JPH0112657B2 - - Google Patents
Info
- Publication number
- JPH0112657B2 JPH0112657B2 JP7837779A JP7837779A JPH0112657B2 JP H0112657 B2 JPH0112657 B2 JP H0112657B2 JP 7837779 A JP7837779 A JP 7837779A JP 7837779 A JP7837779 A JP 7837779A JP H0112657 B2 JPH0112657 B2 JP H0112657B2
- Authority
- JP
- Japan
- Prior art keywords
- hollow container
- preform
- polyester
- heat shrinkage
- crystallinity
- 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.)
- Expired
Links
- -1 polyethylene terephthalate Polymers 0.000 claims description 23
- 229920000728 polyester Polymers 0.000 claims description 18
- 150000001875 compounds Chemical class 0.000 claims description 15
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 11
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 11
- 238000000071 blow moulding Methods 0.000 claims description 9
- ADCOVFLJGNWWNZ-UHFFFAOYSA-N antimony trioxide Chemical compound O=[Sb]O[Sb]=O ADCOVFLJGNWWNZ-UHFFFAOYSA-N 0.000 claims description 8
- 229920005989 resin Polymers 0.000 claims description 7
- 239000011347 resin Substances 0.000 claims description 7
- 239000005995 Aluminium silicate Substances 0.000 claims description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 4
- 235000012211 aluminium silicate Nutrition 0.000 claims description 4
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 4
- WXMKPNITSTVMEF-UHFFFAOYSA-M sodium benzoate Chemical compound [Na+].[O-]C(=O)C1=CC=CC=C1 WXMKPNITSTVMEF-UHFFFAOYSA-M 0.000 claims description 4
- 239000004299 sodium benzoate Substances 0.000 claims description 4
- 235000010234 sodium benzoate Nutrition 0.000 claims description 4
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 238000007664 blowing Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 3
- 238000001746 injection moulding Methods 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 3
- 239000000126 substance 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
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 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
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 125000005907 alkyl ester group Chemical group 0.000 description 2
- QMKYBPDZANOJGF-UHFFFAOYSA-N benzene-1,3,5-tricarboxylic acid Chemical compound OC(=O)C1=CC(C(O)=O)=CC(C(O)=O)=C1 QMKYBPDZANOJGF-UHFFFAOYSA-N 0.000 description 2
