C. for 10 seconds. Specifically, the foam sheets 101 and 101' may have a high temperature elongation of 330-360%, 345-370%, or 335-360% at 200° C. for 10 seconds. More specifically, the foam sheets 101 and 101' may have a high temperature elongation of 345 to 355% at 200° C. for 10 seconds.

前記のようなポリエステルおよび炭酸カルシウムを含むことによって、本発明に係る発泡シート101、101’は優秀な加工性を示すことができる。 By including polyester and calcium carbonate as described above, the foam sheets 101 and 101' according to the present invention can exhibit excellent workability.

本発明に係る成形体10の第1および第2発泡シート101、101’はポリエステル樹脂の発泡体であり、前記第1および第2発泡シート101、101’のポリエステル樹脂は、ポリエチレンテレフタレート(Polyethylene Terephthalate、PET)樹脂であり得る。前記PET樹脂を使うことによって、環境に優しく、再使用が容易である。 The first and second foam sheets 101 and 101' of the molded article 10 according to the present invention are polyester resin foams, and the polyester resin of the first and second foam sheets 101 and 101' is polyethylene terephthalate. , PET) resin. By using the PET resin, it is environmentally friendly and easy to reuse.

食品医薬品安全処の器具および容器包装とその原材料に関する規格を基準として、湧出規格の測定時、総湧出量が30ppm以下であり、アンチモン、ゲルマニウム、テレフタル酸、イソフタル酸、アセトアルデヒド物質が検出されず、残留規格の測定時、揮発性物質が検出されないことを特徴とする。 Based on the standards of the Ministry of Food and Drug Safety for equipment, containers and packaging and their raw materials, the total amount of discharge is less than 30ppm when measuring discharge standards, and antimony, germanium, terephthalic acid, isophthalic acid, and acetaldehyde substances are not detected. It is characterized by the fact that no volatile substances are detected when the residual specification is measured.

具体的には、本発明に係る成形体10は前記のように環境に優しい素材であるポリエステル樹脂を使うことによって、大韓民国食品医薬品安全処で発行している器具および容器包装の基準および規格告示全文告示第2015-7号に記載された憂慮物質を許容範囲内に調節することができる。 Specifically, the molding 10 according to the present invention uses polyester resin, which is an environment-friendly material, as described above, so that the full text of the standards and standard notices for utensils and containers and packaging issued by the Ministry of Food and Drug Safety of the Republic of Korea is satisfied. Substances of concern listed in Notification No. 2015-7 can be adjusted within acceptable limits.

このような素材を利用した成形体10を利用して食品包装容器10を製造することによって、環境に優しい食品容器を提供することができる。 By manufacturing the food packaging container 10 using the molding 10 using such materials, it is possible to provide an environment-friendly food container.

一つの例として、本発明に係る成形体10は、バリアー(Barrier)性能、親水化機能または防水機能を有することができ、界面活性剤、親水化剤、熱安定剤、防水剤、セル大きさ拡大剤、赤外線減衰剤、可塑剤、防火化学薬品、顔料、弾性ポリマー、押出補助剤、酸化防止剤、空転防止剤およびUV吸収剤からなる群から選択される一つ以上の機能性添加剤をさらに含むことができる。具体的には、本発明の樹脂発泡シートは増粘剤、熱安定剤および発泡剤を含むことができる。 As an example, the molded body 10 according to the present invention may have a barrier function, a hydrophilic function, or a waterproof function. one or more functional additives selected from the group consisting of extenders, infrared attenuators, plasticizers, fire retardant chemicals, pigments, elastomeric polymers, extrusion aids, antioxidants, anti-slip agents and UV absorbers. can further include: Specifically, the resin foam sheet of the present invention can contain thickeners, heat stabilizers and foaming agents.

前記増粘剤は特に限定しないが、本発明では例えばピロメリット酸二無水物(PMDA)が使用され得る。 Although the thickener is not particularly limited, pyromellitic dianhydride (PMDA) may be used in the present invention.

