JP2003048239A - Injection molding method, injection molding machine used for the same and screw of injection molding machine - Google Patents

Injection molding method, injection molding machine used for the same and screw of injection molding machine

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Publication number
JP2003048239A
JP2003048239A JP2001241052A JP2001241052A JP2003048239A JP 2003048239 A JP2003048239 A JP 2003048239A JP 2001241052 A JP2001241052 A JP 2001241052A JP 2001241052 A JP2001241052 A JP 2001241052A JP 2003048239 A JP2003048239 A JP 2003048239A
Authority
JP
Japan
Prior art keywords
resin
screw
stirring
injection molding
section
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.)
Withdrawn
Application number
JP2001241052A
Other languages
Japanese (ja)
Inventor
Hiroyuki Hirano
博之 平野
Hitoshi Kawachi
斉 河内
Satoshi Shimura
吏士 志村
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP2001241052A priority Critical patent/JP2003048239A/en
Publication of JP2003048239A publication Critical patent/JP2003048239A/en
Withdrawn legal-status Critical Current

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  • Injection Moulding Of Plastics Or The Like (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an injection foam molding method capable of sufficiently stirring and kneading a resin even if a screw is short, capable of certainly preventing the back flow of the molten resin to a plasticizing part by the resin pressure at the time of injection of a foaming agent impregnated molten resin in a weighing part and capable of also manufacturing a small-sized molded article, an injection molding machine used therein and the screw of the injection molding machine. SOLUTION: A high pressure resin forming part having a stirring blade structure, which makes the absolute value of a resin feed speed less than that of the resin feed speed of the plasticizing part, is provided between the plasticizing part and stirring part of the screw of the injection molding machine and the back flow of the foaming agent impregnated molten resin to the plasticizing part is prevented by the molten resin high pressure part formed by the high pressure resin forming part.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、射出成形方法、射
出発泡成形方法、およびこれらの成形方法に用いる射出
成形機およびこの射出成形機のスクリューに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an injection molding method, an injection foam molding method, an injection molding machine used in these molding methods, and a screw of the injection molding machine.

【0002】[0002]

【従来の技術】易流動化剤および/または発泡剤となる
二酸化炭素ガスや窒素ガスなどの樹脂に対して非反応性
のガス(以下、「非反応性ガス」と記す)を射出前に溶
融樹脂中に含浸させ、この非反応性ガス含浸溶融樹脂を
金型内に射出し発泡させる熱可塑性樹脂発泡体の射出成
形方法として、1)シリンダー内に投入される前の固体
状態の原料樹脂に予め非反応性ガスを高圧下で含浸させ
ておく方法、2)シリンダー内で溶融した溶融樹脂に非
反応性ガスを含浸させる方法などが公知である。
2. Description of the Related Art A gas which is non-reactive with a resin such as carbon dioxide gas or nitrogen gas (hereinafter referred to as "non-reactive gas") which becomes a free-flowing agent and / or a foaming agent is melted before injection. As an injection molding method of a thermoplastic resin foam in which a resin is impregnated and the molten resin impregnated with a non-reactive gas is injected into a mold to foam, 1) a raw material resin in a solid state before being charged into a cylinder Known methods include a method of previously impregnating a non-reactive gas under high pressure, and a method of impregnating a molten resin melted in a cylinder with a non-reactive gas.

【0003】しかし、固体状態の原料樹脂に非反応性ガ
スを含浸させる前者の方法では、熱可塑性樹脂発泡体を
得ることは可能であるが、非反応性ガスを含浸させるの
に、例えば成形機への樹脂の供給を停止し、耐圧チャン
バー内でガスを含浸させる必要があるので、ガス飽和含
浸状態に達するのに数十時間を要してしまい、工業的に
実施するのは困難である。
However, in the former method of impregnating a solid state raw material resin with a non-reactive gas, it is possible to obtain a thermoplastic resin foam, but for impregnating a non-reactive gas, for example, a molding machine is used. Since it is necessary to stop the supply of the resin to and to impregnate the gas in the pressure resistant chamber, it takes several tens of hours to reach the gas saturated impregnation state, which is difficult to carry out industrially.

【0004】一方、後者の方法は、原料供給口からシリ
ンダー内へ供給される樹脂ペレットなどをシリンダー内
の可塑化部で可塑化したのち、撹拌部で炭酸ガス等の非
反応性ガスを発泡剤としてシリンダー内に供給しスクリ
ューを後退させてシリンダーの先端計量部にて溶融樹脂
を計量する間に溶融樹脂中に発泡剤を含浸するようにし
ている。ところで、後者の方法では、計量中の高圧状態
の溶融樹脂に非反応性ガスを供給するため、供給ガスの
圧力を溶融樹脂圧力より高くしないと溶融樹脂にガスを
注入することが困難である。
On the other hand, in the latter method, the resin pellets or the like supplied from the raw material supply port into the cylinder are plasticized in the plasticizing part in the cylinder, and then the non-reactive gas such as carbon dioxide gas is blown in the stirring part. As a result, the foaming agent is impregnated into the molten resin while it is fed into the cylinder and the screw is retracted to measure the molten resin at the tip measuring portion of the cylinder. By the way, in the latter method, since the non-reactive gas is supplied to the high-pressure molten resin during measurement, it is difficult to inject the gas into the molten resin unless the pressure of the supply gas is higher than the molten resin pressure.

【0005】そこで、特開平11−64130号公報で
は、スクリューの可塑化部と撹拌部との間に逆流防止の
ためのチェックリングをスクリュー本体に装着すること
によって、撹拌部の非反応性ガスが供給された高圧の樹
脂が可塑化部側に逆流しないようにしている。しかしな
がら、上記のように、可塑化部と撹拌部との間にチェッ
クリングを設けるようにすると、チェックリング部分で
の樹脂の撹拌ができなくなるため、従来と同じ射出成形
機長さであると、撹拌混練が不十分となる恐れがある。
したがって、樹脂の十分な撹拌を図ろうと、射出成形機
の長さを長いものにしなければならず設備コストがかか
るという問題が発生する。
In view of this, in Japanese Patent Laid-Open No. 11-64130, a check ring for preventing backflow is attached to the screw main body between the plasticizing portion and the stirring portion of the screw, so that the non-reactive gas in the stirring portion is removed. The supplied high-pressure resin is prevented from flowing back to the plasticizing section side. However, as described above, if a check ring is provided between the plasticizing section and the stirring section, it will not be possible to stir the resin at the check ring section. Kneading may be insufficient.
Therefore, in order to sufficiently stir the resin, the length of the injection molding machine must be long, which causes a problem of high equipment cost.

