JPH10305540A - Deep drawn thermoforming polyester container - Google Patents
Deep drawn thermoforming polyester containerInfo
- Publication number
- JPH10305540A JPH10305540A JP13037297A JP13037297A JPH10305540A JP H10305540 A JPH10305540 A JP H10305540A JP 13037297 A JP13037297 A JP 13037297A JP 13037297 A JP13037297 A JP 13037297A JP H10305540 A JPH10305540 A JP H10305540A
- Authority
- JP
- Japan
- Prior art keywords
- polyester
- sheet
- container
- layer
- intrinsic viscosity
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920000728 polyester Polymers 0.000 title claims abstract description 37
- 238000003856 thermoforming Methods 0.000 title description 8
- 239000010410 layer Substances 0.000 claims abstract description 39
- 229920000139 polyethylene terephthalate Polymers 0.000 claims abstract description 20
- 239000005020 polyethylene terephthalate Substances 0.000 claims abstract description 20
- 229920005989 resin Polymers 0.000 claims abstract description 19
- 239000011347 resin Substances 0.000 claims abstract description 19
- 239000000203 mixture Substances 0.000 claims abstract description 15
- 229920001225 polyester resin Polymers 0.000 claims abstract description 15
- 239000004645 polyester resin Substances 0.000 claims abstract description 15
- -1 polyethylene terephthalate Polymers 0.000 claims abstract description 13
- 239000012792 core layer Substances 0.000 claims abstract description 11
- 230000009477 glass transition Effects 0.000 claims abstract description 9
- 229920003207 poly(ethylene-2,6-naphthalate) Polymers 0.000 claims description 4
- 229920001230 polyarylate Polymers 0.000 claims description 4
- 239000011112 polyethylene naphthalate Substances 0.000 claims description 4
- 230000001788 irregular Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 239000011342 resin composition Substances 0.000 description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 230000000704 physical effect Effects 0.000 description 5
- 230000002087 whitening effect Effects 0.000 description 5
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 230000001771 impaired effect Effects 0.000 description 3
- 238000013021 overheating Methods 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 239000002344 surface layer Substances 0.000 description 3
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 101100160821 Bacillus subtilis (strain 168) yxdJ gene Proteins 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- YIMQCDZDWXUDCA-UHFFFAOYSA-N [4-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1CCC(CO)CC1 YIMQCDZDWXUDCA-UHFFFAOYSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- PXGZQGDTEZPERC-UHFFFAOYSA-N 1,4-cyclohexanedicarboxylic acid Chemical group OC(=O)C1CCC(C(O)=O)CC1 PXGZQGDTEZPERC-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 125000002723 alicyclic group Chemical group 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 150000002762 monocarboxylic acid derivatives Chemical class 0.000 description 1
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Containers Having Bodies Formed In One Piece (AREA)
- Laminated Bodies (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は深絞り成形性が良好
で、容器の透明性、偏肉、強度が改善されたポリエステ
ル容器に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyester container having good deep drawability and improved transparency, uneven thickness and strength of the container.
【0002】[0002]
【従来の技術】ポリエステル、特にポリエチレンテレフ
タレート(以下PETと記す)は、機械的特性、耐熱
性、耐薬品性、寸法安定性等が優れているために繊維、
フィルム、プラスチックとして広く利用されている。P
ETを原料とするシートを素材として作られた成形品は
容易に成形可能でかつ良好な透明性、光沢、機械的強度
を有するため、最近種々の商品包装用容器等として利用
する試みがなされている。2. Description of the Related Art Polyesters, especially polyethylene terephthalate (hereinafter referred to as PET), are excellent in mechanical properties, heat resistance, chemical resistance, dimensional stability and the like.
Widely used as film and plastic. P
A molded article made from a sheet made of ET as a raw material is easily moldable and has good transparency, gloss, and mechanical strength, and recently, attempts have been made to use it as a container for packaging various products. I have.
