JPS632777B2 - - Google Patents
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- Publication number
- JPS632777B2 JPS632777B2 JP3502286A JP3502286A JPS632777B2 JP S632777 B2 JPS632777 B2 JP S632777B2 JP 3502286 A JP3502286 A JP 3502286A JP 3502286 A JP3502286 A JP 3502286A JP S632777 B2 JPS632777 B2 JP S632777B2
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- 229930195733 hydrocarbon Natural products 0.000 claims description 24
- 239000004215 Carbon black (E152) Substances 0.000 claims description 18
- 229920001400 block copolymer Polymers 0.000 claims description 18
- 239000004793 Polystyrene Substances 0.000 claims description 16
- 239000011521 glass Substances 0.000 claims description 16
- 229920002223 polystyrene Polymers 0.000 claims description 16
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Natural products C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 15
- -1 styrene hydrocarbon Chemical class 0.000 claims description 15
- 239000011342 resin composition Substances 0.000 claims description 10
- 229920006257 Heat-shrinkable film Polymers 0.000 claims description 5
- 239000008188 pellet Substances 0.000 description 13
- 229920005992 thermoplastic resin Polymers 0.000 description 13
- 230000000977 initiatory effect Effects 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 10
- 230000000694 effects Effects 0.000 description 10
- 150000002430 hydrocarbons Chemical class 0.000 description 9
- 230000000704 physical effect Effects 0.000 description 9
- 229920002725 thermoplastic elastomer Polymers 0.000 description 9
- 238000005336 cracking Methods 0.000 description 8
- 229920000642 polymer Polymers 0.000 description 8
- 238000012360 testing method Methods 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 6
- 230000007423 decrease Effects 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 235000019198 oils Nutrition 0.000 description 5
- 230000002265 prevention Effects 0.000 description 5
- 230000002401 inhibitory effect Effects 0.000 description 4
- 239000005022 packaging material Substances 0.000 description 4
- 238000004806 packaging method and process Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 150000001993 dienes Chemical class 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920002545 silicone oil Polymers 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical group [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 229920001890 Novodur Polymers 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 1
