JPS61222738A - Film coated glass vessel - Google Patents
Film coated glass vesselInfo
- Publication number
- JPS61222738A JPS61222738A JP3502286A JP3502286A JPS61222738A JP S61222738 A JPS61222738 A JP S61222738A JP 3502286 A JP3502286 A JP 3502286A JP 3502286 A JP3502286 A JP 3502286A JP S61222738 A JPS61222738 A JP S61222738A
- Authority
- JP
- Japan
- Prior art keywords
- weight
- film
- parts
- heat
- block copolymer
- 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.)
- Granted
Links
Landscapes
- 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)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、特定の透明熱収縮性フィルムを被憶したガラ
ス容器に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a glass container coated with a specific transparent heat-shrinkable film.
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重量うとから成る平均分子量4
万〜30万の樹脂状ブロック共重合体(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音、公知のテンター法
、あるいはチューブラ−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ィル
ムは、特開昭48−13973号公報に見られる工うに
、熱収縮性、ヒートシール性、ガス透過性に優れ、更に
透明性、高光沢金有するフィルムであり、熱収縮包装等
の包装材料に適している。Conventionally, the average molecular weight is 4, which is composed of 60 to 95% by weight of styrenic hydrocarbon and 5 to 40% by weight of conjugated diene hydrocarbon.
0 to 300,000 polystyrene to 100 parts by weight of resinous block copolymer (hereinafter referred to as thermoplastic resin)
A transparent film obtained by stretching a resin composition containing 30 parts by weight in a uniaxial, uniaxial, biaxial, or multiaxial direction at a stretching ratio of 2 to 8 times by a known tenter method or tubular method is , as seen in JP-A-48-13973, is a film that has excellent heat shrinkability, heat sealability, and gas permeability, as well as transparency and high gloss gold, making it suitable for packaging materials such as heat shrink packaging. ing.
しかしながら、この樹脂組成物から成る延伸フィルムは
熱収縮包装において包装対象物(各洩容器等)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、フィルムに
細いき裂や割れが生じる場合が少なくない(ストレスク
ラッキング現象)。これらのき裂や割れは、シュリンク
ラベルとしての美脆さヲ損うばかりでなく、包装対象物
に対する保農効果を喪失させ、包装材料としての適性金
欠く原因となる。However, in heat-shrink packaging, the stretched film made of this resin composition is susceptible to heat shrinkage stress, residual stress due to the shape of the packaged object, and storage stress of the packaged object after heat shrinkage to the packaged object (leak containers, etc.). In response to changes in the environment, thin cracks and cracks often occur in films (stress cracking phenomenon). These cracks and cracks not only impair the beauty and fragility of the shrink label, but also cause a loss of the protective effect on the packaged object, leading to a lack of suitability as a packaging material.
通常、き裂の防止対策としては、樹脂組成物のブロック
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11−増大
させる方法がとられている。Generally, measures to prevent cracks include increasing the molecular weight of styrenic hydrocarbons or increasing the content of conjugated diene hydrocarbons in the block structure of the resin composition.
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、フィルムのl1lt−
低下させると同時に、熱収a開始温度を低下させ、熱収
縮包装材料としての適性金欠く。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、き裂や割れの発庄は防止できない。However, increasing the molecular weight reduces the flow of the resin, and increasing the content of conjugated dienes decreases the l1lt-
At the same time, it also lowers the starting temperature of heat loss, making it less suitable 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.
本発明の目的は、熱収縮包装後の被覆フィルム面でき裂
や割れの発主のないフィルム被覆ガラス容器全提供する
ことにある。An object of the present invention is to provide a film-covered glass container that is free from cracks and cracks on the surface of the covering film after heat-shrink packaging.
