JPH02249644A - Multilayer vessel - Google Patents

Multilayer vessel

Info

Publication number
JPH02249644A
JPH02249644A JP7143289A JP7143289A JPH02249644A JP H02249644 A JPH02249644 A JP H02249644A JP 7143289 A JP7143289 A JP 7143289A JP 7143289 A JP7143289 A JP 7143289A JP H02249644 A JPH02249644 A JP H02249644A
Authority
JP
Japan
Prior art keywords
layer
resin
polyolefin
multilayer
molding
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
Application number
JP7143289A
Other languages
Japanese (ja)
Other versions
JP2697101B2 (en
Inventor
Yusuke Terauchi
寺内 裕介
Tatsuo Furuse
達雄 古瀬
Toshiaki Kakemura
敏明 掛村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toppan Inc
Original Assignee
Toppan Printing Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toppan Printing Co Ltd filed Critical Toppan Printing Co Ltd
Priority to JP7143289A priority Critical patent/JP2697101B2/en
Publication of JPH02249644A publication Critical patent/JPH02249644A/en
Application granted granted Critical
Publication of JP2697101B2 publication Critical patent/JP2697101B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Laminated Bodies (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To obtain the multilayer vessel having almost no deformation in circumferential direction due to the shrinkage in molding by a method in which the polyolefin resin layers wherein fiber reinforcing material is blended with high nitric resin layer are mutually laminated, and the adhesive layer with a specified shrinkage factor in molding is provided between the high nitrile layer and the polyolefin resin layer. CONSTITUTION:The polyolefin to be used is preferably the material wherein the fiber resin forcing material such as fiber glass or carbon fiber, etc., is blended with polyethylene or polypropylene, etc., in the ratio of 10-40%, and its shrinkage factor in molding is caused to be 0.2-0.5%. An adhesive layer is preferably the block copolymer of butadiene or isoprene and styrene. By using a high speed blow molding machine, the multilayer parison is coextruded so that the outer layer is made of fiber reinforced polyolefin, the intermediate layer is made of adhesive resin and the inner layer is made of high acrylonitrile resin, and then said parison is blow-molded, thereby obtaining a multilayer vessel.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、成形収縮率が0.2〜0.5%である高ニト
リ、ル樹脂を主原料とするバリア性熱可塑性樹脂からな
る少なくとも1個の層を有するプラスチック製の多層容
器に関するものであり、成形収縮によって円周方向の変
形がほとんどない多層容器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention provides at least one barrier thermoplastic resin whose main raw material is a high nitride resin having a molding shrinkage rate of 0.2 to 0.5%. The present invention relates to a multilayer container made of plastic having one layer, and is related to a multilayer container that undergoes almost no deformation in the circumferential direction due to molding shrinkage.

〔従来の技術〕[Conventional technology]

高ニトリル樹脂は透明性、酸素や炭酸ガスばかりでなく
エステル類等の有機溶剤のガスや、フレオン等の液化ガ
スに対するバリヤー性に優れ、また各種薬品に対する耐
薬品性に優れており、特にアルコール類、エステル類、
ガソリンなどの有機溶剤に対する化学的安定性に優れて
いる。さらに香料、香辛料、精油など幅広い香気成分に
対する保香性に優れている0以上の特徴から高ニトリル
樹脂は化粧品、医薬品、トイレタリー用品、!I4薬、
調味量、香料、食用油、エアー・ゾル容器などの包装材
料として広範囲に利用されてきた。
High nitrile resins have excellent transparency and barrier properties against not only oxygen and carbon dioxide gas, but also organic solvent gases such as esters, and liquefied gases such as Freon.They also have excellent chemical resistance against various chemicals, especially alcohols. , esters,
Excellent chemical stability against organic solvents such as gasoline. In addition, high nitrile resin has excellent fragrance retention properties against a wide range of aromatic components such as fragrances, spices, and essential oils, making it ideal for cosmetics, pharmaceuticals, toiletries, etc. I4 drug,
It has been widely used as a packaging material for seasonings, fragrances, edible oils, aerosol containers, etc.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