- 238000010539 anionic addition polymerization reaction Methods 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003796 beauty Effects 0.000 description 1
- 230000001588 bifunctional effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000010382 chemical cross-linking Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- SMBQBQBNOXIFSF-UHFFFAOYSA-N dilithium Chemical compound [Li][Li] SMBQBQBNOXIFSF-UHFFFAOYSA-N 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 150000002900 organolithium compounds Chemical class 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 229920005604 random copolymer Polymers 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Laminated Bodies (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Surface Treatment Of Glass (AREA)
Description
〔産業上の利用分野〕
本発明は、特定の透明熱収縮性フイルムを被覆
したガラス容器に関する。
〔従来の技術〕
従来スチレン系炭化水素を60〜95重量%と共役
ジエン系炭化水素を5〜40重量%とから成る平均
分子量4万〜30万の樹脂状ブロツク共重合体(以
下熱可塑性樹脂という)100重量部に対して、ポ
リスチレンを0〜30重量部含んでなる樹脂組成物
を、公知のテンター法、あるいはチユーブラー法
で、延伸倍率2〜8倍に、縦1軸、横1軸、2軸
又は多軸に延伸して成る透明フイルムは、特開昭
48―13973号公報に見られるように、熱収縮性、
ヒートシール性、ガス透過性に優れ、更に透明
性、高光沢を有するフイルムであり、熱収縮包装
等の包装材料に適している。
しかしながら、この樹脂組成物から成る延伸フ
イルムは熱収縮包装において包装対象物(各種容
器等)への熱収縮後、熱収縮応力や包装対象物の
形状に起因する残留応力や、包装物の保存環境の
変化に呼応して、フイルムに細いき裂や割れが生
じる場合が少なくない(ストレスクラツキング現
象)。これらのき裂や割れは、シユリンクラベル
としての美麗さを損うばかりでなく、包装対象物
に対する保護効果を喪失させ、包装材料としての
適性を欠く原因となる。
通常、き裂の防止対策としては、樹脂組成物の
ブロツク構造において、スチレン系炭化水素の分
子量を増加させる、あるいは、共役ジエン系炭化
水素の含有量を増大させる方法がとられている。
〔発明が解決しようとする問題点〕
しかしながら、分子量の増大は、樹脂の流れを
低下させ、共役ジエンの含有量の増大は、フイル
ムの腰を低下させると同時に、熱収縮開始温度を
低下させ、熱収縮包装材料としての適性を欠く。
このため、樹脂組成物の組成調整だけでは、上記
の様な、厳しい包装状態における、き裂や割れの
発生は防止できない。
本発明の目的は、熱収縮包装後の被覆フイルム
面でき裂や割れの発生のないフイルム被覆ガラス
容器を提供することにある。
〔問題点を解決するための手段〕
本発明を概要すれば、本発明はフイルム被覆ガ
ラス容器に関する発明であつて、
(A) スチレン系炭化水素60〜95重量%と共役ジエ
ン系炭化水素5〜40重量%とからなる平均分子
量4万〜30万の樹脂状ブロツク共重合体100重
量部、
(B) ポリスチレン10〜30重量部、及び
(C) スチレン系炭化水素20〜50重量%と共役ジエ
ン系炭化水素50〜80重量%とからなるゴム状ブ
ロツク共重合体0.3〜10重量部
の樹脂組成物を1軸、2軸又は多軸に延伸した透
明熱収縮性フイルムでガラス容器を加熱収縮被覆
してなることを特徴とする。
本発明において使用する熱可塑性樹脂のブロツ
ク共重合体を構成するスチレン系炭化水素とは、
スチレン、又は、α―メチルスチレン等であり、
共役ジエン系炭化水素とは、ブタジエン又はイソ
プレン等である。これらの単量体からブロツク共
重合体を製造するには、陰イオン系重合開始剤、
中でも有機リチウム化合物を使用し、両炭化水素
単量体を段階的に重合する方法、両単量体の混合
物を不活性溶媒中で共重合する方法、又は、これ
らを適当に併用する方法によつて製造される。該
ブロツク共重合体中に占めるスチレン系炭化水素
の割合は、60〜95重量%である。60%未満では、
得られた樹脂がゴム的な弾性体に似たものになる
ので、フイルムとして不適当であり、また95%を
超えると本発明の目的である前記諸性質を有する
フイルムが得られない。ブロツク共重合体の平均
分子量は、4万〜30万好ましくは6万〜25万の範
囲のものである。4万未満のものでは、機械的な
諸強度が低下し、また30万を超えると、成形加工
性に劣り、延伸成膜が困難となる。ブロツク共重
合体は一般構造式(A−B)o又は(A−B)o−A
(Aはスチレン系炭化水素の重合体のブロツクを、
Bは共役ジエン系炭化水素の重合体のブロツク
を、nは正の整数を表わす)で表わされる直線型
ブロツク共重合体、及び、一般構造式:
〔(A−B)n〕―oX
但し、Aはスチレン系炭化水素の重合体ブロツ
ク、
Bは共役ジエン系炭化水素の重合体ブロ
ツク、
Xは多官能性化合物から誘導される残
基、