本発明を概説すれば、本発明はフィルム被αガラス容器
に関する発明であって、
囚 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〜
30万の樹脂状ブロック共重合体100重量部、
の)ポリメチレフ10〜30g1部、及び(C) ス
チレン系炭化水素20〜50重t%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ック共重合
体cL3〜10重量部
の樹脂組成物’1i−1軸、2軸又は多軸に延伸し次透
明熱収縮性フィ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。To summarize the present invention, the present invention relates to a glass container coated with a film, and comprises an average molecular weight of 40,000 to 40,000, 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 of a resinous block copolymer of 300,000 yen, 1 part of 10 to 30 g of polymethyleff, and (C) a rubber consisting of 20 to 50 wt% of a styrene hydrocarbon and 50 to 80 wt% of a conjugated diene hydrocarbon. 3 to 10 parts by weight of a block copolymer cL resin composition '1i- is characterized in that it is uniaxially, biaxially or multiaxially stretched, and then a glass container is heat-shrinkable covered with a transparent heat-shrinkable film.
本発明において使用する熱可塑性樹脂のブロック共重合
体大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、ブタジェン又はイソプレン等である。これらの単
量体からブロッ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全使用し、内炭
化水素単量体を段階的に重合する方法、両単量体の混合
物を不活性浴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って製造される。該ブロック共重
合体中に占めるスチレン系炭化水素の割合は、60〜9
5重iI′チである。60%未満では、得られ′fC樹
脂がゴム的な弾性体に似たものになるので、フィルムと
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ィルムが得られない。ブロ
ック共重合体の平均分子量は、4万〜30万好IL<f
16万〜25万の範囲のものである。4万未満のもので
は、機械的な猪強度が低下し、ま7’(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。ブロッ
ク共重合体は一般構造式(A −B )n又は(A−B
)n−A (Aはスチレン系炭化水素の重合体のブロッ
クW、BU共役ジエン系炭化水素の重合体のブロックk
、nは正の整数全表わす)で表わされ・る直線型ブロツ
ク共重合体、及び、一般構造式:
%式%)
但し、Aはスチレン系炭化水素の重合体ブロック、
Bは共役ジエン系炭化水素の重合体ブロック、
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。The styrenic hydrocarbon that largely constitutes the block copolymer of the thermoplastic resin used in the present invention is styrene or α-methylstyrene, and the conjugated diene hydrocarbon is butadiene, isoprene, or the like. In order to produce a block copolymer from these monomers, there is a method in which the inner hydrocarbon monomer is polymerized stepwise using an anionic polymerization initiator, especially an organolithium compound. It is produced by a method of copolymerizing a mixture in an inert bath medium, or a method of appropriately using a combination of these methods. The proportion of styrenic hydrocarbon in the block copolymer is 60 to 9.
It is 5-fold iI'chi. If it is less than 60%, the resulting 'fC resin will resemble a rubber-like elastic body, making it unsuitable as a film, and if it exceeds 95%, the film having the above-mentioned properties, which is the object of the present invention, will not be suitable. I can't get it. The average molecular weight of the block copolymer is 40,000 to 300,000. IL<f
It is in the range of 160,000 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 a general structural formula (A -B)n or (A-B
) n-A (A is a block W of a styrene hydrocarbon polymer, a block k of a BU conjugated diene hydrocarbon polymer
, n is a positive integer) and the general structural formula: % formula %) However, A is a styrenic hydrocarbon polymer block, B is a conjugated diene type a hydrocarbon polymer block, X is a residue derived from a polyfunctional compound, m is an integer of 1 or more, and n is 3 or 4.
で表わされる星型ブロック共重合体でめる。ブロックの
構造としては、完全ブロックでも特開昭48−4854
6号公報に見られるごとく、ブロックAとブロックBの
遷移部にABランダム共共重合体金含有友いわゆるテー
パードブロック構造のいずれでも工い。これらのブロッ
ク共重合体を構造的に分類すると次の様になる。It is made of a star-shaped block copolymer represented by As for the structure of the block, even if it is a complete block,
As seen in Publication No. 6, a so-called tapered block structure of AB random copolymer gold-containing copolymer is used in the transition region between block A and block B. These block copolymers can be classified structurally as follows.