高ニトリル樹脂を用いたプラスチック容器としては、コ
ストメリットをあげる点、衝撃強度をあげる点などから
ポリオレフィン系樹脂との多層容器にする方法がとられ
ていたが、ポリオレフィン系樹脂のうち最も一般的に用
いられるポリエチレン、及び、ポリプロピレンは結晶性
熱可塑樹脂で成形収縮率が大きく(ポリエチレン:約3
.2%、ポリプロピレン:約1.7%)、非品性熱可塑
性樹脂で成・形収縮率の小さい(0,2〜0.5%)高
二トリル樹脂と積層接合させると成形後、成形収縮率の
差から容器が変形してしまい、特に胴部円周方向での変
形が大きく容器としての外観を著しく損なうという問題
があった。
For plastic containers using high nitrile resin, multilayer containers with polyolefin resin have been used to increase cost benefits and impact strength, but among the polyolefin resins, the most common The polyethylene and polypropylene used are crystalline thermoplastic resins with a high molding shrinkage rate (polyethylene: about 3
.. 2%, polypropylene: approx. 1.7%), is a non-grade thermoplastic resin with a low molding shrinkage rate (0.2 to 0.5%). When laminated and bonded with high nitrile resin, the molding shrinkage rate after molding will decrease. This difference causes the container to deform, and there is a problem in that the deformation in the circumferential direction of the body is particularly large, and the appearance of the container is significantly impaired.

この高ニトリル樹脂を主原料とするバリア性熱可望性樹
脂からなる少なくとも1個の層を有するプラスチック製
の多層容器の変形を解決する手段は容器胴部にリブを設
ける等して容器の形状を変形しにくいものにするという
方法がとられていたのが現状であり、前記方法では容器
のデザインを狭める結果となっていたため改良が望まれ
ていた。
A means to solve the deformation of a plastic multilayer container having at least one layer made of barrier thermoplastic resin whose main raw material is high nitrile resin is to shape the container by providing ribs on the body of the container. The current method is to make containers difficult to deform, and since this method results in a narrower design of the container, improvements have been desired.

本発明の目的は、成形収縮率が0.2〜0,5%である
高ニトリル樹脂を主原料とするバリア性熱可塑性樹脂か
らなる少なくとも1個の層を有するプラスチック製の多
層容器に関するものであり、成形収縮によって円周方向
の変形がほとんどない多層容器を提供することにある。
The object of the present invention is to relate to a plastic multilayer container having at least one layer made of a barrier thermoplastic resin whose main raw material is a high nitrile resin having a molding shrinkage rate of 0.2 to 0.5%. The object of the present invention is to provide a multilayer container that is hardly deformed in the circumferential direction due to molding shrinkage.

〔発明を解決するための手段〕[Means for solving the invention]

本発明の多層容器は、成形収縮率が0.2〜0.5%で
ある高ニトリル樹脂を主原料とするバリア性熱可塑性樹
脂からなる少なくとも1個の層を有し、前記高ニトリル
樹脂層の片側、あるいは両側に繊維補強材をブレンドし
たポリオレフィン系樹脂層を積層接合し、必要に応じて
前記高ニトリル層と前記ポリオレフィン系樹脂層の間に
成形収縮率が0.3%の接着層を積層接合させて成形さ
れる。
The multilayer container of the present invention has at least one layer made of a barrier thermoplastic resin whose main raw material is a high nitrile resin having a molding shrinkage rate of 0.2 to 0.5%, and the high nitrile resin layer A polyolefin resin layer blended with a fiber reinforcing material is laminated and bonded on one or both sides of the layer, and if necessary, an adhesive layer with a molding shrinkage rate of 0.3% is provided between the high nitrile layer and the polyolefin resin layer. Molded by laminating and bonding.

