JPH0745169B2 - Injection blow molding method for containers - Google Patents
Injection blow molding method for containersInfo
- Publication number
- JPH0745169B2 JPH0745169B2 JP2105000A JP10500090A JPH0745169B2 JP H0745169 B2 JPH0745169 B2 JP H0745169B2 JP 2105000 A JP2105000 A JP 2105000A JP 10500090 A JP10500090 A JP 10500090A JP H0745169 B2 JPH0745169 B2 JP H0745169B2
- Authority
- JP
- Japan
- Prior art keywords
- container
- bottomed parison
- injection
- resin
- blow 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.)
- Expired - Lifetime
Links
- 238000010102 injection blow moulding Methods 0.000 title claims description 9
- 229920005989 resin Polymers 0.000 claims description 57
- 239000011347 resin Substances 0.000 claims description 57
- 230000002093 peripheral effect Effects 0.000 claims description 29
- 238000002347 injection Methods 0.000 claims description 23
- 239000007924 injection Substances 0.000 claims description 23
- 230000000717 retained effect Effects 0.000 claims description 19
- 238000001746 injection moulding Methods 0.000 claims description 13
- 238000000071 blow moulding Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 6
- 229920003002 synthetic resin Polymers 0.000 description 16
- 239000000057 synthetic resin Substances 0.000 description 16
- 239000011148 porous material Substances 0.000 description 4
- 238000007664 blowing Methods 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000002087 whitening effect Effects 0.000 description 1
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
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C45/2701—Details not specific to hot or cold runner channels
-
- 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
- B29C49/071—Preforms or parisons characterised by their configuration, e.g. geometry, dimensions or physical properties
-
- 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
- B29C49/6409—Thermal conditioning of preforms
- B29C49/6436—Thermal conditioning of preforms characterised by temperature differential
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/0715—Preforms or parisons characterised by their configuration the preform having one end closed
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/072—Preforms or parisons characterised by their configuration having variable wall thickness
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/073—Preforms or parisons characterised by their configuration having variable diameter
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/076—Preforms or parisons characterised by their configuration characterised by the shape
- B29C2949/0768—Preforms or parisons characterised by their configuration characterised by the shape characterised by the shape of specific parts of preform
- B29C2949/077—Preforms or parisons characterised by their configuration characterised by the shape characterised by the shape of specific parts of preform characterised by the neck
- B29C2949/0772—Closure retaining means
- B29C2949/0773—Threads
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/076—Preforms or parisons characterised by their configuration characterised by the shape
- B29C2949/0768—Preforms or parisons characterised by their configuration characterised by the shape characterised by the shape of specific parts of preform
- B29C2949/078—Preforms or parisons characterised by their configuration characterised by the shape characterised by the shape of specific parts of preform characterised by the bottom
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/076—Preforms or parisons characterised by their configuration characterised by the shape
- B29C2949/0768—Preforms or parisons characterised by their configuration characterised by the shape characterised by the shape of specific parts of preform
- B29C2949/078—Preforms or parisons characterised by their configuration characterised by the shape characterised by the shape of specific parts of preform characterised by the bottom
- B29C2949/0781—Preforms or parisons characterised by their configuration characterised by the shape characterised by the shape of specific parts of preform characterised by the bottom characterised by the sprue, i.e. injection mark
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/079—Auxiliary parts or inserts
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/20—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer
- B29C2949/22—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer at neck portion
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/20—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer
- B29C2949/24—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer at flange portion
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/20—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer
- B29C2949/26—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer at body portion
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/20—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer
- B29C2949/28—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer at bottom portion
-
- 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
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
- B29C49/06—Injection blow-moulding
-
- 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
- B29C49/6409—Thermal conditioning of preforms
- B29C49/6436—Thermal conditioning of preforms characterised by temperature differential
- B29C49/6458—Thermal conditioning of preforms characterised by temperature differential tangentially, i.e. along circumference
-
- 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
- B29K2105/25—Solid
- B29K2105/253—Preform
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Geometry (AREA)
- Thermal Sciences (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明の容器の射出吹込み成形方法、特に円筒形の有底
パリソンから中空の合成樹脂容器を形成する射出吹込成
形方法の改良に関する。Description: TECHNICAL FIELD The present invention relates to an improvement of the injection blow molding method for a container of the present invention, particularly the injection blow molding method for forming a hollow synthetic resin container from a cylindrical bottomed parison.
[従来の技術] 射出成形により円筒型の有底パリソンを形成し、この有
底パリソンに気体を吹込んで膨張させ、所定形状にした
合成樹脂容器を形成する射出吹込成形方法が周知であ
り、例えば化粧品や洗剤の容器,飲料用のボトル等、各
種中空容器の形成に用いられている。[Prior Art] An injection blow molding method is well known in which a cylindrical bottomed parison is formed by injection molding, and a gas is blown into the bottomed parison to expand it to form a synthetic resin container having a predetermined shape. It is used to form various hollow containers such as cosmetics and detergent containers and beverage bottles.
