JPS60125631A - Medical vessel - Google Patents

Medical vessel

Info

Publication number
JPS60125631A
JPS60125631A JP58233510A JP23351083A JPS60125631A JP S60125631 A JPS60125631 A JP S60125631A JP 58233510 A JP58233510 A JP 58233510A JP 23351083 A JP23351083 A JP 23351083A JP S60125631 A JPS60125631 A JP S60125631A
Authority
JP
Japan
Prior art keywords
propylene
random copolymer
transparency
blow molding
stretch blow
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
JP58233510A
Other languages
Japanese (ja)
Other versions
JPH0419925B2 (en
Inventor
Toru Ueki
徹 植木
Hideo Amamiya
英夫 雨宮
Toyoaki Hata
畑 豊明
Takashi Miyazaki
宮崎 孝志
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP58233510A priority Critical patent/JPS60125631A/en
Priority to EP87110734A priority patent/EP0251340B1/en
Priority to EP84115106A priority patent/EP0151741A3/en
Priority to DE3486446T priority patent/DE3486446T2/en
Priority to AU36543/84A priority patent/AU554076B2/en
Priority to CA000469959A priority patent/CA1240446A/en
Publication of JPS60125631A publication Critical patent/JPS60125631A/en
Publication of JPH0419925B2 publication Critical patent/JPH0419925B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/08Biaxial stretching during blow-moulding
    • B29C49/16Biaxial stretching during blow-moulding using pressure difference for pre-stretching, e.g. pre-blowing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/0005Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor characterised by the material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/18Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor using several blowing steps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/42Component parts, details or accessories; Auxiliary operations
    • B29C49/64Heating or cooling preforms, parisons or blown articles
    • B29C49/6472Heating or cooling preforms, parisons or blown articles in several stages
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/10Homopolymers or copolymers of propene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/42Component parts, details or accessories; Auxiliary operations
    • B29C49/78Measuring, controlling or regulating
    • B29C2049/7879Stretching, e.g. stretch rod
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/07Preforms or parisons characterised by their configuration
    • B29C2949/0715Preforms or parisons characterised by their configuration the preform having one end closed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/02Combined blow-moulding and manufacture of the preform or the parison
    • B29C49/06Injection blow-moulding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/08Biaxial stretching during blow-moulding
    • B29C49/087Means for providing controlled or limited stretch ratio
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING 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
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/10Polymers of propylene
    • B29K2023/12PP, i.e. polypropylene

Landscapes

  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Medical Preparation Storing Or Oral Administration Devices (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Containers Having Bodies Formed In One Piece (AREA)

Abstract

PURPOSE:To improve the transparency and heat resistance of a medical vessel by applying injection stretch blow molding to a propylene-ethylene random copolymer whose melt flow index is 4-20g/10min and to which no nucleation agent is added. CONSTITUTION:A propylene-ethylene random copolymer whose melt flow index is 4-20g/10min and to which no nucleation agent is added is subjected to injection stretch blow molding, and thereby a medical vessel excellent in transparency and heat resistance is obtained. It is desirable that said propylene-ethylene random copolymer contains little ethylene, and in particular, the one containing ethylene of 0.5-8wt%, or more preferably of 1-6wt%, is preferable in terms of transparency and heat resistance. The injection stretch blow molding is executed in such a manner that, after a closed-end parison is molded by injection molding, a process of preliminary blowing and the adjustment of a stretching temperature are executed, and then stretch blowing is conducted.

Description

【発明の詳細な説明】 本発明は透明性、耐熱性に優れたポリプロピレン系補刷
製の医療容器に関する。更に詳しくはリンゲル液、ハル
トマン液等の輸液用に適した容器に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a medical container made of reprinted polypropylene having excellent transparency and heat resistance. More specifically, the present invention relates to a container suitable for infusions such as Ringer's solution and Hartmann's solution.

