JPS60125627A - Blow-molded container - Google Patents
Blow-molded containerInfo
- Publication number
- JPS60125627A JPS60125627A JP58233502A JP23350283A JPS60125627A JP S60125627 A JPS60125627 A JP S60125627A JP 58233502 A JP58233502 A JP 58233502A JP 23350283 A JP23350283 A JP 23350283A JP S60125627 A JPS60125627 A JP S60125627A
- Authority
- JP
- Japan
- Prior art keywords
- blow
- propylene
- olefin
- agent
- transparency
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/0005—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor characterised by the material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/08—Biaxial stretching during blow-moulding
- B29C49/16—Biaxial stretching during blow-moulding using pressure difference for pre-stretching, e.g. pre-blowing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/18—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor using several blowing steps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/42—Component parts, details or accessories; Auxiliary operations
- B29C49/64—Heating or cooling preforms, parisons or blown articles
- B29C49/6472—Heating or cooling preforms, parisons or blown articles in several stages
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/42—Component parts, details or accessories; Auxiliary operations
- B29C49/78—Measuring, controlling or regulating
- B29C2049/7879—Stretching, e.g. stretch rod
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/08—Biaxial stretching during blow-moulding
- B29C49/087—Means for providing controlled or limited stretch ratio
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/10—Polymers of propylene
- B29K2023/12—PP, i.e. polypropylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/0094—Condition, form or state of moulded material or of the material to be shaped having particular viscosity
Abstract
Description
【発明の詳細な説明】 リプロピレン樹脂製ブロー成形容器に関する。[Detailed description of the invention] This invention relates to a blow-molded container made of polypropylene resin.
ポリプロピレン樹脂は耐熱性、耐薬品性、安全衛生面に
優れ、そのブロー成形品は剛性、衝撃強度にも優れるた
め、食品容器、洗剤容器、医療容器等に広く使用されて
いる。しかしながら、ブロー成形品は透明性が不十分で
あるため、市場からの透明性要求に十分に応えていない
のが実情である。Polypropylene resin has excellent heat resistance, chemical resistance, and safety and hygiene, and its blow-molded products also have excellent rigidity and impact strength, so it is widely used in food containers, detergent containers, medical containers, etc. However, since blow molded products have insufficient transparency, the reality is that they do not fully meet market demands for transparency.
従来、ポリプロピレン樹脂の透明性改良方法として、造
核剤を添加する方法、プロピレンにα一オレフインを共
重合させる方法等が知られているが、通常のブロー成形
法にあってはこれらの対策を行なっても十分な透明性を
得ることが困難である。Conventionally, known methods for improving the transparency of polypropylene resin include adding a nucleating agent and copolymerizing α-olefin with propylene, but these measures cannot be taken in normal blow molding. Even if it is done, it is difficult to obtain sufficient transparency.
また、従来から行なわれているブロー成形では、通常、
この為に用いるポリプロピレン樹脂は、剛性、透明性等
が良好であるので、そのメルトフローインデノクス(M
FI)が高々4S’/10分程度のものであり、特に1
〜2fI710分程度のものが多用されている。In addition, in conventional blow molding,
The polypropylene resin used for this purpose has good rigidity and transparency, so its melt flow indenox (M
FI) is at most 4S'/10 minutes, especially 1
~2fI of about 710 minutes is often used.
一方、近年、射出延伸ブロー成形法が開発され、これに
よるブロー成形品も試作されているが、十分な透明性上
偏肉のないポリプロピレン樹脂製ブロー成形容器は得ら
れていないのが実状である。On the other hand, in recent years, an injection stretch blow molding method has been developed, and blow molded products using this method have also been prototyped, but the reality is that a polypropylene resin blow molded container with sufficient transparency and no uneven thickness has not been obtained. .
本発明者らは、射出延伸ブロー成形法で透明性に優れ、
かつ、偏肉性のないポリプロピレン11 服装ブロー成
形容器を得ることを検討した結果、特定のMFIを有す
るプロピレン−α−オレフィン共重合体をポリプロピレ
ン樹脂として用いたならば、良好なブロー成形容器を得
ることができることを見出し、遂に本発明に到達した。The present inventors have achieved excellent transparency using the injection stretch blow molding method,
Polypropylene 11 also has no uneven thickness.As a result of studying to obtain a blow-molded container for clothing, it was found that if a propylene-α-olefin copolymer having a specific MFI is used as the polypropylene resin, a good blow-molded container can be obtained. We have finally arrived at the present invention.
