JP7496678B2 - Polystyrene resin foam sheet and container - Google Patents
Polystyrene resin foam sheet and container Download PDFInfo
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- JP7496678B2 JP7496678B2 JP2019183808A JP2019183808A JP7496678B2 JP 7496678 B2 JP7496678 B2 JP 7496678B2 JP 2019183808 A JP2019183808 A JP 2019183808A JP 2019183808 A JP2019183808 A JP 2019183808A JP 7496678 B2 JP7496678 B2 JP 7496678B2
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- 239000006260 foam Substances 0.000 title claims description 18
- 229920005990 polystyrene resin Polymers 0.000 title claims description 7
- 239000004088 foaming agent Substances 0.000 claims description 64
- 229920005989 resin Polymers 0.000 claims description 45
- 239000011347 resin Substances 0.000 claims description 45
- 239000000126 substance Substances 0.000 claims description 41
- 239000004793 Polystyrene Substances 0.000 claims description 20
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical group [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 20
- 229920002223 polystyrene Polymers 0.000 claims description 19
- IJDNQMDRQITEOD-UHFFFAOYSA-N sec-butylidene Natural products CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 16
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 15
- 239000005001 laminate film Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- 235000017557 sodium bicarbonate Nutrition 0.000 claims description 11
- 229910000030 sodium bicarbonate Inorganic materials 0.000 claims description 10
- 229920003145 methacrylic acid copolymer Polymers 0.000 claims description 9
- 229940117841 methacrylic acid copolymer Drugs 0.000 claims description 9
- JQXYBDVZAUEPDL-UHFFFAOYSA-N 2-methylidene-5-phenylpent-4-enoic acid Chemical compound OC(=O)C(=C)CC=CC1=CC=CC=C1 JQXYBDVZAUEPDL-UHFFFAOYSA-N 0.000 claims description 8
- 229920001577 copolymer Polymers 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 6
- PYSRRFNXTXNWCD-UHFFFAOYSA-N 3-(2-phenylethenyl)furan-2,5-dione Chemical compound O=C1OC(=O)C(C=CC=2C=CC=CC=2)=C1 PYSRRFNXTXNWCD-UHFFFAOYSA-N 0.000 claims description 5
- 229920000147 Styrene maleic anhydride Polymers 0.000 claims description 5
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 4
- 238000003856 thermoforming Methods 0.000 claims description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- FEIQOMCWGDNMHM-UHFFFAOYSA-N 5-phenylpenta-2,4-dienoic acid Chemical compound OC(=O)C=CC=CC1=CC=CC=C1 FEIQOMCWGDNMHM-UHFFFAOYSA-N 0.000 claims 1
- 238000000691 measurement method Methods 0.000 claims 1
- 238000000465 moulding Methods 0.000 description 26
- 230000032683 aging Effects 0.000 description 17
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 14
- 230000032798 delamination Effects 0.000 description 11
- 238000004519 manufacturing process Methods 0.000 description 10
- -1 cyclic aliphatic hydrocarbons Chemical class 0.000 description 9
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 9
- 229920000098 polyolefin Polymers 0.000 description 8
- 239000001273 butane Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 4
- 239000010410 layer Substances 0.000 description 4
- 229920005604 random copolymer Polymers 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 238000001746 injection moulding Methods 0.000 description 3
- 238000003475 lamination Methods 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 150000007524 organic acids Chemical class 0.000 description 3
- 229910052623 talc Inorganic materials 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 239000001282 iso-butane Substances 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 229920001955 polyphenylene ether Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002356 single layer Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 239000000454 talc Substances 0.000 description 2
- 238000009823 thermal lamination Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 1
- NPNPZTNLOVBDOC-UHFFFAOYSA-N 1,1-difluoroethane Chemical compound CC(F)F NPNPZTNLOVBDOC-UHFFFAOYSA-N 0.000 description 1
- BHNZEZWIUMJCGF-UHFFFAOYSA-N 1-chloro-1,1-difluoroethane Chemical compound CC(F)(F)Cl BHNZEZWIUMJCGF-UHFFFAOYSA-N 0.000 description 1
- 239000004156 Azodicarbonamide Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical class OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- PMPVIKIVABFJJI-UHFFFAOYSA-N Cyclobutane Chemical compound C1CCC1 PMPVIKIVABFJJI-UHFFFAOYSA-N 0.000 description 1
- 239000004338 Dichlorodifluoromethane Substances 0.000 description 1
- MWRWFPQBGSZWNV-UHFFFAOYSA-N Dinitrosopentamethylenetetramine Chemical compound C1N2CN(N=O)CN1CN(N=O)C2 MWRWFPQBGSZWNV-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 235000010724 Wisteria floribunda Nutrition 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 1
- 235000019399 azodicarbonamide Nutrition 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 238000000071 blow moulding Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- NEHMKBQYUWJMIP-NJFSPNSNSA-N chloro(114C)methane Chemical compound [14CH3]Cl NEHMKBQYUWJMIP-NJFSPNSNSA-N 0.000 description 1
- HRYZWHHZPQKTII-UHFFFAOYSA-N chloroethane Chemical compound CCCl HRYZWHHZPQKTII-UHFFFAOYSA-N 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 229960003750 ethyl chloride Drugs 0.000 description 1
- 229920006226 ethylene-acrylic acid Polymers 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010097 foam moulding Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000005003 food packaging material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 description 1
- 150000002429 hydrazines Chemical class 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229940073584 methylene chloride Drugs 0.000 description 1
- 150000002832 nitroso derivatives Chemical class 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000001175 rotational moulding Methods 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 150000003349 semicarbazides Chemical class 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000001509 sodium citrate Substances 0.000 description 1
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 1
- 229940029284 trichlorofluoromethane Drugs 0.000 description 1
- 238000007666 vacuum forming Methods 0.000 description 1
Landscapes
- Containers Having Bodies Formed In One Piece (AREA)
- Wrappers (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Laminated Bodies (AREA)
Description
本発明は、生産性及び成形性に優れるポリスチレン系樹脂発泡シート(PSPシート)及び該PSPシートを成形して得られる容器に関する。 The present invention relates to a polystyrene resin foam sheet (PSP sheet) that is excellent in productivity and moldability, and a container obtained by molding the PSP sheet.