前記熱安定剤は、有機または無機リン化合物であり得る。前記有機または無機リン化合物は、例えば、リン酸およびその有機エステル、亜リン酸およびその有機エステルであり得る。例えば、前記熱安定剤は商業的に入手可能な物質であって、リン酸、アルキルホスフェートまたはアリールホスフェートであり得る。具体的には、本発明で熱安定剤はトリフェニルホスフェートであり得るが、これに制限されるものではなく、前記樹脂発泡シートの熱的安定性を向上させることができるものであれば、通常の範囲内で制限なく使用可能である。 The thermal stabilizer can be an organic or inorganic phosphorus compound. Said organic or inorganic phosphorus compounds can be, for example, phosphoric acid and its organic esters, phosphorous acid and its organic esters. For example, the thermal stabilizer is a commercially available substance and can be phosphoric acid, alkyl phosphate or aryl phosphate. Specifically, the thermal stabilizer in the present invention may be triphenyl phosphate, but it is not limited to this. It can be used without restrictions within the range of

前記発泡剤の例としては、N、CO、フレオン、ブタン、ペンタン、ネオペンタン、ヘキサン、イソヘキサン、ヘプタン、イソヘプタン、メチルクロライドなどの物理的発泡剤またはアゾジカルボンアミド(azodicarbonamide)系化合物、P、P’-オキシビス(ベンゼンスルホニルヒドラジド)[P、P’-oxy bis(benzene sulfonyl hydrazide)]系化合物、N、N’-ジニトロソペンタメチレンテトラミン(N、N’-dinitroso pentamethylene tetramine)系化合物などの化学的発泡剤があり、具体的には、本発明ではCOが使用され得る。 Examples of the blowing agent include physical blowing agents such as N 2 , CO 2 , freon, butane, pentane, neopentane, hexane, isohexane, heptane, isoheptane, methyl chloride, or azodicarbonamide-based compounds, P, P'-oxybis (benzenesulfonyl hydrazide) [P, P'-oxy bis (benzene sulfonyl hydrazide)] type compounds, N, N'-dinitrosopentamethylene tetramine (N, N'-dinitroso pentamethylene tetramine) type compounds, etc. There are chemical blowing agents, specifically CO2 can be used in the present invention.

また、本発明は成形体の製造方法を提供する。 The present invention also provides a method for producing a molded article.

図2は、本発明に係る成形体の製造方法を順に図示した図面である。図2を参照すると、本発明は、第1発泡シート、ガスバリアー層および第2発泡シートが順に積層された構造のシート1を成形装置の雌型金型21と雄型金型22の間に配置させる段階;および雄型金型22を加圧して成形体10を成形する段階を含み、前記第1発泡シートおよび第2発泡シートはポリエステル樹脂の発泡体であることを特徴とする成形体の製造方法を提供する。 2A to 2C are drawings sequentially illustrating the method for manufacturing a molded body according to the present invention. Referring to FIG. 2, the present invention provides a sheet 1 having a structure in which a first foam sheet, a gas barrier layer and a second foam sheet are laminated in order, between a female mold 21 and a male mold 22 of a molding device. and pressing the male mold 22 to form the molded article 10, wherein the first foam sheet and the second foam sheet are polyester resin foams. A manufacturing method is provided.

一方、第1および第2発泡シートについての製造方法は具体的に限定されないが、例えば、第1および第2発泡シートはポリエステル樹脂を押出発泡して製造することができる。具体的には、発泡方法の種類には大きくビーズ発泡または押出発泡がある。前記ビーズ発泡は、一般的に、樹脂ビーズを加熱して1次発泡させ、これを適当な時間の間熟成させた後に板状、筒状の金型に満たしてさらに加熱し、2次発泡によって融着、成形して製品を作る方法である。その反面、押出発泡は樹脂を加熱して溶融させ、前記樹脂溶融物を連続的に押出および発泡させることによって、工程段階を単純化することができ、大量生産が可能であり、ビーズ発泡時のビーズの間で亀裂と粒状破壊現象などを防止することができる。 On the other hand, the manufacturing method for the first and second foam sheets is not specifically limited, but for example, the first and second foam sheets can be manufactured by extruding and foaming a polyester resin. Specifically, foaming methods are broadly classified into bead foaming and extrusion foaming. Generally, the beads are foamed by heating the resin beads for primary foaming, aging them for an appropriate time, filling them in a plate-like or cylindrical mold, heating them further, and performing secondary foaming. It is a method of making products by fusing and molding. On the other hand, in extrusion foaming, the resin is heated and melted, and the resin melt is continuously extruded and foamed, which simplifies the process steps and enables mass production. Cracks and granulation phenomena between beads can be prevented.