- 235000013361 beverage Nutrition 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
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 239000002537 cosmetic Substances 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 235000013305 food Nutrition 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
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- BDJRBEYXGGNYIS-UHFFFAOYSA-N nonanedioic acid Chemical compound OC(=O)CCCCCCCC(O)=O BDJRBEYXGGNYIS-UHFFFAOYSA-N 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- ARCGXLSVLAOJQL-UHFFFAOYSA-N trimellitic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C(C(O)=O)=C1 ARCGXLSVLAOJQL-UHFFFAOYSA-N 0.000 description 2
- VPWNQTHUCYMVMZ-UHFFFAOYSA-N 4,4'-sulfonyldiphenol Chemical class C1=CC(O)=CC=C1S(=O)(=O)C1=CC=C(O)C=C1 VPWNQTHUCYMVMZ-UHFFFAOYSA-N 0.000 description 1
- 229930185605 Bisphenol Natural products 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
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 1
- ORLQHILJRHBSAY-UHFFFAOYSA-N [1-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1(CO)CCCCC1 ORLQHILJRHBSAY-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- UBAZGMLMVVQSCD-UHFFFAOYSA-N carbon dioxide;molecular oxygen Chemical compound O=O.O=C=O UBAZGMLMVVQSCD-UHFFFAOYSA-N 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- QYQADNCHXSEGJT-UHFFFAOYSA-N cyclohexane-1,1-dicarboxylate;hydron Chemical compound OC(=O)C1(C(O)=O)CCCCC1 QYQADNCHXSEGJT-UHFFFAOYSA-N 0.000 description 1
- GHLKSLMMWAKNBM-UHFFFAOYSA-N dodecane-1,12-diol Chemical compound OCCCCCCCCCCCCO GHLKSLMMWAKNBM-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000178 monomer Substances 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
- 239000002667 nucleating agent Substances 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 229920005990 polystyrene resin Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
Landscapes
- Containers Having Bodies Formed In One Piece (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は耐熱収縮性に優れたポリエステル製中
空容器に関するものである。
近年ガラス製容器の代替品としてプラスチツク
製容器が用いられるようになつてきている。最近
ではポリエチレンテレフタレートが機械的性質,
耐薬品性に優れ,しかもポリ塩化ビニルの如き可
塑剤や残存モノマーによる人体への影響がなく、
またポリエチレン,ポリプロピレン等に比べ酸
素、炭酸ガス等のガス透過率が低く透明性に優れ
ていることから食料品、飲料品、化粧品等の容器
に使用することが試みられている。
ところでポリエチレンテレフタレートを主とし
て用いたポリエステル製容器は耐熱収縮性に劣
り、特に熱処理を施さない二軸配向ボトルは60℃
から70℃以上の高温雰囲気中では熱収縮を起こし
容器が変形したり、容積が変化したりするなどの
問題が生じている。このため耐熱性を向上せしめ
る熱処理技術の開発が望まれており、これまで幾