この射出成形方法では、ブロー成形時における有底パリ
ソン各部の膨張比率を良好に制御することが、形成され
る中空容器の肉厚分布を均一なものとするために極めて
重要になる。In this injection molding method, it is extremely important to control the expansion ratio of each part of the bottomed parison during blow molding in order to make the wall thickness distribution of the hollow container formed uniform.
すなわち、円筒形の有底パリソンから、円筒形の中空容
器を形成した場合における容器の肉厚分布は、有底パリ
ソンの肉厚と温度分布とが一定である限り、そこに生ず
る膨張比率も一定となり各部分の伸長に差がないことか
ら、全体的に均一になるとされている。That is, when the cylindrical hollow container is formed from a cylindrical bottomed parison, the thickness distribution of the container has a constant expansion ratio as long as the thickness and temperature distribution of the bottomed parison are constant. Since there is no difference in the extension of each part, it is said that the parts are uniform throughout.
しかし、円筒形の有底パリソンから、断面形状が角型の
中空容器や、偏平な円形,楕円形等の偏平中空容器を形
成する場合には、パリソン各部の線膨張率に差が生じ、
容器の肉厚分布、特にその周面(側面)の肉厚分布が不
均一となる偏肉が生ずる。However, when a hollow container with a rectangular cross section or a flat hollow container such as a flat circle or an ellipse is formed from a cylindrical bottomed parison, a difference occurs in the linear expansion coefficient of each part of the parison.
The thickness distribution of the container, in particular, the thickness distribution of the peripheral surface (side surface) of the container becomes uneven, resulting in uneven thickness.
この偏肉は、容器を厚肉に形成する場合にはわずかな差
となって現れるだけだが、薄肉に形成する場合には肉厚
が著しい差として現われ、極端な場合には、周面の一部
がフィルムのように薄く形成されて容器としての機能が
全く損われてしまうことがある。This uneven thickness appears only as a slight difference when the container is formed to be thick, but when the container is formed to be thin, the thickness is significantly different, and in an extreme case, the peripheral surface has a small difference. The part may be thinly formed like a film and the function as a container may be impaired at all.
このような問題を解決するため、従来より偏平容器の射
出吹込成形方法に関する提案がなされている(特公昭59
−42925号公報参照)。この成形方法では、第11図に示
すような断面が円形の有底パリソン1に空気を吹込ん
で、第12図に示すように、平断面における縦横の膨張比
率が著しく異なる偏平容器2を形成する。In order to solve such a problem, conventionally, there has been proposed a method for injection blow molding of a flat container (Japanese Patent Publication No. 59).
-42925 gazette). In this molding method, air is blown into a bottomed parison 1 having a circular cross section as shown in FIG. 11 to form a flat container 2 having significantly different vertical and horizontal expansion ratios in a flat cross section, as shown in FIG. .
このとき、前記有底パリソン1は、第13図に示すよう
に、平断面が円形で、対向部分1a,1aを他の部分1b,1bよ
りも若干厚肉に形成してある。この厚肉の部分1a,1a
は、第14図に示すよう前記偏平容器2の膨張比率が大き
い前後面2a,2aを形成し、また他の部分1b,1bは偏平容器
2の膨張比率が小さい両周面2b,2bを形成する。At this time, as shown in FIG. 13, the bottomed parison 1 has a circular plane section and the facing portions 1a, 1a are formed to be slightly thicker than the other portions 1b, 1b. This thick part 1a, 1a
As shown in FIG. 14, the flat container 2 forms front and rear surfaces 2a, 2a having a large expansion ratio, and the other portions 1b, 1b form both peripheral surfaces 2b, 2b having a small expansion ratio of the flat container 2. To do.
すなわち、前記有底パリソン1の厚肉部分1a,1aは、他
の部分1b,1bよりも熱容量が大きいため、縦横の膨張比
率が異なる吹込み成形であっても、熱容量の差をもって
その膨張比率の差を補い、結果的に均一膨張を可能とす
る。これにより、円筒形の有底パリソン1を用いたにも
かかわらず、肉厚分布は均一な偏平中空容器2を形成す
ることができる。That is, since the thick portions 1a, 1a of the bottomed parison 1 have a larger heat capacity than the other portions 1b, 1b, even in blow molding with different vertical and horizontal expansion ratios, there is a difference in heat capacity between the expansion ratios. The difference is compensated for, resulting in uniform expansion. As a result, the flat hollow container 2 having a uniform wall thickness distribution can be formed even though the cylindrical bottomed parison 1 is used.
[発明が解決しようとする課題] しかし、この従来方法では、肉厚分布が微妙に異なるパ
リソン1を形成する必要がある。このため、射出成形に
用いる金型の加工が複雑になるという問題があった。[Problems to be Solved by the Invention] However, in this conventional method, it is necessary to form the parison 1 having a slightly different wall thickness distribution. Therefore, there has been a problem that processing of a mold used for injection molding becomes complicated.
特に前記従来技術では、射出成形金型のコア型を、パリ
ソンの内側形状に合わせて偏平に形成する複雑な加工が
必要となり、製造装置全体が高価なものとなってしまう
という問題があった。Particularly, in the above-mentioned conventional technique, there is a problem that a complicated process for forming the core die of the injection molding die into a flat shape in conformity with the inner shape of the parison is required, and the whole manufacturing apparatus becomes expensive.