【0003】しかしながら、従来のPETを原料とする
シートは結晶性を有しているために、熱成形時に加熱し
過ぎると結晶化による白化を起こし、本来の透明性を失
ってしまうと言う問題がある。特に、容器の深さと開口
の径との比(以下絞り比と記す)が0.8以上の深絞り
容器を熱成形する場合には、通常の熱成形に比べて十分
な加熱を行う必要があり、従来のPETシートでは白化
による容器の曇りや過加熱による偏肉が生じ易く改善が
望まれていた。また、絞り比が0.8以上の深絞り容器
の実用強度を考えるとシートの厚みは1mm以上の厚物
シートが必要であるが、このような厚物シートの場合更
に十分な加熱を行うため、白化による容器の曇りや過加
熱による偏肉が更に生じ易い問題がある。However, since the conventional sheet made of PET has crystallinity, if heated excessively during thermoforming, whitening due to crystallization occurs, and the original transparency is lost. is there. In particular, when a deep-drawn container having a ratio of the depth of the container to the diameter of the opening (hereinafter referred to as a drawing ratio) of 0.8 or more is thermoformed, it is necessary to perform sufficient heating as compared with normal thermoforming. In the conventional PET sheet, clouding of the container due to whitening and uneven thickness due to overheating are apt to occur, and improvement has been desired. Further, in consideration of the practical strength of a deep drawing container having a drawing ratio of 0.8 or more, a thick sheet having a thickness of 1 mm or more is necessary. In the case of such a thick sheet, more sufficient heating is performed. In addition, there is a problem that clouding of the container due to whitening and uneven thickness due to overheating are more likely to occur.
【0004】ポリエステルシートの熱成形性を改善する
方法として、ポリエステルの結晶性を阻害する成分を共
重合し、加熱時の結晶化を防止する方法が提案されてい
る(特開昭51−81857号公報、特開昭51−38
335号公報)。しかしながら、結晶性を阻害する成分
を共重合することにより、シートの結晶化による白化は
改善されるものの、過加熱による偏肉は改善できない。
また、共重合成分の配合によるシート物性の低下が起こ
り好ましくない。As a method for improving the thermoformability of a polyester sheet, a method has been proposed in which a component which inhibits the crystallinity of polyester is copolymerized to prevent crystallization during heating (Japanese Patent Laid-Open No. 51-81857). Gazette, JP-A-51-38
No. 335). However, by copolymerizing a component that inhibits crystallinity, whitening due to crystallization of the sheet is improved, but uneven thickness due to overheating cannot be improved.
Further, the physical properties of the sheet are deteriorated due to the blending of the copolymer component, which is not preferable.
【0005】また、特開平8−1766号公報には、
1,4−シクロヘキサンジメタノールを共重合したポリ
エステル層とPET層を積層したシートにより熱成形性
を改善する方法が提案されているが、このような積層シ
ートにおいても厚みが1mm未満の薄物シートの成形性
は改善できるものの、厚みが1mm以上の厚物シートに
ついては効果が見られず偏肉が起こる。すなわち、厚物
シートにおいては加熱時の表層温度とシート内部温度と
の差が大きく、シート内部が熱成形可能な温度まで加熱
された時の表層温度が共重合ポリエステル層のガラス転
移温度を大きく超え、表層部分の変形が起こるために偏
肉が生じると考えられる。[0005] Also, Japanese Patent Application Laid-Open No. Hei 8-1766 discloses that
A method of improving thermoformability by a sheet obtained by laminating a polyester layer and a PET layer obtained by copolymerizing 1,4-cyclohexanedimethanol has been proposed. However, even such a laminated sheet has a thickness of less than 1 mm. Although the moldability can be improved, the effect is not seen for a thick sheet having a thickness of 1 mm or more and uneven thickness occurs. That is, in a thick sheet, the difference between the surface layer temperature during heating and the temperature inside the sheet is large, and the surface layer temperature when the inside of the sheet is heated to a temperature at which thermoforming is possible greatly exceeds the glass transition temperature of the copolymerized polyester layer. It is considered that uneven thickness occurs due to deformation of the surface layer portion.