つかの熱処理方法が提案されているが未だ経済的
に有効な方法が見出されていないのが現状であ
る。
本発明者らは上述した如き現状に鑑み耐熱収縮
性に優れたポリエステル製中空容器を得るべく鋭
意検討した結果ポリエチレンテレフタレートに対
し核剤効果のある特定の化合物からなる群から選
ばれた少なくとも一種の化合物を特定量含有した
中空容器で、しかもこの容器が胴部の結晶化度が
特定の範囲にある有底予備成形体を吹込成形して
得られたものである場合に上述した如き特性を満
足するものであることを見出し本発明に到達し
た。
即ち本発明の要旨とするところはカオリン、安
息香酸ナトリウム、三酸化アンチモンおよび酸化
チタンからなる群から選ばれた少なくとも一種の
化合物を0.002〜0.5重量%含有するポリエチレン
テレフタレート系樹脂よりなる中空容器であつ
て、該中空容器が胴部の結晶化度が1.0〜10.0%
である有底予備成形体を吹込成形して得られたポ
リエステル製中空容器にある。
本発明において用いるポリエチレンテレフタレ
ート系樹脂とはテレフタル酸又はそのエステル形
成性誘導体(例えば低級アルキルエステル、フエ
ニルエステル等)とエチレングリコール又はその
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)とを重合せしめて
得られるポリエステルであり、約20モル%未満の
他のジカルボン酸又はグリコール成分が共重合さ
れていてもよい。また該ポリエステルはトリメチ
ロールプロパン、ペンタエリスリトール、トリメ
リツト酸、トリメシン酸等の如き多官能化合物を
2モル%未満の範囲で共重合されていてもよい。
前記共重合成分として用いられる他のジカルボン
酸成分としてはフタル酸、イソフタル酸、ナフタ
リンジカルボン酸、ジフエニルジカルボン酸類、
ジフエノキシエタンジカルボン酸類等の如き芳香
族ジカルボン酸類、アジピン酸、セバチン酸、ア
ゼライン酸、デカンジカルボン酸、シクロヘキサ
ンジカルボン酸等の如き脂肪族又は脂環族ジカル
ボン酸類等が挙げられる。また他の共重合成分と
して用いられる他のグリコール成分としてはトリ
メチレングリコール、プロピレングリコール、テ
トラメチレングリコール、ネオベンチルグリコー
ル、ヘキサメチレングリコール、ドデカメチレン
グリコール、シクロヘキサンジメタノール等の如
き脂肪族又は脂環族グリコール類、ビスフエノー
ル類、ハイドロキノン、2,2―ビス(4―β―
ヒドロキシエトキシフエニル)プロパン、その他
の芳香族ジオール類が挙げられる。またその他p
―ヒドロキシエトキシ安息香酸、ε―オキシカプ
ロン酸等の如きオキシ酸類を用いることも可能で
ある。またこれらオキシ酸類の低級アルキルエス
テル、その他のエステル形成性誘導体を用いるこ
とも可能である。またさらに本発明におけるポリ
エチレンテレフタレート系樹脂とは上記ポリエス
テルに対しポリエチレン、ポリプロピレン等のポ
リオレフイン系樹脂、ポリスチレン系樹脂、ポリ
メタクリル系樹脂等を0.5〜20重量%の範囲で配
合した樹脂混合物をも含むものである。上記ポリ
エステルは固有粘度〔η〕が0.5以上、好ましく
は0.55以上、さらに好ましくは0.6以上のものが
好ましく用いられる。ポリエステルの固有粘度
〔η〕が0.5未満のものを用いる場合には容器の落
下衝撃強度が著しく低下するため好ましくない。
固有粘度〔η〕はフエノール/テトラクロルエタ
ン=50/50(重量比)溶液中25℃で測定した溶液
粘度より求めた値である。
本発明のポリエステル製中空容器に含有される
カオリン、安息香酸ナトリウム、三酸化アンチモ
ンおよび酸化チタンはポリエチレンテレフタレー
トに対し核剤効果のあるものであり耐熱収縮性に
大きく寄与するものである。中空容器中には上記
特定の化合物が少なくとも一種含有されているこ
とが必要であり上記以外の化合物では本発明の目
的とする耐熱収縮性に優れた中空容器とすること
が困難である。またこれら化合物の少なくとも一
種の中空容器中の含有量は上述した如き0.002〜
0.5重量%であることが必要であり、0.002重量%
未満の量では中空容器の耐熱収縮性が充分満足す
るものではなく、また0.5重量%を超える量では
後述する如き有底予備成形体の結晶化が促進され
引き続き行なわれる吹込成形による成形が著しく
困難となり目的とする中空容器とすることができ
ない。
また本発明のポリエステル製中空容器は胴部の
結晶化度が1.0〜10.0%である有底予備成形体を
吹込成形して得られたものであることが必要であ
る。上記胴部における結晶化度が1.0〜10.0%な
る有底予備成形体はポリエチレンテレフタレート
に対し核剤効果を有する上記特定の化合物群から
選ばれた少なくとも一種の化合物を0.002〜0.5重
量%の範囲で含有するポリエチレンテレフタレー
ト系樹脂を水分含有率が0.01%未満になるまで乾
燥した後通常の射出成形法または押出成形法等に
より所望の有底予備成形体とすることにより得る
ことができる。この場合核剤効果を有する特定の
化合物はポリエステルの重合中に所定量添加した
り、ポリエステルの重合後のチツプとブレンドし
て押出したり、或いは射出成形直前にホツパー内
でブレンドする等いずれの方法を用いてもよい。
有底予備成形体の胴部における結晶化度は1.0
〜10.0%の範囲であることが必要で、1.0%未満
の有底予備成形体ではこれを吹込成形して得られ