次いで、加工する段階は、第1発泡シート、ガスバリアー層および第2発泡シートが順に積層された構造のシート1を、成形体成形装置20の雌型金型21と雄型金型22の間に配置させる段階および雄型金型22を加圧して成形体10を成形する段階を提供する。 Next, in 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 laminated in this order is placed between the female mold 21 and the male mold 22 of the molded body molding device 20. and pressing the male mold 22 to form the compact 10 .

具体的には、雌型金型21と雄型金型22の間に配置されたシート1は、熱成形されることによって成形体10に成形され得る。前記熱成形としては、真空成形、圧空成形または真空成形と圧空成形を組み合わせた真空圧空成形、雄型金型(プラグ)を使いつつ、または雄型金型22を使った後、真空および/または圧空成形するなどの熱成形がある。 Specifically, the sheet 1 placed between the female mold 21 and the male mold 22 can be formed into the compact 10 by being thermoformed. The thermoforming includes vacuum forming, pressure forming, or vacuum pressure forming combining vacuum forming and pressure forming, using a male mold (plug), or after using a male mold 22, vacuum and/or There is thermoforming such as pressure forming.

図2を参照すると、図2の(a)はシート1を成形する前にシート1を成形装置の雌型金型21と雄型金型22の間に配置する配置段階を示す。図2の(b)は延伸工程および熱工程を示す図面であって、図2(b)のように、雄型金型22を下降させてシート1を延伸し、雌型金型21からの真空吸引によって雌型金型21のキャビティの形状に賦形され、熱が加えられる。図2(c)は、雄型金型22の加圧と雌型金型21からの圧縮空気によって、成形されているシート1が雄型金型22の形状に賦形されて最終成形品である成形体10が成形されることを示す。次いで、成形された成形体10は冷却後に雄型金型22を上昇させることによって取り出され得る。 Referring to FIG. 2, FIG. 2(a) shows the placing step of placing the sheet 1 between the female mold 21 and the male mold 22 of the forming apparatus before molding the sheet 1. As shown in FIG. FIG. 2(b) is a drawing showing the stretching process and the heating process. As shown in FIG. It is formed into the shape of the cavity of the female mold 21 by vacuum suction and heat is applied. FIG. 2(c) shows that the molded sheet 1 is shaped into the shape of the male mold 22 by the pressurization of the male mold 22 and the compressed air from the female mold 21, resulting in the final molded product. A certain molding 10 is shown to be molded. The molded compact 10 can then be removed by raising the male mold 22 after cooling.

併せて、成形する段階は、シートの表面温度が140~160℃となるように熱を印加し、前記雌型金型21および雄型金型22の表面温度を60℃~200℃に設定して成形体10を成形することができる。 In addition, in the molding step, heat is applied so that the surface temperature of the sheet is 140 to 160°C, and the surface temperatures of the female mold 21 and the male mold 22 are set to 60°C to 200°C. The molded body 10 can be molded by pressing.

一方、成形段階で雄型金型22の表面と雌型金型21のキャビティの表面温度は互いに異なり得る。好ましくは、雄型金型22の表面温度はそれぞれ250~280℃、255~275℃、260~270℃または265℃であり得、雌型金型21のキャビティの表面温度は200~250℃、210~240℃、215~235℃、220~230℃または225±3℃であり得る。 Meanwhile, the surface temperatures of the male mold 22 and the cavity of the female mold 21 may differ from each other during the molding process. Preferably, the surface temperature of the male mold 22 can be 250-280°C, 255-275°C, 260-270°C or 265°C, respectively, and the surface temperature of the cavity of the female mold 21 is 200-250°C, It can be 210-240°C, 215-235°C, 220-230°C or 225±3°C.