mは1以上の整数、
nは3又は4である。
で表わされる星型ブロツク共重合体である。ブロ
ツクの構造としては、完全ブロツクでも特開昭48
―48546号公報に見られるごとく、ブロツクAと
ブロツクBの遷移部にABランダム共重合体を含
有したいわゆるテーパードブロツク構造のいずれ
でもよい。これらのブロツク共重合体を構造的に
分類すると次の様になる。
(1) A−B
(2) A−B−A
(3) A−B−A−B
(4) A−B−A−B−A
(5) A−B−A−B−A−B
(6) A−B−A−B−A−B−A
(7) 〔(A−B)n〕―3X(但しm及びXは前記のと
おり)
(8) 〔(A−B)n〕―4X(但し、m及びXは前記の
とおり)
前記構造(1)のブロツク共重合体は、フイルム成
膜時、高温における引張強度が小さく成膜できな
い。構造(2),(7),(8)のブロツク共重合体は、延伸
成膜加工性に欠けると同時に、熱収縮性に欠け
る。これに対し、構造(3),(4),(5),(6)のいわゆる
マルチブロツク化されたブロツク共重合体は、延
伸成膜性が良好で、且つ熱収縮性に優れている。
すなわち、一般構造式(A−B)o−Aでnが2以
上好ましくは3〜5であるものが良い。
次にポリスチレンとは、一般の透明ポリスチレ
ンであり、成形機で成形できる分子量10万以上の
ものであればよい。ポリスチレンの添加量は、10
〜30重量部である。ポリスチレンの添加は、フイ
ルムの腰、透明性、光沢の向上を目的とするが、
添加量が30重量部を超える場合、ポリスチレンの
影響が強く現われ、衝撃強度の低下、延伸温度の
上昇を余儀なくする等の、フイルムの包装材料適
性、加工性を損ねる原因となる。
本発明で使用するゴム状ブロツク共重合体(以
下熱可塑性ゴムという)とは、スチレン系炭化水
素を20〜50重量%と共役ジエン系炭化水素を50〜
80重量%とから成るブロツク共重合体である。こ
のブロツク共重合体は、共役ジエン系炭化水素含
有量が50〜80重量%と高いため、化学的な架橋剤
なしに、固体でゴム弾性を示し、再溶融が可能な
ものである。共役ジエン系炭化水素が50重量%未
満では、樹脂的性質を示しかつ耐油性が低下して
好ましくなくなり、また80重量%を超えると、フ
イルムの透明性及び腰の低下を招く。
本発明で使用する透明熱収縮フイルムに用いる
樹脂組成物としては、熱可塑性樹脂100重量部と
ポリスチレン10〜30重量部及び熱可塑性ゴム0.3
〜10重量部からなつている。すなわち、熱可塑性
樹脂100重量部に対して熱可塑性ゴムを0.3〜10重
量部添加するのであり、0.3重量部未満では耐油
性が悪く熱収縮後のフイルムに対するき裂発生抑
止効果が小さく、また10重量部を超えると透明性
が低下してガラス容器に被覆後の内容物の判別が
困難となり、しかもフイルムの腰の低下を招く。
更にポリスチレンを10〜30重量部添加する。ポリ
スチレンを10重量部以上添加すると透明性が向上
するが、30重量部を超えると耐油性すなわち熱収
縮性フイルムのき裂発生抑止効果が減少し、更に
衝撃強度の低下及び延伸温度の上昇があり好まし
くない。
更に、前記樹脂組成物は、必要に応じて滑剤、
酸化防止剤、紫外線吸収剤及び着色剤等を添加す
ることもできる。本発明に用いる樹脂組成物の場
合は、通常のヘンシエルミキサー、リボンブレン
ダー、スーパーミキサー及びVブレンダー等でド
ライブレンドしてもよく、更に押出機で溶融して
ペレツト化してもよく、好ましくは、溶融混合が
よい。
次に、本発明で用いた延伸方法は、テンター法
あるいはチユブラー法のいずれでもよく、延伸
は、縦又は横1軸、2軸あるいは多軸に延伸する
ことができる。
そして、本発明におけるガラス容器の被覆は通
常の方法で行つてよく、例えば延伸したフイルム
をガラス容器の形状に適合させた形態とし、それ
をガラス容器にかぶせ、それに熱風吹付け、又は
オーブン中での加熱等を行うことにより、フイル
ムを熱収縮させてガラス容器に密着させればよ
い。
〔実施例〕
以下、本発明を実施例により更に具体的に説明
するが、本発明はこれら実施例に限定されない。
なお、フイルムの物性測定方法、及びそれをガ
ラス容器に適用した際の耐油性及び耐ストレスク
ラツキング性の指標となる、き裂発生促進試験方
法は、以下のとおりである。
VICAT軟化点 JIS―K―6870
熱収縮応力 東洋精機社製熱収縮応力測定機を使
用し、下記条件で熱収縮応力を測定
した。
サンプル形状:表記厚×20mm(幅)×100mm
(長)
長さ方向が延伸方向
測定温度:140℃(熱媒:シリコンオイル)表値
は、応力(g)/厚×幅(mm2)
引張強度 JIS―K―6732(タテ―延伸方向)
伸 び 〃
フイルムインパクト テスター産業社製フイルム
インパクトテスターを使用し、下記
条件でフイルムの衝撃打ち抜きに対
する強度を測定した。
衝撃球面1″、20℃
ヘイズ ASTM―D―1003
熱収縮率 下記の条件でフイルムを恒温槽中につ
け、熱収縮率を測定した。
熱媒:シリコンオイル(恒温槽中)
時間:60sec
サンプル形状 10×10cm
き裂発生促進試験方法 フイルムをガラス容器に
かぶせ、ギヤオープン中190℃、
60secで熱収縮させた冷却後、フイ
ルム表面に均一に菜種油を塗布し、
き裂の発生を観察した。塗布後、長
さ5mm以上のき裂が発生した時間を
き裂発生時間とした。
実施例 1
100のジヤケツト付の反応缶に、十分脱水、
精製したベンゼン80を仕込み、スチレン9Kgと
ブタジエン1Kgの混合物を添加したのち、2官能
のブタジエンオリゴマージリチウム開始剤を活性
末端リチウムとして0.3モル添加し、同内容物を
50℃まで昇温させることにより重合を完結させ
る。次いで更にスチレン8Kgとブタジエン2Kgの
混合物を添加し、重合させる。
得られた重合溶液は、スチームストリツピング