る中空容器の結晶化度が充分でなく耐熱収縮性に
乏しいものとなり好ましくない。また結晶化度が
10.0%を超える有底予備成形体ではこれを吹込成
形することが困難であり所望の中空容器とするこ
とができない。
本発明のポリエステル製中空容器は上述した如
き特性を有する有底予備成形体を吹込成形して得
られるものであるが、この際の吹込成形法として
はいわゆる二軸延伸吹込成形法が特に好ましく、
この方法はかかる有底予備成形体を延伸配向可能
な温度範囲に保持して二軸延伸ブローすることに
より延伸配向による結晶化を増加せしめ耐熱収縮
性が著しく向上した中空容器とすることができ
る。この延伸配向による中空容器の結晶化の度合
は二軸延伸ブロー時の延伸倍率によつても異なる
が結晶化度が10.0〜50.0%程になる。
本発明を実施するに際して用いる有底予備成形
体の肉厚は目的とする容器の形態及び後述の面延
伸倍率等によつて任意に変更しうるが成形加工性
の面から1〜12mmの範囲にあることが好ましい。
本発明のポリエステル製中空容器を得る方法は
具体的には上記範囲の結晶化度を有する有底予備
成形体を引き続き行なわれるブロー延伸配向を可
能ならしめるために予め80〜150℃の温度範囲に
保持する。有底予備成形体をこの温度範囲に保持
せしめるには溶融成形して得た高温状態の有底予
備成形体を上記温度範囲にまで放冷するか、又は
この高温状態の有底予備成形体を一旦室温程度に
冷却した後赤外線ヒーターなどの加熱ヒーターで
当該予備成形体を回転せしめながら均一に加熱す
る方法などを適宜用いる。しかる後直ちにこの有
底予備成形体を吹込金型内に装填し延伸ロツドに
より縦方向に延伸した後、或いは該延伸と同時に
圧縮空気、窒素のような加圧流体により周方向に
一気に吹込膨張させ二軸延伸配向させる。また上
記吹込金型内で吹込膨張させる際に吹込金型を加
温しておくことにより吹込膨張と同時に熱処理を
施す方法を採用すると上記核剤効果を有する特定
化合物の含有量が例えば0.002〜0.1重量%のよう
な僅量でも十分満足しうる耐熱収縮性や易スリツ
プ性を有する中空容器とすることができ、顕著な
効果を発揮する。本発明のポリエステル製中空容
器はその肩部及び胴部が相当する延伸前の有底予
備成形体の肩部分及び胴部分に対して面延伸倍率
で3倍以上、好ましくは4倍以上、特に好ましく
は6倍以上に二軸延伸配向されていることが必要
である。また面延伸倍率の上限は25倍迄、さらに
は16倍迄が好ましい。
本発明のポリエステル製中空容器は機械的強
度、耐熱収縮性に優れたものであり、さらには上
記特定の化合物を含有している結果これを含有し
ていない容器に比較し容器同士がスリツプし易く
なり運搬中に容器同士のぶつかりによる擦傷が減
少したり、また容器に液を充填する工場のライン
上での容器同士の詰りがなくなるなどスリツプ性
が著しく向上されたものであり、優れた特徴を有
する。本発明の中空容器は食料品、飲料品、化粧
品等の容器に供し得るものである。
以下実施例により本発明を具体的に説明する。
なお実施例中の熱収縮率は次のようにして求めた
ものである。即ち成形して得られたボトル容器の
容積を測定した後70℃の温水をボトル容器内に充
填する。温水を充填してから2時間後に温水を捨
て再びボトル容器の容積を測定し熱収縮率を次式
により求めた。
熱収縮率=A―B/A×100(%)
但し
Aは70℃の温水を充填する前のボトル容器の容
積(ml)
Bは70℃の温水を捨てた後のボトル容器の容積
(ml)
また結晶化度は30℃のn―ヘプタン/四塩化炭
素系の密度勾配管にて求めた密度から次式により
計算して求めたものである。
X=(12.125―1/δ×16.18)×100
但し X:結晶化度(%)
δ:密度(g/cm3)
実施例1〜15,比較例1〜20
〔η〕=0.66、軟化点262℃のポリエチレンテレ
フタレートチツプにカオリン、安息香酸ナトリウ
ム、三酸化アンチモンおよび酸化チタン等を第1
表に示すように種々の量添加してタンブリングし
た後150℃、5時間熱風乾燥機にて加熱し乾燥チ
ツプを得た。尚乾燥チツプの水分含有量は0.008
重量%であつた。このチツプを射出成形機によつ
て外径25mm、内径19mm、長さ130mmの有底円筒状
プリフオームに成形した。
次にこのプリフオームを回転させながら赤外線
ヒーター装置内に入れてプリフオームの温度がほ
ぼ105℃になるように均一に加熱した後成形用吹
込金型内に挿入し、圧縮窒素をプリフオーム内部
に圧入し、延伸ブローを行つて面延伸倍率約8倍
のボトルを得た。
得られたボトルの熱収縮率を測定した結果を第
1表に示す。
また比較のため無添加若しくは本発明で規定す
る化合物以外の物質を添加し、上記と同様にして
成形して得たボトルの熱収縮率の結果を第2表に
示す。
The present invention relates to a polyester hollow container with excellent heat shrinkage resistance. In recent years, plastic containers have come to be used as an alternative to glass containers. Recently, polyethylene terephthalate has been developed with mechanical properties.