即ち、本発明は、プロピレンとα−オレフィンのランダ
ム共重合体を射出延伸ブロー成形したポリプロピレン製
容器であって、該プロピレン−α−オレフィンランダム
共重合体がメルトフローインテックス4〜soy/io
分のものであることを慣徴とする透明性が改良され、偏
肉のないポリプロピレン樹脂製ブロー成形容器である。That is, the present invention is a polypropylene container made by injection stretch blow molding a random copolymer of propylene and α-olefin, wherein the propylene-α-olefin random copolymer is melt flow intex 4 to soy/io.
This is a polypropylene resin blow molded container with improved transparency and no uneven thickness.
本発明に用いるプロピレン−α−オレフィンランダム共
重合体とは、プロピレンを主とするエチレン、1−ブテ
ン、1−ペンテン、1−ヘキセン等のα−オレフィンと
のランダム共重合体であり、そのJIS K−7210
の条件14で測定したMFIが4〜50f710分であ
ることが望丑しい。また、透明性が良好になることから
エチレンとの共重合体が特に望ましい。更に、ポリグロ
ピレンホモボリマ−では偏肉が著しく、成形性が不良で
ある。The propylene-α-olefin random copolymer used in the present invention is a random copolymer mainly composed of propylene with α-olefins such as ethylene, 1-butene, 1-pentene, and 1-hexene, and its JIS K-7210
It is desirable that the MFI measured under condition 14 is 4 to 50 f710 minutes. Furthermore, a copolymer with ethylene is particularly desirable because it provides good transparency. Furthermore, polyglopylene homopolymer has significant thickness deviation and poor moldability.
プロピレン−α−オレフィンランダム共M合体のMFI
が4f/1[]分未満では十分な透明性が得られない。MFI of propylene-α-olefin random co-M composite
If it is less than 4f/1[] minutes, sufficient transparency cannot be obtained.
捷だ、MFIがsoy、、’1o分を越えると偏肉が著
しくなるため安定して良好な容器を得ることができない
。However, if the MFI exceeds 10, it is impossible to stably obtain a good container because the unevenness of thickness becomes significant.
本発明においては、透明性が更に良好になるので造核剤
を添加しておくことができる。その場合にはプロピレン
−α−オレフィンランダム共重合体に対し1M量係以下
か適当である。In the present invention, a nucleating agent can be added because the transparency is further improved. In that case, it is appropriate that the amount is 1M or less relative to the propylene-α-olefin random copolymer.
更に、酸化防止剤5.紫外線吸収剤1.帯電防止剤、滑
剤、着色剤などの添加剤や、他の厨脂やエラストマーが
添加配合されたものであってもよい。Furthermore, antioxidant5. Ultraviolet absorber 1. Additives such as antistatic agents, lubricants, and colorants, as well as other cooking fats and elastomers may be added and blended.
本発明の成形法である射出延伸ブロー成形法とは、有底
パリソンを射出成形によって成形し、次いで予備ブロー
、延伸温度調整後、延伸ブローすることによって製品を
得る成形法であり延伸の方法としてはロッドによる機械
的なたて延伸とエアー吹込による方法の組合せが行なわ
れる。この成形法に適した成形機としては、例えば日精
ASB機械株式会社製、射出延伸ブロー成形機: AS
B−50。The injection stretch blow molding method, which is the molding method of the present invention, is a molding method in which a bottomed parison is molded by injection molding, and then a product is obtained by pre-blowing, stretching temperature adjustment, and stretch blowing. A combination of mechanical vertical stretching using a rod and air blowing is performed. As a molding machine suitable for this molding method, for example, injection stretch blow molding machine manufactured by Nissei ASB Machinery Co., Ltd.: AS
B-50.
ASB−150、ASB−250、ASB−650等が
あげられる。Examples include ASB-150, ASB-250, and ASB-650.
本発明において、特に優れた透明性を得るには、例えば
成形機として射出延伸ブロー成形機ASB−50を用い
た場合、下記の条件が望ましい。In the present invention, in order to obtain particularly excellent transparency, the following conditions are desirable when, for example, an injection stretch blow molding machine ASB-50 is used as the molding machine.