することによりポリマーを回収する。このポリマ
ーの数平均分子量は17.5万である。(スチレン含
有量85%、ブタジエン含有量15%)このポリマー
は、式(A−B)o−A(n=3)で表わされるブ
ロツク共重合体であり、これをペレツト化した。
この熱可塑性樹脂100重量部に対して、ポリス
チレン〔電気化学工業(株)社製デンカスチロール
GP―1〕を10重量部、及び熱可塑性ゴム〔旭化
成(株)社製・タフプレン―A〕を5重量部添加、溶
融混合ペレツト化した。
この樹脂組成物を熱板プレス機で、成形温度
170℃でプレス板成形し、厚さ225μ12×12cmのシ
ートを得た。このシートを東洋精機2軸延伸機で
1軸延伸した。
予熱温度105℃、予熱時間90秒、延伸倍率4.5
倍、延伸速度1.8m/minで12×54cm、厚さ48〜
52μのフイルムが得られた。フイルム特性及び成
膜条件等を後記表1に他の例と共に示す。
次に、このフイルムをガラス容器にかぶせ、加
熱収縮させて、フイルム被覆ガラス容器を作製し
た。その透明性及びき裂発生を試験した結果を、
同じく表1に示す。
ヘイズ及びき裂発生抑止効果共良好であつた。
実施例 2
実施例1と同じ方法で合成した熱可塑性樹脂
100重量部に対してポリスチレン〔電気化学工業
(株)社製デンカスチロールGP―1〕を15重量部、
及び熱可塑性ゴム〔旭化成(株)社製―タフプレン―
A〕を8重量部添加、溶融混合ペレツト化した。
このペレツトを使用して、以下、実施例1と同
様にしてフイルム成膜、き裂発生促進試験を実施
した。この結果を、成膜条件及びフイルム一般物
性とあわせて表1に示した。ヘイズ及びき裂発生
抑止防止効果共良好であつた。
実施例 3
実施例1と同じ方法で合成した熱可塑性樹脂
100重量部に対してポリスチレン〔電気化学工業
(株)社製デンカスチロールGP―1〕を30重量部及
び熱可塑性ゴム〔旭化成(株)社製―タフプレン―
A〕を10重量部添加、溶融混合ペレツト化した。
このペレツトを使用して、以下実施例1と同様
にして、フイルム成膜、き裂発生促進試験を実施
した。この結果を、成膜条件及びフイルム一般物
性とあわせて表1に示した。ヘイズ及びき裂発生
抑止効果共良好であつた。
比較例 1
実施例1と同じ方法で合成した熱可塑性樹脂の
みを用いて、実施例1と同様にしてフイルム成
膜、き裂発生促進試験を実施した。この結果を、
成膜条件及びフイルム一般物性とあわせて表1に
示した。ヘイズは良好であるがき裂発生抑止効果
は22分間と悪化している。
比較例 2
実施例1と同じ方法で合成した熱可塑性樹脂
100重量部に対して、ポリスチレン〔電気化学工
業(株)社製デンカスチロールGP―1〕を10重量部
添加、溶融混合ペレツト化した。
このペレツトを使用して、実施例1と同様にし
てフイルム成膜、き裂発生促進試験を実施した。
この結果を、成膜条件及びフイルム一般物性とあ
わせて表1に示す。ヘイズは良好であつたが、き
裂発生抑止効果が80秒と非常に悪化している。
比較例 3
実施例1と同様にして合成した熱可塑性樹脂
100重量部に対して、熱可塑性ゴム〔旭化成(株)社
製―タフプレン―A〕を5重量部添加、溶融混合
ペレツト化した。
このペレツトを使用して実施例1と同様にし
て、フイルム成膜、き裂発生促進試験を実施し
た。この結果を成膜条件及びフイルム一般物性と
あわせて表1に示す。
き裂発生抑止効果は良好であるが、実施例1に
比べヘイズが高い。
比較例 4
実施例1と同じ方法で合成した熱可塑性樹脂
100重量部に対して、熱可塑性ゴム〔旭化成(株)社
製―タフプレン―A〕を10重量部添加、溶融混合
ペレツト化した。
このペレツトを使用して、以下、実施例1と同
様にしてフイルム成膜、き裂発生促進試験を実施
した。この結果を、成膜条件及びフイルム一般物
性とあわせて表1に示した。き裂発生抑止効果は
良好であるが、実施例3に比べヘイズが高い。
比較例 5
実施例1と同様にして合成した熱可塑性樹脂
100重量部に対して、熱可塑性ゴム〔旭化成(株)社
製―タフプレン―A〕を15重量部添加し、溶融混
合ペレツト化した。
このペレツトを使用して実施例1と同様にし
て、フイルム成膜、き裂発生促進試験を実施し
た。この結果を成膜条件及びフイルム一般物性と
あわせて表―1に示す。
き裂発生抑止効果は良好であるが、ヘイズが高
く内容物の判別ができない。
[Industrial Field of Application] The present invention relates to a glass container coated with a specific transparent heat-shrinkable film. [Prior art] Conventionally, resinous block copolymers (hereinafter referred to as thermoplastic resins) having an average molecular weight of 40,000 to 300,000 are composed of 60 to 95% by weight of styrene hydrocarbons and 5 to 40% by weight of conjugated diene hydrocarbons. A resin composition containing 0 to 30 parts by weight of polystyrene per 100 parts by weight (100 parts by weight of A transparent film formed by biaxially or multiaxially stretching is disclosed in Japanese Patent Application Laid-open No.