【0006】また、上記のように可塑化部と撹拌部との
間にチェックリングを設けた構造のスクリューは、スク
リューを撹拌羽根が軸の周囲に形成された可塑化部用ス
クリュー部材と撹拌部用スクリュー部材とが、撹拌部用
スクリュー部材の後端部にチェックリングを外嵌したの
ち、可塑化部用スクリュー部材の先端からスクリューの
中心軸に沿って延出する雄ネジ部を、撹拌部用スクリュ
ー部材の後端にスクリューの中心軸に沿って設けられた
ネジ孔に螺合させることによって連結されることによっ
て得られるようになっている。
Further, the screw having the structure in which the check ring is provided between the plasticizing section and the stirring section as described above has a screw member for the plasticizing section in which stirring blades are formed around the shaft and the stirring section. Screw member for external use, after the check ring is externally fitted to the rear end portion of the screw member for the stirring unit, a male screw unit extending along the central axis of the screw from the tip of the screw member for the plasticizing unit is added to the stirring unit. It is obtained by connecting by screwing into a screw hole provided along the central axis of the screw at the rear end of the screw member for use.

【0007】しかし、上記のようなスクリューの構造
を、50φ以下等の小口径の射出成形機に採用しようと
すると、雄ねじ部も小径化せざるをえないため、雄ねじ
部が射出時の樹脂圧で破損する恐れがある。したがっ
て、上記のように可塑化部と撹拌部との間にチェックリ
ングを設ける構造では、小型の成形品の製造が難しいと
いう問題がある。
However, if the screw structure as described above is to be adopted in an injection molding machine having a small diameter such as 50φ or less, the male screw portion is forced to be small in diameter, and therefore the male screw portion has a resin pressure at the time of injection. May be damaged by. Therefore, with the structure in which the check ring is provided between the plasticizing section and the stirring section as described above, it is difficult to manufacture a small molded product.

【0008】[0008]

【発明が解決しようとする課題】本発明は、このような
事情に鑑みて、スクリュー長さが短くても十分に樹脂を
撹拌混練でき、計量部の易流動化剤含浸溶融樹脂の射出
時の樹脂圧によって、可塑化部側への溶融樹脂の逆流を
確実に防止できるとともに、小型の成形品の製造も可能
である射出発泡成形方法、この射出発泡成形方法に用い
る射出成形機およびこの射出成形機のスクリューを提供
することを目的としている。
In view of such circumstances, the present invention is capable of sufficiently agitating and kneading a resin even when the screw length is short, and is effective for injection of molten fluid-impregnated molten resin in a measuring section. An injection foam molding method capable of reliably preventing the backflow of the molten resin to the plasticizing portion side by the resin pressure and also capable of manufacturing a small molded product, an injection molding machine used for this injection foam molding method, and this injection molding Intended to provide machine screw.

【0009】[0009]

【課題を解決するための手段】このような目的を達成す
るために、本発明の請求項1に記載の射出成形方法(以
下、「請求項1の成形方法」と記す)は、射出成形機の
シリンダー内で、スクリューの回転によって、シリンダ
ー内の可塑化部で可塑化され溶融状態にされた溶融樹脂
に、スクリューの撹拌部を臨む位置でシリンダー内に易
流動化剤および/または発泡剤として作用するガスを供
給して、シリンダー内で前記ガスを溶融樹脂に混合し含
浸させるガス含浸工程と、得られたガス含浸溶融樹脂を
計量した後に計量樹脂を金型キャビティ内へ射出して成
形品を得る射出成形工程とを含む射出成形方法であっ
て、スクリューの可塑化部と撹拌部との間に、撹拌部の
溶融樹脂圧力よりも溶融樹脂圧力が高い高圧樹脂形成部
を設け可塑化部側への溶融樹脂の逆流を防止するように
した。本発明の請求項2に記載の射出発泡成形方法(以
下、「請求項2の成形方法」と記す)は、請求項1の整
形方法において、スクリューの可塑化部と撹拌部との間
に、その樹脂送り速度の絶対値が、可塑化部の樹脂送り
速度の絶対値より小さくなる撹拌羽根構造をした高圧樹
脂形成部を設けるようにした。
In order to achieve such an object, an injection molding method according to claim 1 of the present invention (hereinafter referred to as "molding method of claim 1") is an injection molding machine. As a freezing agent and / or a foaming agent in the cylinder at the position facing the stirring part of the screw, the molten resin that has been plasticized and melted in the plasticizing part in the cylinder by the rotation of the screw A gas impregnating step of supplying a working gas and mixing and impregnating the gas with a molten resin in a cylinder, and measuring the obtained gas-impregnated molten resin, and then injecting the measuring resin into a mold cavity to form a molded article. And a high-pressure resin forming section having a molten resin pressure higher than the molten resin pressure of the stirring section is provided between the plasticizing section and the stirring section of the screw. To the side And to prevent the backflow of molten resin. An injection foam molding method according to claim 2 of the present invention (hereinafter, referred to as "molding method of claim 2") is the shaping method according to claim 1, in which between the plasticizing portion and the stirring portion of the screw, A high-pressure resin forming section having a stirring blade structure is provided in which the absolute value of the resin feed rate is smaller than the absolute value of the resin feed rate of the plasticizing section.

【0010】本発明の請求項3に記載の射出発泡成形方
法(以下、「請求項3の成形方法」と記す)は、請求項
1または請求項2の成形方法において、ガスをスクリュ
ーロッド内を通り、スクリューの撹拌部に開口するガス
供給路を介してシリンダー内に供給するようにした。
An injection foam molding method according to claim 3 of the present invention (hereinafter referred to as "molding method of claim 3") is the same as the molding method of claim 1 or 2, wherein gas is introduced into the screw rod. As a result, the gas was supplied to the inside of the cylinder through a gas supply passage opened to the stirring portion of the screw.

【0011】本発明の請求項4に記載の射出発泡成形方
法(以下、「請求項4の成形方法」と記す)は、請求項
1〜請求項3のいずれかの成形方法において、ガスとし
て樹脂に対して非反応性ガスを用いるようにした。ここ
で、用いられる非反応性のガスとは、常温・常圧で気体
状態の有機または無機物質であって、樹脂を劣化させる
などの悪影響を与えないガスを示す。このようなガス
は、上記の条件を満たせば特に限定されず、例えば、無
機ガス、有機ガス(例えば、フロンガス、低分子量の炭
化水素ガス)などが挙げられる。環境に与える悪影響が
低く、そしてガスの回収の必要としない点で、無機ガス
が好ましく、樹脂に対する溶解度が高く、樹脂の溶融粘
度の低下が大きい観点から、二酸化炭素が好ましい。な
お、この非反応性ガスは、単独で用いられてもよく、あ
るいは2種類以上の非反応性ガスを併用してもよい。
The injection foam molding method according to claim 4 of the present invention (hereinafter referred to as "molding method of claim 4") is the resin as gas in the molding method according to any one of claims 1 to 3. A non-reactive gas was used. Here, the non-reactive gas used is an organic or inorganic substance that is in a gaseous state at room temperature and atmospheric pressure, and does not adversely affect the resin or the like. Such a gas is not particularly limited as long as it satisfies the above conditions, and examples thereof include an inorganic gas and an organic gas (for example, CFC gas, low molecular weight hydrocarbon gas) and the like. Inorganic gas is preferred because it has a low adverse effect on the environment and does not require gas recovery, and carbon dioxide is preferred from the viewpoints of high solubility in resin and large decrease in melt viscosity of resin. The non-reactive gas may be used alone or in combination of two or more kinds.