多層容器を製造する方法としては、胴部と底部が一体化
した多層容器を射出成形、ブロー成形または射出延伸ブ
ロー成形によって製造する方法、前記構成積層体をフィ
ルム状またはシート状に押し出し、溶融ラミネートする
方法が適用できる。
Methods for manufacturing a multilayer container include methods of manufacturing a multilayer container with an integrated body and bottom by injection molding, blow molding, or injection stretch blow molding, extruding the constituent laminate into a film or sheet shape, and melt laminating. This method can be applied.

ブロー成形においては、前記の各樹脂を共押し出しする
ことによって、多層パリソンを得、これをそのまま、あ
るいは延伸してからブロー成形して多層容器を得る。
In blow molding, a multilayer parison is obtained by coextruding each of the above-mentioned resins, and this is blow molded as it is or after being stretched to obtain a multilayer container.

なお、成形された多層容器の各層の厚さは特に限定され
ない。
Note that the thickness of each layer of the molded multilayer container is not particularly limited.

本発明に用いられる高ニトリル樹脂は、不飽和ニトリル
化合物を主体とする共重合体であって、不飽和ニトリル
化合物を50重量%以上含むものが好ましい。
The high nitrile resin used in the present invention is a copolymer mainly composed of an unsaturated nitrile compound, and preferably contains 50% by weight or more of the unsaturated nitrile compound.

コモノマーとしては、スチレン、ブタジェン、イソプレ
ン等が挙げられ、これらの1種または2種以上を不飽和
ニトリル化合物と共重合させたものが好ましく、物性を
損なわない範囲で、必要に応じて安定剤、滑剤、帯電防
止剤、紫外線防止剤、着色顔料を添加しても構わない。
Examples of the comonomer include styrene, butadiene, isoprene, etc., and it is preferable to copolymerize one or more of these with an unsaturated nitrile compound, and if necessary, stabilizers, A lubricant, an antistatic agent, an ultraviolet inhibitor, and a coloring pigment may be added.

本発明に用いられるポリオレフィンは、ポリエチレン、
ポリプロピレン、エチレン−プロピレン共重合体、及び
、これらの混合物に、ファイバーガラス、カーボン繊維
などの繊維補強材を10〜40%の割合でブレンドし、
成形収縮率を0.2〜0.5%にしたものが好ましく、
必要に応じて安定剤、滑剤、帯電防止剤、紫外線防止剤
、着色顔料を添加しても構わない。
The polyolefin used in the present invention includes polyethylene,
A fiber reinforcing material such as fiber glass or carbon fiber is blended into polypropylene, ethylene-propylene copolymer, or a mixture thereof at a ratio of 10 to 40%,
It is preferable that the molding shrinkage rate is 0.2 to 0.5%,
If necessary, stabilizers, lubricants, antistatic agents, ultraviolet inhibitors, and coloring pigments may be added.

本発明に用いられる接着層は、例えばブタジェンあるい
はイソプレンとスチレンのブロック共重合体が好ましい
The adhesive layer used in the present invention is preferably, for example, butadiene or a block copolymer of isoprene and styrene.

〔実施例〕〔Example〕

以下、実施例により本発明を説明する。 The present invention will be explained below with reference to Examples.