また、このような従来技術では、射出成形された有底パ
リソン1を、一旦加熱炉に送ってパリソン温度を調整し
た後、偏平容器をブロー成形することが多い。この場合
に、加熱炉内に設けられる温調コア型にも、有底パリソ
ンの内形に合せた複雑な加工が必要となり、この面から
も製造装置全体のコスト高を招いてしまうという問題が
あった。In such a conventional technique, the bottomed parison 1 injection-molded is often sent to a heating furnace to adjust the parison temperature, and then the flat container is often blow-molded. In this case, the temperature control core type provided in the heating furnace also requires complicated processing according to the inner shape of the bottomed parison, which also causes a problem of increasing the cost of the entire manufacturing apparatus. there were.
本発明は、このような従来の課題に鑑みてなされたもの
であり、その目的は、前述した課題を解決し良好な肉厚
分布を有する容器を形成することができる容器の射出吹
込成形方法を提供することにある。The present invention has been made in view of such conventional problems, and an object thereof is to provide a container injection blow molding method capable of forming a container having a good wall thickness distribution by solving the problems described above. To provide.
[問題点を解決するための手段] 前記目的を達成するため、本発明は、 射出金型を用いて射出成形された有底パリソンをブロー
成形し中空容器を形成する方法において、 前記射出金型内に樹脂を注入するゲートを、射出成形時
に前記有底パリソンの底面から周面にかけての樹脂流を
制御する樹脂流制御用ゲートとして設けることにより、
最終成形品の形状に応じた保有熱量分布を有するよう有
底パリソンを形成し、ブロー成形時における中空容器の
周面の肉厚分布を制御することを特徴とする。[Means for Solving the Problems] In order to achieve the above object, the present invention provides a method for blow molding a bottomed parison injection-molded using an injection mold to form a hollow container, wherein the injection mold By providing a gate for injecting resin into the resin as a resin flow control gate for controlling the resin flow from the bottom surface of the bottomed parison to the peripheral surface during injection molding,
The bottomed parison is formed so as to have a retained heat quantity distribution according to the shape of the final molded product, and the wall thickness distribution of the peripheral surface of the hollow container during blow molding is controlled.
[作 用] 次に本発明の作用を説明する。[Operation] Next, the operation of the present invention will be described.
有底パリソンは、溶融樹脂をランナーからゲートを通し
て射出金型内へ注入することにより形成される。このと
き有底パリソンの底面には、射出成形金型に形成されて
いるゲートに存在する樹脂が冷却固化し、ゲート部とい
われる突起が形成される。The bottomed parison is formed by injecting a molten resin from a runner through a gate into an injection mold. At this time, the resin present in the gate formed in the injection mold is cooled and solidified on the bottom surface of the bottomed parison, and a projection called a gate portion is formed.
本発明の特徴は、前記ゲートを、射出成形時に有底パリ
ソンの底面から周面にかけての樹脂流を制御する樹脂制
御用ゲートとして設けることにより、有底パリソンの底
面またはこの底面から周面にかけて、最終成形品である
中空容器の形状に応じた保有熱量分布を与えることにあ
る。これにより、ブロー成形時における中空容器周面
(側面)の肉厚分布を制御することが可能となる。The feature of the present invention is that the gate is provided as a resin control gate for controlling the resin flow from the bottom surface of the bottomed parison to the peripheral surface during injection molding, so that the bottom surface of the bottomed parison or this bottom surface to the peripheral surface, The purpose is to give the distribution of heat quantity possessed according to the shape of the hollow container which is the final molded product. This makes it possible to control the wall thickness distribution of the peripheral surface (side surface) of the hollow container during blow molding.
すなわち、射出金型のゲートから樹脂を注入すると、こ
の注入樹脂は、樹脂流制御用ゲートを通過し、有底パリ
ソンの底面に対応する部分から周面に対応する部分に回
り込んでいく。このとき、射出成形金型に形成されてい
るゲートの横断面形状を、例えば楕円形状、スター形状
あるいは平板形状の樹脂流制御用ゲートとして形成する
ことにより、ランナーからこの樹脂流制御用ゲートを通
って金型内に流れ込む樹脂流の流れは、樹脂流制御用ゲ
ートの形状に応じて制御され、有底パリソンに任意の保
有熱量分布を与えることができる。That is, when the resin is injected from the gate of the injection mold, the injected resin passes through the resin flow control gate and wraps around from the portion corresponding to the bottom surface of the bottomed parison to the portion corresponding to the peripheral surface. At this time, the gate formed in the injection molding die is formed, for example, as an elliptical, star-shaped, or flat-shaped resin flow control gate so that the runner passes through the resin flow control gate. The flow of the resin flow flowing into the mold is controlled according to the shape of the resin flow control gate, so that the bottomed parison can be provided with an arbitrary distribution of heat quantity.