It has excellent chemical resistance and has no effect on the human body due to plasticizers such as polyvinyl chloride or residual monomers.
In addition, since it has a lower gas permeability for oxygen, carbon dioxide, etc. and excellent transparency than polyethylene, polypropylene, etc., attempts have been made to use it in containers for foods, beverages, cosmetics, etc. However, polyester containers mainly made of polyethylene terephthalate have poor heat shrinkage resistance, especially biaxially oriented bottles that are not heat-treated at 60°C.
In a high-temperature atmosphere of 70°C or higher, problems arise such as thermal contraction of the container, deformation of the container, and change in volume. Therefore, there is a desire to develop a heat treatment technique that improves heat resistance, and although several heat treatment methods have been proposed so far, no economically effective method has yet been found. In view of the above-mentioned current situation, the present inventors conducted intensive studies to obtain a polyester hollow container with excellent heat shrinkage resistance. A hollow container containing a specific amount of a compound, and which is obtained by blow molding a bottomed preform whose body has a crystallinity within a specific range, satisfies the above characteristics. The present invention was achieved based on the discovery that this is the case. That is, the gist of the present invention is a hollow container made of a polyethylene terephthalate resin containing 0.002 to 0.5% by weight of at least one compound selected from the group consisting of kaolin, sodium benzoate, antimony trioxide, and titanium oxide. The crystallinity of the hollow container in the body is 1.0 to 10.0%.
The polyester hollow container is obtained by blow molding a bottomed preform. The polyethylene terephthalate resin used in the present invention is composed of terephthalic acid or its ester-forming derivatives (e.g., lower alkyl esters, phenyl esters, etc.) and ethylene glycol or its ester-forming derivatives (e.g., monocarboxylic acid ester, ethylene oxide, etc.). It is a polyester obtained by polymerization, and may be copolymerized with less than about 20 mol% of other dicarboxylic acid or glycol components. The polyester may also be copolymerized with a polyfunctional compound such as trimethylolpropane, pentaerythritol, trimellitic acid, trimesic acid, etc. in an amount of less than 2 mol %.
Other dicarboxylic acid components used as the copolymerization component include phthalic acid, isophthalic acid, naphthalene dicarboxylic acid, diphenyl dicarboxylic acids,
Examples include aromatic dicarboxylic acids such as diphenoxyethane dicarboxylic acids, aliphatic or alicyclic dicarboxylic acids such as adipic acid, sebacic acid, azelaic acid, decane dicarboxylic acid, cyclohexane dicarboxylic acid, and the like. Other glycol components used as other copolymerization components include aliphatic or alicyclic glycols such as trimethylene glycol, propylene glycol, tetramethylene glycol, neobentyl glycol, hexamethylene glycol, dodecamethylene glycol, cyclohexanedimethanol, etc. group glycols, bisphenols, hydroquinone, 2,2-bis(4-β-
Examples include hydroxyethoxyphenyl)propane and other aromatic diols. Also other pages
It is also possible to use oxyacids such as -hydroxyethoxybenzoic acid, ε-oxycaproic acid and the like. It is also possible to use lower alkyl esters of these oxyacids and other ester-forming derivatives. Furthermore, the polyethylene terephthalate resin in the present invention also includes a resin mixture in which a polyolefin resin such as polyethylene or polypropylene, a polystyrene resin, a polymethacrylic resin, etc. is blended with the above polyester in a range of 0.5 to 20% by weight. . The above-mentioned polyester preferably has an intrinsic viscosity [η] of 0.5 or more, preferably 0.55 or more, more preferably 0.6 or more. If a polyester having an intrinsic viscosity [η] of less than 0.5 is used, it is not preferable because the drop impact strength of the container will be significantly reduced.