〔実施例1] 高アクリロニトリル樹脂”バレックス101ON”  
(商品名、三井東圧化学■製)と高密度ポリエチレン″
FF−1004” (商品名、LNPCORP、、製)
に20%のファイバーグラスブレンド)をブレンドした
樹脂とを、接着性樹脂としてブタジェン−スチレン共重
合体”タフプレン200” (商品名、旭化成工業■製
)を用い、ベクム高速吹込成形機BA−2を用い、外層
が繊維強化ポリオレフィン、中間層が接着性樹脂、内層
カ高アクリロニトリル樹脂となるように多層パリソンを
共押し出しし、これをブロー成形して、多層容器を得た
[Example 1] High acrylonitrile resin “Valex 101ON”
(Product name, manufactured by Mitsui Toatsu Chemicals) and high-density polyethylene
FF-1004” (Product name, manufactured by LNPCORP)
Using a butadiene-styrene copolymer "Tuffprene 200" (trade name, manufactured by Asahi Kasei Corporation) as an adhesive resin, a Bekum high-speed blow molding machine BA-2 was used. A multilayer parison was coextruded so that the outer layer was a fiber-reinforced polyolefin, the middle layer was an adhesive resin, and the inner layer was a high-power acrylonitrile resin, and this was blow molded to obtain a multilayer container.

なお、多層パリソンの共押し出しは、高アクリロニトリ
ル樹脂、接着性樹脂用には、それぞれ口径25mmの押
出機を用い、繊維強化ポリオレフィン用には口径50m
mの押出機を用い、3Nグイヘツドを用いて行った。 
押出湯度は、高アクリロニトリル樹脂がスクリュー・フ
ィードゾーンより170〜210°C1せん断発熱によ
る温度の上昇を防ぐためブロアーを使用、接着性樹脂が
スクリュー・フィードゾーンより155〜200 ’C
For co-extrusion of the multilayer parison, extruders with a diameter of 25 mm are used for high acrylonitrile resin and adhesive resin, and extruders with a diameter of 50 mm are used for fiber-reinforced polyolefin.
The experiment was carried out using a 3N hard head and a 3N extruder.
The extrusion temperature is 170-210'C higher than the screw/feed zone for high acrylonitrile resin.A blower is used to prevent temperature rise due to shear heat generation, and 155-200'C higher than the screw/feed zone for adhesive resin.
.

繊維強化ポリオエフインが170〜220°C、グイヘ
ッドが210〜220°Cであった。 金型温度は16
’C1冷却時間12秒、吹き込み圧力8kg/cI12
で成形を行った。
The temperature was 170-220°C for the fiber-reinforced polyolefin, and 210-220°C for the Gui head. The mold temperature is 16
'C1 cooling time 12 seconds, blowing pressure 8kg/cI12
The molding was done with.

得られた容器の形状は、胴径70mm、高さ185mm
、容器口内径19mm、容量500m1の円筒状容器で
あり、胴部の各層の肉厚は、外層が540μ、中間層が
125μ、内層が170μであった。
The shape of the obtained container was 70 mm in diameter and 185 mm in height.
It was a cylindrical container with an inner diameter of 19 mm and a capacity of 500 m1, and the thickness of each layer of the body was 540 μm for the outer layer, 125 μm for the middle layer, and 170 μm for the inner layer.

上記により得た多層容器の胴部を円周方向の形状を測定
し直径が最大を示す部分の寸法と最小を示す寸法との差
を求めた。
The circumferential shape of the body of the multilayer container obtained above was measured, and the difference between the maximum diameter and the minimum diameter was determined.

その結果を第1表に示す。The results are shown in Table 1.

[実施例2) 高アクリロニトリル樹脂”バレックス101ON” (
商品名、三井東圧化学■製)と高密度ポリエチレン’ 
RPE−7210″ (商品名、Ferro  C0R
P、、製)に10%のファイバーグラスブレンド)をブ
レンドした樹脂とを、接着性樹脂としてブタジェン−ス
チレン共重合体゛クフブレン200″ (商品名、旭化
成工業■製)を用い、ベクム高速吹込成形機BA−2を
用い、外層が繊維強化ポリオレフィン、中間層が接着性
樹脂、内層が高アクリロニトリル樹脂の多層パリソンを
共押し出しし、これをブロー成形して、多層容器を得た
[Example 2] High acrylonitrile resin “Valex 101ON” (
Product name: Mitsui Toatsu Chemical Co., Ltd.) and high-density polyethylene'
RPE-7210″ (Product name, Ferro C0R
Using a butadiene-styrene copolymer ``Kufubrene 200'' (trade name, manufactured by Asahi Kasei Corporation) as an adhesive resin, a resin blended with 10% fiberglass blend) (manufactured by P. Using machine BA-2, a multilayer parison having an outer layer of fiber-reinforced polyolefin, an intermediate layer of adhesive resin, and an inner layer of high acrylonitrile resin was coextruded, and this was blow molded to obtain a multilayer container.