【0012】本発明の請求項5に記載の射出成形機(以
下、「請求項5の射出成形機」と記す)は、スクリュー
がスクリューの回転によりシリンダー内に供給された樹
脂を溶融してシリンダー先端方向に搬送する撹拌羽根を
有する可塑化部と、可塑化部で溶融状態になった溶融樹
脂をさらに撹拌混練する撹拌部とを備えるとともに、ス
クリューの撹拌部を臨む位置でシリンダー内の溶融樹脂
に易流動化剤および/または発泡剤として作用するガス
を供給するガス供給手段を備えた射出成形機であって、
スクリューが、その可塑化部と撹拌部との間にその樹脂
送り速度の絶対値が、可塑化部の樹脂送り速度の絶対値
より小さくなる撹拌羽根構造をした高圧樹脂形成部を備
えている構成とした。
An injection molding machine according to claim 5 of the present invention (hereinafter referred to as "injection molding machine according to claim 5") is a cylinder in which a screw melts resin supplied into the cylinder by rotation of the screw. The molten resin in the cylinder is provided with a plasticizing section having a stirring blade that conveys in the distal direction and a stirring section that further stirs and kneads the molten resin that has become molten in the plasticizing section, and faces the stirring section of the screw. An injection molding machine equipped with gas supply means for supplying a gas that acts as a freezing agent and / or a foaming agent to
A configuration in which the screw has a high-pressure resin forming section having a stirring blade structure between the plasticizing section and the stirring section, in which the absolute value of the resin feeding rate is smaller than the absolute value of the resin feeding rate of the plasticizing section. And

【0013】本発明の請求項6に記載の射出成形機(以
下、「請求項6の射出成形機」と記す)は、請求項5の
射出成形機において、高圧樹脂形成部の撹拌羽根が、可
塑化部の撹拌羽根に対し逆フライト構造に形成されてい
る構成とした。
An injection molding machine according to claim 6 of the present invention (hereinafter referred to as "injection molding machine according to claim 6") is the same as the injection molding machine according to claim 5, in which the stirring blade of the high-pressure resin forming part is It was configured to have a reverse flight structure with respect to the stirring blade of the plasticizing part.

【0014】本発明の請求項7に記載の射出成形機(以
下、「請求項7の射出成形機」と記す)は、請求項5ま
たは請求項6の射出成形機において、高圧樹脂形成部が
ダルメージ型の撹拌羽根構造に形成されている構成とし
た。
An injection molding machine according to claim 7 of the present invention (hereinafter referred to as "injection molding machine according to claim 7") is the same as the injection molding machine according to claim 5 or 6, The structure is such that it is formed into a dullage-type stirring blade structure.

【0015】本発明の請求項8に記載の射出成形機(以
下、「請求項8の射出成形機」と記す)は、請求項5〜
請求項7のいずれかの射出成形機において、ガス供給手
段がスクリュー後端に設けられたガス導入口からスクリ
ュー内部を通りスクリューの撹拌部壁面に開口するガス
供給路を備えている構成とした。
An injection molding machine according to claim 8 of the present invention (hereinafter, referred to as "injection molding machine according to claim 8") comprises:
In the injection molding machine according to any one of claims 7 to 9, the gas supply means is provided with a gas supply passage that is opened from the gas inlet provided at the rear end of the screw through the inside of the screw to the wall surface of the stirring portion of the screw.

【0016】本発明の請求項9に記載のスクリュー(以
下、「請求項9のスクリュー」と記す)は、スクリュー
の回転によりシリンダー内に供給された樹脂を撹拌羽根
によって溶融状態にしてシリンダー先端方向に搬送する
撹拌羽根を有する可塑化部と、可塑化部で溶融状態にな
った溶融樹脂をさらに撹拌羽根によって撹拌混練する撹
拌部と、可塑化部と撹拌部との間に設けられ、可塑化部
の樹脂送り速度の絶対値より小さくなる撹拌羽根構造を
した高圧樹脂形成部とを備える構成とした。
The screw according to claim 9 of the present invention (hereinafter referred to as "the screw of claim 9") is a cylinder tip direction in which the resin supplied into the cylinder by the rotation of the screw is melted by a stirring blade. Is provided between the plasticizing section and the stirring section, and the stirring section for stirring and kneading the molten resin melted in the plasticizing section by the stirring blade And a high-pressure resin forming section having a stirring blade structure that is smaller than the absolute value of the resin feeding speed of the section.

【0017】本発明の請求項10に記載のスクリュー
(以下、「請求項10のスクリュー」と記す)は、請求
項9のスクリューにおいて、スクリュー後端に設けられ
たガス導入口からスクリューロッド内部を通りスクリュ
ーの撹拌部壁面に開口するガス供給路を備えている構成
とした。
According to a tenth aspect of the present invention (hereinafter, referred to as "screw of the tenth aspect"), the screw of the ninth aspect is such that the inside of the screw rod extends from the gas inlet provided at the rear end of the screw. The gas supply passage opened to the wall surface of the stirring portion of the passing screw is provided.

【0018】本発明において、高圧樹脂形成部の撹拌羽
根の搬送方向および搬送速度は、可塑化部と撹拌部との
間に、撹拌部の溶融樹脂が可塑化部側へ逆流するのを防
止できれば特に限定されないが、可塑化部の溶融樹脂に
対し、1.2〜3倍、撹拌部の溶融樹脂に対し、1.1
〜5倍程度高圧となるように設定することが好ましい。
In the present invention, the carrying direction and carrying speed of the stirring blade of the high-pressure resin forming section should be such that the molten resin in the stirring section can be prevented from flowing back to the plasticizing section between the plasticizing section and the stirring section. Although not particularly limited, it is 1.2 to 3 times that of the molten resin in the plasticizing portion, and 1.1 times that of the molten resin in the stirring portion.
It is preferable to set the pressure to be about 5 times higher.