+IIA−B
121 A−B−A
(31A−B−A−B
+41 A−B−A−B−A
(51A−B−A−B−A−B
(8) A−B−A−B−A−B−A(7) (
(A−B凡+3X(但しm及びXは前記のとおり)
(8) ((A−B)m37X (但し、m及びxh
前記のとおV)
前記構造(1)のブロック共重合体は、フィルム成膜時
、高温における引張強度が小さく成膜できない。構造(
2)s(7L(3)のブロック共重合体は、延伸g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+3L (41,(5)、(6)のいわゆるマル
チブロック化されたブロック共重合体は、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、−膜構
造式(A−B)n−Aでnが2以上針1しくは3〜5で
あるものが良い。+IIA-B 121 A-B-A (31A-B-A-B +41 A-B-A-B-A (51A-B-A-B-A-B (8) A-B-A-B- A-B-A (7) (
(A-B +3X (However, m and X are as above) (8) ((A-B) m37X (However, m and xh
V) The block copolymer having the structure (1) cannot be formed into a film due to its low tensile strength at high temperatures. structure(
2) The block copolymer with s(7L(3)) lacks stretch g film processability and also lacks heat shrinkability.On the other hand, the so-called multi-block copolymer with structure +3L(41, (5), (6)) The block copolymer has good stretching film formability and excellent heat shrinkability. That is, - film structural formula (A-B) n-A where n is 2 or more and needle 1 or Those with a rating of 3 to 5 are good.
次にポリスチレンとは、一般の透明ポリスチレンでめり
、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11’は、10〜30重量部
である。ポリスチレンの添加は、フィルムの腰、透明性
、光沢の向上を目的とするが、添加蓋が30TL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、延伸温度の上昇全余儀なくする等の、フィル
ムの包装材料適性、加工性を損ねる原因となる。Next, the polystyrene may be general transparent polystyrene with a molecular weight of 100,000 or more that can be molded using a molding machine. The polystyrene addition 11' is 10 to 30 parts by weight. The purpose of adding polystyrene is to improve the stiffness, transparency, and gloss of the film, but if the added amount exceeds 30 TL, the influence of polystyrene will be strong, resulting in a decrease in impact strength and an increase in stretching temperature. etc., which may impair the film's suitability as a packaging material and processability.
本発明で使用するゴム状ブロック共重合体(以下熱可塑
性ゴムという)とは、スチレン系炭化水素t−20〜5
oxtsと共役ジエン系炭化水素を50〜80重量うと
から成るブロック共重合体である。このブロック共重合
体は、共役ジエン系炭化水素含有量が50〜8ON11
%と高い九め、化学的7!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501i1%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重倉%全
超えると、フィルムの透明性及び腰の低下を招く。The rubbery block copolymer (hereinafter referred to as thermoplastic rubber) used in the present invention is a styrene hydrocarbon t-20 to 5
It is a block copolymer consisting of 50 to 80% by weight of oxts and conjugated diene hydrocarbon. This block copolymer has a conjugated diene hydrocarbon content of 50 to 8ON11.
% and high 9th, chemical 7! It is solid, exhibits rubber elasticity, and can be remelted without a crosslinking agent. If the conjugated diene hydrocarbon content is less than 501i1%, it exhibits resinous properties and oil resistance is reduced, making it undesirable.If it exceeds 80%, the transparency and stiffness of the film will decrease.