輸液用プラスチック容器の規格については日本薬局法に
定められているが、中でも透明性については、内容液中
の異物を観察するのにできるだけ高いことが要求されて
いる。ポリプロピレン系樹脂は機械的性質、滅菌時の耐
熱性、安全衛生性に優れた樹脂としてこの輸液用容器と
して使用されているが、透明性の点で不十分であり、押
出成形式2軸延伸ブロー成形等により透明性の改良が行
なわれているが、未だ不十分である。
The standards for plastic containers for infusions are stipulated by the Japanese Pharmacy Law, and in particular, transparency is required to be as high as possible to allow observation of foreign substances in the liquid contents. Polypropylene resin is used for this infusion container because it has excellent mechanical properties, heat resistance during sterilization, and safety and hygiene. Transparency has been improved by molding, etc., but it is still insufficient.

本発明者らはポリプロピレン系樹脂製の輸液容器の透明
性を改良すべく鋭意検討した結果、特定のポリプロピレ
ン系樹脂を使用して、射出延伸ブロー成形を行なうこと
により、透明性の漬れた容器が得られることを見出し、
本発明に到達した。
As a result of intensive studies to improve the transparency of infusion containers made of polypropylene resin, the inventors of the present invention succeeded in creating a transparent container by performing injection stretch blow molding using a specific polypropylene resin. It was found that it was possible to obtain
We have arrived at the present invention.

即ち、本発明は、メルトフローインデックスが4〜20
1i’710分であるプロピレン−エチレンランダム共
重合体を、造核剤を添加することなく、射出延坤ブロー
成形法により成形されたことを特徴とする医療容器であ
る。
That is, the present invention has a melt flow index of 4 to 20.
This medical container is characterized by being molded from a propylene-ethylene random copolymer having a molecular weight of 1i'710 minutes by an injection spread blow molding method without adding a nucleating agent.

本発明において用いるプロピレン−エチレンランダム共
重合体とは日本工業規格JISK−7210の条件14
に従って測定したメルトフローインデックス(以下、M
FIと略す)が4〜20f710分のものである。MF
Iが4171.0分以下では得られる容器の透明性は不
十分であり’1 、20 f/10分を越えると容器の
偏肉が著しくなる。
The propylene-ethylene random copolymer used in the present invention is condition 14 of Japanese Industrial Standard JISK-7210.
Melt flow index (hereinafter referred to as M
(abbreviated as FI) is 4 to 20 f710 minutes. Midfielder
If I is less than 4171.0 minutes, the resulting container will have insufficient transparency, and if it exceeds 20 f/10 minutes, the thickness of the container will be significantly uneven.

又、本発明においてはプロピレン−エチレンランダム共
重合体としてはエチレンが少ないものが望ましく、特に
エチレン含量が05〜8重量%好丑しくは1〜6重量係
置部るものが透明性、耐熱性の上から好適に用いうる。
In addition, in the present invention, the propylene-ethylene random copolymer preferably has a low ethylene content, and in particular, one with an ethylene content of 05 to 8% by weight, preferably 1 to 6% by weight, has good transparency and heat resistance. It can be suitably used from above.

更に造核剤を用いれば、透明性は向上するのであるが、
本用途においては使用する必要はない程に良好な透明性
が得られる。
Furthermore, transparency can be improved by using a nucleating agent, but
In this application, the transparency is so good that it is not necessary to use it.

本発明において用い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、ついで予備ブロー
、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ンドによる機
械的なたて延伸と空気吹込みによる方法の組合せが普通
に行なわれる。
The injection stretch blow molding method used in the present invention is a molding method in which a bottomed parison is molded by injection molding, and then a product is obtained by stretching and blowing after preliminary blowing and stretching temperature adjustment. A combination of mechanical warp stretching and air blowing methods is commonly used.

これに用いる成形機としては日精ASB機械株式会社製
射出延伸ブロー成形機A’5B−50、ASB−150
The molding machines used for this are injection stretch blow molding machines A'5B-50 and ASB-150 manufactured by Nissei ASB Machinery Co., Ltd.
.

ASB−250、ASB−650等をあげることができ
る。
Examples include ASB-250 and ASB-650.

本発明の高透明で偏肉の少ないプロピレン−エチレンラ
ンダム共重合体製の医療容器を成形する条件としては、
例えば射出延伸ブロー成形機ASB−50を用いた場合
、下記条件が望ましい。
Conditions for molding the medical container made of the propylene-ethylene random copolymer of the present invention, which is highly transparent and has less uneven thickness, are as follows:
For example, when using an injection stretch blow molding machine ASB-50, the following conditions are desirable.