PSPシートは、軽量で熱成形性に優れていることから、各種食品包装材及び簡易容器として広く用いられている。PSPシートは一般に、押出機内で溶融されたポリスチレン系樹脂にブタン及びペンタン等の脂肪族炭化水素等からなる物理発泡剤を圧入しながら、シート状に押出す方法により製造されている。 PSP sheets are widely used as various food packaging materials and simple containers because they are lightweight and have excellent thermoformability. PSP sheets are generally manufactured by extruding molten polystyrene resin in an extruder into a sheet while pressing in a physical foaming agent made of aliphatic hydrocarbons such as butane and pentane.
発泡シートに含まれる発泡剤は、製造後、徐々に散逸する。発泡剤の残存量が発泡シートの成形性に影響を与えることが知られている。例えば、発泡剤の残存量が少なすぎると、成形品の強度不足や賦形性の低下が生じ易く、多すぎると成形品の収縮や反り、及び表面荒れ等の成形異常を来すことが知られている(特許文献1及び2参照)。そのため、発泡剤の残存量を適量とするために、PSPシートを製造した後、エージング期間を経ることが必要なことが知られている。 The foaming agent contained in the foam sheet gradually dissipates after production. It is known that the remaining amount of foaming agent affects the moldability of the foam sheet. For example, if the amount of remaining foaming agent is too small, the molded product is likely to have insufficient strength and reduced formability, while if the amount of remaining foaming agent is too large, it is known to cause molding abnormalities such as shrinkage, warping, and surface roughness of the molded product (see Patent Documents 1 and 2). Therefore, it is known that an aging period is necessary after production of the PSP sheet in order to ensure that the remaining amount of foaming agent is appropriate.
一般のPSPシートでは、物理発泡剤のノルマルブタンの含有量が多いと、発泡剤の散逸速度が速いことが知られている(特許文献1)。一方、ポリスチレン系樹脂として、メタクリル酸等と共重合させたスチレン系共重合体を含む耐熱性PSPシートの場合、ノルマルブタンの含有量が多くても、発泡剤残存量の低下が遅い。そのため、エージング期間が一般のPSPシートと比較して長く、生産性が低いという問題がある。 It is known that in general PSP sheets, the higher the content of normal butane, a physical foaming agent, the faster the foaming agent dissipates (Patent Document 1). On the other hand, in the case of heat-resistant PSP sheets that contain a styrene copolymer copolymerized with methacrylic acid or the like as a polystyrene resin, the decrease in the remaining amount of foaming agent is slow even if the normal butane content is high. Therefore, the aging period is longer than that of general PSP sheets, resulting in a problem of low productivity.
本発明は、エージング期間が短く、生産性に優れると共に、成形性に優れるPSPシート及び該シートを成形して得られる容器を提供することを目的とする。 The present invention aims to provide a PSP sheet that has a short aging period, excellent productivity, and excellent moldability, and a container obtained by molding the sheet.
本発明のPSPシートは、スチレン-メタクリル酸共重合体、スチレン-アクリル酸系共重合体、又はスチレン-無水マレイン酸系共重合体を含有する基材樹脂に、ノルマルブタンを含む物理発泡剤及び化学発泡剤を添加して発泡させることにより得られるポリスチレン系樹脂発泡シートであって、前記化学発泡剤の添加量が1質量%以上5質量%以下であり、前記ポリスチレン系樹脂発泡シート内の残存ガス量が0.161g以下であることを特徴とする。 The PSP sheet of the present invention is a polystyrene-based resin foam sheet obtained by adding a physical foaming agent and a chemical foaming agent containing normal butane to a base resin containing a styrene-methacrylic acid copolymer, a styrene-acrylic acid copolymer, or a styrene-maleic anhydride copolymer, and foaming the base resin, and is characterized in that the amount of the chemical foaming agent added is 1% by mass or more and 5% by mass or less, and the amount of gas remaining in the polystyrene-based resin foam sheet is 0.161 g or less.
本発明の容器は、本発明のPSPシートを熱成形することにより成形された容器であることを特徴とする。 The container of the present invention is characterized in that it is a container formed by thermoforming the PSP sheet of the present invention.
本発明のPSPシートは、従来の耐熱性PSPシートと比べてエージング期間が短いことから、生産性に優れている。また、本発明のPSPシートを用いた場合、容器成形時のデラミ(ラミネートフィルムの剥がれ)を抑制することができる等、従来の耐熱性PSPシートと比べて成形性に優れている。 The PSP sheet of the present invention has a shorter aging period than conventional heat-resistant PSP sheets, and therefore has excellent productivity. In addition, when the PSP sheet of the present invention is used, it is possible to suppress delamination (peeling of the laminate film) during container molding, and it has superior moldability compared to conventional heat-resistant PSP sheets.
本発明の実施の形態について以下に説明する。本実施形態は本発明を実施する一例であって、本発明は本実施形態に限定されるものではない。 The following describes an embodiment of the present invention. This embodiment is an example of implementing the present invention, and the present invention is not limited to this embodiment.