一つの例示において、雄型金型22の表面温度は265±1℃であり得、雌型金型21の表面温度は225℃であり得、雄型金型22は0.5秒~15秒の間雌型金型21に接触させることが好ましい。併せて、雌型金型21は一側に内部空間であるキャビティを減圧するための減圧ホール23が形成された構造であり得る。 In one example, the surface temperature of the male mold 22 can be 265±1° C., the surface temperature of the female mold 21 can be 225° C., and the male mold 22 can be heated for 0.5 to 15 seconds. It is preferable to contact the female mold 21 during In addition, the female mold 21 may have a structure in which a decompression hole 23 for decompressing a cavity, which is an internal space, is formed on one side.

これにより、前述した成形体の製造方法によってポリエステル樹脂の第1発泡シート、ガスバリアー層、およびポリエステル樹脂の第2発泡シートが順に積層された容器の形状の成形体または前記成形体を含む包装容器を製造することができる。 As a result, a container-shaped molded body in which the first polyester resin foam sheet, the gas barrier layer, and the second polyester resin foam sheet are laminated in order by the above-described molded body manufacturing method, or a packaging container including the molded body can be manufactured.

以下、本発明を実施例および実験例によってより詳細に説明する。 Hereinafter, the present invention will be described in more detail with reference to Examples and Experimental Examples.

ただし、下記の実施例および実験例は本発明を例示するためのものに過ぎず、本発明の内容は下記の実施例および実験例に限定されるものではない。 However, the following examples and experimental examples are only for illustrating the present invention, and the content of the present invention is not limited to the following examples and experimental examples.

製造例1.
PET樹脂100重量部を130℃で乾燥させて水分を除去したし、第1押出機で前記水分が除去されたPET樹脂100重量部、PMDA(pyromellitic dianhydride)1重量部、炭酸カルシウム(CaCO)1重量部、Irganox(IRG 1010)0.1重量部を混合し、280℃に加熱して樹脂溶融物を製造した。その後、第1押出機に発泡剤としてブタンガスを混合し、樹脂溶融物を第2押出機に送って220℃に冷却した。冷却された樹脂溶融物はダイ(Die)を通過しながら発泡シートを形成した。
Production example 1.
100 parts by weight of PET resin was dried at 130° C. to remove moisture, and 100 parts by weight of PET resin from which moisture was removed by a first extruder, 1 part by weight of PMDA (pyromellitic dianhydride), and calcium carbonate (CaCO 3 ). 1 part by weight and 0.1 part by weight of Irganox (IRG 1010) were mixed and heated to 280° C. to prepare a resin melt. After that, butane gas was mixed as a foaming agent in the first extruder, and the resin melt was sent to the second extruder and cooled to 220°C. The cooled resin melt was passed through a die to form a foam sheet.

この時、製造されたポリエステル樹脂発泡シートの密度は380kg/mであり、厚さは1mmであった。 At this time, the manufactured polyester resin foam sheet had a density of 380 kg/m 3 and a thickness of 1 mm.

実施例1
製造例1で製造した発泡シートの一面にバリアー層として0.05mmのEVOHフィルムをラミネーティングし、その上に製造例1で製造した発泡シートを積層した。そして、積層した3層構造のシートを容器の形状に成形し、H/D=0.3の成形体(H:収容部の深さD:開口部の直径)を製造した。前記成形体の開口部の直径は10cmであった。一方、成形体の成形時に、雄型金型の表面温度は60℃であり、雌型金型の表面温度は120℃であった。
Example 1
A 0.05 mm EVOH film was laminated as a barrier layer on one surface of the foamed sheet produced in Production Example 1, and the foamed sheet produced in Production Example 1 was laminated thereon. Then, the laminated three-layer structure sheet was molded into a container shape to produce a molded body with H/D=0.3 (H: depth of container portion D: diameter of opening portion). The diameter of the opening of the molding was 10 cm. On the other hand, the surface temperature of the male mold was 60°C and the surface temperature of the female mold was 120°C during molding of the compact.

実施例2.
バリアー層としては、EVOH0.02mmとPET0.03mmフィルム2 Layerで構成されたことを除いては実施例1と同じ方法で成形体を製造した。
Example 2.
A molded body was manufactured in the same manner as in Example 1, except that the barrier layer consisted of 2 layers of 0.02 mm EVOH and 0.03 mm PET film.

実施例3.
H/Dの値が0.5であることを除いては実施例1と同じ方法で成形体を製造した。
Example 3.
A compact was produced in the same manner as in Example 1, except that the H/D value was 0.5.