なお、多層パリソンの共押し出しは、高アクリロニトリ
ル樹脂、接着性樹脂用には、それぞれ口径25mmの押
出機を用い、繊維強化ポリオレフィン用には口径50m
mの押出機を用い、3層グイヘッドを用いて行った。 
押出温度は、高アクリロニトリル樹脂がスクリュー・フ
ィードゾーンより170〜210°C1せん断発熱によ
る温度の上昇を防ぐためブロアーを使用、接着性樹脂が
スクリュー・フィードゾーンより155〜200°C1
繊維強化ポリオエフインが170〜220°C、グイヘ
ッドが210〜220°Cであった。 金型温度は16
℃、冷却時間12秒、吹き込み圧力8kg/C鵬3で成
形を行った。
For co-extrusion of the multilayer parison, extruders with a diameter of 25 mm are used for high acrylonitrile resin and adhesive resin, and extruders with a diameter of 50 mm are used for fiber-reinforced polyolefin.
The experiment was carried out using a 3-layer Gouy head using a 3-layer extruder.
The extrusion temperature is 170-210°C higher than the screw/feed zone for high acrylonitrile resin, 155-200°C higher than the screw/feed zone for adhesive resin using a blower to prevent temperature rise due to shear heat generation.
The temperature was 170-220°C for the fiber-reinforced polyolefin, and 210-220°C for the Gui head. The mold temperature is 16
℃, cooling time 12 seconds, and blowing pressure 8 kg/C Peng 3.

得られた容器の形状は、胴径85mm、高さ227mm
、容器口内径18mm、容量10100Oの円筒状容器
であり、胴部の各層の肉厚は、外層が800μ、中間層
が125μ、内層が300μであった。
The shape of the obtained container was 85 mm in diameter and 227 mm in height.
It was a cylindrical container with an inner diameter of 18 mm and a capacity of 10,100 O, and the thickness of each layer of the body was 800 μm for the outer layer, 125 μm for the middle layer, and 300 μm for the inner layer.

得られた多層容器について実施例1と同様の測定を行っ
た。
The same measurements as in Example 1 were performed on the obtained multilayer container.

その結果も第1表に合わせて示す。The results are also shown in Table 1.

[比較例1] 高アクリロニトリル樹脂゛バレックス101ON°° 
(商品名、三井東圧化学■製)と高密度ポリエチレン”
ハイゼックス6200B” (商品名、三片石油化学■
製)とを、接着性樹脂としてブタジェン−スチレン共重
合体”タフブレン200’“(商品名、旭化成工業■製
)を用い、ベクム高速吹込成形機BA−2により、外層
がポリオレフィン、中間層が接着性樹脂、内層が高アク
リロニトリル樹脂からなる多層パリソンを共押し出しし
、これをブロー成形して、多層容器を得た。
[Comparative Example 1] High acrylonitrile resin “Valex 101ON°°”
(Product name, manufactured by Mitsui Toatsu Chemical ■) and high-density polyethylene”
HIZEX 6200B” (Product name, Mikata Petrochemical ■
Using a butadiene-styrene copolymer "Toughblane 200'" (trade name, manufactured by Asahi Kasei Corporation) as an adhesive resin, the outer layer is polyolefin and the middle layer is bonded using a Bekum high-speed blow molding machine BA-2. A multilayer parison whose inner layer was made of a high acrylonitrile resin and a high acrylonitrile resin was coextruded and blow molded to obtain a multilayer container.