【0019】本発明の射出発泡成形方法で使用される樹
脂としては、特に限定されるものではないが、好ましく
は、発泡に適した溶融張力(具体的には、200℃で
0.069N=7g,以上)、伸張粘度特性を有するも
のであって、例えば、ポリエチレン系樹脂、ポリプロピ
レン系樹脂等のポリオレフィン系樹脂の他、ポリスチレ
ン系樹脂、アクリルニトリル−ブタジエン−スチレン共
重合体(ABS樹脂)、ポリ塩化ビニル系樹脂などが挙
げられ、これらを単独で、あるいは2種以上併用して用
いることができるが、これらの樹脂の内でも、ポリプロ
ピレン系樹脂を用いることがリサイクル性や物性等の点
で特に好ましい。
The resin used in the injection foam molding method of the present invention is not particularly limited, but preferably has a melt tension suitable for foaming (specifically, 0.069 N = 7 g at 200 ° C.). , And the above), which have extensional viscosity characteristics, and include, for example, polyolefin resins such as polyethylene resins and polypropylene resins, polystyrene resins, acrylonitrile-butadiene-styrene copolymers (ABS resins), and poly resins. Vinyl chloride resins and the like can be mentioned, and these can be used alone or in combination of two or more kinds. Among these resins, it is particularly preferable to use polypropylene resin from the viewpoint of recyclability and physical properties. preferable.

【0020】ここでいうポリプロピレン系樹脂は、ポリ
プロピレンのホモポリマーに限られず、他の共重合性モ
ノマーとのランダムコポリマーやブロックコポリマー等
の一般的なポリプロピレン、及び、メタロセンを触媒等
として得られたメタロセンポリプロピレン、またポリプ
ロピレンに長鎖分岐を持たせたもの、他成分をグラフト
重合したものも含み、これらは単独で使用されても良い
し、2種以上併用されても良い。
The polypropylene resin referred to here is not limited to a homopolymer of polypropylene, but is a general polypropylene such as a random copolymer or a block copolymer with another copolymerizable monomer, or a metallocene obtained by using metallocene as a catalyst or the like. It also includes polypropylene, polypropylene having long-chain branching, and graft-polymerized other components, and these may be used alone or in combination of two or more.

【0021】本発明の射出成形機で使用可能な樹脂とし
ては、特に限定されないが、たとえば、本発明の射出発
泡成形方法で用いられる樹脂以外に、溶融粘度が高いた
め溶融成形が困難な樹脂、熱分解し易い樹脂、低沸点の
添加剤もしくは熱分解し易い添加剤を含有する難成形樹
脂などが挙げられる。
The resin that can be used in the injection molding machine of the present invention is not particularly limited. For example, in addition to the resin used in the injection foam molding method of the present invention, a resin that is difficult to melt mold because of its high melt viscosity, Examples thereof include a resin which is easily decomposed by heat, a low-boiling-point additive or a difficult-molding resin containing an additive which is easily decomposed by heat.

【0022】溶融粘度が高いため溶融成形が困難な樹脂
としては、例えば、超高分子量ポリエチレン、超高重合
度ポリ塩化ビニル、ポリテトラフルオロエチレン、ポリ
イミド、フッ素樹脂などのエンジニアリングプラスチッ
ク用の樹脂が挙げられる。
Examples of the resin which is difficult to be melt-molded due to its high melt viscosity include resins for engineering plastics such as ultra high molecular weight polyethylene, ultra high polymerization degree polyvinyl chloride, polytetrafluoroethylene, polyimide and fluororesin. To be

【0023】熱分解し易い樹脂としては、ポリ乳酸、ポ
リヒドロキシブチレート等の生分解性樹脂や、高塩素化
度ポリ塩化ビニル、ポリアクリロニトリル等が挙げられ
る。請求項7の射出成形機および請求項9のスクリュー
において、ガス供給口の位置は、撹拌部であれば特に限
定されないが、スクリュー先端部より後端側で溶融樹脂
の圧力が計量部での溶融樹脂圧に比べ低い位置、すなわ
ち、溶融樹脂がまだスクリューとシリンダーとの間に完
全に充満していない部分が好ましい。
Examples of the resin which is easily decomposed by heat include biodegradable resins such as polylactic acid and polyhydroxybutyrate, polyvinyl chloride having a high degree of chlorination, and polyacrylonitrile. In the injection molding machine according to claim 7 and the screw according to claim 9, the position of the gas supply port is not particularly limited as long as it is a stirring part, but the pressure of the molten resin on the rear end side of the screw front end melts at the measuring part. A position lower than the resin pressure, that is, a portion where the molten resin is not completely filled between the screw and the cylinder is preferable.

【0024】例えば、撹拌部には、前後スクリューフラ
イトのピッチが大きくなされることによって、及び/又
は、スクリュー軸径が小さくなされることによって、フ
ライト間空間中に前後のフライト間空間よりも内容積が
大きい拡大ガス含浸ゾーンを形成する拡大ガス含浸ゾー
ン形成部が設けられた構造とするとともに、スクリュー
のこの拡大ガス含浸ゾーン形成部にガス供給口を開口さ
せるようにすることが好ましく、この拡大ガス含浸ゾー
ンの前側フライト寄りの樹脂非充満部分を臨む位置に開
口させることがより好ましい。
For example, in the agitator, by increasing the pitch of the front and rear screw flights and / or by decreasing the screw shaft diameter, the internal volume of the inter-flight space is larger than that of the front and rear inter-flight spaces. It is preferable to have a structure in which an expanded gas impregnation zone forming part that forms a large expanded gas impregnation zone is provided, and to open a gas supply port in this expanded gas impregnation zone forming part of the screw. It is more preferable to open the resin non-filled portion near the front flight of the impregnation zone so as to face it.

【0025】[0025]

【発明の実施の形態】以下に、本発明の実施の形態を、
図面を参照しつつ詳しく説明する。図1〜図4は本発明
に係る射出成形機の第1の実施の形態を示すものであ
る。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below.
A detailed description will be given with reference to the drawings. 1 to 4 show a first embodiment of an injection molding machine according to the present invention.

【0026】図1〜図3に示すように、この射出成形機
1aは、シリンダー2と、その内部に配されたスクリュ
ー3aと、シールボックス4とから主に構成されてい
る。シリンダー2は、樹脂原料が供給される原料樹脂供
給口25を後端側に備え、先端にシャットオフ弁24を
備えている。
As shown in FIGS. 1 to 3, the injection molding machine 1a is mainly composed of a cylinder 2, a screw 3a arranged inside the cylinder 2, and a seal box 4. The cylinder 2 is provided with a raw material resin supply port 25 through which a resin raw material is supplied, on the rear end side, and a shutoff valve 24 at the front end.

【0027】スクリュー3aは、可塑化部31と、高圧
樹脂形成部32と、撹拌部33と、ガス供給路5と、先
端部チェックリング38とを備えている。可塑化部31
は、スクリューロッド30の周面に第1撹拌羽根35が
設けられていて、ホッパー13から原料樹脂供給口25
を経てシリンダー2内に供給された樹脂原料をスクリュ
ーロッド30の回転に伴って第1撹拌羽根35で撹拌し
シリンダー2の先端方向に向かって所定の速度で搬送し
ながら溶融状態にするようになっている。
The screw 3a includes a plasticizing section 31, a high-pressure resin forming section 32, a stirring section 33, a gas supply passage 5, and a tip check ring 38. Plasticizing part 31
Is provided with a first stirring blade 35 on the peripheral surface of the screw rod 30, and from the hopper 13 to the raw material resin supply port 25.
The resin raw material supplied into the cylinder 2 through the above is agitated by the first agitating blade 35 as the screw rod 30 rotates, and is brought into a molten state while being conveyed toward the tip end of the cylinder 2 at a predetermined speed. ing.