比較例1
厚さが2mmであることを除いては製造例1と同じ方法で製造した発泡シートの一面に、バリアー層として0.05mmのEVOHフィルムをラミネーティングして2層構造のシートを製造した。そして、積層した2層構造のシートを容器の形状に成形し、H/D=0.3の成形体(H:収容部の深さD:開口部の直径)を製造した。前記成形体の開口部の直径は10cmであった。一方、雄型金型の表面温度は60℃であり、雌型金型の表面温度は120℃であった。
Comparative example 1
A 0.05 mm thick EVOH film was laminated as a barrier layer on one surface of the foamed sheet manufactured in the same manner as in Preparation Example 1 except that the thickness was 2 mm, thereby manufacturing a two-layer sheet. Then, the laminated two-layered sheet was molded into a container shape to produce a molded body with H/D=0.3 (H: depth of container portion D: diameter of opening portion). The diameter of the opening of the molding was 10 cm. On the other hand, the surface temperature of the male mold was 60°C and the surface temperature of the female mold was 120°C.

比較例2
PP多層シート(PP/EVOH/PP)を使ってH/D0.3の実施例1と同じ構造の容器を成形したし、成形する時の金型の温度は20℃を維持した。
Comparative example 2
A PP multilayer sheet (PP/EVOH/PP) was used to mold a container having the same structure as Example 1 with H/D of 0.3, and the temperature of the mold was maintained at 20°C during molding.

実施例および比較例で成形体のシートの種類および成形条件を下記の表1のように異ならせて成形体を製造した。 In Examples and Comparative Examples, molded bodies were produced by changing the type of sheet and molding conditions as shown in Table 1 below.

Figure 0007110422000001
Figure 0007110422000001

実験例1.酸素透過度の測定
実施例と比較例で製造した成形体に対して、23℃の温度および50%の相対湿度条件下で酸素透過度を測定した。一方、ガスバリアー層が成形体内に均一に分布されたかを確認するために、成形体の試片をランダムに切って測定した。そして、その結果を下記の表2に表した。
Experimental example 1. Measurement of Oxygen Permeability The molded articles produced in Examples and Comparative Examples were measured for oxygen permeability under conditions of a temperature of 23° C. and a relative humidity of 50%. On the other hand, in order to confirm whether the gas barrier layer was evenly distributed in the molded article, a test piece of the molded article was randomly cut and measured. The results are shown in Table 2 below.

<酸素透過度試験>
-試験方法:ASTM D 3985
-試験機器:OX-TRAN 702(MOCON社、アメリカ)
-試験温度:23℃
-試験時間:30分
-測定範囲:0.1~2000cc/mday
-試片の大きさ:横×縦×高さ40mm×40mm×3mm
<Oxygen permeability test>
- Test method: ASTM D 3985
- Test equipment: OX-TRAN 702 (MOCON, USA)
- Test temperature: 23°C
-Test time: 30 minutes -Measurement range: 0.1 to 2000 cc/m 2 day
- Specimen size: width x length x height 40mm x 40mm x 3mm

Figure 0007110422000002
Figure 0007110422000002

前記表2を参照すると、本発明に係る成形体は酸素透過度が低いことを確認することができ、これに伴い、酸素の透過をほぼ防止できることが分かる。これは、ガスバリアー層が成形体の全体面積に均一に分布されていることを意味する。その反面、比較例1の成形体は酸素透過度が高いことを確認することができた。これは、成形体の成形時にガスバリアー層が損傷したためであると判断される。併せて、非発泡製品である比較例2の場合、酸素透過度は低いものの、後述される熱遮断性試験で熱遮断性が優秀でないことを確認することができる。 Referring to Table 2, it can be seen that the molded article according to the present invention has a low oxygen permeability, and accordingly, it can be seen that oxygen permeation can be substantially prevented. This means that the gas barrier layer is uniformly distributed over the entire area of the compact. On the other hand, it was confirmed that the molded article of Comparative Example 1 had a high oxygen permeability. It is considered that this is because the gas barrier layer was damaged during molding of the molded article. In addition, in the case of Comparative Example 2, which is a non-foamed product, although the oxygen permeability is low, it can be confirmed that the heat barrier property is not excellent in the heat barrier property test described below.