本発明で使用する透明熱収縮フィ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コム(L3〜10重量部
からなっている。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α3〜10重量部添加するので
あり、[13重量部未満では耐油性が悪く熱収縮後のフ
ィ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、しかもフィルムの腰の低下
を招く。東にポリスチレンを10〜50重量部龜加置部
。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
性フィルムのき裂発生抑止効果が減少μ東に衝撃強度の
低下及び延伸温度の上昇がおり好ましくない。The resin composition used in the transparent heat-shrinkable film used in the present invention consists of 100 parts by weight of a thermoplastic resin, 10 to 30 parts by weight of polystyrene, and 3 to 10 parts by weight of a thermoplastic comb (L3 to 10 parts by weight). Thermoplastic rubber is added in an amount of α3 to 10 parts by weight per 100 parts by weight; if it is less than 13 parts by weight, the oil resistance will be poor and the effect of inhibiting cracking on the film after heat shrinkage will be small, and if it exceeds 10 parts by weight, 10 to 50 parts by weight of polystyrene is added to the glass container.More than 10 parts by weight of polystyrene is added. When added, the transparency is improved, but if it exceeds 30 parts by weight, the oil resistance, that is, the effect of inhibiting the generation of cracks in the heat-shrinkable film decreases, and the impact strength decreases and the stretching temperature increases, which is not preferable.
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混合は、通常のヘンシェ
ルミキサー、リボンブレンダー、スーパーミキサー及び
V)゛レンダー等でトライブレンドしても工く、史に押
出機で溶融してベレット化してもよく、好ましくは、溶
融混合が工い。Furthermore, a lubricant, an antioxidant, an ultraviolet absorber, a coloring agent, etc. can be added to the resin composition as necessary. The resin composition used in the present invention may be mixed by tri-blending using a conventional Henschel mixer, ribbon blender, super mixer, V) blender, etc., or may be melted and pelletized using an extruder. Preferably, melt mixing is used.
次に、本発明で用いた延伸方法は、テンター法おるいは
チュブラ−法のいずれでもよ<、延伸は、縦又は横1軸
、2軸おるいは多軸に延伸することができる。Next, the stretching method used in the present invention may be either the tenter method or the tubular method.
そして、本発明におけるガラス容器の被稜セ通常の方法
で行ってよく、例えば延伸したフィ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、フィルムを熱収縮させてガラス容器に密着
させればよい。The edge-setting 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 form 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.
以下、本発明を実施例により史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0
lお、フィ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。Hereinafter, the present invention will be explained in detail with reference to examples.
The present invention is not limited to these examples.The method for measuring the physical properties of the film and the crack initiation accelerated test method that serves as an index of oil resistance and stress cracking resistance when applied to glass containers are as follows: , are as follows.
VICAT 軟化点 JIS−に−6870熱収縮応力
東洋稍機社夷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。VICAT Softening Point JIS-6870 Heat Shrinkage Stress Heat shrinkage stress was measured under the following conditions using a heat shrinkage stress measuring machine manufactured by Toyo Koki Co., Ltd.
サンプル形状二表記厚X 20 wm (幅)×100
籠(長)
長さ方向が低伸方向
測定iPA反: 14oc(熱媒:シリコンオイル)
表値は、応力(f)
/厚×幅(Wa”)
引 張 強 度 JIS−に−6752(タテー砥伸方
向)伸 び
条件でフィルムの衝撃打ち抜き
に対する強度を測定した。Sample shape (2) Thickness x 20 wm (width) x 100
Basket (long) Length direction is measured in low elongation direction iPA resistance: 14oc (heating medium: silicone oil)
The table values are stress (f)/thickness x width (Wa'') Tensile strength The strength against impact punching of the film was measured under JIS-6752 (vertical elongation direction) elongation conditions.
衝撃球面1′、20℃
ヘ イ ズ ASTM−D−1005熱収縮
率 下記の条件でフィルムを恒温槽中につけ、熱収縮
率全測定した。Impact spherical surface 1', 20°C haze ASTM-D-1005 heat shrinkage rate The film was placed in a constant temperature bath under the following conditions, and all heat shrinkage rates were measured.