射出成形温度:200〜260℃
予備ブロー延伸倍率:縦10〜1.8倍、横12〜20
倍
予備ブローエア圧力=3〜7 K9/ 7延伸温度調整
金形温度=90〜140℃延伸ブロー延伸倍率:縦12
〜65倍、横1.2〜60倍
延伸プローエア圧力ニ4〜20Ky/cηツ本発明のポ
リプロピレン製ブロー容器は、ポリプロピレンに安定剤
、帯電防止剤、紫外線吸収剤、着色剤1.造核助剤等の
添加剤を添加したのち、通常、上記射出延伸ブローによ
りその胴部肉厚が02〜10闘に製造される。捷だ1、
きわめて透明性に優れ、乃・つ耐熱性、#r4衝撃性等
にも優れるので、その性質を利用して食器容器、洗剤容
器、ンヤングー容器、トイレタリー容器、医療容器等に
好適に使用できる。Injection molding temperature: 200-260℃ Pre-blow stretching ratio: 10-1.8 times vertically, 12-20 times horizontally
Double preliminary blow air pressure = 3~7 K9/7 Stretching temperature adjustment mold temperature = 90~140℃ Stretching blow Stretching ratio: Longitudinal 12
- 65 times, width 1.2 - 60 times stretching blow air pressure 4 - 20 Ky/cη The polypropylene blow container of the present invention contains polypropylene with a stabilizer, an antistatic agent, an ultraviolet absorber, and a coloring agent. After adding additives such as a nucleating aid, the body is usually manufactured to a thickness of 0.2 to 10 mm by the above-mentioned injection stretch blowing. Sword 1,
It has excellent transparency, heat resistance, and #r4 impact resistance, so it can be suitably used for tableware containers, detergent containers, baby food containers, toiletry containers, medical containers, etc. by utilizing these properties.
以下、実施例により本発明の詳細な説明する。Hereinafter, the present invention will be explained in detail with reference to Examples.
なお、胴部霞度は日本重色社製のヘイズメ=り=を用い
、JIS K−6714に記載された方法に従って測定
したものである。Incidentally, the body haze was measured using a haze meter manufactured by Nihon Juishoku Co., Ltd. according to the method described in JIS K-6714.
実施例1
ポリプロピレン柄脂としてエチレン含有量4重量%、M
FI 15グ/10分であり、かつ造核を
助剤03重量係含むプロピレン−エチレンランダム共重
合体を、射出延伸プロー成形機ASB−釘を用い、下記
条件で成形して、胴部直径70mm、内容量500蛯の
丸型ボトルを成形した。Example 1 Ethylene content 4% by weight as polypropylene pattern fat, M
A propylene-ethylene random copolymer having an FI of 15 g/10 minutes and containing a nucleation aid of 0.3 weight percent was molded using an injection stretch blow molding machine ASB-Nail under the following conditions to obtain a body diameter of 70 mm. A round bottle with a content of 500 lbs was molded.
射出成形温度=220℃
射出成形金型温度:15℃
予備ブロー延伸倍率:縦1倍、$14倍予備ブローエア
圧力=51<+ン/ crl延伸温度調整金型淵度:1
00℃
延伸ブロー延伸倍率:縦18倍、横12倍延伸フローエ
ア圧力=91(り/ Cf1t′得られたホトルはその
重量が247であり、透明性の極めて優れたポリプロピ
レン製ブロー成形容器であった。捷だ1.胴部の肉厚は
0.58 mmで、霞度は31%であり、内容液を入れ
たときの透明性も良好であった。Injection molding temperature = 220°C Injection molding mold temperature: 15°C Pre-blow stretching ratio: 1x length, $14x Pre-blow air pressure = 51<+n/crl Stretching temperature adjustment mold depth: 1
00°C Stretch blow Stretch ratio: 18 times vertical, 12 times horizontal Stretch Flow air pressure = 91 (ri/Cf1t') The weight of the obtained hotlet was 247, and it was a polypropylene blow-molded container with extremely excellent transparency. 1. The wall thickness of the body was 0.58 mm, the degree of haze was 31%, and the transparency when the liquid was added was also good.
実施例2〜4、比較例1〜3
実施例1において、ポリプロピレン樹脂として表1に示
すエチレン含量及びM F Iであるプロピレン−α−
オレフィン共重合体を用いる他は実施例1と同様にして
、元型ボトルを成形した。Examples 2 to 4, Comparative Examples 1 to 3 In Example 1, propylene-α- having the ethylene content and M F I shown in Table 1 was used as the polypropylene resin.
A master bottle was molded in the same manner as in Example 1 except that an olefin copolymer was used.
得られたボトルの性能を表1に示す。Table 1 shows the performance of the obtained bottle.
表1
参考例1
比較例1において用いたプロピレン−エチレンランダム
共重合体を用い、押出延伸ブロー成形法により得られた
実施例1と同様のボトルでは胴部肉厚(058mm )
は均一であるが薄白く霞みがががり透明性に不十分でそ
の霞度は60%であった。Table 1 Reference Example 1 A bottle similar to Example 1 obtained by extrusion stretch blow molding using the propylene-ethylene random copolymer used in Comparative Example 1 had a body wall thickness (058 mm).
Although it was uniform, it was pale white and hazy, and its transparency was insufficient, with a haze level of 60%.
尚、押出延伸ブロー成形法とは押出成形されたパイプを
一定の長さに切断してパリソンを得、これを延伸温度捷
で再加熱した後、延伸ブローすることによって製品を得
る成形法をいう。The extrusion stretch blow molding method is a molding method in which an extrusion-molded pipe is cut into a certain length to obtain a parison, which is then reheated in a stretching temperature chamber and then stretch-blown to obtain a product. .