反面、比較例1の成形体は酸素透過度が高いことを確認することができた。これは、成形体の成形時にガスバリアー層が損傷したためであると判断される。併せて、非発泡製品である比較例2の場合、酸素透過度は低いものの、後述される熱遮断性試験で熱遮断性が優秀でないことを確認することができる。 On the other hand, it was confirmed that the molded article of Comparative Example 1 had a high oxygen permeability. It is considered that this is because the gas barrier layer was damaged during molding of the molded article. In addition, although Comparative Example 2, which is a non-foamed product, has low oxygen permeability, it can be confirmed that the heat barrier property is not excellent in the heat barrier property test described below.

実験例2.水蒸気透過度の測定
実施例と比較例で製造した成形体に対して、ASTM F 1249を基準として、37℃の温度および100%の相対湿度条件下で、水蒸気透過度を測定した。そして、その結果を下記の表3に表した。
Experimental example 2. Measurement of Water Vapor Permeability The molded bodies produced in Examples and Comparative Examples were measured for water vapor permeability under conditions of a temperature of 37° C. and a relative humidity of 100% based on ASTM F 1249. The results are shown in Table 3 below.

Figure 0007110422000003
Figure 0007110422000003

表3を参照すると、実施例1-3による成形体の場合、それぞれ8.5g/mday、17g/mdayおよび18g/mdayと低い結果を示した。これは、ガスバリアー層が成形体の全体面積に均一に分布されていることを意味する.併せて、比較例1の場合、19g/mdayであって、実施例より高い結果を示した。これは比較例1成形体の成形時にガスバリアー層が損傷したためであると判断される。併せて、非発泡製品である比較例2の場合、酸素透過度は低いものの、後述される熱遮断性試験で熱遮断性が優秀でないことを確認することができる。 Referring to Table 3, the compacts according to Examples 1-3 showed low results of 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 uniformly distributed over the entire area of the compact. In addition, in the case of Comparative Example 1, it was 19 g/m 2 day, which was higher than that of the Examples. It is considered that this is because the gas barrier layer was damaged during molding of the molded article of Comparative Example 1. In addition, although Comparative Example 2, which is a non-foamed product, has low oxygen permeability, it can be confirmed that the heat barrier property is not excellent in the heat barrier property test described below.

実験例3.熱遮断性測定
実施例と比較例による成形体の熱遮断性を評価するために、成形体の内部に100℃の水を70%(v/v)入れた状態で、2分経過した時点で、成形体内部の任意の地点と容器外部の任意の地点の温度を測定した。そして、その結果を表4と表5に表した:
Experimental example 3. Measurement of Thermal Insulation Properties In order to evaluate the thermal insulation properties of the molded articles of Examples and Comparative Examples, 70% (v/v) water at 100° C. was added to the interior of the molded articles, and after 2 minutes, , the temperature was measured at an arbitrary point inside the compact and at an arbitrary point outside the container. And the results are shown in Tables 4 and 5:

[数学式2]
|T-T|≧10℃
[Mathematical formula 2]
|T 2 −T 1 |≧10° C.

前記数学式2において、Tは20℃、1atm条件で、成形体に100℃の水を入れて1分経過したときに測定した成形体の外側の表面温度であり、Tは20℃、1atm条件で、成形体に100℃の水を入れて1分経過したときに測定した成形体の内部の水の温度である。 In the above formula 2 , T1 is the outer surface temperature of the molded body measured after one minute has elapsed after the molded body is filled with water of 100°C under the conditions of 20°C and 1 atm, and T2 is 20°C. It is the temperature of the water inside the molded body measured when water of 100° C. is poured into the molded body under 1 atm condition and one minute has passed.

Figure 0007110422000004
Figure 0007110422000004

前記表4を参照すると、実施例に係る成形体は成形体の内部に収容された水の温度と成形体表面の温度差が10℃以上に示されて、優れた熱遮断性を示すことが分かる。その反面、比較例1および2による成形体は、|T-T|がそれぞれ27℃と0℃であり、熱遮断性が顕著に低かった。したがって、本発明に係る成形体はPET発泡シートを含むことによって優秀な熱遮断性を有し、これによって優れた保温特性および取り扱いの安全性を具現することができることを確認した。 Referring to Table 4, the molded articles according to the examples showed a temperature difference of 10° C. or more between the temperature of the water contained inside the molded article and the temperature of the surface of the molded article, indicating excellent heat shielding properties. I understand. On the other hand, the molded articles according to Comparative Examples 1 and 2 had |T 2 -T 1 | Therefore, it has been confirmed that the molded article according to the present invention has excellent heat insulation properties by including the PET foam sheet, thereby realizing excellent heat retention properties and safe handling.