このように本発明によれば、前記制御用ゲートの形状
を、ブロー成形する容器の形状に応じた保有熱量分布を
与える形状に形成することにより、角型の中空容器や、
長円形や楕円形をした偏平中空容器を、その周面がほぼ
均一な肉厚分布を有するよう形成することができる。Thus, according to the present invention, by forming the shape of the control gate into a shape that gives a retained heat quantity distribution according to the shape of the container to be blow molded, a rectangular hollow container,
The oblong or elliptical flat hollow container can be formed so that the peripheral surface thereof has a substantially uniform wall thickness distribution.
特に、本発明では、従来のように有底パリソン周面の肉
厚を制御して保有熱量分布を与えるというものではな
く、射出金型のゲートを、射出成形時の樹脂の流れを制
御する樹脂流制御用ゲートとして形成し、この樹脂の流
れにより保有熱量分布を与えるという全く新たな発想に
基づきなされたものである。従って、射出金型,温調金
型には、従来のように複雑な肉厚分布に対応した複雑な
加工が要求されることがなく、装置全体のコストダウン
を図ることができる。In particular, in the present invention, the thickness of the peripheral surface of the bottomed parison is not controlled as in the prior art to give the retained heat quantity distribution, but the gate of the injection mold is provided with a resin that controls the flow of resin during injection molding. It was formed based on a completely new idea of forming a flow control gate and giving the distribution of heat quantity retained by the flow of this resin. Therefore, the injection mold and the temperature control mold are not required to have complicated processing corresponding to a complicated wall thickness distribution as in the conventional case, and the cost of the entire apparatus can be reduced.
[実施例] 次に本発明の好適な実施例を図面に基づき詳細に説明す
る。[Embodiment] Next, a preferred embodiment of the present invention will be described in detail with reference to the drawings.
第1図〜第7図には本発明の好適な第1実施例が示され
ている。1 to 7 show a first preferred embodiment of the present invention.
本実施例の射出吹込成形方法では、第1図に示す円筒形
の有底パリソン10にエアーを吹込んで、第2図に示すよ
うな偏平な中空合成樹脂容器110を形成する。In the injection blow molding method of this embodiment, air is blown into the cylindrical bottomed parison 10 shown in FIG. 1 to form a flat hollow synthetic resin container 110 as shown in FIG.
第3図(a)には、前記有底パリソン10の射出成形に用
いられる射出金型20が示されている。この射出金型20
は、射出コア型24と、射出型22とを有する。そして、こ
の射出金型20の樹脂注入用のゲート26には、ホットラン
ナノズル40が断熱剤42を介して接続されている。FIG. 3A shows an injection mold 20 used for injection molding the bottomed parison 10. This injection mold 20
Has an injection core mold 24 and an injection mold 22. A hot runner nozzle 40 is connected to the resin injection gate 26 of the injection mold 20 via a heat insulating agent 42.
そして、ランナー40aからゲート26を通過して射出金型2
0内へ溶融樹脂を注入することにより、有底パリソン10
が形成される。このとき射出金型20に形成されているゲ
ート26に存在する樹脂が冷却固化し、ゲート部12といわ
れる突起が形成される。Then, the injection mold 2 is passed from the runner 40a through the gate 26.
By injecting molten resin into 0, bottomed parison 10
Is formed. At this time, the resin existing in the gate 26 formed in the injection mold 20 is cooled and solidified, and a projection called a gate portion 12 is formed.
本発明の特徴は、金型20内へ注入される溶融樹脂の流れ
をゲート26を用いて制御し、有底パリソン10、特にその
底面16から周面17にかけて最終成形品たる合成樹脂容器
110の形状に応じた保有熱量分布を与えることにある。
これにより、パリソン10にエアーを吹込み、縦横の膨張
比率が異なる偏平な合成樹脂容器110をブロー形成する
場合でも、その膨張比率の差を保有熱量分布をもって補
うことを可能とする。この結果、円筒型の有底パリソン
10を用いたにもかかわらず、周面110a,110bの肉厚分布
が均一な偏平の合成樹脂容器110を得ることができる。The feature of the present invention is that the flow of the molten resin injected into the mold 20 is controlled by using the gate 26, and the bottomed parison 10, particularly the synthetic resin container as the final molded product from the bottom surface 16 to the peripheral surface 17 thereof.
The purpose is to give a distribution of heat quantity possessed according to the shape of 110.
As a result, even when air is blown into the parison 10 to blow-form the flat synthetic resin container 110 having different vertical and horizontal expansion ratios, it is possible to compensate for the difference in expansion ratio with the retained heat quantity distribution. As a result, the cylindrical bottomed parison
Despite the use of 10, it is possible to obtain a flat synthetic resin container 110 having a uniform thickness distribution on the peripheral surfaces 110a and 110b.
第3図(b),(c)に示すよう、実施例のゲート26
は、初期注入口としての細孔ゲート26aと、これに続く
樹脂流制御用ゲート26bとから構成され、これにより、
有底パリソン10の底面16には前記各ゲート26a,26bに対
応して、突起状の初期ゲート部26aと、これに連なる板
状の制御用ゲート部26bとが形成される。As shown in FIGS. 3B and 3C, the gate 26 of the embodiment is shown.