なお、多層パリソンの共押し出しは、高アクリロニトリ
ル樹脂、接着性樹脂用には、それぞれ口径25 m m
の押出機を用い、ポリオレフィン用には口径50mmの
押出機を用い、当社製3層グイヘッドで行った。 押出
温度は、高アクリロニトリル樹脂がスクリュー・フィー
ドゾーンより170〜210°C2せん断発熱による温
度の上昇を防ぐためブロアーを使用、接着性樹脂がスク
リュー・フィードゾーンより155〜200°C、ポリ
オエフインが170〜220°C、グイヘッドが210
〜220°Cであった。
In addition, for coextrusion of multilayer parisons, high acrylonitrile resin and adhesive resin have a diameter of 25 mm, respectively.
For polyolefins, an extruder with a diameter of 50 mm was used, and a three-layer Gouy head made by our company was used. The extrusion temperature is 170-210°C above the screw/feed zone for high-acrylonitrile resin.2 A blower is used to prevent temperature rise due to shear heat generation, adhesive resin is 155-200°C above the screw/feed zone, and 170-210°C for polyolefin. 220°C, Gui head is 210
The temperature was ~220°C.

金型温度は16°C2冷却時間12秒、吹き込み圧力8
 kg/c−で成形を行った。
Mold temperature was 16°C, cooling time was 12 seconds, and blowing pressure was 8
Molding was carried out at kg/c-.

以上から得られた多層容器は容器形状は実施例1と同様
、胴部の各層の肉厚は、外層が540μ、中間層が12
5μ、内層が170μであった。
The multilayer container obtained above has the same container shape as Example 1, and the thickness of each layer of the body is 540 μm for the outer layer and 12 μm for the middle layer.
The inner layer was 170μ.

得られた多層容器について実施例1と同様の試験を行っ
た。
The same test as in Example 1 was conducted on the obtained multilayer container.

その結果も第1表に合わせて示す。The results are also shown in Table 1.

[比較例21 高アクリロニトリル樹脂”バレックス101ON” (
商品名、三井東圧化学■製)と高密度ポリエチレン′°
ハイゼックス6200B”  (商品名、三井石油化学
■製)とを、接着性樹脂としてブタジェン−スチレン共
重合体°゛タフブレン200”(商品名、旭化成工業■
製)を用い、ベクム高速吹込成形IBA−2により、外
層がポリオレフィン、中間層が接着性樹脂、内層が高ア
クリロニトリル樹脂からなる多層パリソンを共押し出し
し、これをブロー成形して、多層容器を得た。
[Comparative Example 21 High acrylonitrile resin “Valex 101ON” (
Product name: Mitsui Toatsu Chemical ■) and high-density polyethylene
Hyzex 6200B" (trade name, manufactured by Mitsui Petrochemical Corporation) and butadiene-styrene copolymer "Toughblen 200" (trade name, Asahi Kasei Corporation) as an adhesive resin.
A multilayer parison consisting of an outer layer of polyolefin, an intermediate layer of adhesive resin, and an inner layer of high acrylonitrile resin was coextruded using Bekum high-speed blow molding IBA-2, and this was blow molded to obtain a multilayer container. Ta.

なお、多層パリソンの共押し出しは、高アクリロニトリ
ル樹脂、接着性樹脂用には、それぞれ口径25mmの押
出機を用い、ポリオレフィン用には口径50mmの押出
機を用い、当社製3層グイヘッドで行った。 押出温度
は、高アクリロニトリル樹脂がスクリュー・フィードゾ
ーンより170〜210℃、せん断発熱による温度の上
昇を防ぐためブロアーを使用、接着性樹脂がスクリュー
・フィードゾーンより155〜200 ’C、ポリオエ
フインが170〜220°C、グイヘッドが21θ〜2
20°Cであった。
The multilayer parison was coextruded using a 3-layer Gouy head made by our company, using an extruder with a diameter of 25 mm for high acrylonitrile resin and adhesive resin, and an extruder with a diameter of 50 mm for polyolefin. The extrusion temperature is 170-210'C above the screw feed zone for high acrylonitrile resin, a blower is used to prevent temperature rise due to shear heat generation, 155-200'C above the screw feed zone for adhesive resin, and 170-210'C for polyolefin. 220°C, Gui head is 21θ~2
It was 20°C.