本実施形態に係るPSPシート(以下、「本PSPシート」という。)は、スチレン-メタクリル酸共重合体、スチレン-アクリル酸系共重合体、又はスチレン-無水マレイン酸系共重合体を含有する基材樹脂に、ノルマルブタンを含む物理発泡剤及び化学発泡剤を添加して発泡させることにより得られ、前記化学発泡剤の添加量が1質量%以上であり、前記ポリスチレン系樹脂発泡シート内の残存ガス量が0.161g以下である。 The PSP sheet according to this embodiment (hereinafter referred to as "this PSP sheet") is obtained by adding a physical foaming agent and a chemical foaming agent containing normal butane to a base resin containing a styrene-methacrylic acid copolymer, a styrene-acrylic acid copolymer, or a styrene-maleic anhydride copolymer, and foaming the base resin, the amount of the chemical foaming agent added being 1% by mass or more, and the amount of gas remaining in the polystyrene resin foam sheet being 0.161 g or less.
前記基材樹脂は、スチレン-メタクリル酸共重合体、スチレン-アクリル酸系共重合体、又はスチレン-無水マレイン酸系共重合体(以下、「スチレン-メタクリル酸共重合体等」という。)を含有する。そのため、本PSPシートは耐熱性に優れている。前記基材樹脂は、スチレン-メタクリル酸共重合体、スチレン-アクリル酸系共重合体、及びスチレン-無水マレイン酸系共重合体の1種のみを含んでもよく、2種以上を含んでもよい。前記基材樹脂は、前記スチレン-メタクリル酸共重合体等のみで構成されていてもよく、前記スチレン-メタクリル酸共重合体等を主成分として、他の重合体、樹脂、及びゴムの1種又は2種以上を副成分として混合した混合樹脂でもよい。前記副成分として混合することができる樹脂として例えば、ポリフェニレンエーテル系樹脂が挙げられる。前記基材樹脂中の前記スチレン-メタクリル酸共重合体等の割合は、通常70質量%以上、好ましくは80質量%以上である。 The base resin contains a styrene-methacrylic acid copolymer, a styrene-acrylic acid copolymer, or a styrene-maleic anhydride copolymer (hereinafter referred to as "styrene-methacrylic acid copolymer, etc."). Therefore, the PSP sheet has excellent heat resistance. The base resin may contain only one of styrene-methacrylic acid copolymer, styrene-acrylic acid copolymer, and styrene-maleic anhydride copolymer, or may contain two or more of them. The base resin may be composed of only the styrene-methacrylic acid copolymer, etc., or may be a mixed resin in which the styrene-methacrylic acid copolymer, etc. is the main component and one or more of other polymers, resins, and rubbers are mixed as secondary components. An example of a resin that can be mixed as the secondary component is a polyphenylene ether resin. The ratio of the styrene-methacrylic acid copolymer, etc. in the base resin is usually 70% by mass or more, preferably 80% by mass or more.
前記物理発泡剤は、ノルマルブタンを含み、前記基材樹脂を発泡させることができる限り特に限定はない。前記物理発泡剤として具体的には、例えば、プロパン、n-ブタン、i-ブタン、n-ブタンとi-ブタンとの混合物、ペンタン、ヘキサン等の脂肪族炭化水素;シクロブタン、シクロペンタン等の環式脂肪族炭化水素;及びトリクロロフロロメタン、ジクロロジフロロメタン、1,1-ジフルオロエタン、1,1-ジフルオロ-1-クロロエタン、1,1,1,2-テトラフルオロエタン、メチルクロライド、エチルクロライド、メチレンクロライド等のハロゲン化炭化水素;並びにこれらの混合物等の低沸点の有機化合物が挙げられる。前記発泡剤として、ブタン及びブタンと他の脂肪族炭化水素(例えば、イソブタン)との混合物が好ましく、特に、n-ブタン:i-ブタン=50~100:0~50(質量基準)の混合物が好ましい。 The physical foaming agent is not particularly limited as long as it contains normal butane and can foam the base resin. Specific examples of the physical foaming agent include aliphatic hydrocarbons such as propane, n-butane, i-butane, a mixture of n-butane and i-butane, pentane, and hexane; cyclic aliphatic hydrocarbons such as cyclobutane and cyclopentane; and halogenated hydrocarbons such as trichlorofluoromethane, dichlorodifluoromethane, 1,1-difluoroethane, 1,1-difluoro-1-chloroethane, 1,1,1,2-tetrafluoroethane, methyl chloride, ethyl chloride, and methylene chloride; and low-boiling organic compounds such as mixtures thereof. As the foaming agent, butane and a mixture of butane and other aliphatic hydrocarbons (e.g., isobutane) are preferred, and a mixture of n-butane:i-butane=50-100:0-50 (by mass) is particularly preferred.
前記物理発泡剤の添加量は、必要に応じて適宜選択することができる。前記添加量は通常、前記基材樹脂と前記化学発泡剤(添加量)との合計100質量部に対し、0.05~5.0質量部とすることができる。より具体的には、前記物理発泡剤として、ブタンと他の脂肪族炭化水素(例えば、イソブタン)との混合物、特にn-ブタン:i-ブタン=50~100:0~50(質量基準)の混合物を、前記基材樹脂と前記化学発泡剤(添加量)との合計100質量部に対し、0.05~5.0質量部用いることが好ましい。 The amount of the physical foaming agent added can be appropriately selected as needed. The amount can usually be 0.05 to 5.0 parts by mass per 100 parts by mass of the total of the base resin and the chemical foaming agent (amount added). More specifically, it is preferable to use a mixture of butane and other aliphatic hydrocarbons (e.g., isobutane), particularly a mixture of n-butane:i-butane = 50-100:0-50 (by mass), as the physical foaming agent, in an amount of 0.05 to 5.0 parts by mass per 100 parts by mass of the total of the base resin and the chemical foaming agent (amount added).