特許出願人 三井東圧化学株式会社patent applicant Mitsui Toatsu Chemical Co., Ltd.
Claims (1)
出延伸ブロー成形したポリプロピレン樹脂製ブロー成形
容器であって、該プロピレン−α−オレフィンランダム
共重合体がメルルトフローインデノクス4〜50ft’
710分のものであることを特徴とする透明性が改良さ
れ、偏肉のないポリプロピレン樹脂製ブロー成形容器。 2α−オレフィンがエチレンである特許請求の範囲第1
項記載のポリプロピレン樹脂製ブロー成形容器。[Scope of Claims] A blow-molded container made of a polypropylene resin made by injection stretch blow-molding a random copolymer of 1 propylene and an α-olefin, the propylene-α-olefin random copolymer being Meltflow Indenox 4. ~50ft'
A blow-molded container made of polypropylene resin with improved transparency and no uneven thickness, characterized in that it has a thickness of 710 minutes. Claim 1 in which the 2α-olefin is ethylene
A blow-molded polypropylene resin container as described in Section 1.
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58233502A JPS60125627A (en) | 1983-12-13 | 1983-12-13 | Blow-molded container |
DE3486446T DE3486446T2 (en) | 1983-12-13 | 1984-12-10 | Injection blow molding |
EP87110734A EP0251340B1 (en) | 1983-12-13 | 1984-12-10 | Injection stretch-blow molding process |
EP84115106A EP0151741A3 (en) | 1983-12-13 | 1984-12-10 | Injection stretch-blow molded container and resin composition therefor |
CA000469959A CA1240446A (en) | 1983-12-13 | 1984-12-12 | Injection stretch-blow molded container and resin composition therefor |
AU36543/84A AU554076B2 (en) | 1983-12-13 | 1984-12-12 | Ethylene-propylene copolymer compositions and containers |
KR1019840007922A KR860001736B1 (en) | 1983-12-13 | 1984-12-13 | Injection stretch-blow molded container and resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58233502A JPS60125627A (en) | 1983-12-13 | 1983-12-13 | Blow-molded container |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60125627A true JPS60125627A (en) | 1985-07-04 |
Family
ID=16956026
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58233502A Pending JPS60125627A (en) | 1983-12-13 | 1983-12-13 | Blow-molded container |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60125627A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100436217B1 (en) * | 2002-02-25 | 2004-06-16 | 우진기업(주) | Manufacturing method of polypropylene bottle for sterilize |
WO2005074428A3 (en) * | 2004-01-23 | 2005-12-22 | Milliken & Co | Process of making two-stage injection stretch blow molded polypropylene articles |
WO2006116510A1 (en) * | 2005-04-26 | 2006-11-02 | Milliken & Company | Articles and process of making polypropylene articles |
EP1947143A1 (en) * | 2007-01-19 | 2008-07-23 | Borealis Technology Oy | Polypropylene-based resin composition and molded article thereof |
EP2479013A1 (en) | 2011-01-19 | 2012-07-25 | Linear Overmoulding Applications, SL | Preform for forming containers with light barrier effect by stretch blow molding |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5941344A (en) * | 1982-08-31 | 1984-03-07 | Mitsui Petrochem Ind Ltd | Biaxially drawn blow-molded article |
-
1983
- 1983-12-13 JP JP58233502A patent/JPS60125627A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5941344A (en) * | 1982-08-31 | 1984-03-07 | Mitsui Petrochem Ind Ltd | Biaxially drawn blow-molded article |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100436217B1 (en) * | 2002-02-25 | 2004-06-16 | 우진기업(주) | Manufacturing method of polypropylene bottle for sterilize |
WO2005074428A3 (en) * | 2004-01-23 | 2005-12-22 | Milliken & Co | Process of making two-stage injection stretch blow molded polypropylene articles |
EP1722957A2 (en) * | 2004-01-23 | 2006-11-22 | Milliken & Company | Process of making two-stage injection stretch blow molded polypropylene articles |
EP1722957A4 (en) * | 2004-01-23 | 2007-09-19 | Milliken & Co | Process of making two-stage injection stretch blow molded polypropylene articles |
WO2006116510A1 (en) * | 2005-04-26 | 2006-11-02 | Milliken & Company | Articles and process of making polypropylene articles |
EP1947143A1 (en) * | 2007-01-19 | 2008-07-23 | Borealis Technology Oy | Polypropylene-based resin composition and molded article thereof |
EP2479013A1 (en) | 2011-01-19 | 2012-07-25 | Linear Overmoulding Applications, SL | Preform for forming containers with light barrier effect by stretch blow molding |
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