特に、ガスバリアー層の両面にそれぞれ第1および第2発泡シートを含むことによって優秀な熱遮断性を有することを確認することができた。 In particular, it can be confirmed that the gas barrier layer has excellent heat shielding properties by including the first and second foam sheets on both sides thereof.

これを通じて、本発明に係る成形体は、低い水蒸気透過度および酸素透過度を有し、熱遮断性が優秀であることが分かる。 Through this, it can be seen that the molded article according to the present invention has low water vapor permeability and low oxygen permeability, and excellent heat shielding properties.

本発明に係る成形体は、ガスバリアー層の両面にそれぞれ第1および第2発泡シートを含むことによって酸素および水分透過度を最小化することができるため、これを食品包装容器に使う場合、酸素および水分による食品の腐敗などを防止することができ、食品の保存が容易である。 The molded article according to the present invention can minimize oxygen and moisture permeability by including the first and second foam sheets on both sides of the gas barrier layer, respectively. In addition, it is possible to prevent food from spoiling due to moisture, and it is easy to store food.

1:シート
10:成形体
101:第1発泡シート
101’:第2発泡シート
102:ガスバリアー層
11:底部
12:壁部
13:フランジ
20:金型
21:雌型金型
22:雄型金型
23:減圧ホール
1: Sheet 10: Molded body 101: First foam sheet 101': Second foam sheet 102: Gas barrier layer 11: Bottom part 12: Wall part 13: Flange 20: Mold 21: Female mold 22: Male mold Type 23: decompression hole

Claims (14)