【0006】[0006]
【発明が解決しようとする課題】本発明の目的とすると
ころは前記のPETを原料とするシートの欠点をなく
し、1mm以上の厚物シートを深絞り成形した透明性、
強度、偏肉が改善されたポリエステル容器を提供するこ
とにある。SUMMARY OF THE INVENTION An object of the present invention is to eliminate the above-mentioned drawbacks of a sheet made of PET, to obtain a transparent sheet obtained by deep drawing a sheet having a thickness of 1 mm or more.
An object of the present invention is to provide a polyester container having improved strength and uneven thickness.
【0007】[0007]
【課題を解決するための手段】本発明者らはかかる目的
で鋭意研究を重ねた結果、PET樹脂からなる主構成層
の両面にガラス転移温度が90℃以上のポリエステル樹
脂組成物からなる補強層を設けた多層構造シートは、深
絞り成形性に優れ、透明性、強度、偏肉が改善されたポ
リエステル容器が得られることを見出し、本発明に到達
したものである。Means for Solving the Problems The inventors of the present invention have conducted intensive studies for this purpose and as a result, have found that a reinforcing layer made of a polyester resin composition having a glass transition temperature of 90 ° C. or more is provided on both sides of a main constituent layer made of PET resin. It has been found that a multi-layered sheet provided with a polyester container is excellent in deep drawability and that a polyester container having improved transparency, strength, and uneven thickness can be obtained, and has reached the present invention.
【0008】すなわち本発明は、三層構造のポリエステ
ルシートからなり、深さの開口径に対する比が0.8以
上のポリエステル容器であって、該多層ポリエステルシ
ートの厚さが1mm以上であり、スキン層のガラス転移
温度が90℃以上及び、スキン層が極限粘度0.6以上
のポリエステル樹脂組成物からなり、コア層が極限粘度
0.6以上のポリエチレンテレフタレートからなり、ス
キン層の全層中の重量比率が10%以上であることを特
徴とするポリエステル容器である。That is, the present invention is a polyester container comprising a polyester sheet having a three-layer structure, wherein the ratio of the depth to the opening diameter is 0.8 or more, wherein the thickness of the multilayer polyester sheet is 1 mm or more, The glass transition temperature of the layer is 90 ° C. or higher, and the skin layer is made of a polyester resin composition having an intrinsic viscosity of 0.6 or more, and the core layer is made of polyethylene terephthalate having an intrinsic viscosity of 0.6 or more. A polyester container having a weight ratio of 10% or more.
【0009】[0009]
【発明の実施の形態】本発明に用いられる多層構造ポリ
エステルシートのコア層に用いられるPET樹脂は、テ
レフタル酸またはそのエステル形成性誘導体(例えば低
級アルキルエステル等)と、エチレングリコールまたは
そのエステル形成性誘導体(例えばモノカルボン酸エス
テルエチレンオキサイド等)とを公知の方法によって重
縮合せしめて得られるものであるが、本来の物性を損な
わない範囲で他の共重合成分を含んでいても良い。BEST MODE FOR CARRYING OUT THE INVENTION The PET resin used for the core layer of the multilayer polyester sheet used in the present invention comprises terephthalic acid or an ester-forming derivative thereof (for example, lower alkyl ester) and ethylene glycol or an ester-forming derivative thereof. It is obtained by polycondensing a derivative (for example, monocarboxylic acid ester ethylene oxide or the like) by a known method, but may contain other copolymer components as long as the original physical properties are not impaired.
【0010】このような共重合可能な成分としては、イ
ソフタル酸、ナフタレンジカルボン酸等の芳香族ジカル
ボン酸、アジピン酸、セバシン酸等の脂肪族ジカルボン
酸、1,4−シクロヘキサンジカルボン酸等の脂環族ジ
カルボン酸、ジエチレングリコール、1,4−ブタンジ
オール、ネオペンチルグリコール、1,4−シクロヘキ
サンジメタノール等のジオール、ポリエチレングリコー
ル、ポリテトラエチレンオキシドグリコール等のポリア
ルキレングリコール等が挙げられる。これらの共重合成
分の配合量は通常10モル%以下、好ましくは5モル%
以下である。[0010] Such copolymerizable components include aromatic dicarboxylic acids such as isophthalic acid and naphthalenedicarboxylic acid, aliphatic dicarboxylic acids such as adipic acid and sebacic acid, and alicyclic rings such as 1,4-cyclohexanedicarboxylic acid. Diols such as aromatic dicarboxylic acids, diethylene glycol, 1,4-butanediol, neopentyl glycol and 1,4-cyclohexanedimethanol, and polyalkylene glycols such as polyethylene glycol and polytetraethylene oxide glycol. The amount of these copolymer components is usually 10 mol% or less, preferably 5 mol%.