前記化学発泡剤は、分解して炭酸ガス等の気体を発生するものであれば特に限定はない。前記化学発泡剤は1種単独でもよく、2種以上を併用してもよい。前記化学発泡剤は、有機系又は無機系の化学発泡剤のいずれでもよい。前記有機系化学発泡剤として具体的には、例えば、クエン酸ナトリウム等の有機酸塩、アゾジカルボンアミド等のアゾ化合物及びN,N’-ジニトロソペンタメチレンテトラミン等のニトロソ化合物、トルエンスルホニルヒドラジド等のヒドラジン誘導体、及びトルエンスルホニルセミカルバジド等のセミカルバジド化合物が挙げられる。前記無機系化学発泡剤として具体的には、例えば、炭酸ナトリウム等の炭酸塩及び炭酸水素ナトリウム等の炭酸水素塩が挙げられる。更に、前記化学発泡剤として、炭酸水素ナトリウムとクエン酸等の有機酸との混合物を用いることができる。前記化学発泡剤として好ましくは、炭酸水素ナトリウム並びに炭酸水素ナトリウム及び有機酸(クエン酸等)の混合物から選択される。 The chemical foaming agent is not particularly limited as long as it decomposes to generate a gas such as carbon dioxide gas. The chemical foaming agent may be one type alone or two or more types in combination. The chemical foaming agent may be either an organic or inorganic chemical foaming agent. Specific examples of the organic chemical foaming agent include organic acid salts such as sodium citrate, azo compounds such as azodicarbonamide, nitroso compounds such as N,N'-dinitrosopentamethylenetetramine, hydrazine derivatives such as toluenesulfonylhydrazide, and semicarbazide compounds such as toluenesulfonylsemicarbazide. Specific examples of the inorganic chemical foaming agent include carbonates such as sodium carbonate and bicarbonates such as sodium bicarbonate. Furthermore, a mixture of sodium bicarbonate and an organic acid such as citric acid can be used as the chemical foaming agent. The chemical foaming agent is preferably selected from sodium bicarbonate and a mixture of sodium bicarbonate and an organic acid (such as citric acid).
前記化学発泡剤の添加量は、前記基材樹脂と前記化学発泡剤との合計100質量%中、下限が1質量%以上、好ましくは1.1質量%以上、より好ましくは1.5質量%以上であり、上限が5質量%以下、好ましくは3質量%以下である。前記化学発泡剤の添加量の下限が前記範囲未満であると、発泡剤残存量の低下が遅く、エージング期間が長くなる結果、発泡シートの生産性に劣るので好ましくない。より具体的には、前記化学発泡剤として、有機系又は無機系の化学発泡剤、特に炭酸水素ナトリウム並びに炭酸水素ナトリウム及び有機酸(クエン酸等)の混合物から選択される化学発泡剤を、前記基材樹脂と前記化学発泡剤との合計100質量%中、1質量%以上用いることが好ましい。尚、前記化学発泡剤の添加量の上限は、特許請求の範囲の記載の明確化の観点から画定したに過ぎず、上限を超えた場合に本PSPシートが得られないことを自認するものでもなく、また、上限を超えた場合に得られた本PSPシートを、特許請求の範囲の範囲から除外することを積極的に意図するものでもない。 The amount of the chemical foaming agent added is 1% by mass or more, preferably 1.1% by mass or more, more preferably 1.5% by mass or more, and 5% by mass or less, preferably 3% by mass or less, based on the total 100% by mass of the base resin and the chemical foaming agent. If the lower limit of the amount of the chemical foaming agent added is less than the above range, the remaining amount of the foaming agent decreases slowly, and the aging period becomes longer, resulting in poor productivity of the foamed sheet, which is not preferable. More specifically, it is preferable to use an organic or inorganic chemical foaming agent, particularly a chemical foaming agent selected from sodium bicarbonate and a mixture of sodium bicarbonate and an organic acid (such as citric acid), as the chemical foaming agent, in an amount of 1% by mass or more based on the total 100% by mass of the base resin and the chemical foaming agent. The upper limit of the amount of the chemical foaming agent added is merely determined from the perspective of clarifying the claims, and does not acknowledge that the PSP sheet cannot be obtained when the upper limit is exceeded, nor does it actively intend to exclude the PSP sheet obtained when the upper limit is exceeded from the scope of the claims.
前記化学発泡剤の添加方法には特に限定はない。前記化学発泡剤は例えば、前記基材樹脂と予め混合してから押出機や射出成形機に供給される方法、押出機中の前記基材樹脂に添加する方法、及びポリスチレン系樹脂をベースとするマスターバッチを作成し添加する方法により添加することができる。また、前記化学発泡剤と前記物理発泡剤の添加順序にも限定はない。両者は同時に添加してもよく、いずれか一方を先に添加し、他方を後に添加してもよい。 There is no particular limitation on the method of adding the chemical foaming agent. For example, the chemical foaming agent can be added by mixing it with the base resin beforehand and then feeding it to an extruder or injection molding machine, adding it to the base resin in an extruder, or creating and adding a master batch based on a polystyrene resin. There is also no limitation on the order of addition of the chemical foaming agent and the physical foaming agent. Both may be added at the same time, or one may be added first and the other added later.
本PSPシートの形成において、前記物理発泡剤及び前記化学発泡剤と共に気泡調整剤を併用することができる。該気泡調整剤として具体的には、例えば、タルク、シリカ等の無機粉末;多価カルボン酸の酸性塩;及び多価カルボン酸と炭酸ナトリウム又は重炭酸ナトリウムとの反応混合物が挙げられる。 In forming the PSP sheet, a bubble regulator can be used in combination with the physical foaming agent and the chemical foaming agent. Specific examples of the bubble regulator include inorganic powders such as talc and silica; acid salts of polycarboxylic acids; and reaction mixtures of polycarboxylic acids with sodium carbonate or sodium bicarbonate.