Is composed of a pore gate 26a as an initial injection port and a resin flow control gate 26b following the pore gate 26a.
On the bottom surface 16 of the bottomed parison 10, a protrusion-shaped initial gate portion 26a and a plate-shaped control gate portion 26b connected to the protrusion-shaped initial gate portion 26a are formed corresponding to the gates 26a and 26b.
以上の構成とすることにより、初期ゲート26aから樹脂
流制御用ゲート26bを介して金型内に注入された溶融樹
脂流は、底部形成空間28a,周面形成空間28bを通りなが
ら金型の奥へ向って流れ込んでいく。このときの樹脂の
流れは、第4図に示すように制御されるものと推定され
る。With the above configuration, the molten resin flow injected into the mold from the initial gate 26a through the resin flow control gate 26b passes through the bottom forming space 28a and the peripheral surface forming space 28b, and is deep inside the mold. It flows toward. It is estimated that the resin flow at this time is controlled as shown in FIG.
すなわち、制御用ゲート26bから底面形成空間28aに流れ
込んだ溶融樹脂流は、制御用ゲート26bの両端側から周
面形成空間28bへ向かって矢印100aで示すよう素直に入
り込んでいくが、制御用ゲート26bの中心付近において
底面形成空間28aへ流れ込んだ樹脂流は、矢印100bで示
すよう射出コア型24にぶつかって一旦横に流れた後、周
面形成空間28bへ流れ込むことになる。That is, the molten resin flow that has flowed from the control gate 26b into the bottom surface forming space 28a directly enters from the both ends of the control gate 26b toward the peripheral surface forming space 28b as shown by the arrow 100a. The resin flow that has flowed into the bottom surface forming space 28a near the center of 26b collides with the injection core mold 24 as shown by the arrow 100b, flows once laterally, and then flows into the peripheral surface forming space 28b.
第5図(a)には、第4図のVa−Vaの断面における樹脂
流の推定図が示され、第5図(b)には、第5図Va−Va
と直交するVb−Vbの断面における樹脂流の推定図が示さ
れている。これらの推定図からも理解されるように、実
施例の射出成形により形成された有底パリソン10は、樹
脂流が素直に入り込んでいく10a,10a領域における保有
熱量が大きく、樹脂流が流れ込みにくい10b,10b領域の
保有熱量が低くなるものと推定される。なぜなら、100a
の樹脂流が、100bの樹脂流の方へまわり込んでいく過程
で、金型によって冷却され、この結果、10bの領域より1
0aの領域の方が保有熱量が高いと推定されるからであ
る。Fig. 5 (a) shows an estimated diagram of the resin flow in the cross section Va-Va of Fig. 4, and Fig. 5 (b) shows Va-Va of Fig. 5.
The estimated diagram of the resin flow in the cross section of Vb-Vb orthogonal to is shown. As can be understood from these estimation diagrams, the bottomed parison 10 formed by the injection molding of the embodiment has a large amount of heat retained in the 10a and 10a regions where the resin flow directly enters, and the resin flow hardly flows in. It is estimated that the amount of heat retained in the 10b and 10b regions will be low. Because 100a
The resin flow of 10b is cooled by the mold in the process of wrapping around to the resin flow of 100b.
This is because it is estimated that the amount of heat retained is higher in the region of 0a.
従って、保有熱量が大きい10a,10aの領域は、後述のブ
ロー成形工程において樹脂が伸びやすく、保有熱量が小
さい10b,10bの領域は、ブロー成形工程において樹脂が
伸びにくいことが理解されよう。Therefore, it will be understood that in the regions 10a, 10a having a large retained heat amount, the resin easily expands in the blow molding process described later, and in the regions 10b, 10b having a small retained heat amount, the resin hardly expands in the blow molding process.
そして、前記有底パリソン10は、第6図に示す吹込金型
30にて偏平の合成樹脂容器110としてブロー成形され
る。このときの吹込金型30への移送は、有底パリソン10
を射出金型20から離型した後、ただちに吹込金型30に移
送する場合と、一端加熱炉に送ってパリソン温度を再調
整した後に吹込金型30に移送する場合とがあるが、本発
明はこのいずれをも採用し得る。The bottomed parison 10 is a blow mold shown in FIG.
At 30, a flat synthetic resin container 110 is blow-molded. At this time, the transfer to the blow mold 30 is performed by the bottomed parison 10
After being released from the injection mold 20, there are cases where it is immediately transferred to the blow mold 30 and cases where it is transferred to the one-end heating furnace to readjust the parison temperature and then transferred to the blow mold 30. Can adopt any of these.