射出成形温度:200〜260℃ 予備ブロー :たて延伸倍率10〜18倍横延伸倍率 
12〜20倍 ブロー圧力 3〜6に9/cm 延伸温度調整金型温度=90〜140℃延伸ブロー 二
たて延伸倍率12〜65倍横延伸倍率 12〜60倍 ブロー圧力 4〜20 Kg / cr1本発明の医療
容器は上記ブロピレンーエチレンランダム共重合体(て
、必要に応じ、安定剤等の添加物を極く少量、添加し、
上記射出延伸ブロー成形法により通常胴部の肉厚が02
〜tommになる様に成形されたものである。
Injection molding temperature: 200-260℃ Preliminary blowing: Warp stretch magnification 10-18 times Horizontal stretch magnification
12-20 times blowing pressure 3-6 to 9/cm Stretching temperature adjustment mold temperature = 90-140℃ Stretching blowing Fresh stretching ratio 12-65 times Lateral stretching ratio 12-60 times Blow pressure 4-20 Kg / cr1 The medical container of the present invention is made of the above-mentioned propylene-ethylene random copolymer (and, if necessary, a very small amount of additives such as stabilizers is added,
By the above injection stretch blow molding method, the wall thickness of the body is usually 0.2 mm.
~tomm.

本発明の医療容器は透明性、耐熱性に優れているので高
温滅菌が可能であり、輸液用容器として好適に用いうる
Since the medical container of the present invention has excellent transparency and heat resistance, it can be sterilized at high temperature and can be suitably used as an infusion container.

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 MFIが151i’/10分で、エチレン含有量が4重
置部であるプロピレン−エチレンランダム共重合体を日
清ASB機械(掬製、射出延伸ブロー成形機ASB−5
0にて下記条件で射出延伸ブロー成形を行ない、胴部直
径70闘、容量500 Ccの丸型ボトルを成形した。
Example 1 A propylene-ethylene random copolymer having an MFI of 151 i'/10 minutes and an ethylene content of 4 parts was processed using a Nisshin ASB machine (manufactured by Kiki, injection stretch blow molding machine ASB-5).
Injection stretch blow molding was carried out under the following conditions at 0 Cc to form a round bottle with a body diameter of 70 mm and a capacity of 500 Cc.

射出延伸ブロー成形条件 射出成形温度:220℃ 射出成形金型温度=15℃ 予備ブロー:たで1倍、横14倍 予備ブローエアー圧力ニ5Ky/cJ 延伸温度調節金型温度:100℃ 延伸プロm:たて18倍、横12倍 延伸ブロー圧力=9にり/cng 得られたボトルは重量247で肉厚の均一性が良く、透
明性の優れた容器であシ、特に内容液を入れた時の透視
性は良好で、輸液容器等の医療容器として好適なもので
あった。胴部の肉厚は0.507n7nで、切取った試
験片の霞度を日本重色製のヘーズメーターを用い、JI
S K−6714記載の方法によって測定したところ7
8チであった。
Injection stretch blow molding conditions Injection molding temperature: 220°C Injection mold temperature = 15°C Preliminary blowing: 1x vertically, 14x horizontally Preliminary blowing air pressure 5 Ky/cJ Stretching temperature control mold temperature: 100°C Stretching pro m : Vertical 18 times, horizontal 12 times stretching Blow pressure = 9 cm/cng The resulting bottle weighed 247 cm, had good wall thickness uniformity, and was a container with excellent transparency, especially when containing the liquid. It had good transparency and was suitable for medical containers such as infusion containers. The wall thickness of the body is 0.507n7n, and the haze of the cut test piece was measured using a Nippon Juishiki haze meter.
7 as measured by the method described in SK-6714
It was 8chi.