It is as follows.
【0011】本発明の容器のスキン層は、ガラス転移温
度が90℃以上である必要がある。ガラス転移温度が9
0℃に満たないとシートを成形して容器を製造する際の
予熱により収縮が発生し、外観を損なう。[0011] The skin layer of the container of the present invention must have a glass transition temperature of 90 ° C or higher. Glass transition temperature 9
If the temperature is lower than 0 ° C., shrinkage occurs due to preheating when the sheet is formed to produce a container, and the appearance is impaired.
【0012】本発明において、多層構造ポリエステルシ
ートのスキン層に用いられるポリエステル樹脂組成物の
極限粘度は0.6以上である。極限粘度が0.6より低
い場合は、容器の機械的強度が低く、特に低温時の衝撃
強度が劣る。更に、熱成形時にシートがドローダウンし
成形品に偏肉が生じたり、シートの結晶化速度が速くな
るために熱成形品が不透明になる。In the present invention, the limiting viscosity of the polyester resin composition used for the skin layer of the multilayer structured polyester sheet is 0.6 or more. When the intrinsic viscosity is lower than 0.6, the mechanical strength of the container is low, and particularly, the impact strength at low temperature is inferior. In addition, the sheet is drawn down during thermoforming, resulting in uneven thickness of the molded product, and the crystallization speed of the sheet is increased, so that the thermoformed product becomes opaque.
【0013】このような極限粘度の樹脂組成物は、各々
の樹脂を固相重合することにより得られるが、固相重合
時の操作性等を勘案すると、極限粘度が0.9以下とす
ることが好ましい。The resin composition having such an intrinsic viscosity can be obtained by solid-state polymerization of each resin. However, in consideration of the operability during solid-state polymerization, the intrinsic viscosity should be 0.9 or less. Is preferred.
【0014】本発明の容器のスキン層に用いられるポリ
エステル樹脂組成物としては、例えばポリエチレンテレ
フタレート樹脂40〜90重量部とポリアリレート樹脂
10〜60重量部とからなるポリエステル樹脂組成物、
およびPET樹脂0〜70重量部とポリエチレンナフタ
レート樹脂30〜100重量部とからなるポリエステル
樹脂組成物等が例示できる。The polyester resin composition used for the skin layer of the container of the present invention includes, for example, a polyester resin composition comprising 40 to 90 parts by weight of a polyethylene terephthalate resin and 10 to 60 parts by weight of a polyarylate resin.
And a polyester resin composition comprising 0 to 70 parts by weight of a PET resin and 30 to 100 parts by weight of a polyethylene naphthalate resin.
【0015】前者のポリエステル樹脂組成物を用いる場
合、スキン層の極限粘度を0.6以上とするために、P
ET樹脂の極限粘度が0.6以上、及びポリアリレート
樹脂の極限粘度を0.5〜0.7とすることが好まし
い。In the case of using the former polyester resin composition, in order to make the intrinsic viscosity of the skin layer 0.6 or more, P
It is preferable that the intrinsic viscosity of the ET resin is 0.6 or more, and the intrinsic viscosity of the polyarylate resin is 0.5 to 0.7.
【0016】又、後者のポリエステル樹脂組成物を用い
る場合、スキン層の極限粘度を0.6以上とするため
に、PET樹脂、及びポリエチレンナフタレート樹脂の
極限粘度をともに0.6以上とすることが好ましい。When the latter polyester resin composition is used, the intrinsic viscosity of both the PET resin and the polyethylene naphthalate resin should be 0.6 or more in order to make the intrinsic viscosity of the skin layer 0.6 or more. Is preferred.