【0028】高圧樹脂形成部32は、可塑化部31の第
1撹拌羽根35に対して送り方向が逆になる、所謂逆フ
ライト形状になっているとともに、その搬送速度の絶対
値が第1撹拌羽根35より遅い第2撹拌羽根36がスク
リューロッド30の周面に設けられている。撹拌部33
は、第1撹拌羽根35と同じ搬送方向の第3撹拌羽根3
7がスクリューロッド30の周面に設けられていて、フ
ライト間空間の内容積が大きくなるとともに上流側より
も樹脂の送り速度が速くなっている拡大ガス含浸ゾーン
11がシリンダー2と撹拌部33との間に形成されるよ
うになっている。
The high-pressure resin forming section 32 has a so-called reverse flight shape in which the feeding direction is opposite to the first stirring blade 35 of the plasticizing section 31, and the absolute value of the conveying speed is the first stirring. A second stirring blade 36, which is slower than the blade 35, is provided on the peripheral surface of the screw rod 30. Stirrer 33
Is the third stirring blade 3 in the same transport direction as the first stirring blade 35.
7 is provided on the peripheral surface of the screw rod 30, and the expanded gas impregnation zone 11 in which the internal volume of the inter-flight space is large and the resin feeding speed is faster than that on the upstream side is the cylinder 2 and the stirring section 33. It is supposed to be formed between.

【0029】図1中、12は計量部、13は樹脂供給ホ
ッパー、14はスクリュー駆動ユニット、15はシール
ボックス4の接続アームである。
In FIG. 1, 12 is a measuring section, 13 is a resin supply hopper, 14 is a screw drive unit, and 15 is a connecting arm of the seal box 4.

【0030】ガス供給路5は、図2〜図4に示すよう
に、シリンダー2外のスクリュー後端側外壁面に開口す
る1つのガス導入口51と、撹拌部33の外壁面に開口
するガス供給口52とを備えている。シールボックス4
は、スクリュー3aの前後進および回転に対し,ガス導
入口51との位置がずれないように、射出成形機1の駆
動ユニット14に接続アーム15で固定されて、スクリ
ュー3aのガス導入口51形成部分を囲繞している。
As shown in FIGS. 2 to 4, the gas supply path 5 has one gas inlet port 51 opening to the outer wall surface of the screw outside the cylinder 2 and a gas opening to the outer wall surface of the stirring section 33. And a supply port 52. Seal box 4
Is fixed to the drive unit 14 of the injection molding machine 1 by the connecting arm 15 so that the position of the gas introduction port 51 does not shift with respect to the forward and backward movement and rotation of the screw 3a. Surrounding the part.

【0031】また、シールボックス4は、ガス導入口5
1が臨む位置にリング状の凹溝41が設けられていると
ともに、この凹溝41をスクリュー3aの前後両側から
挟むように、スクリューロッド30の周面に弾接し、凹
溝41内からのガスリークを防止する一対のシール部材
42が設けられている。
The seal box 4 has a gas inlet 5
1 is provided with a ring-shaped recessed groove 41, and the recessed groove 41 is elastically contacted with the peripheral surface of the screw rod 30 so as to sandwich the recessed groove 41 from both front and rear sides of the screw 3a to prevent gas leakage from the inside of the recessed groove 41. A pair of seal members 42 for preventing the above are provided.

【0032】また、シールボックス4の凹溝41には、
シールボックス4外に開口するガス注入装置9から注入
されるガスとしての炭酸ガスの注入口43が穿設されて
いる。図1中、9はガス供給装置である。
Further, in the concave groove 41 of the seal box 4,
An injection port 43 for carbon dioxide gas as a gas injected from the gas injection device 9 is provided outside the seal box 4. In FIG. 1, 9 is a gas supply device.

【0033】射出成形機1aは、以上のように構成され
ているので、ホッパー13から原料供給口を経てシリン
ダー2内へ原料樹脂が供給されると、原料樹脂はスクリ
ュー3aの回転によってまず可塑化部31の第1撹拌羽
根35によって溶融混練されながらシリンダー2の先端
方向へ送られる。
Since the injection molding machine 1a is constructed as described above, when the raw material resin is supplied from the hopper 13 into the cylinder 2 through the raw material supply port, the raw material resin is first plasticized by the rotation of the screw 3a. While being melted and kneaded by the first stirring blade 35 of the portion 31, it is sent toward the tip of the cylinder 2.

【0034】そして、高圧樹脂形成部32まできた溶融
樹脂は、第2撹拌羽根36によってさらに溶融混練され
るが、第2撹拌羽根36が逆フライト構造になっている
ので、可塑化部31からシリンダー2の先端方向へ送ら
れようとする溶融樹脂の搬送を妨げる方向に力が働く。
しかし、第1撹拌羽根35による搬送速度の方が、第2
撹拌羽根36の搬送速度の絶対値が大きいため、高圧樹
脂形成部32まできた溶融樹脂が減速され高圧状態にな
って撹拌部33に送られる。すなわち、可塑化部31の
溶融樹脂より高圧の溶融樹脂部が可塑化部31と撹拌部
33との間に形成される。
The molten resin that has reached the high-pressure resin forming section 32 is further melted and kneaded by the second stirring blade 36. However, since the second stirring blade 36 has the reverse flight structure, the plasticizing section 31 is connected to the cylinder. The force acts in a direction that hinders the conveyance of the molten resin that is about to be sent in the direction of the tip of No. 2.
However, the transport speed by the first stirring blade 35 is the second
Since the absolute value of the conveying speed of the stirring blade 36 is large, the molten resin that has reached the high-pressure resin forming section 32 is decelerated to a high pressure state and sent to the stirring section 33. That is, a molten resin portion having a higher pressure than the molten resin of the plasticizing portion 31 is formed between the plasticizing portion 31 and the stirring portion 33.