The intrinsic viscosity [η] is a value determined from the solution viscosity measured at 25°C in a phenol/tetrachloroethane=50/50 (weight ratio) solution. Kaolin, sodium benzoate, antimony trioxide, and titanium oxide contained in the polyester hollow container of the present invention have a nucleating effect on polyethylene terephthalate and greatly contribute to heat shrinkage resistance. It is necessary that the hollow container contains at least one of the above-mentioned specific compounds, and if compounds other than those mentioned above are used, it is difficult to obtain a hollow container with excellent heat shrinkage resistance, which is the objective of the present invention. In addition, the content of at least one of these compounds in the hollow container is 0.002~
Must be 0.5% by weight and 0.002% by weight
If the amount is less than 0.5% by weight, the heat shrinkage resistance of the hollow container will not be sufficiently satisfactory, and if the amount exceeds 0.5% by weight, crystallization of the bottomed preform as described below will be promoted, making subsequent blow molding extremely difficult. Therefore, the desired hollow container cannot be formed. Further, the polyester hollow container of the present invention must be obtained by blow molding a bottomed preform whose body has a degree of crystallinity of 1.0 to 10.0%. The bottomed preform having a crystallinity of 1.0 to 10.0% in the body contains at least one compound selected from the above specific compound group having a nucleating effect on polyethylene terephthalate in a range of 0.002 to 0.5% by weight. It can be obtained by drying the polyethylene terephthalate resin contained therein until the water content becomes less than 0.01%, and then forming the desired bottomed preform by a conventional injection molding method, extrusion molding method, or the like. In this case, the specific compound having a nucleating effect can be added in a predetermined amount during polyester polymerization, blended with chips after polyester polymerization and extruded, or blended in a hopper immediately before injection molding. May be used. The degree of crystallinity in the body of the bottomed preform is 1.0.
-10.0%, and if it is less than 1.0%, the hollow container obtained by blow molding the preform will not have sufficient crystallinity and will have poor heat shrinkage resistance, which is not preferable. Also, the crystallinity
If the content exceeds 10.0%, it is difficult to blow mold the preform with a bottom, and the desired hollow container cannot be obtained. The polyester hollow container of the present invention is obtained by blow molding a bottomed preform having the above-mentioned characteristics, and the so-called biaxial stretch blow molding method is particularly preferred as the blow molding method at this time.