熱媒:シリコンオイル(恒温槽中) 時間:6Qsec サンプル形状 10X10crn で熱収縮させた冷却後、フィルム 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5m以上のき裂が発生した時間 全き裂発生時間とした。Heat medium: silicone oil (in constant temperature bath) Time: 6Qsec Sample shape: 10X10crn After cooling, the film is heat-shrinked with Apply rapeseed oil evenly to the surface and The occurrence of cracks was observed. After application, long Time at which a crack of 5 m or more in length occurred This was taken as the total crack initiation time.
実施例1
100tのジャケット付の反応缶に、十分脱水、精製し
几ベンゼンaoz’6仕込み、スチレン9ゆとブタジェ
ン1時の混合物を添加したのち、2官能のブタジェンオ
リゴマージリチウム開始剤全活性末端リチウムとしてα
3モル象添加、同門答物を50℃1で昇温させることに
LV重合を完結させる。次いで更にスチレン8時とブタ
ジェン2ゆの混合物を添加し、重合させる。Example 1 Into a 100 t jacketed reaction vessel, fully dehydrated and purified benzene Aoz'6 was added, and a mixture of 9 parts styrene and 1 part butadiene was added, and the total activity of the difunctional butadiene oligomer dilithium initiator was added. α as terminal lithium
The LV polymerization is completed by adding 3 moles of the product and raising the temperature of the same product to 50°C. Next, a mixture of 8 parts of styrene and 2 parts of butadiene is further added and polymerized.
得られた重合溶液は、スチームストリッピングすること
にニジポリマーを回収する。このポリマーの数平均分子
fi−f117.5万である。(スチレン含有量85%
、ブタジェン含、[t15%)このポリマーは、式(A
−B)n−A (n= 3 )で表わされるブロック共
重合体でめり、これ全ペレット化した。The obtained polymerization solution is subjected to steam stripping to recover the rainbow polymer. The number average molecule fi-f of this polymer is 1,175,000. (Styrene content 85%
, containing butadiene, [t15%] This polymer has the formula (A
-B) A block copolymer represented by n-A (n=3) was milled and the whole was pelletized.
この熱可塑性樹脂100M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)
’i10重量部、及び熱可塑性ゴム〔旭化成(株)社製
・タフグレン−A]’に5i址部添加、浴融混合ベレッ
ト化した。For 100 M parts of this thermoplastic resin, polystyrene (Denka Styrol GP-1 manufactured by Denki Kagaku Kogyo Co., Ltd.)
10 parts by weight of i and 5 parts by weight of thermoplastic rubber [Toughgrain-A manufactured by Asahi Kasei Corporation] were added to form a bath-melt mixture into pellets.
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225μm2X12anのシート
を得た。このシート金東洋精機2軸廷伸磯で1軸廷伸し
た。This resin composition was press plate molded using a hot plate press machine at a molding temperature of 170° C. to obtain a sheet having a thickness of 225 μm 2×12 an. This sheet metal Toyo Seiki 2-shaft stretching was carried out with a single-shaft stretching.
予熱温度105C,予熱時間90秒、延伸倍率4.5倍
、延伸速反1. B rn/minで12 X 54
cm。Preheating temperature: 105C, preheating time: 90 seconds, stretching ratio: 4.5 times, stretching speed: 1. 12 x 54 at Brn/min
cm.
厚さ48〜52μのフィルムが得られた。フィルム特性
及び成膜条件等を後記表1に他の例と共に示す。A film with a thickness of 48-52μ was obtained. Film characteristics, film forming conditions, etc. are shown in Table 1 below along with other examples.
次に、このフィルムをガラス容器にかぶせ、加熱収縮さ
せて、フィルム被僅ガラス容器全作製した。その透明性
及びき装発生金試験した結果を、同じく表1に示す。Next, this film was placed on a glass container and heat-shrinked to produce a complete glass container covered with the film. The results of the transparency and cladding gold tests are also shown in Table 1.