【0035】つぎに、撹拌部33に送られてきた溶融樹
脂は、フライト間空間の内容積が大きくなる拡大ガス含
浸ゾーン11に入り込むとともに、第3撹拌羽根37が
第1撹拌羽根35と同一方向に搬送するようになってい
て高圧樹脂形成部にある溶融樹脂より搬送速度が速くな
るので、樹脂圧が高圧樹脂形成部32より低くなる。そ
して、この樹脂圧が低くなって撹拌されながらスクリュ
ー先端方向へ搬送されるが、撹拌部33の拡大ガス含浸
ゾーン11を臨む位置に設けられたガス供給口52から
供給される炭酸ガスが拡大ガス含浸ゾーン11で溶融樹
脂と撹拌されて溶融樹脂中に含浸され発泡剤含浸溶融樹
脂となって計量部12に送られる。
Next, the molten resin sent to the stirring section 33 enters the expanded gas impregnation zone 11 in which the inner volume of the space between flights becomes large, and the third stirring blade 37 is in the same direction as the first stirring blade 35. Since the conveying speed is higher than that of the molten resin in the high-pressure resin forming section, the resin pressure becomes lower than that in the high-pressure resin forming section 32. Then, the resin pressure is lowered and the resin is conveyed to the screw tip direction while being stirred. In the impregnation zone 11, the molten resin is agitated and impregnated in the molten resin to form a foaming agent-impregnated molten resin, which is sent to the measuring section 12.

【0036】すなわち、ガス注入装置9を出た炭酸ガス
は、ガス配管91および注入口43を経てシールボック
ス4の凹溝41内に入り、凹溝41を臨む位置に開口す
るガス導入口51からガス供給路5内に入りガス供給口
52から拡大ガス含浸ゾーン11に供給され、拡大ガス
含浸ゾーン11内に充填された溶融樹脂に含浸させられ
る。
That is, the carbon dioxide gas that has flowed out of the gas injection device 9 enters the groove 41 of the seal box 4 through the gas pipe 91 and the gas inlet 43, and from the gas inlet 51 that opens at a position facing the groove 41. It enters into the gas supply path 5 and is supplied to the expanded gas impregnation zone 11 from the gas supply port 52, and is impregnated with the molten resin filled in the expanded gas impregnation zone 11.

【0037】そして、計量部12にガス含浸溶融樹脂が
送り込まれるに伴って、図1に示すように、スクリュー
3aは送られた樹脂量に応じて徐々に後退し、シリンダ
ー2の先端計量部12にて所定量のガス含浸溶融樹脂が
計量される。
Then, as the gas-impregnated molten resin is fed to the measuring section 12, the screw 3a is gradually retracted in accordance with the amount of the resin fed, as shown in FIG. At, a predetermined amount of gas-impregnated molten resin is measured.

【0038】このようにして、計量が終了したガス含浸
溶融樹脂はスクリュー3aを停止した状態で射出金型
(図示せず)内に射出され、発泡成形品が得られる。な
お、高圧樹脂形成部で高圧になった高圧樹脂は、射出が
完了するまで撹拌部33および計量部12の樹脂圧より
高い状態に保たれるようになっている。
In this way, the gas-impregnated molten resin whose metering has been completed is injected into an injection mold (not shown) with the screw 3a stopped, and a foamed molded product is obtained. The high-pressure resin having a high pressure in the high-pressure resin forming section is kept higher than the resin pressures of the stirring section 33 and the measuring section 12 until the injection is completed.

【0039】以上のように構成された射出成形機1aを
用いた成形方法によれば、スクリューの可塑化部31と
攪拌部33の間に、高圧樹脂形成部32設けるようにし
たので、高圧樹脂形成部32によって可塑化部31と撹
拌部33との間に撹拌部33の樹脂圧より高圧状態の樹
脂部が形成され、撹拌部33のガス含浸溶融樹脂の可塑
化部31側への逆流がこの高圧樹脂部によって防止され
る。しかも、高圧樹脂形成部32は、第2撹拌羽根36
を逆フライト構造にしただけであるので、高圧樹脂形成
部32でも樹脂が混練される。したがって、可塑化部3
1と撹拌部33との間にチェックリングを設けた場合に
比べ、射出成形機1aのスクリュー長さを短くしても樹
脂の混練を十分に行える。
According to the molding method using the injection molding machine 1a configured as described above, since the high-pressure resin forming portion 32 is provided between the plasticizing portion 31 and the stirring portion 33 of the screw, the high-pressure resin is formed. The forming portion 32 forms a resin portion between the plasticizing portion 31 and the agitating portion 33, which has a higher pressure than the resin pressure of the agitating portion 33. It is prevented by this high-pressure resin part. Moreover, the high-pressure resin forming portion 32 is provided with the second stirring blade 36.
Since only the reverse flight structure is used, the resin is kneaded also in the high-pressure resin forming section 32. Therefore, the plasticizing part 3
As compared with the case where a check ring is provided between the No. 1 and the stirring unit 33, the resin can be sufficiently kneaded even if the screw length of the injection molding machine 1a is shortened.

【0040】また、可塑化部31と撹拌部33との間に
チェックリングを設けないので、スクリューロッド30
が1本につながったものでよく、小口径の射出成形機の
場合もスクリュー強度に問題がない。したがって、小さ
な成形品の成形も可能となる。さらに、計量部12より
低圧の拡大ガス含浸ゾーン11部分で炭酸ガスを溶融樹
脂に含浸させるようにしたので、炭酸ガスの供給圧をそ
れほど高くしなくても短時間で均一に溶融樹脂中にガス
を含浸させることができる。すなわち、装置全体を耐圧
構造にする必要がなく、装置の製造コストを低減でき
る。
Since no check ring is provided between the plasticizing section 31 and the stirring section 33, the screw rod 30
It can be connected to one screw, and there is no problem in screw strength even in the case of small diameter injection molding machines. Therefore, it is possible to form a small molded product. Further, since the molten resin is impregnated with the carbon dioxide gas in the expanded gas impregnation zone 11 where the pressure is lower than that of the metering unit 12, the gas can be uniformly dispersed in the molten resin in a short time without increasing the supply pressure of the carbon dioxide gas so much. Can be impregnated. That is, it is not necessary to make the entire device a pressure resistant structure, and the manufacturing cost of the device can be reduced.

【0041】図5は、本発明に係る射出成形機の第2の
実施の形態を示すものである。図5に示すように、この
射出成形機1bは、スクリュー3bの高圧樹脂形成部3
2'の第2攪拌羽根36'がダルメージ型の攪拌羽根構造
をしている以外は、上記実施の形態と同様になってい
る。図6および図7は、本発明に係る射出成形機の第3
の実施の形態を示すものである。図6および図7に示す
ように、この射出成形機1cは、高圧樹脂形成部39
が、スクリュー3cの可塑化部31と攪拌部33との間
のフライト間でスクリューロッド30に堰39aを梯子
状に設けることによって形成されている以外は、上記の
実施の形態と同様になっている。
FIG. 5 shows a second embodiment of the injection molding machine according to the present invention. As shown in FIG. 5, the injection molding machine 1b includes a high-pressure resin forming section 3 of a screw 3b.
The second embodiment is the same as the above embodiment except that the second stirring blade 36 'of 2'has a dullage type stirring blade structure. 6 and 7 show the third embodiment of the injection molding machine according to the present invention.
FIG. As shown in FIGS. 6 and 7, the injection molding machine 1c includes a high-pressure resin forming section 39.
Is similar to the above embodiment except that it is formed by providing a weir 39a in a ladder shape on the screw rod 30 between the flights between the plasticizing part 31 and the stirring part 33 of the screw 3c. There is.