As seen in Publication No. 48-13973, heat shrinkability,
This film has excellent heat sealability and gas permeability, as well as transparency and high gloss, making it suitable for packaging materials such as heat shrink packaging. However, in heat shrink packaging, the stretched film made of this resin composition is exposed to heat shrinkage stress, residual stress due to the shape of the packaged object, and the environment in which the packaged product is stored. In response to changes in the film, thin cracks and cracks often occur in the film (stress cracking phenomenon). These cracks and cracks not only impair the beauty of the Shrink label, but also cause the label to lose its protective effect on the object to be packaged, making it unsuitable as a packaging material. Normally, crack prevention measures include increasing the molecular weight of styrenic hydrocarbons or increasing the content of conjugated diene hydrocarbons in the block structure of resin compositions. [Problems to be Solved by the Invention] However, an increase in the molecular weight reduces the flow of the resin, and an increase in the content of conjugated diene reduces the stiffness of the film and at the same time lowers the temperature at which heat shrinkage starts. Lacks suitability as a heat shrink packaging material.
Therefore, simply adjusting the composition of the resin composition cannot prevent the occurrence of cracks and cracks under severe packaging conditions as described above. An object of the present invention is to provide a film-covered glass container that is free from cracking or cracking on the surface of the covering film after heat-shrink packaging. [Means for Solving the Problems] To summarize the present invention, the present invention relates to a film-coated glass container, which comprises: (A) 60 to 95% by weight of styrenic hydrocarbon and 5 to 5% by weight of conjugated diene hydrocarbon; (B) 10 to 30 parts by weight of polystyrene, and (C) 20 to 50 parts by weight of styrenic hydrocarbon and conjugated diene. A glass container is heat-shrinkable coated with a transparent heat-shrinkable film made by stretching uniaxially, biaxially, or multiaxially a resin composition containing 0.3-10 parts by weight of a rubbery block copolymer consisting of 50-80% by weight of a hydrocarbon. It is characterized by: The styrenic hydrocarbons constituting the thermoplastic resin block copolymer used in the present invention are:
Styrene or α-methylstyrene, etc.
Conjugated diene hydrocarbons include butadiene, isoprene, and the like. To produce a block copolymer from these monomers, an anionic polymerization initiator,
Among them, a method using an organolithium compound and stepwise polymerization of both hydrocarbon monomers, a method of copolymerizing a mixture of both monomers in an inert solvent, or a method of appropriately using these in combination. manufactured by The proportion of styrenic hydrocarbon in the block copolymer is 60 to 95% by weight. Below 60%,
Since the resulting resin resembles a rubber-like elastic body, it is unsuitable for use as a film, and if it exceeds 95%, a film having the above-mentioned properties, which is the object of the present invention, cannot be obtained. The average molecular weight of the block copolymer is in the range of 40,000 to 300,000, preferably 60,000 to 250,000. If it is less than 40,000, the mechanical strength will decrease, and if it exceeds 300,000, the moldability will be poor and it will be difficult to form a film by stretching. The block copolymer has the general structural formula (A-B) o or (A-B) o -A
(A is a block of styrenic hydrocarbon polymer,
B is a block of a conjugated diene hydrocarbon polymer, n is a positive integer), and a linear block copolymer represented by the general structural formula: [(A-B) n ] - o X However, , A is a polymer block of styrenic hydrocarbon, B is a polymer block of conjugated diene hydrocarbon, X is a residue derived from a polyfunctional compound, m is an integer of 1 or more, n is 3 or 4. be. It is a star-shaped block copolymer represented by As for the structure of the block, even if it is a complete block, it is
As seen in Japanese Patent No. 48546, any so-called tapered block structure containing an AB random copolymer in the transition region between block A and block B may be used. These block copolymers can be classified structurally as follows. (1) A-B (2) A-B-A (3) A-B-A-B (4) A-B-A-B-A (5) A-B-A-B-A-B (6) A-B-A-B-A-B-A (7) [(A-B) n ] - 3 X (m and X are as above) (8) [(A-B) n ] - 4 X (where m and The block copolymers of structures (2), (7), and (8) lack film-forming processability by stretching and heat shrinkability. On the other hand, the so-called multiblock block copolymers of structures (3), (4), (5), and (6) have good stretching film formability and excellent heat shrinkability.