第6図には、吹込金型30内における有底パリソン10の位
置が示されている。実施例において有底パリソン10は、
偏平に形成したキャビティ32の中央に位置させ、偏平容
器110の前後周面110a,110aを形成する型面32a,32aに保
有熱量の高い領域10a,10aを臨ませる。そして、有底パ
リソン10内への空気の吹込みにより、保有熱量の高い領
域10a,10aを、型面32a,32aと接する方向に、また保有熱
量の低い領域10b,10bを偏平容器110の左右両周面110b,1
10bを成形する型面32b,32bと接する方向へと膨張させ
る。FIG. 6 shows the position of the bottomed parison 10 in the blow mold 30. The bottomed parison 10 in the embodiment is
Located in the center of the flatly formed cavity 32, the mold surfaces 32a and 32a forming the front and rear peripheral surfaces 110a and 110a of the flat container 110 are exposed to the regions 10a and 10a having a high retained heat amount. Then, by blowing air into the bottomed parison 10, the areas 10a, 10a having a high retained heat amount are brought into contact with the mold surfaces 32a, 32a, and the areas 10b, 10b having a low retained heat amount are provided on the left and right sides of the flat container 110. Both sides 110b, 1
10b is expanded in a direction in which it contacts the mold surfaces 32b, 32b for molding.
このとき、有底パリソン10の保有熱量が大きい領域10a,
10aは、保有熱量の小さい領域10b,10bに比べ十分に伸長
する。これにより、第1図に示すような円筒形の有底パ
リソン10から、第2図に示すよう、周面110a,110bの肉
厚分布が均一な偏平の中空容器110を得ることができ
る。At this time, the area 10a where the bottom parison 10 has a large amount of heat,
The area 10a is sufficiently elongated as compared with the areas 10b and 10b having a small heat quantity. As a result, from the cylindrical bottomed parison 10 as shown in FIG. 1, it is possible to obtain a flat hollow container 110 having a uniform wall thickness distribution on the peripheral surfaces 110a, 110b as shown in FIG.
特に、本発明によれば、従来のように偏平容器110の両
周面110b,110bがフィルムのように薄く形成されて強度
不足になったり、応力白化して美感を著しく損うような
ことはなく、良好な偏平合成樹脂容器を得ることができ
る。In particular, according to the present invention, both peripheral surfaces 110b, 110b of the flat container 110 are thinly formed like a film and have insufficient strength as in the conventional case, or stress whitening does not significantly impair aesthetics. Therefore, a good flat synthetic resin container can be obtained.
また、このようにして合成樹脂容器110を形成した後、
その底面116のゲート部112a,112bが邪魔になる場合があ
る。この場合には、吹込成形時にこれらゲート部112a,1
12bを押しつぶしてもよく、またその後にゲート部112a,
112bのみを切除してもよい。In addition, after forming the synthetic resin container 110 in this way,
The gate portions 112a and 112b on the bottom surface 116 may interfere. In this case, these gate portions 112a, 1
12b may be crushed, and after that, the gate portion 112a,
Only 112b may be excised.
また、合成樹脂容器110の底面116の樹脂流制御用ゲート
部112bを積極的に活用してもよく、例えば制御用ゲート
部112bに穴120等を開けることによって、容器110を吊下
げる吊り具としても用いることができる。Further, the resin flow control gate portion 112b on the bottom surface 116 of the synthetic resin container 110 may be positively utilized, for example, as a suspending tool for suspending the container 110 by making a hole 120 or the like in the control gate portion 112b. Can also be used.
なお、本実施例では有底パリソン10の底面にかなり大き
な制御用ゲート部12bを形成した場合を例にとり説明し
たが、この制御用ゲート部12bはこのように大きなもの
でなくても、例えば第7図に示すような小形なものでも
十分な効果を得ることができる。In the present embodiment, the case where the considerably large control gate portion 12b is formed on the bottom surface of the bottomed parison 10 has been described as an example, but even if the control gate portion 12b is not so large, for example, Even a small one as shown in FIG. 7 can obtain a sufficient effect.
なお、本実施例では、樹脂流制御用ゲート26bを、有底
パリソンの底面16に板状の制御用ゲート部12bを設ける
よう形成した場合を例にとり説明したが、本発明はこれ
に限らず、形成する合成樹脂容器110の形状に応じて、
制御用ゲート部12bを任意の形状、例えば星型,楕円形
とするよう樹脂流制御用ゲート26bを形成してもよい。In the present embodiment, the resin flow control gate 26b is described as an example in which the plate-shaped control gate portion 12b is provided on the bottom surface 16 of the bottomed parison, but the present invention is not limited to this. , According to the shape of the synthetic resin container 110 to be formed,
The resin flow control gate 26b may be formed so that the control gate portion 12b has an arbitrary shape, for example, a star shape or an elliptical shape.
例えば、第9図に示すような角柱型の中空合成樹脂容器
110を形成する場合には、樹脂流制御ようゲート26bを用
いて第8図に示すよう底面に十字形状した星型の制御用
ゲート部12bを形成すればよい。これにより、第8図
(c)に示すよう、有底パリソン10、特にその底面16に
は、樹脂流が流れ込みやすく保有熱量の大きな領域10a
と、樹脂流が流れ込みにくく保有熱量の低い領域10bと
が交互に形成される。このため、この有底パリソン10に
空気を吹込むことにより、保有熱量の高い領域10aは合
成樹脂容器110の周面110aを形成し、保有熱量の低い領
域10bは容器110のコーナー部110bを形成することにな
る。For example, a prismatic hollow synthetic resin container as shown in FIG.