実施例−2 実施例1において、プロピレン−エチレンランダム共重
合体としてMFIが6f/10分でエチレン含有量が2
重量裂のプロピレン−エチレンランダム共重合体を用い
た他は、実施例−1と同様にして、射出延伸ブロー成形
を行ない、容量500ccの丸型ボトルを成形した。得
られたボトルは重量24fで、肉厚の均一性が良く、透
明性の優れた容器であり、特に内容液を入れた時の透視
性は良好で、輸液容器等の医療容器として好適なもので
あった。胴部の肉厚は0.50 mmで、霞度は92ヂ
であった。
Example 2 In Example 1, the propylene-ethylene random copolymer had an MFI of 6 f/10 min and an ethylene content of 2.
Injection stretch blow molding was carried out in the same manner as in Example 1, except that a heavy propylene-ethylene random copolymer was used, and a round bottle with a capacity of 500 cc was molded. The obtained bottle weighs 24 f, has good wall thickness uniformity, and is a container with excellent transparency.It has particularly good transparency when filled with liquid, and is suitable as a medical container such as an infusion container. Met. The wall thickness of the body was 0.50 mm, and the degree of haze was 92 degrees.

比較例1 実施例1において、プロピレン−エチレンランダム共重
合体としてMFIが2ii’710分で、エチレン含有
量が2重置部であるプロピレン−エチレンランダム共重
合体を用いた他は、実施例1と同様にして、射出延伸ブ
ロー成形を行ない容量500ccの丸型ボトルを得た。
Comparative Example 1 In Example 1, except that a propylene-ethylene random copolymer having an MFI of 2ii'710 minutes and an ethylene content of 2 folds was used as the propylene-ethylene random copolymer. In the same manner as above, injection stretch blow molding was performed to obtain a round bottle with a capacity of 500 cc.

得られたボトルの透明性は不十分で、胴部の肉厚0.4
9 mmであり、霞度は198チであった。
The resulting bottle had insufficient transparency, with a body wall thickness of 0.4
9 mm, and the degree of haze was 198 degrees.

比較例2 11Ti例1において、プロピレン−エチレンランダム
共重合体としてMFIが251710分で、エチレン含
有量が20%であるプロピレン−エチレンランダム共重
合体を用いた他は、実施例1と同様にして、射出延伸ブ
ロー成形を行彦っだが、得られたボトルはたて方向、横
方向いずれの方向でも偏肉が大きく、使用できないもの
であった。
Comparative Example 2 In 11Ti Example 1, a propylene-ethylene random copolymer having an MFI of 251,710 minutes and an ethylene content of 20% was used as the propylene-ethylene random copolymer, but in the same manner as in Example 1. Although injection stretch blow molding was carried out, the resulting bottle had a large uneven thickness in both the vertical and horizontal directions, making it unusable.

特許出願人 三井東圧化学株式会社patent applicant Mitsui Toatsu Chemical Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] メルトフローインデックスが4〜2of/1゜分である
プロピレン−エチレンランダム共重合体を、造核剤を添
加することなく、射出延伸ブロー成形法により成形され
たことを特徴とする医療容器
A medical container characterized by being molded by injection stretch blow molding of a propylene-ethylene random copolymer having a melt flow index of 4 to 2 of/1° without adding a nucleating agent.
JP58233510A 1983-12-13 1983-12-13 Medical vessel Granted JPS60125631A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP58233510A JPS60125631A (en) 1983-12-13 1983-12-13 Medical vessel
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
DE3486446T DE3486446T2 (en) 1983-12-13 1984-12-10 Injection blow molding
AU36543/84A AU554076B2 (en) 1983-12-13 1984-12-12 Ethylene-propylene copolymer compositions and containers
CA000469959A CA1240446A (en) 1983-12-13 1984-12-12 Injection stretch-blow molded container and resin composition therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58233510A JPS60125631A (en) 1983-12-13 1983-12-13 Medical vessel

Publications (2)

Publication Number Publication Date
JPS60125631A true JPS60125631A (en) 1985-07-04
JPH0419925B2 JPH0419925B2 (en) 1992-03-31

Family

ID=16956154

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58233510A Granted JPS60125631A (en) 1983-12-13 1983-12-13 Medical vessel

Country Status (1)

Country Link
JP (1) JPS60125631A (en)

Also Published As

Publication number Publication date
JPH0419925B2 (en) 1992-03-31

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