【0042】本発明は、上記の実施の形態に限定されな
い。たとえば、上記の実施の形態では、ガス供給路5が
1本であったが、複数本設け、各ガス供給路のガス導入
口を臨む部分に個別にシールボックスを設け、ガス供給
口へのガス供給経路を個別に設けるようにしても構わな
い。上記の実施の形態では、スクリューロッド30にそ
の内部を通るガス供給路5を設け、このガス供給路5を
介してシリンダー2内の溶融樹脂に炭酸ガスを供給する
ようにしたが、撹拌部を臨むシリンダーの壁面にガス供
給口を設け、このガス供給口からガスを供給するように
しても構わない。また、スクリューロッド側およびシリ
ンダー側の両側からガスを供給するようにしても構わな
い。
The present invention is not limited to the above embodiment. For example, in the above-described embodiment, the number of the gas supply path 5 is one, but a plurality of gas supply paths 5 are provided, and a seal box is individually provided at a portion facing the gas introduction port of each gas supply path, and the gas to the gas supply port is The supply paths may be individually provided. In the above-described embodiment, the screw rod 30 is provided with the gas supply passage 5 passing therethrough, and the carbon dioxide gas is supplied to the molten resin in the cylinder 2 through the gas supply passage 5, but the stirring portion is provided. A gas supply port may be provided on the wall surface of the facing cylinder, and gas may be supplied from this gas supply port. Further, the gas may be supplied from both sides of the screw rod side and the cylinder side.

【0043】[0043]

【発明の効果】本発明にかかる射出発泡成形方法は、以
上のように構成されているので、計量部のガス含浸溶融
樹脂の射出時の樹脂圧によって、可塑化部側への溶融樹
脂の逆流を確実に防止できるとともに、小型の成形品の
製造も可能である。しかも、スクリュー長さが短くても
十分に樹脂を混練でき、装置の小型化を図ることができ
る。
Since the injection foam molding method according to the present invention is configured as described above, the backflow of the molten resin to the plasticizing portion side is caused by the resin pressure at the time of injection of the gas-impregnated molten resin in the measuring portion. Can be reliably prevented and a small molded product can be manufactured. Moreover, the resin can be sufficiently kneaded even if the screw length is short, and the device can be downsized.

【0044】請求項3の成形方法によれば、シリンダー
を耐圧構造にする必要がなく、装置の小型化を図ること
ができる。請求項4の成形方法によれば、樹脂を劣化さ
せることなく良好な成形品を得ることができる。
According to the molding method of the third aspect, it is not necessary to make the cylinder a pressure resistant structure, and the size of the apparatus can be reduced. According to the molding method of the fourth aspect, a good molded product can be obtained without degrading the resin.

【0045】本発明にかかる射出成形機は、以上のよう
に構成されているので、小型の成形品の製造も可能であ
る。しかも、スクリュー長さが短くても十分に樹脂を混
練でき、装置の小型化を図ることができる。特に、請求
項8の成形機のようにすれば、シリンダーを耐圧構造に
する必要がなく、装置の小型化を図ることができる。
Since the injection molding machine according to the present invention is constructed as described above, it is possible to manufacture a small molded product. Moreover, the resin can be sufficiently kneaded even if the screw length is short, and the device can be downsized. In particular, if the molding machine according to the eighth aspect is used, it is not necessary to make the cylinder a pressure resistant structure, and the device can be downsized.

【0046】本発明のスクリューは、以上のようになっ
ているので、既存の射出成形機のシリンダーのセットす
るだけで、本発明の成形方法を実施することができる。
Since the screw of the present invention is as described above, the molding method of the present invention can be carried out only by setting the cylinder of the existing injection molding machine.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明にかかる射出成形機の第1の実施の形態
をあらわす断面図である。
FIG. 1 is a cross-sectional view showing a first embodiment of an injection molding machine according to the present invention.

【図2】図1の射出成形機の要部断面図である。FIG. 2 is a cross-sectional view of main parts of the injection molding machine of FIG.

【図3】図1の射出成形機のシールボックス部分の断面
図である。
3 is a cross-sectional view of a seal box portion of the injection molding machine of FIG.

【図4】図3のシールボックスのシール材をあらわし、
同図(a)はその正面図、同図(b)はその側面断面図
である。
FIG. 4 shows the seal material of the seal box of FIG.
The figure (a) is the front view, and the figure (b) is the side sectional view.

【図5】本発明にかかる射出成形機の第2の実施の形態
をあらわす要部断面図である。
FIG. 5 is a cross-sectional view of essential parts showing a second embodiment of the injection molding machine according to the present invention.

【図6】本発明にかかる射出成形機の第3の実施の形態
をあらわす要部断面図である。
FIG. 6 is a cross-sectional view of essential parts showing a third embodiment of an injection molding machine according to the present invention.

【図7】図6の要部拡大断面図である。FIG. 7 is an enlarged cross-sectional view of the main parts of FIG.

【符号の説明】[Explanation of symbols]

1a,1b,1c 射出成形機 12 計量部 2 シリンダー 3a,3b スクリュー 30 スクリューロッド 31 可塑化部 32,32',39 高圧樹脂形成部 33 撹拌部 35 第1撹拌羽根 36,36' 第2撹拌羽根 37 第3撹拌羽根 1a, 1b, 1c injection molding machine 12 Weighing department 2 cylinders 3a, 3b screw 30 screw rod 31 Plasticizing part 32, 32 ', 39 High-pressure resin forming part 33 Stirrer 35 First stirring blade 36,36 'Second stirring blade 37 Third stirring blade

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4F206 AB02 AB07 JA07 JD03 JM01 JN03 JN27    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4F206 AB02 AB07 JA07 JD03 JM01                       JN03 JN27