【0017】本発明において、多層構造ポリエステルシ
ートのコア層に用いられるPET樹脂組成物の極限粘度
は0.6以上である。極限粘度が0.6より低い場合
は、容器の機械的強度が低く、特に低温時の衝撃強度が
劣る。更に、熱成形時にシートがドローダウンし成形品
に偏肉が生じ易い。また、成形品に偏肉が発生するのを
抑制させるという観点から極限粘度を0.9以下とする
ことが好ましい。In the present invention, the intrinsic viscosity of the PET resin composition used in the core layer of the multilayer polyester sheet is 0.6 or more. When the intrinsic viscosity is lower than 0.6, the mechanical strength of the container is low, and particularly, the impact strength at low temperature is inferior. Further, the sheet is drawn down during thermoforming, and the molded product is likely to be uneven in thickness. Further, the intrinsic viscosity is preferably set to 0.9 or less from the viewpoint of suppressing the occurrence of uneven thickness in the molded product.
【0018】本発明に用いられるポリエステル樹脂に
は、本来の物性を損なわない範囲で、制電剤、耐熱剤、
酸化防止剤等を配合することが出来る。これらの添加剤
はポリマーの重合時に加えもよいし、重合ポリマーチッ
プを再溶融させて二軸混練機等を使用して配合してもよ
いし、シート製造の際の溶融ポリマーに添加してもよ
い。The polyester resin used in the present invention includes an antistatic agent, a heat-resistant agent, and the like as long as the original physical properties are not impaired.
An antioxidant and the like can be added. These additives may be added at the time of polymerizing the polymer, may be re-melted the polymerized polymer chip and blended using a twin-screw kneader or the like, or may be added to the molten polymer at the time of sheet production. Good.
【0019】本発明に用いられる多層構造ポリエステル
シートとは前記の組成物を通常の製膜手段によって得た
実質的に未延伸状態のシートである。本発明の未延伸シ
ートは密度が1.34g/cm3 以下で、実質的に非晶
性のものが好ましい。シートの密度が1.34g/cm
3 以下だと、シートの透明性が良好であり、またシート
の衝撃強度も十分高い為好ましい。かかる非晶性のポリ
エステルシートは、本発明の樹脂組成物を押出し機によ
り溶融混合せしめた後、一般の多層押出し用ダイから吐
出せしめ冷却ドラムにより急冷することにより得られ
る。The multilayer polyester sheet used in the present invention is a substantially unstretched sheet obtained by the above-mentioned composition by a usual film-forming means. The unstretched sheet of the present invention preferably has a density of 1.34 g / cm 3 or less and is substantially amorphous. The density of the sheet is 1.34 g / cm
A value of 3 or less is preferable because the transparency of the sheet is good and the impact strength of the sheet is sufficiently high. Such an amorphous polyester sheet can be obtained by melt-mixing the resin composition of the present invention with an extruder, then discharging the resin composition from a general multilayer extrusion die and rapidly cooling it with a cooling drum.
【0020】本発明に用いられる多層構造ポリエステル
シートの構成は、コア層の両側にスキン層がある三層シ
ートである。スキン層がコア層の片側にしかない場合、
成形時の加熱により、コア層のPETが白化するので成
形品の透明性が損なわれる。The structure of the multilayer polyester sheet used in the present invention is a three-layer sheet having a skin layer on both sides of a core layer. If the skin layer is only on one side of the core layer,
Heating during molding causes the PET of the core layer to whiten, thereby impairing the transparency of the molded article.
【0021】本発明に用いられる多層構造ポリエステル
シートのスキン層の全層に対する重量比率は10%以上
である事が必要である。スキン層の重量比率が10%よ
り小さい場合は、深絞り熱成形性の改善効果が十分では
なく、成形品の白化や偏肉が発生する。また成形時の操
作性、経済性を考慮するとスキン層の比率は20%以下
が好ましい。It is necessary that the weight ratio of the skin layer of the multilayered polyester sheet used in the present invention to all the layers is 10% or more. When the weight ratio of the skin layer is less than 10%, the effect of improving the deep drawing thermoformability is not sufficient, and whitening and uneven thickness of the molded product occur. Further, in consideration of the operability and economy at the time of molding, the ratio of the skin layer is preferably 20% or less.