本PSPシート内の残存ガス量は0.161g以下である。該残存ガス量が前記範囲内であると、容器成形時のデラミの抑制等により、成形性を向上させることができるので好ましい。前記残存ガス量は、実施例に記載の方法により算出される揮発量(g)として定義される。前記残存ガス量は、PSPシート製造時点の量に限定されない。前記残存ガス量は、製造後、一定のエージング期間(例えば、製造から70日後、65日後、60日後、50日後、又は45日後)を経た後の量でもよい。また、後述のように、本PSPシートは、少なくとも片面にラミネートフィルムが積層されていてもよい。この場合、前記残存ガス量は、ラミネートフィルムが積層されていない発泡シート単体に基づいて算出される。 The amount of residual gas in the PSP sheet is 0.161 g or less. It is preferable that the amount of residual gas is within the above range, since it is possible to improve moldability by suppressing delamination during container molding. The amount of residual gas is defined as the amount of volatilization (g) calculated by the method described in the Examples. The amount of residual gas is not limited to the amount at the time of manufacturing the PSP sheet. The amount of residual gas may be the amount after a certain aging period (e.g., 70 days, 65 days, 60 days, 50 days, or 45 days after manufacturing) has passed after manufacturing. In addition, as described later, the PSP sheet may have a laminate film laminated on at least one side. In this case, the amount of residual gas is calculated based on the foam sheet alone without the laminate film laminated thereon.
本PSPシートに含まれる気泡構造には特に限定はない。前記気泡構造は、気泡の間で気層の交換がなされない独立気泡構造でもよく、樹脂膜に孔が開いており、気層が行き来する連続気泡構造のいずれでもよい。本PSPシートでは、独立気泡構造を含むことが好ましい。独立気泡構造を有すると、デラミの抑制等、本PSPシートの成形性を向上させることができるので好ましい。具体的には、本PSPシートの独立気泡率が、気泡全体の体積の少なくとも90体積%以上であることが好ましく、より好ましくは95体積%以上、更に好ましくは97.0体積%以上である。前記独立気泡率は、実施例に記載の方法により算出される。本PSPシートの独立気泡率が90体積%未満になると、揮発量0.161g以下でもデラミが発生しやすくなり、2次厚みのバラツキが大きくなる。本PSPシートの独立気泡率が90体積%以上であると、揮発量が0.161g以下において、デラミの発生及び2次厚みのバラツキを抑制することができるので好ましい。 There is no particular limitation on the bubble structure contained in the PSP sheet. The bubble structure may be either a closed bubble structure in which no air layers are exchanged between the bubbles, or a continuous bubble structure in which holes are opened in the resin film and air layers move back and forth. It is preferable that the PSP sheet contains a closed bubble structure. Having a closed bubble structure is preferable because it can improve the moldability of the PSP sheet, such as suppressing delamination. Specifically, it is preferable that the closed bubble rate of the PSP sheet is at least 90% by volume or more of the total volume of the bubbles, more preferably 95% by volume or more, and even more preferably 97.0% by volume or more. The closed bubble rate is calculated by the method described in the examples. If the closed bubble rate of the PSP sheet is less than 90% by volume, delamination is likely to occur even with an amount of evaporation of 0.161 g or less, and the variation in secondary thickness increases. If the closed bubble rate of the PSP sheet is 90% by volume or more, it is preferable because it can suppress the occurrence of delamination and the variation in secondary thickness when the amount of evaporation is 0.161 g or less.
本PSPシートの具体的形状には特に限定はない。本PSPシートの具体的形状は、必要に応じて適宜決定することができる。よって、前記「シート」の用語には、フィルム状も含まれる。本シートの厚みは、例えば、0.1~5mm、あるいは0.5~3mmとすることができる。 There is no particular limitation on the specific shape of the PSP sheet. The specific shape of the PSP sheet can be appropriately determined as needed. Therefore, the term "sheet" also includes a film-like shape. The thickness of the sheet can be, for example, 0.1 to 5 mm, or 0.5 to 3 mm.
本PSPシートの製造方法には特に限定はない。本PSPシートは通常、前記基材樹脂、前記物理発泡剤、及び前記化学発泡剤を混合した発泡性溶融樹脂を、押出機により押出して発泡させることにより得ることができる。前記化学発泡剤の添加量は、前記基材樹脂と前記化学発泡剤との合計100質量%中、1質量%以上、好ましくは1.1質量%以上、より好ましくは1.5質量%以上である。本PSPシートの製造に関し、前記化学発泡剤の種類及び添加量の上限並びに前記物理発泡剤の種類及び添加量については、上記の説明が該当する。また、本PSPシートの製造方法において、シート中の残存ガス量を適宜の範囲とするために、製造されたシートを室温(例えば、10~25℃)で一定期間(エージング期間;例えば、製造から70日後、65日後、60日後、50日後、又は45日後)保管してもよい。 There is no particular limitation on the manufacturing method of the PSP sheet. The PSP sheet can usually be obtained by extruding a foamable molten resin, which is a mixture of the base resin, the physical foaming agent, and the chemical foaming agent, with an extruder to foam it. The amount of the chemical foaming agent added is 1% by mass or more, preferably 1.1% by mass or more, and more preferably 1.5% by mass or more, based on 100% by mass of the total of the base resin and the chemical foaming agent. The above explanation applies to the type and upper limit of the amount of the chemical foaming agent and the type and amount of the physical foaming agent in the manufacturing method of the PSP sheet. In addition, in the manufacturing method of the PSP sheet, the manufactured sheet may be stored at room temperature (e.g., 10 to 25°C) for a certain period (aging period; e.g., 70 days, 65 days, 60 days, 50 days, or 45 days after manufacturing) in order to set the amount of residual gas in the sheet to an appropriate range.
本PSPシートは、少なくとも片面、好ましくは両面にラミネートフィルムが積層されていてもよい。本PSPシートにラミネートフィルムを積層した場合、容器内側に耐油性を付与することができて、容器内外には意匠性を付与することができるので好ましい。前記ラミネートフィルムを積層する方法には特に限定はない。該方法として、公知のラミネート方法、例えば熱ラミネート及び押出しラミネートを用いることができる。 The PSP sheet may have a laminate film laminated on at least one side, preferably both sides. When a laminate film is laminated on the PSP sheet, it is preferable because it can impart oil resistance to the inside of the container and can impart design to the inside and outside of the container. There is no particular limitation on the method for laminating the laminate film. As the method, a known lamination method, such as thermal lamination and extrusion lamination, can be used.