That is, it is preferable that n is 2 or more, preferably 3 to 5 in the general structural formula (A-B) o -A. Next, polystyrene is general transparent polystyrene, and any polystyrene with a molecular weight of 100,000 or more that can be molded with a molding machine is sufficient. The amount of polystyrene added is 10
~30 parts by weight. The purpose of adding polystyrene is to improve the stiffness, transparency, and gloss of the film.
If the amount added exceeds 30 parts by weight, the influence of polystyrene will be strong, causing a decrease in impact strength and an unavoidable increase in stretching temperature, which will impair the film's suitability as a packaging material and processability. The rubbery block copolymer (hereinafter referred to as thermoplastic rubber) used in the present invention consists of 20 to 50% by weight of styrene hydrocarbon and 50 to 50% by weight of conjugated diene hydrocarbon.
It is a block copolymer consisting of 80% by weight. Since this block copolymer has a high conjugated diene hydrocarbon content of 50 to 80% by weight, it exhibits rubber elasticity as a solid and can be remelted without a chemical crosslinking agent. If the conjugated diene hydrocarbon content is less than 50% by weight, the film exhibits resin-like properties and oil resistance is reduced, making it undesirable. If it exceeds 80% by weight, the film becomes less transparent and stiff. The resin composition used for the transparent heat-shrinkable film used in the present invention includes 100 parts by weight of thermoplastic resin, 10 to 30 parts by weight of polystyrene, and 0.3 parts by weight of thermoplastic rubber.
~10 parts by weight. That is, 0.3 to 10 parts by weight of thermoplastic rubber is added to 100 parts by weight of thermoplastic resin; if it is less than 0.3 parts by weight, the oil resistance will be poor and the effect of suppressing cracking on the film after heat shrinkage will be small; If the amount exceeds 1 part by weight, the transparency decreases, making it difficult to distinguish the contents after coating the glass container, and furthermore, the stiffness of the film decreases.
Furthermore, 10 to 30 parts by weight of polystyrene is added. Adding 10 parts by weight or more of polystyrene improves transparency, but if it exceeds 30 parts by weight, the oil resistance, that is, the effect of suppressing cracking in the heat-shrinkable film, decreases, and furthermore, the impact strength decreases and the stretching temperature increases. Undesirable. Furthermore, the resin composition may contain a lubricant, if necessary.
Antioxidants, ultraviolet absorbers, colorants, etc. can also be added. In the case of the resin composition used in the present invention, it may be dry-blended using a conventional Henschel mixer, ribbon blender, super mixer, V-blender, etc., and may also be melted and pelletized using an extruder. Preferably, Melt mixing is better. Next, the stretching method used in the present invention may be either the tenter method or the tubular method, and the stretching may be uniaxial, biaxial, or multiaxial in the longitudinal direction or in the transverse direction. The coating of the glass container in the present invention may be carried out by a conventional method, for example, by forming a stretched film into a shape that conforms to the shape of the glass container, covering the glass container, and blowing hot air onto it, or placing it in an oven. The film may be heat-shrinked by heating, etc., and brought into close contact with the glass container. [Examples] Hereinafter, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to these Examples. The method for measuring the physical properties of the film and the crack initiation test method that serves as an indicator of oil resistance and stress cracking resistance when applied to glass containers are as follows. VICAT Softening Point JIS-K-6870 Heat Shrinkage Stress Heat shrinkage stress was measured under the following conditions using a heat shrinkage stress measuring machine manufactured by Toyo Seiki Co., Ltd. Sample shape: Indicated thickness x 20mm (width) x 100mm
(Length) Length direction is stretching direction Measurement temperature: 140℃ (heating medium: silicone oil) Table values are stress (g)/thickness x width (mm 2 ) Tensile strength JIS-K-6732 (vertical-stretching direction) Elongation Film Impact Using a film impact tester manufactured by Tester Sangyo Co., Ltd., the strength against impact punching of the film was measured under the following conditions. Shock spherical surface 1", 20℃ Haze ASTM-D-1003 Heat shrinkage rate The film was placed in a constant temperature oven under the following conditions and the heat shrinkage rate was measured. Heat medium: Silicone oil (in a constant temperature oven) Time: 60 seconds Sample shape 10 ×10cm Crack initiation test method Cover the glass container with the film, and heat it at 190℃ while the gear is open.