When forming 110, the gate 26b for resin flow control may be used to form a star-shaped control gate portion 12b having a cross shape on the bottom surface as shown in FIG. As a result, as shown in FIG. 8 (c), the resin flow easily flows into the bottomed parison 10 and particularly the bottom surface 16 thereof, and the area 10a having a large amount of heat is retained.
And the regions 10b in which the resin flow is less likely to flow and the amount of heat retained is low are formed alternately. Therefore, by blowing air into the bottomed parison 10, the region 10a having a high retained heat amount forms the peripheral surface 110a of the synthetic resin container 110, and the region 10b having a low retained heat amount forms the corner portion 110b of the container 110. Will be done.
特に、従来このような角型の中空容器110を形成する場
合に、コーナー部110bは吹込み成形時に伸びやすく強度
不足になりがちであったが、本発明によれば、このコー
ナー部110bの肉厚を良好に保つことができる。In particular, when forming such a rectangular hollow container 110 in the past, the corner portion 110b tended to be easily stretched during blow molding, resulting in insufficient strength, but according to the present invention, the meat of the corner portion 110b is The thickness can be kept good.
また、前記実施例では、ゲート26を、初期注入口として
の細孔ゲート26aと、これに続く樹脂流制御用ゲート26b
とから構成したが、本発明はこれに限らず、必要に応じ
て細孔ゲート26aを設けることなく、樹脂流制御用ゲー
ト26bのみを設けるような構成としてもよい。この場合
には、例えば有底パリソン10の制御用ゲート部12bを、
第10図に示す形状とするよう樹脂流制御用ゲート26bを
形成すればよい。Further, in the above-mentioned embodiment, the gate 26 is composed of the fine pore gate 26a as the initial injection port and the resin flow control gate 26b subsequent thereto.
Although the present invention is not limited to this, the present invention is not limited to this, and may be configured such that only the resin flow control gate 26b is provided without providing the fine pore gate 26a if necessary. In this case, for example, the control gate portion 12b of the bottomed parison 10 is
The resin flow control gate 26b may be formed to have the shape shown in FIG.
なお、本発明は、上記実施例に限定されるものではな
く、本発明の要旨の範囲内で種々の変形実施が可能であ
る。The present invention is not limited to the above embodiment, and various modifications can be made within the scope of the present invention.
[発明の効果] 以上説明したように本発明によれば、射出金型内に樹脂
を注入するゲートを、射出成形時に有底パリソンの底面
から周面にかけての樹脂流を制御する樹脂流制御用ゲー
トとして設けることにより、最終成形品の形状に応じた
保有熱量分布を有するよう有底パリソンを形成すること
ができ、これにより、ブロー成形時における中空容器の
周面の肉厚を良好に制御することができる。[Effects of the Invention] As described above, according to the present invention, the gate for injecting the resin into the injection mold is for resin flow control for controlling the resin flow from the bottom surface of the bottomed parison to the peripheral surface during injection molding. By providing it as a gate, it is possible to form a bottomed parison so as to have a retained heat quantity distribution according to the shape of the final molded product, which allows good control of the wall thickness of the peripheral surface of the hollow container during blow molding. be able to.
特に、本発明によれば、周面の肉厚が正確に制御された
有底パリソンを用いることなく、ブロー成形時における
中空容器周面の肉厚を制御できるため、射出金型,温調
金型に従来のような複雑な加工が必要とされず、射出成
形装置自体のコストダウンを図ることが可能となる。In particular, according to the present invention, the thickness of the peripheral surface of the hollow container during blow molding can be controlled without using a bottomed parison whose peripheral surface thickness is accurately controlled. The mold does not need to be complicatedly processed as in the past, and the cost of the injection molding apparatus itself can be reduced.