In this method, the bottomed preform is biaxially stretched and blown while being held in a temperature range that allows stretching and orientation, thereby increasing crystallization due to stretching and orientation, thereby producing a hollow container with significantly improved heat shrinkage resistance. The degree of crystallization of the hollow container due to this stretching orientation varies depending on the stretching ratio during biaxial stretching blowing, but the crystallinity is about 10.0 to 50.0%. The wall thickness of the bottomed preform used in carrying out the present invention can be arbitrarily changed depending on the form of the intended container and the area stretching ratio described below, but it is within the range of 1 to 12 mm from the viewpoint of moldability. It is preferable that there be. Specifically, the method for obtaining the polyester hollow container of the present invention is such that a bottomed preform having a degree of crystallinity within the above range is heated in advance to a temperature range of 80 to 150°C in order to enable subsequent blow-stretching orientation. Hold. In order to maintain the bottomed preform in this temperature range, the bottomed preform in a high temperature state obtained by melt molding is left to cool to the above temperature range, or the bottomed preform in a high temperature state is A method of uniformly heating the preform while rotating it with a heater such as an infrared heater after cooling the preform to about room temperature is appropriately used. Immediately thereafter, this bottomed preform is loaded into a blowing mold and stretched in the longitudinal direction with a stretching rod, or simultaneously with the stretching, it is simultaneously blown and expanded in the circumferential direction with a pressurized fluid such as compressed air or nitrogen. Biaxially stretched and oriented. Furthermore, if a method is adopted in which heat treatment is performed at the same time as the blowing expansion by heating the blowing mold during blowing expansion in the blowing mold, the content of the specific compound having the nucleating agent effect can be reduced to 0.002 to 0.1, for example. Even a small amount, such as % by weight, can produce a hollow container with satisfactory heat shrinkage resistance and slip resistance, and exhibits a remarkable effect. The polyester hollow container of the present invention has an areal stretching ratio of at least 3 times, preferably at least 4 times, particularly preferably at least 4 times that of the shoulder and body portions of the bottomed preform before stretching, to which the shoulders and body correspond. is required to be biaxially stretched and oriented six times or more. Further, the upper limit of the areal stretching ratio is preferably up to 25 times, more preferably up to 16 times. The polyester hollow container of the present invention has excellent mechanical strength and heat shrinkage resistance, and as a result of containing the above-mentioned specific compound, the containers are more likely to slip into each other than containers that do not contain this compound. It has excellent features such as reducing scratches caused by containers colliding with each other during transportation, and eliminating clogging between containers on the factory line where containers are filled with liquid. have The hollow container of the present invention can be used as a container for foods, beverages, cosmetics, and the like. The present invention will be specifically explained below using Examples.
The heat shrinkage rates in the examples were determined as follows. That is, after measuring the volume of the bottle obtained by molding, hot water at 70° C. is filled into the bottle. Two hours after filling with hot water, the hot water was discarded, the volume of the bottle container was measured again, and the thermal shrinkage rate was determined using the following formula. Heat shrinkage rate = AB/A x 100 (%) where A is the volume of the bottle before filling with 70℃ hot water (ml) B is the volume of the bottle after discarding the 70℃ hot water (ml) ) The degree of crystallinity was calculated from the density determined in an n-heptane/carbon tetrachloride density gradient tube at 30°C using the following formula. X=(12.125-1/δ×16.18)×100 However, X: Crystallinity (%) δ: Density (g/cm 3 ) Examples 1 to 15, Comparative Examples 1 to 20 [η] = 0.66, Softening point Kaolin, sodium benzoate, antimony trioxide, titanium oxide, etc. are first added to polyethylene terephthalate chips at 262℃.
After adding various amounts as shown in the table and tumbling, the chips were heated in a hot air dryer at 150°C for 5 hours to obtain dry chips. The moisture content of dried chips is 0.008
It was in weight%. This chip was molded into a bottomed cylindrical preform having an outer diameter of 25 mm, an inner diameter of 19 mm, and a length of 130 mm using an injection molding machine. Next, this preform is placed in an infrared heater while rotating, heated uniformly so that the temperature of the preform reaches approximately 105°C, and then inserted into a blow mold for molding, and compressed nitrogen is injected into the inside of the preform. Stretch blowing was performed to obtain a bottle with a surface stretching ratio of about 8 times. Table 1 shows the results of measuring the heat shrinkage rate of the obtained bottles. For comparison, Table 2 shows the results of the heat shrinkage rates of bottles molded in the same manner as above with no additives or with the addition of substances other than the compounds specified in the present invention.