After cooling by heat shrinking for 60 seconds, apply rapeseed oil evenly to the film surface.
The occurrence of cracks was observed. After coating, the time when a crack of 5 mm or more in length occurred was defined as the crack initiation time. Example 1 Thoroughly dehydrate the reaction vessel with a 100mm jacket.
After charging 80 g of purified benzene and adding a mixture of 9 kg of styrene and 1 kg of butadiene, 0.3 mol of a bifunctional butadiene oligomer dilithium initiator was added as active terminal lithium, and the same contents were added.
Polymerization is completed by raising the temperature to 50°C. Then, a mixture of 8 kg of styrene and 2 kg of butadiene is further added and polymerized. The obtained polymer solution is subjected to steam stripping to recover the polymer. The number average molecular weight of this polymer is 175,000. (Styrene content: 85%, butadiene content: 15%) This polymer is a block copolymer represented by the formula (AB) o -A (n=3), and was pelletized. For 100 parts by weight of this thermoplastic resin, add polystyrene (Denka Styrene manufactured by Denki Kagaku Kogyo Co., Ltd.) to 100 parts by weight of this thermoplastic resin.
10 parts by weight of GP-1] and 5 parts by weight of thermoplastic rubber [Tuffrene-A manufactured by Asahi Kasei Corporation] were melted and mixed to form pellets. This resin composition is molded using a hot plate press machine at a molding temperature of
A press plate was formed at 170°C to obtain a sheet with a thickness of 225μ12×12cm. This sheet was uniaxially stretched using a Toyo Seiki biaxial stretching machine. Preheating temperature 105℃, preheating time 90 seconds, stretching ratio 4.5
12 x 54 cm at a stretching speed of 1.8 m/min, thickness 48 ~
A 52μ film was obtained. Film characteristics, film forming conditions, etc. are shown in Table 1 below together with other examples. Next, this film was placed on a glass container and heated and shrunk to produce a film-covered glass container. The results of testing its transparency and crack initiation,
It is also shown in Table 1. Both haze and crack generation inhibiting effects were good. Example 2 Thermoplastic resin synthesized by the same method as Example 1
Polystyrene per 100 parts by weight [Denki Kagaku Kogyo
15 parts by weight of Dencastyrol GP-1 manufactured by Co., Ltd.
and thermoplastic rubber [manufactured by Asahi Kasei Corporation - Toughprene]
A] was added in an amount of 8 parts by weight, and the mixture was melted and mixed into pellets. Using these pellets, film formation and crack initiation tests were carried out in the same manner as in Example 1. The results are shown in Table 1 together with the film forming conditions and general physical properties of the film. Both haze and crack generation prevention effects were good. Example 3 Thermoplastic resin synthesized by the same method as Example 1
Polystyrene per 100 parts by weight [Denki Kagaku Kogyo
30 parts by weight of Dencastyrol GP-1 (manufactured by Asahi Kasei Corporation) and thermoplastic rubber (Tuffprene, manufactured by Asahi Kasei Corporation)
A] was added in an amount of 10 parts by weight, and the mixture was melted and mixed into pellets. Using these pellets, film formation and crack initiation tests were carried out in the same manner as in Example 1. The results are shown in Table 1 together with the film forming conditions and general physical properties of the film. Both haze and crack generation inhibiting effects were good. Comparative Example 1 A film was formed and a crack initiation test was conducted in the same manner as in Example 1 using only a thermoplastic resin synthesized in the same manner as in Example 1. This result,
Table 1 shows the film forming conditions and general physical properties of the film. Although the haze was good, the crack prevention effect was poor at 22 minutes. Comparative Example 2 Thermoplastic resin synthesized by the same method as Example 1
To 100 parts by weight, 10 parts by weight of polystyrene (Denka Styrol GP-1 manufactured by Denki Kagaku Kogyo Co., Ltd.) was added and melted and mixed to form pellets. Using this pellet, film formation and crack initiation tests were conducted in the same manner as in Example 1.