ヘイズ及びき裂発生抑止効果共良好であった。Both haze and crack generation inhibition effects were good.
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
カステロールGP−1)il 5重量部、及び熱可塑性
ゴム〔旭化成(株)社g−タフプレン−A)を8重量部
祭加、溶融混合ペレット化した。Example 2 5 parts by weight of polystyrene [Dencasterol GP-1 manufactured by Denki Kagaku Kogyo Co., Ltd.] il and thermoplastic rubber [Dencasterol GP-1 manufactured by Denki Kagaku Kogyo Co., Ltd.] were added to 100 parts by weight of a thermoplastic resin synthesized in the same manner as in Example 1. 8 parts by weight of Co. g-Tuffrene-A) were added and melted and mixed into pellets.
このベレット全使用して、以下、実施例1と同様にして
フィルム成膜、き裂発生促進試験全実施した。この結果
を、成膜条件及びフイルム−膜物性とあわせて衣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った
。Using all of these pellets, film formation and crack initiation tests were carried out in the same manner as in Example 1. The results are shown in Cloth 1 along with the film-forming conditions and film-membrane physical properties. Both haze and crack generation prevention effects were good.
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]’i50重量部及び熱可塑性ゴ
ム〔旭化成(株ン社製−タフダレ/−A〕i10重量部
添加、溶融混合ペレット化した。Example 3 50 parts by weight of polystyrene [Denka Styrol GP-1 manufactured by Denki Kagaku Kogyo Co., Ltd.] and thermoplastic rubber [Denka Styrol GP-1 manufactured by Denki Kagaku Kogyo Co., Ltd.] and 100 parts by weight of thermoplastic resin synthesized in the same manner as in Example 1 were added. 10 parts by weight of I was added and melted and mixed into pellets.
このベレットを使用して、以下実施例1と同様にして、
フィルム成膜、き裂発生促進試験を実施した。この結果
を、成膜条件及びフィルム−膜物性とあわせて表1に示
した。ヘイズ及びき裂発生抑止効果共良好であった。Using this pellet, in the same manner as in Example 1,
Film deposition and crack initiation tests were conducted. The results are shown in Table 1 together with the film-forming conditions and film-membrane physical properties. Both haze and crack generation inhibition effects were good.
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t用い
て、実施例1と同様にしてフィルム成膜、き裂発生促進
試験を実施した。この結果を、成膜条件及びフィルム−
膜物性とあわせて表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。Comparative Example 1 A film was formed and a crack initiation test was carried out in the same manner as in Example 1, using only the thermoplastic resin synthesized in the same manner as in Example 1. This result was calculated based on the film formation conditions and film-forming conditions.
Table 1 shows the properties of the film. Although the haze was good, the crack prevention effect was poor at 22 minutes.
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−13il。Comparative Example 2 Polystyrene [Denka Styrol GP-13il manufactured by Denki Kagaku Kogyo Co., Ltd.] was added to 100 parts by weight of a thermoplastic resin synthesized in the same manner as in Example 1.
重量部添加、溶融混合ペレット化した。Parts by weight were added and melted and mixed to form pellets.
このベレンif便片して、実施例1と同様にしてフィル
ム成膜、き裂発生促進試験を実施した。この結果を、成
膜条件及びフィルム−膜物性とあわせて表1に示す。ヘ
イズは良好でめったが、き裂発生抑止効果が80秒と非
常に悪化している。Using this Belen if stool piece, film formation and a crack initiation acceleration test were conducted in the same manner as in Example 1. The results are shown in Table 1 together with the film-forming conditions and film-membrane physical properties. Although the haze was good and rare, the crack generation prevention effect was very poor at 80 seconds.
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
レンーA]’ii5重量部添加、溶融混合ペレット化し
次。Comparative Example 3 To 100 parts by weight of a thermoplastic resin synthesized in the same manner as in Example 1, 5 parts by weight of thermoplastic rubber [Toughprene A manufactured by Asahi Kasei Corporation]'ii was added, melted and mixed to form pellets.