【表】【table】
【表】【table】
【表】
実施例13〜24、比較例21〜40
ポリエチレンテレフタレート90重量%に対しポ
リメチルメタクリレートを10重量%ブレンドした
ポリエステル系樹脂を150℃、5時間熱風乾燥機
にて加熱し乾燥した。この乾燥ブレンドポリマー
の水分含有率は0.008重量%であつた。この乾燥
ブレンドポリマーを実施例1〜12と同様の方法に
て第3表に示す添加剤を含むプリフオームを成形
してから実施例1〜12と同様の方法にてボトルに
成形した。得られたボトルの熱収縮率を測定した
結果を第3表に示す。
また比較のための無添加若しくは本発明で規定
する化合物以外の物質を添加し、上記と同様にし
て成形して得たボトルの熱収縮率の結果を第4表
に示す。[Table] Examples 13 to 24, Comparative Examples 21 to 40 A polyester resin prepared by blending 90% by weight of polyethylene terephthalate with 10% by weight of polymethyl methacrylate was heated and dried in a hot air dryer at 150°C for 5 hours. The moisture content of this dry blended polymer was 0.008% by weight. This dry blended polymer was molded into a preform containing the additives shown in Table 3 in the same manner as in Examples 1-12, and then molded into bottles in the same manner as in Examples 1-12. Table 3 shows the results of measuring the heat shrinkage rate of the obtained bottles. For comparison, Table 4 shows the results of the heat shrinkage rates of bottles molded in the same manner as above without any additives or with the addition of substances other than the compounds specified in the present invention.
【表】【table】
【表】【table】
Claims (1)
チモン及び酸化チタンからなる群から選ばれた少
なくとも一種の化合物を0.002〜0.5重量%含有す
るポリエチレンテレフタレート系樹脂よりなる中
空容器であつて、該中空容器が胴部の結晶化度が
1.0〜10.0%である有底予備成形体を吹込成形し
て得られたポリエステル製中空容器。1 A hollow container made of a polyethylene terephthalate resin containing 0.002 to 0.5% by weight of at least one compound selected from the group consisting of kaolin, sodium benzoate, antimony trioxide, and titanium oxide, the hollow container having a body portion. The crystallinity of
A polyester hollow container obtained by blow molding a bottomed preform having a content of 1.0 to 10.0%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7837779A JPS562342A (en) | 1979-06-21 | 1979-06-21 | Hollow vessel made of polyester resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7837779A JPS562342A (en) | 1979-06-21 | 1979-06-21 | Hollow vessel made of polyester resin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS562342A JPS562342A (en) | 1981-01-12 |
| JPH0112657B2 true JPH0112657B2 (en) | 1989-03-01 |
Family
ID=13660320
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7837779A Granted JPS562342A (en) | 1979-06-21 | 1979-06-21 | Hollow vessel made of polyester resin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS562342A (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE7411960L (en) * | 1974-09-24 | 1976-03-25 | Fabriker As Haustrups | METHOD OF MANUFACTURING CONTAINERS LIKE POLYESTER BOTTLES OR CANS |
| JPS5621833A (en) * | 1979-07-30 | 1981-02-28 | Mitsubishi Rayon Co Ltd | Manufacture of blow-molded container made from polyester |
| JPS5634432A (en) * | 1979-08-31 | 1981-04-06 | Teijin Ltd | Preparation of hollow body made of polyester resin |
| JPH0621224B2 (en) * | 1986-11-26 | 1994-03-23 | 電気化学工業株式会社 | Crystallized polyester molded article and method for producing the same |
| JP2614200B2 (en) * | 1989-03-29 | 1997-05-28 | 鐘紡株式会社 | Thermoformed polyester container |
| JP4624590B2 (en) * | 2001-04-05 | 2011-02-02 | 三井化学株式会社 | Method for producing metal compound-containing polyester resin composition, preform for hollow molded article, and method for producing hollow molded article |
| CN110396181B (en) * | 2018-04-24 | 2021-12-07 | 中国石油化工股份有限公司 | Fast crystallization polyester and preparation method of hot-filling polyester bottle chip thereof |
-
1979
- 1979-06-21 JP JP7837779A patent/JPS562342A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS562342A (en) | 1981-01-12 |
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