前記ラミネートフィルムの材質には特に限定はない。前記ラミネートフィルムとして具体的には、例えば、ポリスチレン(PS)フィルム及びポリオレフィンフィルムが挙げられる。前記ポリオレフィンフィルムとして無延伸ポリオレフィンフィルムを用いることができる。無延伸ポリオレフィンフィルムは、エチレン又はプロピレンを主成分とするポリオレフィン類からなるフィルムをいう。前記無延伸ポリオレフィンフィルムとして具体的には、例えば、1-ブテンを含む直鎖状低密度ポリエチレン、ポリプロピレン、エチレン-酢酸ビニルランダム共重合体、エチレン-アクリル酸エステルランダム共重合体、プロピレン-エチレンランダム共重合体、又は、プロピレン-エチレン-1-ブテンランダム共重合体からなるフィルムが挙げられる。前記無延伸ポリオレフィンフィルムとして好ましくは、無延伸ポリプロピレンフィルム(CPPフィルム)である。 There is no particular limitation on the material of the laminate film. Specific examples of the laminate film include polystyrene (PS) film and polyolefin film. As the polyolefin film, a non-stretched polyolefin film can be used. The non-stretched polyolefin film refers to a film made of polyolefins whose main component is ethylene or propylene. Specific examples of the non-stretched polyolefin film include films made of linear low-density polyethylene containing 1-butene, polypropylene, ethylene-vinyl acetate random copolymer, ethylene-acrylic acid ester random copolymer, propylene-ethylene random copolymer, or propylene-ethylene-1-butene random copolymer. The non-stretched polyolefin film is preferably a non-stretched polypropylene film (CPP film).
前記ラミネートフィルムは単層フィルムでもよく、2層以上積層された多層フィルム、例えばCPPフィルム/PSフィルムでもよい。 The laminate film may be a single layer film or a multilayer film having two or more layers laminated together, such as a CPP film/PS film.
両面にラミネートフィルムを積層する場合、両面のラミネートフィルムの材質及び構造は同じでもよく、異なってもよい。例えば、片面に単層フィルムを積層し、他方の面に多層フィルムを積層してもよい。また、片面にPSフィルムを積層し、他方の面に上記で例示されるポリオレフィンフィルムを積層してもよい。 When laminating films on both sides, the materials and structures of the laminate films on both sides may be the same or different. For example, a single-layer film may be laminated on one side and a multi-layer film may be laminated on the other side. Also, a PS film may be laminated on one side and a polyolefin film such as those exemplified above may be laminated on the other side.
本PSPシートは、生産性及び成形性を著しく損なわない範囲で、必要に応じて他の成分を含んでいてもよい。前記他の成分として具体的には、例えば、公知の樹脂シートに用いられている添加剤、例えば、難燃剤、紫外線吸収剤、蛍光増白剤、帯電防止剤、防曇剤、滑剤、アンチブロッキング剤、流動性改良剤、可塑剤、分散剤、及び抗菌剤が挙げられる。 The PSP sheet may contain other components as necessary, provided that the productivity and moldability are not significantly impaired. Specific examples of the other components include additives used in known resin sheets, such as flame retardants, ultraviolet absorbers, fluorescent brighteners, antistatic agents, antifogging agents, lubricants, antiblocking agents, flow improvers, plasticizers, dispersants, and antibacterial agents.
本実施形態に係る容器(以下、「本容器」という。)は、本PSPシートを熱成形することにより得られる。この成形方法には特に限定はない。前記成形方法として、ポリスチレン系発泡樹脂について一般に採用されている公知の成形方法、具体的には、例えば、真空成形法(プラグアシスト成形法等)、射出成形法、超高速射出成形法、射出圧縮成形法、二色成形法、ガスアシスト等の中空成形法、断熱金型を使用した成形法、急速加熱金型を使用した成形法、発泡成形(超臨界流体も含む)、インサート成形、IMC(インモールドコーティング成形)成形法、押出成形法、シート成形法、熱成形法、回転成形法、積層成形法、プレス成形法、ブロー成形法が挙げられる。また、成形条件も特に限定はない。成形条件は必要に応じて適宜決定することができる。 The container according to this embodiment (hereinafter referred to as the "container") is obtained by thermoforming the PSP sheet. There is no particular limitation on this molding method. The molding method includes known molding methods generally used for polystyrene-based foamed resins, specifically, for example, vacuum molding (plug-assist molding, etc.), injection molding, ultra-high-speed injection molding, injection compression molding, two-color molding, gas-assist and other hollow molding methods, molding using an insulated mold, molding using a rapidly heated mold, foam molding (including supercritical fluids), insert molding, IMC (in-mold coating molding) molding, extrusion molding, sheet molding, thermoforming, rotational molding, lamination molding, press molding, and blow molding. There is also no particular limitation on the molding conditions. The molding conditions can be appropriately determined as needed.
本容器の形状、寸法、及び具体的用途には特に限定はない。本容器の用途としては、包装用容器等の容器、例えば、飲食品包装用容器が挙げられる。尚、前記「容器」は、容器全体だけでなく、容器の一部も含む。例えば、前記「容器」には、容器の本体のみならず、容器の蓋体も含まれる。 There are no particular limitations on the shape, dimensions, or specific uses of the container. Uses of the container include containers for packaging, such as food and beverage packaging containers. The term "container" includes not only the entire container, but also a portion of the container. For example, the term "container" includes not only the main body of the container, but also the lid of the container.