第1発泡シート、ガスバリアー層および第2発泡シートが順に積層された構造であり、
前記第1発泡シートおよび第2発泡シートはポリエステル樹脂の発泡体であり、
前記第1発泡シートおよび第2発泡シートの平均厚さはそれぞれ0.5~1.5mmであることを特徴とする、成形体。
A structure in which a first foam sheet, a gas barrier layer and a second foam sheet are laminated in order,
The first foam sheet and the second foam sheet are polyester resin foams,
A molded article, wherein the average thickness of the first foam sheet and the second foam sheet is 0.5 to 1.5 mm.
下記の数学式1を満足することを特徴とする、請求項1に記載の成形体:
[数学式1]
H/D≧0.01
数学式1において、
収容部および開口部を含む容器構造の成形体を形成するものの、
Hは収容部の深さを示し、1cm~10cmであり、
Dは開口部の直径を示したものである。
The compact according to claim 1, characterized in that it satisfies the following mathematical formula 1:
[Mathematical formula 1]
H/D≧0.01
In formula 1,
Although forming a molded body of a container structure including a container and an opening,
H indicates the depth of the housing portion and is 1 cm to 10 cm,
D indicates the diameter of the opening.
ASTM F 1249による水蒸気透過度が37℃、100%の相対湿度条件下で、50g/m・day以下であり、
ASTM 3985による酸素透過度が23℃の条件下で、20cc/m・day以下であることを特徴とする、請求項1または2に記載の成形体。
Water vapor transmission rate according to ASTM F 1249 is 50 g/m 2 ·day or less under conditions of 37 ° C. and 100% relative humidity,
3. The molded article according to claim 1, wherein the oxygen permeability according to ASTM D 3985 is 20 cc/m< 2 > .day or less at 23[deg.]C.
ガスバリアー層の平均厚さは0.01~2mmであり、成形体の平均厚さは1mm~5mm範囲であることを特徴とする、請求項1~3のいずれかに記載の成形体。 The molded article according to any one of claims 1 to 3, wherein the gas barrier layer has an average thickness of 0.01 to 2 mm, and the molded article has an average thickness of 1 mm to 5 mm. ガスバリアー層は、エチレンビニルアルコール、ポリビニリデンクロライドおよびポリエチレンテレフタレートのうち1種以上を含むことを特徴とする、請求項1~4のいずれかに記載の成形体。 The molded article according to any one of claims 1 to 4, wherein the gas barrier layer contains one or more of ethylene vinyl alcohol, polyvinylidene chloride and polyethylene terephthalate. ガスバリアー層の融点(T)は、平均150℃~190℃であり、
第1および第2発泡シートの融点(T)は、平均240℃~260℃であることを特徴とする、請求項1~5のいずれかに記載の成形体。
The melting point (T m ) of the gas barrier layer is 150° C. to 190° C. on average,
The molded article according to any one of claims 1 to 5, wherein the melting point (T m ) of the first and second foam sheets is 240°C to 260°C on average.
ポリエステル樹脂は、ポリエチレンテレフタレート(polyethylene terephthalate)樹脂であることを特徴とする、請求項1~6のいずれかに記載の成形体。 The molded article according to any one of claims 1 to 6, wherein the polyester resin is a polyethylene terephthalate resin. 第1および第2発泡シートはそれぞれ0.5~9.0重量%の炭酸カルシウムを含むことを特徴とする、請求項1~7のいずれかに記載の成形体。 The molding according to any one of claims 1 to 7, characterized in that the first and second foam sheets each contain 0.5 to 9.0% by weight of calcium carbonate. 下記の数学式2を満足することを特徴とする、請求項1~8のいずれかに記載の成形体:
[数学式2]
|T-T|≧10℃
前記数学式2において、
は20℃、1atm条件で、成形体に100℃の水を入れて1分経過したときに測定した成形体の外側の表面温度であり、
は20℃、1atm条件で、成形体に100℃の水を入れて1分経過したときに測定した成形体の内部の水の温度である。
The molded article according to any one of claims 1 to 8, characterized in that it satisfies the following mathematical formula 2:
[Mathematical formula 2]
|T 2 −T 1 |≧10° C.
In the mathematical formula 2,
T 1 is the outer surface temperature of the molded body measured after 1 minute has passed after the molded body is filled with water of 100 ° C. under the conditions of 20 ° C. and 1 atm,
T2 is the temperature of the water inside the compact measured after one minute has passed after the compact was filled with water of 100°C under the conditions of 20 °C and 1 atm.
請求項1~9のいずれかに記載された成形体を含む、包装容器。 A packaging container comprising the molded article according to any one of claims 1 to 9. 包装容器は食品包装容器であることを特徴とする、請求項10に記載の包装容器。 11. The packaging container according to claim 10, wherein the packaging container is a food packaging container. 第1発泡シート、ガスバリアー層および第2発泡シートが順に積層された構造のシートを、成形装置の雌型金型と雄型金型の間に配置させる段階;および
雄型金型を加圧して成形体を成形する段階;を含み、
前記第1発泡シートおよび第2発泡シートはポリエステル樹脂の発泡体であり、
前記第1発泡シートおよび第2発泡シートの平均厚さはそれぞれ0.5~1.5mmであることを特徴とする、成形体の製造方法。
disposing a sheet having a structure in which a first foam sheet, a gas barrier layer and a second foam sheet are laminated in order between a female mold and a male mold of a molding device; and pressurizing the male mold. forming the compact with;
The first foam sheet and the second foam sheet are polyester resin foams,
A method for producing a molded article, wherein the first foam sheet and the second foam sheet each have an average thickness of 0.5 to 1.5 mm.
成形する段階は、シートの表面温度が140~160℃となるように熱を印加し、前記雌型金型および雄型金型の表面温度を60~200℃に設定して成形体を成形することを特徴とする、請求項12に記載の成形体の製造方法。 In the molding step, heat is applied so that the surface temperature of the sheet is 140 to 160° C., and the surface temperature of the female mold and the male mold is set to 60 to 200° C. to mold the molded body. 13. The method for producing a molded article according to claim 12, characterized by: 雌型金型は、一側に内部空間を減圧する減圧ホールが形成された構造であることを特徴とする、請求項12または13に記載の成形体の製造方法。 14. The method of claim 12 or 13, wherein the female mold has a structure in which a decompression hole for decompressing the internal space is formed on one side.
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