このベレットを使用して実施例1と同様にして、フィル
ム成膜、き裂発生促進試験を実施し次。この結果を成膜
条件及びフィルム−膜物性とあわせて表1に示す。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 film-membrane physical properties.
き裂発生抑止効果は良好であるが、実施例1に比ベヘイ
ズが高い。Although the effect of inhibiting crack generation is good, the haze is higher than in Example 1.
比較例4
実施例1と同じ方法で合成し交熱可塑性樹脂100重量
部に対して、熱可塑性ゴム〔旭化成(株)社製−タフプ
レンーA:li10重量部添加、溶融混合ペレット化し
た。Comparative Example 4 Comparative example 4 was synthesized in the same manner as in Example 1, and 10 parts by weight of a thermoplastic rubber [manufactured by Asahi Kasei Corporation - Toughprene A: li] was added to 100 parts by weight of an exchange thermoplastic resin, and the mixture was melted and mixed into pellets.
このベレットヲ使用して、以下、実施例1と同様にして
フィルム成膜、き裂発生促進試験を実施した。この結果
を、成膜条件及びフィルム−膜物性とあわせて表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
ベヘイズが高い。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 film-membrane physical properties. The effect of inhibiting crack generation is good, but the haze is higher than in Example 3.
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、溶融混合ペレット化し
た。Comparative Example 5 To 100 parts by weight of a thermoplastic resin synthesized in the same manner as in Example 1, 15 parts by weight of thermoplastic rubber (manufactured by Asahi Kasei Corporation - Tuffrene-A) was added, and the mixture was melted and mixed into pellets.
このベレン)?使用して実施例1と同様にして、フィル
ム成膜、@鋏発生促進試験會笑施した。この結果全成膜
条件及びフィルム−膜物性とあわせて表−1に示す。This Belen)? A film was formed and a scissors generation acceleration test was conducted in the same manner as in Example 1. The results are shown in Table 1 along with the total film forming conditions and film properties.
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。Although the cracking prevention effect is good, the haze is high and the contents cannot be distinguished.
以上説明した工うに、本発明のフィルム被覆ガラス容器
ハ、wl覆したスチレン糸樹脂のフィルムとしての特徴
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エリ、従来エ
リも美麗で、耐久性が良いという顕著な効果を奏するも
のである。In addition to the above-described method, the film-coated glass container of the present invention is characterized by transparency, gloss, air permeability, and moisture permeability as well as heat-shrinkability and heat-sealability, which are the characteristics of the coated styrene thread resin film. It has excellent physical properties such as excellent oil resistance and stress cracking resistance, and has the remarkable effect of being beautiful and durable compared to conventional materials.
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 ロック共重合体100重量部、 (B)ポリスチレン10〜50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ック共重合体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
縮性フィルムでガラス容器を加熱収縮被覆してなること
を特徴とするフィルム被覆ガラス容器。[Scope of Claims] 1. (A) 100% by weight of a resinous block copolymer having an average molecular weight of 40,000 to 300,000 and consisting of 60 to 95% by weight of a styrene hydrocarbon and 5 to 40% by weight of a conjugated diene hydrocarbon. (B) 10 to 50 parts by weight of polystyrene, and (C) 0.3 to 10 parts by weight of a rubbery block copolymer consisting of 20 to 50 parts by weight of a styrene hydrocarbon and 50 to 80 parts by weight of a conjugated diene hydrocarbon. 1. A film-coated glass container, characterized in that the glass container is heat-shrinkable and coated with a transparent heat-shrinkable film obtained by stretching parts 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 true JPS61222738A (en) | 1986-10-03 |
JPS632777B2 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) |
Cited By (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
Cited By (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 |
Also Published As
Publication number | Publication date |
---|---|
JPS632777B2 (en) | 1988-01-20 |
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