第1図は、本発明に用いられる有底パリソンの説明図で
あり、同図(a)はその周面説明図、同図(b)は同図
(a)を矢印b方向からみた周面説明図、同図(c)は
同図(a)を矢印c方向からみた底面説明図、 第2図は、第1図に示す有底パリソンにエアーを吹込ん
で形成された偏平の中空合成樹脂容器の説明図であり、
同図(a)はその斜視説明図、同図(b)はその底面説
明図、 第3図は、第1図に示す有底パリソンを成形するために
用いる射出金型の説明図であり、同図(a)はその全体
の縦断面説明図、同図(b)はその要部縦断面説明図、
同図(c)は同図(b)と直交する方向の縦断面説明
図、 第4図(a),(b)は、第3図に示す金型内における
樹脂の流れを示す説明図、 第5図(a),(b)は、第3図(b),(c)に示す
金型内における樹脂の流れの説明図、 第6図は、有底パリソンと吹込金型との位置関係を示す
横断面説明図、 第7図は、有底パリソンの底面に形成される樹脂流制御
用ゲート部をより小さく形成した場合の一例を示す説明
図であり、同図(a)はその樹脂流制御用ゲート部を横
方向からみた説明図、同図(b)は正面方向からみた説
明図、 第8図は、底面に横断面が星型の制御用ゲート部を形成
した有底パリソンの説明図であり、同図(a)はその周
面説明図、同図(b)はその有底パリソンを斜め下方か
らみた状態の斜視説明図、同図(c)はその底面の説明
図、 第9図は、第8図に示す有底パリソンを用いて形成され
た角型の中空合成樹脂容器の説明図であり、同図(a)
はその斜視説明図、同図(b)はその底面の説明図、 第10図は、底面に制御用ゲート部のみを形成した有底パ
リソンの説明図、 第11図〜第14図は、従来の射出吹込成形方法の一例を示
す説明図である。 10……有底パリソン、10a,10b……領域、12b……制御用
ゲート部、16……底面、26……ゲート、26b……樹脂流
制御用ゲート、110……合成樹脂容器。FIG. 1 is an explanatory view of a bottomed parison used in the present invention. FIG. 1 (a) is an explanatory view of a peripheral surface thereof, and FIG. 1 (b) is a peripheral surface of the same shown in FIG. Explanatory drawing, the same figure (c) is an explanatory bottom view of the same figure (a) seen from the arrow c direction, and FIG. 2 is a flat hollow synthetic resin formed by blowing air into the bottomed parison shown in FIG. It is an explanatory view of a container,
1A is a perspective view thereof, FIG. 1B is a bottom view thereof, and FIG. 3 is an illustration of an injection mold used for molding the bottomed parison shown in FIG. FIG. 1A is an explanatory view of a longitudinal section of the whole, FIG.
FIG. 4C is a vertical cross-sectional explanatory view in a direction orthogonal to FIG. 4B, and FIGS. 4A and 4B are explanatory views showing the flow of resin in the mold shown in FIG. FIGS. 5 (a) and 5 (b) are explanatory views of the flow of resin in the mold shown in FIGS. 3 (b) and 3 (c), and FIG. 6 is the position of the bottomed parison and the blow mold. FIG. 7 is a cross-sectional explanatory view showing the relationship, and FIG. 7 is an explanatory view showing an example in which the resin flow control gate portion formed on the bottom surface of the bottomed parison is formed smaller, and FIG. FIG. 8B is an explanatory view of the resin flow control gate portion viewed from the lateral direction, FIG. 8B is an explanatory view of the resin flow control gate portion viewed from the front direction, and FIG. FIG. 4A is an explanatory view of the peripheral surface thereof, FIG. 3B is a perspective explanatory view of the bottomed parison as seen obliquely from below, and FIG. The illustration of the bottom surface thereof, FIG. 9 is an explanatory view of a hollow synthetic resin container formed rectangular with a bottomed parison shown in FIG. 8, FIG. (A)
Is a perspective explanatory view thereof, FIG. 10B is an explanatory view of the bottom surface thereof, FIG. 10 is an explanatory view of a bottomed parison having only a control gate portion formed on the bottom surface, and FIGS. 11 to 14 are conventional drawings. It is explanatory drawing which shows an example of the injection blow molding method of this. 10: bottomed parison, 10a, 10b: area, 12b: control gate, 16: bottom, 26: gate, 26b: resin flow control gate, 110: synthetic resin container.
Claims (1)
ソンをブロー成形し中空容器を形成する方法において、 前記射出金型内に樹脂を注入するゲートを、射出成形時
に前記有底パリソンの底面から周面にかけての樹脂流を
制御する樹脂流制御用ゲートとして設けることにより、
最終成形品の形状に応じた保有熱量分布を有するよう有
底パリソンを形成し、ブロー成形時における中空容器の
周面の肉厚分布を制御することを特徴とする容器の射出
吹込成形方法。1. A method for blow molding a bottomed parison injection-molded using an injection mold to form a hollow container, wherein a gate for injecting resin into the injection mold is provided with the bottomed parison during injection molding. By providing it as a resin flow control gate that controls the resin flow from the bottom surface to the peripheral surface,
An injection blow molding method for a container, which comprises forming a bottomed parison so as to have a retained heat quantity distribution according to the shape of the final molded product, and controlling the wall thickness distribution of the peripheral surface of the hollow container during blow molding.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2105000A JPH0745169B2 (en) | 1990-04-20 | 1990-04-20 | Injection blow molding method for containers |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2105000A JPH0745169B2 (en) | 1990-04-20 | 1990-04-20 | Injection blow molding method for containers |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH044119A JPH044119A (en) | 1992-01-08 |
JPH0745169B2 true JPH0745169B2 (en) | 1995-05-17 |
Family
ID=14395822
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2105000A Expired - Lifetime JPH0745169B2 (en) | 1990-04-20 | 1990-04-20 | Injection blow molding method for containers |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0745169B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4552422B2 (en) * | 2003-11-20 | 2010-09-29 | 東洋製罐株式会社 | Method for manufacturing container with extension |
JP2019130251A (en) * | 2018-02-02 | 2019-08-08 | テルモ株式会社 | Cylindrical preform for manufacturing medical liquid storage container body and method of manufacturing medical liquid storage container body |
-
1990
- 1990-04-20 JP JP2105000A patent/JPH0745169B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH044119A (en) | 1992-01-08 |
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