【0022】本発明に用いられる多層構造ポリエステル
シートは、前述の通り、コア層の両側にスキン層がある
三層シートであるが、両側のスキン層の重量比率を近い
範囲にしておけば、製膜時のシート表面の凹凸が小さく
なるため好ましい。従って両側のスキン層の重量比率は
40:60〜50:50の範囲とすることが好ましい。As described above, the multilayer structured polyester sheet used in the present invention is a three-layer sheet having skin layers on both sides of the core layer. This is preferable because unevenness of the sheet surface during film formation is reduced. Therefore, the weight ratio of the skin layers on both sides is preferably in the range of 40:60 to 50:50.
【0023】本発明に用いられる多層構造ポリエステル
シートは、厚みが1mm以上の厚物シートである。厚み
が1mmに満たない場合、得られた深絞り容器の強度は
実用に耐えられないほど低い。すなわち、容器に内容物
を充填した際自重によって変形したり、また、容器を手
に持つだけで変形が生じる。The multi-layered polyester sheet used in the present invention is a thick sheet having a thickness of 1 mm or more. When the thickness is less than 1 mm, the strength of the obtained deep drawn container is so low that it cannot be practically used. That is, when the container is filled with the contents, the container is deformed by its own weight, or the container is deformed just by holding the container.
【0024】本発明のポリエステル容器は、該多層構造
ポリエステルシートから絞り比が0.8以上の深絞り熱
成形により得られる。熱成形方法としては、シートを加
熱軟化せしめて所望の型に押し当て型と材料の間隙にあ
る空気を除去し大気圧により型に密着せしめて成形する
真空成形、あるいは大気圧以上の圧縮空気によりシート
を型に密着せしめる圧空成形、および真空、圧空を併用
する成形などが適用できる。The polyester container of the present invention can be obtained from the multilayer structured polyester sheet by deep drawing thermoforming with a drawing ratio of 0.8 or more. As a thermoforming method, a sheet is heated and softened, pressed against a desired mold, air in a gap between the mold and the material is removed, and the sheet is closely adhered to the mold by atmospheric pressure to form the sheet. Pneumatic molding in which the sheet is brought into close contact with the mold, and molding using both vacuum and compressed air can be applied.
【0025】[0025]
【発明の効果】本発明のポリエステル容器は、透明性、
機械物性等のPETシート本来が有する特性を維持し、
偏肉がなく飲料コップに最適である。The polyester container of the present invention has transparency,
Maintain the original properties of PET sheet such as mechanical properties,
Ideal for beverage cups without uneven thickness.
【0026】[0026]
【実施例】以下、実施例により本発明を更に詳細に説明
する。尚、実施例における主な物性値の測定は以下に示
す方法で行った。The present invention will be described in more detail with reference to the following examples. In addition, the measurement of the main physical property value in an Example was performed by the method shown below.
【0027】(1)極限粘度(IV) フェノール60重量%、1,1,2,2−テトラクロロ
エタン40重量%の混合溶媒50mlに試料0.5gを
溶かし20℃にて測定した。(1) Intrinsic viscosity (IV) 0.5 g of a sample was dissolved in 50 ml of a mixed solvent of 60% by weight of phenol and 40% by weight of 1,1,2,2-tetrachloroethane and measured at 20 ° C.
【0028】(2)密度(ρ) 密度勾配法により、23℃にて測定した。(2) Density (ρ) Measured at 23 ° C. by a density gradient method.
【0029】(3)ガラス転移温度(Tg) ポリエステル容器のスキン層部分をミクロトームにより
切削した試料約10mgを、パーキンエルマー社製DS
Cにて、窒素気流中10℃/minの昇温速度にて測定
した。(3) Glass transition temperature (Tg) About 10 mg of a sample obtained by cutting a skin layer portion of a polyester container with a microtome was used in a DS manufactured by PerkinElmer.