The results are shown in Table 1 together with the film forming conditions and general physical properties of the film. Although the haze was good, the crack initiation prevention effect was very poor at 80 seconds. Comparative Example 3 Thermoplastic resin synthesized in the same manner as Example 1
To 100 parts by weight, 5 parts by weight of thermoplastic rubber [Tuffrene-A, manufactured by Asahi Kasei Corporation] was added and melted and mixed to form pellets. Using this pellet, film formation and crack initiation tests were conducted in the same manner as in Example 1. The results are shown in Table 1 together with the film forming conditions and general physical properties of the film. Although the effect of inhibiting crack generation is good, the haze is higher than in Example 1. Comparative Example 4 Thermoplastic resin synthesized by the same method as Example 1
To 100 parts by weight, 10 parts by weight of thermoplastic rubber [Tuffrene-A, manufactured by Asahi Kasei Corporation] was added and melted and mixed to form pellets. Using these pellets, film formation and crack initiation tests were carried out in the same manner as in Example 1. The results are shown in Table 1 together with the film forming conditions and general physical properties of the film. Although the effect of inhibiting crack generation is good, the haze is higher than in Example 3. Comparative Example 5 Thermoplastic resin synthesized in the same manner as Example 1
To 100 parts by weight, 15 parts by weight of thermoplastic rubber (Tuffprene-A, manufactured by Asahi Kasei Corporation) was added and melted and mixed to form pellets. Using this pellet, film formation and crack initiation tests were conducted in the same manner as in Example 1. The results are shown in Table 1 along with the film forming conditions and general physical properties of the film. Although the cracking prevention effect is good, the haze is high and the contents cannot be distinguished.
以上説明したように、本発明のフイルム被覆ガ
ラス容器は、被覆したスチレン系樹脂のフイルム
としての特徴である、透明性、光沢、通気、通湿
性の他に、熱収縮性、ヒートシール性に優れ、更
に耐油性及び耐ストレスクラツキング性を有する
という好適な物性により、従来よりも美麗で、耐
久性が良いという顕著な効果を奏するものであ
る。
As explained above, the film-coated glass container of the present invention has excellent heat-shrinkability and heat-sealability in addition to transparency, gloss, air permeability, and moisture permeability, which are characteristics of a coated styrenic resin film. Furthermore, due to its favorable physical properties of oil resistance and stress cracking resistance, it has the remarkable effect of being more beautiful and having better durability than conventional products.
Claims (1)
ジエン系炭化水素5〜40重量%とからなる平均
分子量4万〜30万の樹脂状ブロツク共重合体
100重量部、 (B) ポリスチレン10〜30重量部、及び (C) スチレン系炭化水素20〜50重量%と共役ジエ
ン系炭化水素50〜80重量%とからなるゴム状ブ
ロツク共重合体0.3〜10重量部 の樹脂組成物を1軸、2軸又は多軸に延伸した透
明熱収縮性フイルムでガラス容器を加熱収縮被覆
してなることを特徴とするフイルム被覆ガラス容
器。[Scope of Claims] 1 (A) A resinous block copolymer with an average molecular weight of 40,000 to 300,000, consisting of 60 to 95% by weight of a styrene hydrocarbon and 5 to 40% by weight of a conjugated diene hydrocarbon.
100 parts by weight, (B) 10 to 30 parts by weight of polystyrene, and (C) 0.3 to 10% of a rubbery block copolymer consisting of 20 to 50% by weight of a styrene hydrocarbon and 50 to 80% by weight of a conjugated diene hydrocarbon. 1. A film-coated glass container, characterized in that the glass container is heat-shrinkable coated with a transparent heat-shrinkable film obtained by stretching part by weight of a resin composition uniaxially, biaxially, or multiaxially.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3502286A JPS61222738A (en) | 1986-02-21 | 1986-02-21 | Film coated glass vessel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3502286A JPS61222738A (en) | 1986-02-21 | 1986-02-21 | Film coated glass vessel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61222738A JPS61222738A (en) | 1986-10-03 |
| JPS632777B2 true JPS632777B2 (en) | 1988-01-20 |
Family
ID=12430432
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3502286A Granted JPS61222738A (en) | 1986-02-21 | 1986-02-21 | Film coated glass vessel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61222738A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10323894A (en) * | 1997-05-28 | 1998-12-08 | Sumitomo Chem Co Ltd | Inflation processing method of polystyrene resin and blown film |
-
1986
- 1986-02-21 JP JP3502286A patent/JPS61222738A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61222738A (en) | 1986-10-03 |
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