以下、実施例により本発明を具体的に説明する。尚、本発明は、実施例に示す形態に限定されない。本発明の実施形態は、目的及び用途等に応じて、本発明の範囲内で種々変更することができる。 The present invention will be specifically explained below with reference to examples. Note that the present invention is not limited to the forms shown in the examples. The embodiment of the present invention can be modified in various ways within the scope of the present invention depending on the purpose, application, etc.
1.PSPシートの製造
原料として、以下の各成分を用いた。
(A)耐熱PS樹脂(基材樹脂);東洋スチレン株式会社製「TEP220」(ポリフェニレンエーテル樹脂:9質量%、メタクリル酸共重合PS樹脂:86質量%、PS樹脂:5質量%)
(B)物理発泡剤;ブタンガス(n-ブタン/i-ブタン=7/3)
(C)化学発泡剤;永和化成工業株式会社製「ES405」(炭酸水素ナトリウムとクエン酸との混合物)
(D)気泡調整剤;タルク(富士タルク工業株式会社製「ML110」
1. Production of PSP Sheet The following components were used as raw materials.
(A) Heat-resistant PS resin (base resin); "TEP220" manufactured by Toyo Styrene Co., Ltd. (polyphenylene ether resin: 9% by mass, methacrylic acid copolymerized PS resin: 86% by mass, PS resin: 5% by mass)
(B) Physical foaming agent: butane gas (n-butane/i-butane=7/3)
(C) Chemical foaming agent: "ES405" (a mixture of sodium bicarbonate and citric acid) manufactured by Eiwa Chemical Industry Co., Ltd.
(D) Cell regulator; talc ("ML110" manufactured by Fuji Talc Co., Ltd.)
前記耐熱PS樹脂並びに化学発泡剤及び気泡調整剤を混合した後、押出機に投入し加熱溶融した。次いで、押出機内の溶融樹脂中に、前記物理発泡剤を圧入した。その後、該溶融樹脂を押出成形することにより、発泡シート(厚さ:1.7mm、坪量:180g/m2)を得た。該発泡シートの片面にCPP/PSフィルムを、反対面にPSフィルムを熱ラミネートで接着することにより、PSPシート1~3を製造した。また、化学発泡剤を用いない他は、PSPシート1~3と同様の方法により、PSPシート4~6を製造した。PSPシート1~6の各原料の配合割合(質量基準)及び押出成形におけるシリンダー温度を表1に示す。 The heat-resistant PS resin, chemical foaming agent, and cell regulator were mixed, then charged into an extruder and heated to melt. Next, the physical foaming agent was pressed into the molten resin in the extruder. The molten resin was then extruded to obtain a foamed sheet (thickness: 1.7 mm, basis weight: 180 g/m 2 ). A CPP/PS film was attached to one side of the foamed sheet and a PS film was attached to the other side by thermal lamination to produce PSP sheets 1 to 3. PSP sheets 4 to 6 were produced in the same manner as PSP sheets 1 to 3, except that no chemical foaming agent was used. Table 1 shows the blending ratio (by mass) of each raw material of PSP sheets 1 to 6 and the cylinder temperature during extrusion.
2.性能評価
(1)エージング期間
PSPシート1~6から、シート片(大きさ:縦5cm×横8cm)を切り取り、該シート片13枚を束ねてシート束を得て、その重量を計測した(n=2)。次いで、該シート束をアルミカップに入れ、150℃に設定したオーブン内に12分間静置し、加熱後の該シート束の重量を測定した。
2. Performance evaluation (1) Aging period Sheet pieces (size: 5 cm length × 8 cm width) were cut from PSP sheets 1 to 6, and 13 of the sheet pieces were bundled to obtain a sheet bundle, whose weight was measured (n = 2). The sheet bundle was then placed in an aluminum cup and left to stand in an oven set at 150 ° C for 12 minutes, and the weight of the sheet bundle after heating was measured.
以下の式に基づいて、揮発量(g)を算出した。算出された揮発量を残存ガス量と定義した。そして、PSPシート内の残存ガス量が0.161gに到達するのに要した日数をエージング期間とした。その結果を表1に併記する。
揮発量(g)=W1-W2
W1;加熱前のシート束の重量(g)、W2;加熱後のシート束の重量(g)
The amount of volatilization (g) was calculated based on the following formula. The calculated amount of volatilization was defined as the amount of remaining gas. The number of days required for the amount of remaining gas in the PSP sheet to reach 0.161 g was defined as the aging period. The results are shown in Table 1.
Volatilization amount (g) = W1 - W2
W1: weight of sheet stack before heating (g), W2: weight of sheet stack after heating (g)
(2)独立気泡率
PSPシート1~6から、サンプル(大きさ:2cm×2cm)を9枚切り取り、それぞれの重量を測定した。該サンプルを水に浸透させ、0.02MPa以下の真空下で3分間静置した。その後、サンプルを取り出して表面及び断面の水分をよく拭き取り、サンプルの重量を測定した。
(2) Closed cell ratio Nine samples (size: 2 cm x 2 cm) were cut from PSP sheets 1 to 6, and the weight of each was measured. The samples were immersed in water and left to stand for 3 minutes under a vacuum of 0.02 MPa or less. Thereafter, the samples were taken out, the surface and cross section were thoroughly wiped to remove moisture, and the weight of each sample was measured.
以下の式(I)及び式(II)に基づいて、独立気泡率(体積%)を算出した。その結果を表1に併記する。
F=(V2/V)×100
={(M-m)/[m×(f-1)/S0]}×100・・・(I)
独立気泡率=(100-F)・・・(II)
F;連続気泡率(体積%)、V2;連続気泡分体積(cm3)、V;発泡体の実気泡体積(cm3)、m;水浸漬前のサンプル質量(g)、M;真空引後のサンプル質量(g)、f;発泡倍率、S0;積層体固体成分の比重
The closed cell ratio (volume %) was calculated based on the following formulas (I) and (II). The results are shown in Table 1.