At C, the temperature was measured at a rate of 10 ° C./min in a nitrogen stream.
【0030】(4)透明性(ヘーズ) ポリエステル容器の胴体部を用い、日本電色社製ヘイズ
メーターにてJIS−K7105に従って測定した。測
定値が3%以下のものを「○」、3%を超えるものを
「×」として評価した。(4) Transparency (Haze) Using a body part of a polyester container, a haze meter manufactured by Nippon Denshoku Co., Ltd. measured according to JIS-K7105. A sample having a measured value of 3% or less was evaluated as "O", and a sample exceeding 3% was evaluated as "X".
【0031】(5)熱成形性 プラグアシスト付の1個取り圧空成形機にて深さ90m
m、開口径60mm、絞り比1.5の容器を作製した。
完全な容器ができたものを○、賦形不良あるいは偏肉を
起こしたものを×とした。(5) Thermoformability 90 m depth by a single-cavity pressure forming machine with plug assist
m, an opening diameter of 60 mm, and a draw ratio of 1.5 were prepared.
The case where a complete container was completed was evaluated as ○, and the case where shape improper or uneven thickness occurred was evaluated as ×.
【0032】(6)容器強度 容器に150gの水を充填し、高さ2.5mの位置より
コンクリート面に落下させて評価を行った。落下試験を
20回行って容器が割れた回数が1回以下の場合を
「○」、2回以上割れた場合を「×」とした。(6) Container Strength A container was filled with 150 g of water and dropped on a concrete surface from a position having a height of 2.5 m for evaluation. When the drop test was performed 20 times and the number of times the container was cracked was 1 or less, it was rated "○", and when it was broken 2 or more times, it was rated "x".
【0033】実施例1〜9 比較例1〜3 3つの1軸押出し機を備えた幅80cmのTダイを有す
る多層シート押出し機を用い、表1に示した原料を使用
して厚み1.5mmの三層シートを押し出した。スキン
層に用いたPET樹脂、ポリアリレート樹脂、PEN樹
脂の極限粘度は各々0.85、0.51、0.63であ
った。押出し機のシリンダー温度は285℃、Tダイの
温度は280℃、冷却ローラーの温度は40℃で行っ
た。得られたシートの物性を表2に示す。Examples 1 to 9 Comparative Examples 1 to 3 Using a multilayer sheet extruder having a T-die of 80 cm in width equipped with three single-screw extruders, using the raw materials shown in Table 1, a thickness of 1.5 mm Was extruded. The intrinsic viscosities of the PET resin, polyarylate resin, and PEN resin used for the skin layer were 0.85, 0.51, and 0.63, respectively. The temperature of the cylinder of the extruder was 285 ° C., the temperature of the T-die was 280 ° C., and the temperature of the cooling roller was 40 ° C. Table 2 shows the physical properties of the obtained sheet.
【0034】次いで、上記シートをスキン層樹脂組成物
のガラス転移温度以上融点以下に予熱し、プラグアシス
ト付の1個取り圧空成形機にて深さ90mm、開口径6
0mm、絞り比1.5の容器を作製した。容器の評価結
果を表2に示す。Next, the above-mentioned sheet is preheated to a temperature not lower than the glass transition temperature of the resin composition for the skin layer and not higher than the melting point, and has a depth of 90 mm and an opening diameter of 6 using a single-cavity pressure forming machine with plug assist.
A container having 0 mm and a draw ratio of 1.5 was produced. Table 2 shows the evaluation results of the containers.
【0035】比較例4 実施例1と同じ樹脂組成物をスキン層、コア層に用い
て、同様の押出し機を用い、同様の条件でスキン層がコ
ア層の片面にしか積層されていない、二層シートを作製
した。この二層シートを実施例1と同様の方法で容器を
作製し、評価を行った。以上の結果を表1、表2に示
す。Comparative Example 4 The same resin composition as in Example 1 was used for the skin layer and the core layer, and the same extruder was used. Under the same conditions, the skin layer was laminated only on one side of the core layer. A layer sheet was prepared. A container was produced from this two-layer sheet in the same manner as in Example 1, and the container was evaluated. The above results are shown in Tables 1 and 2.