金型温度は16°C1冷却時間12秒、吹き込み圧力8
 kg/Cmで成形を行った。
Mold temperature: 16°C, cooling time: 12 seconds, blowing pressure: 8
Molding was performed at kg/cm.

得られた容器の形状は、胴径85mm、高さ227mm
、容器口内径18mm、容量10100Oの円筒状容器
であり、胴部の各層の肉厚は、外層が800μ、中間層
が125μ、内層が300μであった。
The shape of the obtained container was 85 mm in diameter and 227 mm in height.
It was a cylindrical container with an inner diameter of 18 mm and a capacity of 10,100 O, and the thickness of each layer of the body was 800 μm for the outer layer, 125 μm for the middle layer, and 300 μm for the inner layer.

得られた多層容器について実施例1と同様の測定を行っ
た。
The same measurements as in Example 1 were performed on the obtained multilayer container.

その結果も第1表に合わせて示す。The results are also shown in Table 1.

第1表 寸法測定結果 〔発明の効果〕 本発明の多層容器は、第1表にみられるように従来の高
ニトリル樹脂をポリオレフィン系樹脂との多層容器にし
たものに比べ、容器胴部での円周方向の直径が最大を示
す部分の寸法と最小を示す寸法との差が小さい、金型の
キャビティは真円になっていることから考えると、容器
の円周方向に対する変形がほとんどないといえ、橿めて
優れた形状を保った多層容器である。
Table 1: Dimensional measurement results [Effects of the invention] As shown in Table 1, the multilayer container of the present invention has a smaller diameter at the container body than the conventional multilayer container made of high nitrile resin and polyolefin resin. Considering that the mold cavity is a perfect circle with a small difference between the maximum circumferential diameter and the minimum circumferential diameter, it is assumed that there is almost no deformation of the container in the circumferential direction. No, it's a multi-layered container that maintains an excellent shape.

Claims (2)

【特許請求の範囲】[Claims] (1)高ニトリル樹脂層の片側、あるいは両側に繊維補
強材をブレンドしたポリオレフィン系樹脂層を積層接合
したことを特徴とする多層容器。
(1) A multilayer container characterized by laminating and bonding a polyolefin resin layer blended with a fiber reinforcing material on one or both sides of a high nitrile resin layer.
(2)請求項(1)の前記高ニトリル層と前記ポリオレ
フィン系樹脂層の間に成形収縮率が0.3%の接着層を
積層接合したことを特徴とした多層容器。
(2) A multilayer container characterized in that an adhesive layer having a mold shrinkage rate of 0.3% is laminated and bonded between the high nitrile layer and the polyolefin resin layer according to claim (1).
JP7143289A 1989-03-23 1989-03-23 Multilayer container Expired - Fee Related JP2697101B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7143289A JP2697101B2 (en) 1989-03-23 1989-03-23 Multilayer container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7143289A JP2697101B2 (en) 1989-03-23 1989-03-23 Multilayer container

Publications (2)

Publication Number Publication Date
JPH02249644A true JPH02249644A (en) 1990-10-05
JP2697101B2 JP2697101B2 (en) 1998-01-14

Family

ID=13460361

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7143289A Expired - Fee Related JP2697101B2 (en) 1989-03-23 1989-03-23 Multilayer container

Country Status (1)

Country Link
JP (1) JP2697101B2 (en)

Also Published As

Publication number Publication date
JP2697101B2 (en) 1998-01-14

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