F = (V2/V) x 100
= {(M-m) / [m x (f-1) / S0]} x 100 ... (I)
Closed cell ratio=(100-F)...(II)
F: open cell ratio (volume %), V2: open cell volume (cm 3 ), V: actual cell volume of foam (cm 3 ), m: sample mass before immersion in water (g), M: sample mass after evacuation (g), f: expansion ratio, S0: specific gravity of solid component of laminate
(3)成形性
表2に示すエージング期間が経過した時点でのPSPシート1~6の残存ガス量を、上記(1)に記載の方法により算出した。その結果を表2に併記する。
(3) Moldability The amount of residual gas in PSP sheets 1 to 6 after the aging period shown in Table 2 had elapsed was calculated by the method described in (1) above. The results are also shown in Table 2.
前記エージング期間が経過した後のPSPシート1~6を、両真空成形により熱成形することにより、容器を製造した。該容器を目視することにより、デラミ(ラミネートフィルムの剥がれ)の有無を確認した。その結果を表2に併記する。 After the aging period, PSP sheets 1 to 6 were thermoformed by both vacuum forming to produce containers. The containers were visually inspected for delamination (peeling of the laminate film). The results are shown in Table 2.
3.結果
表1より、化学発泡剤を使用していないPSPシート4~6では、エージング期間が105日以上必要であった。一方、化学発泡剤を使用したPSPシート1~3はいずれも、エージング期間がPSPシート4~6よりも短く、生産性が向上していることが分かる。
3. Results As shown in Table 1, the aging period of 105 days or more was required for PSP sheets 4 to 6, which did not use a chemical foaming agent. On the other hand, the aging period of PSP sheets 1 to 3, which used a chemical foaming agent, was shorter than that of PSP sheets 4 to 6, and it is understood that the productivity was improved.
表2より、エージング期間前のPSPシート1~3を用いた比較例1~3は、残存ガス量が0.161gを超えており、容器成形時にデラミが発生していた。一方、エージング期間後のPSPシート1~3を用いた実施例1~6は、残存ガス量が0.161g以下であり、容器成形時にデラミが発生しなかった。 As can be seen from Table 2, Comparative Examples 1 to 3, which used PSP sheets 1 to 3 before the aging period, had residual gas amounts exceeding 0.161 g, and delamination occurred during container molding. On the other hand, Examples 1 to 6, which used PSP sheets 1 to 3 after the aging period, had residual gas amounts of 0.161 g or less, and no delamination occurred during container molding.
尚、化学発泡剤を使用していないPSPシート4で残存ガス量が0.161g以下である比較例4及び5では、容器成形時にデラミが発生していないが、表1と同様に、実施例1~6と比べてエージング期間が長かった。そのため、実施例1~6と比べて、比較例4及び5ではシートの保管期間が長くなり、また、容器の生産性にも劣ることが分かる。 In addition, in Comparative Examples 4 and 5, in which the PSP sheet 4, which does not use a chemical foaming agent, has a residual gas amount of 0.161 g or less, no delamination occurs during container molding, but as in Table 1, the aging period is longer than in Examples 1 to 6. Therefore, it can be seen that the storage period of the sheet is longer in Comparative Examples 4 and 5 than in Examples 1 to 6, and the productivity of the container is also inferior.
また、表2より、化学発泡剤を使用せず、独立気泡率が90体積%未満であるPSPシート5及び6を用いた比較例7及び8でも、容器成形時にデラミが発生していた。特に、比較例7は、エージング期間が長い上、残存ガス量が0.161g以下であってもデラミが発生しており、容器の生産性にも劣ることが分かる。 Table 2 also shows that delamination occurred during container molding in Comparative Examples 7 and 8, which used PSP sheets 5 and 6 that did not use a chemical foaming agent and had a closed cell rate of less than 90% by volume. In particular, in Comparative Example 7, delamination occurred even though the aging period was long and the residual gas amount was 0.161 g or less, and the container productivity was poor.
Claims (6)
前記化学発泡剤の添加量が1質量%以上5質量%以下であり、以下に記載の方法により測定した前記ポリスチレン系樹脂発泡シート内の残存ガス量が0.161g以下であることを特徴とする、ポリスチレン系樹脂発泡シート;
<測定方法>
PSPシートから、シート片(大きさ:縦5cm×横8cm)を切り取り、該シート片13枚を束ねてシート束を得て、その重量を計測する。次いで、該シート束をアルミカップに入れ、150℃に設定したオーブン内に12分間静置し、加熱後の該シート束の重量を測定する。以下の式に基づいて揮発量(g)を算出し、算出された揮発量を残存ガス量と定義する。
揮発量(g)=W1-W2
W1;加熱前のシート束の重量(g)、W2;加熱後のシート束の重量(g)。 A polystyrene-based resin foamed sheet obtained by adding a physical foaming agent and a chemical foaming agent containing normal butane to a base resin containing a styrene-methacrylic acid copolymer, a styrene-acrylic acid-based copolymer, or a styrene-maleic anhydride-based copolymer,
A polystyrene-based resin foamed sheet, characterized in that the amount of the chemical foaming agent added is 1% by mass or more and 5% by mass or less, and the amount of residual gas in the polystyrene-based resin foamed sheet, as measured by the method described below, is 0.161 g or less ;
<Measurement method>
A sheet piece (size: 5 cm length x 8 cm width) is cut from the PSP sheet, 13 pieces of the sheet piece are bundled to obtain a sheet bundle, and the weight of the bundle is measured. The sheet bundle is then placed in an aluminum cup and left to stand in an oven set at 150°C for 12 minutes, and the weight of the sheet bundle after heating is measured. The amount of volatilization (g) is calculated based on the following formula, and the calculated amount of volatilization is defined as the amount of remaining gas.
Volatilization amount (g) = W1 - W2
W1: weight of the sheet stack before heating (g), W2: weight of the sheet stack after heating (g) .
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