【0036】[0036]
【表1】 [Table 1]
【0037】[0037]
【表2】 [Table 2]
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B65D 1/26 B65D 1/26 Z // B29K 67:00 B29L 22:00 C08L 67:00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI B65D 1/26 B65D 1/26 Z // B29K 67:00 B29L 22:00 C08L 67:00
Claims (3)
り、深さの開口径に対する比が0.8以上のポリエステ
ル容器であって、該多層ポリエステルシートの厚さが1
mm以上であり、スキン層のガラス転移温度が90℃以
上及び、スキン層が極限粘度0.6以上のポリエステル
樹脂組成物からなり、コア層が極限粘度0.6以上のポ
リエチレンテレフタレートからなり、スキン層の全層中
の重量比率が10%以上であることを特徴とするポリエ
ステル容器。1. A polyester container comprising a polyester sheet having a three-layer structure and having a ratio of depth to opening diameter of 0.8 or more, wherein the multilayer polyester sheet has a thickness of 1
mm or more, the glass transition temperature of the skin layer is 90 ° C. or more, and the skin layer is made of a polyester resin composition having an intrinsic viscosity of 0.6 or more, and the core layer is made of polyethylene terephthalate having an intrinsic viscosity of 0.6 or more. A polyester container, wherein the weight ratio of all the layers in the layer is 10% or more.
0.6以上のポリエチレンテレフタレート樹脂40〜9
0重量部と極限粘度が0.5〜0.7のポリアリレート
樹脂10〜60重量部とからなるポリエステル樹脂組成
物である請求項1に記載のポリエステル容器。2. A polyester resin composition comprising: a polyethylene terephthalate resin having an intrinsic viscosity of 0.6 or more;
The polyester container according to claim 1, which is a polyester resin composition comprising 0 parts by weight and 10 to 60 parts by weight of a polyarylate resin having an intrinsic viscosity of 0.5 to 0.7.
0.6以上のポリエチレンテレフタレート樹脂0〜70
重量部と極限粘度が0.6以上のポリエチレンナフタレ
ート樹脂30〜100重量部とからなるポリエステル樹
脂組成物である請求項1に記載のポリエステル容器。3. A polyester resin composition comprising a polyethylene terephthalate resin having an intrinsic viscosity of 0.6 or more.
The polyester container according to claim 1, which is a polyester resin composition comprising parts by weight and 30 to 100 parts by weight of a polyethylene naphthalate resin having an intrinsic viscosity of 0.6 or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13037297A JPH10305540A (en) | 1997-05-02 | 1997-05-02 | Deep drawn thermoforming polyester container |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13037297A JPH10305540A (en) | 1997-05-02 | 1997-05-02 | Deep drawn thermoforming polyester container |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10305540A true JPH10305540A (en) | 1998-11-17 |
Family
ID=15032800
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13037297A Pending JPH10305540A (en) | 1997-05-02 | 1997-05-02 | Deep drawn thermoforming polyester container |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10305540A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003043819A1 (en) * | 2001-11-21 | 2003-05-30 | Kyodo Printing Co., Ltd. | Laminates and packaging containers |
JP2003285409A (en) * | 2002-03-29 | 2003-10-07 | Teijin Chem Ltd | Multilayered molded object and container |
-
1997
- 1997-05-02 JP JP13037297A patent/JPH10305540A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003043819A1 (en) * | 2001-11-21 | 2003-05-30 | Kyodo Printing Co., Ltd. | Laminates and packaging containers |
US7118800B2 (en) | 2001-11-21 | 2006-10-10 | Kyodo Printing Co., Ltd. | Laminates and packaging containers |
US7371455B2 (en) | 2001-11-21 | 2008-05-13 | Kydo Printing Co., Ltd. | Laminates and packaging containers |
JP2003285409A (en) * | 2002-03-29 | 2003-10-07 | Teijin Chem Ltd | Multilayered molded object and container |
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