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】射出成形機のシリンダー内で、スクリュー
の回転によって、シリンダー内の可塑化部で可塑化され
溶融状態にされた溶融樹脂に、スクリューの撹拌部を臨
む位置でシリンダー内に易流動化剤および/または発泡
剤として作用するガスを供給して、シリンダー内で前記
ガスを溶融樹脂に混合し含浸させるガス含浸工程と、得
られたガス含浸溶融樹脂を計量した後に計量樹脂を金型
キャビティ内へ射出して成形品を得る射出成形工程とを
含む射出成形方法であって、スクリューの可塑化部と撹
拌部との間に、撹拌部の溶融樹脂圧力よりも溶融樹脂圧
力が高い高圧樹脂形成部を設け可塑化部側への溶融樹脂
の逆流を防止することを特徴とする射出成形方法。
1. A molten resin, which has been plasticized and melted in a plasticizing section in the cylinder by the rotation of the screw in the cylinder of an injection molding machine, flows easily into the cylinder at a position facing the stirring section of the screw. A gas impregnating step of supplying a gas acting as an agent and / or a foaming agent to mix and impregnate the molten resin with the molten resin in a cylinder, and weigh the obtained gas-impregnated molten resin, and then mold the measuring resin into a mold. An injection molding method including an injection molding step of injecting into a cavity to obtain a molded product, wherein the molten resin pressure is higher than the molten resin pressure of the stirring section between the plasticizing section of the screw and the stirring section. An injection molding method, characterized in that a resin forming portion is provided to prevent the molten resin from flowing back to the plasticizing portion side.
【請求項2】スクリューの可塑化部と撹拌部との間に、
その樹脂送り速度の絶対値が、可塑化部の樹脂送り速度
の絶対値より小さくなる撹拌羽根構造をした高圧樹脂形
成部を設ける請求項1に記載の射出成形方法。
2. Between the plasticizing section and the stirring section of the screw,
The injection molding method according to claim 1, wherein a high-pressure resin forming section having a stirring blade structure is provided in which the absolute value of the resin feed rate is smaller than the absolute value of the resin feed rate of the plasticizing section.
【請求項3】ガスをスクリューロッド内を通り、スクリ
ューの撹拌部に開口するガス供給路を介してシリンダー
内に供給する請求項1および請求項2に記載の射出成形
方法。
3. The injection molding method according to claim 1 or 2, wherein the gas is supplied into the cylinder through a screw rod and a gas supply passage opened to a stirring portion of the screw.
【請求項4】ガスが樹脂に対して非反応性ガスである請
求項1〜請求項3のいずれか1項に記載の射出成形方
法。
4. The injection molding method according to claim 1, wherein the gas is a non-reactive gas with respect to the resin.
【請求項5】スクリューがスクリューの回転によりシリ
ンダー内に供給された樹脂を溶融してシリンダー先端方
向に搬送する撹拌羽根を有する可塑化部と、可塑化部で
溶融状態になった溶融樹脂をさらに撹拌混練する撹拌部
とを備えるとともに、スクリューの撹拌部を臨む位置で
シリンダー内の溶融樹脂に易流動化剤および/または発
泡剤として作用するガスを供給するガス供給手段を備え
た射出成形機であって、スクリューが、その可塑化部と
撹拌部との間にその樹脂送り速度の絶対値が、可塑化部
の樹脂送り速度の絶対値より小さくなる撹拌羽根構造を
した高圧樹脂形成部を備えていることを特徴とする射出
成形機。
5. A plasticizing section having a stirring blade for the screw to melt the resin supplied into the cylinder by the rotation of the screw and convey the resin toward the tip of the cylinder, and a molten resin melted in the plasticizing section. An injection molding machine having a stirring section for stirring and kneading, and a gas supply means for supplying a gas acting as a freezing agent and / or a foaming agent to the molten resin in the cylinder at a position facing the stirring section of the screw. The screw is equipped with a high-pressure resin forming section having a stirring blade structure between the plasticizing section and the stirring section, in which the absolute value of the resin feeding rate is smaller than the absolute value of the resin feeding rate in the plasticizing section. An injection molding machine characterized in that
【請求項6】高圧樹脂形成部の撹拌羽根が、可塑化部の
撹拌羽根に対し逆フライト構造に形成されている請求項
5に記載の射出成形機。
6. The injection molding machine according to claim 5, wherein the stirring blade of the high-pressure resin forming portion is formed in a reverse flight structure with respect to the stirring blade of the plasticizing portion.
【請求項7】高圧樹脂形成部がダルメージ型の撹拌羽根
構造に形成されている請求項5または請求項6に記載の
射出成形機。
7. The injection molding machine according to claim 5, wherein the high-pressure resin forming portion is formed in a dullage-type stirring blade structure.
【請求項8】ガス供給手段がスクリュー後端に設けられ
たガス導入口からスクリュー内部を通りスクリューの撹
拌部壁面に開口するガス供給路を備えている請求項5〜
請求項7のいずれかに記載の射出成形機。
8. The gas supply means is provided with a gas supply passage that is opened from the gas inlet provided at the rear end of the screw through the inside of the screw to the wall surface of the stirring portion of the screw.
The injection molding machine according to claim 7.
【請求項9】スクリューの回転によりシリンダー内に供
給された樹脂を撹拌羽根によって溶融状態にしてシリン
ダー先端方向に搬送する撹拌羽根を有する可塑化部と、
可塑化部で溶融状態になった溶融樹脂をさらに撹拌羽根
によって撹拌混練する撹拌部と、可塑化部と撹拌部との
間に設けられ、可塑化部の樹脂送り速度の絶対値より小
さくなる撹拌羽根構造をした高圧樹脂形成部とを備える
スクリュー。
9. A plasticizing section having a stirring blade that melts the resin supplied into the cylinder by the rotation of the screw by the stirring blade and conveys the resin toward the tip of the cylinder.
A stirring unit that stirs and kneads the molten resin that has become molten in the plasticizing unit with stirring blades, and stirring that is provided between the plasticizing unit and the stirring unit and that is smaller than the absolute value of the resin feeding speed of the plasticizing unit. A screw provided with a high-pressure resin forming part having a blade structure.
【請求項10】スクリュー後端に設けられたガス導入口
からスクリューロッド内部を通りスクリューの撹拌部壁
面に開口するガス供給路を備えている請求項9に記載の
スクリュー。
10. The screw according to claim 9, further comprising a gas supply passage which is provided at a rear end of the screw, passes through the inside of the screw rod, and opens to a wall surface of a stirring portion of the screw.
JP2001241052A 2001-08-08 2001-08-08 Injection molding method, injection molding machine used for the same and screw of injection molding machine Withdrawn JP2003048239A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001241052A JP2003048239A (en) 2001-08-08 2001-08-08 Injection molding method, injection molding machine used for the same and screw of injection molding machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001241052A JP2003048239A (en) 2001-08-08 2001-08-08 Injection molding method, injection molding machine used for the same and screw of injection molding machine

Publications (1)

Publication Number Publication Date
JP2003048239A true JP2003048239A (en) 2003-02-18

Family

ID=19071567

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2003048239A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005074794A (en) * 2003-08-29 2005-03-24 Mitsui Chemicals Inc Apparatus for molding foamed thermoplastic resin composition molding
JP2009166463A (en) * 2008-01-21 2009-07-30 Toyo Mach & Metal Co Ltd Gas foam injection molding machine

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000334764A (en) * 1999-05-25 2000-12-05 Sekisui Chem Co Ltd Injection molding method and apparatus for thermoplastic resin molded article
JP2001001379A (en) * 1999-06-18 2001-01-09 Japan Steel Works Ltd:The Plasticizing device for molding thermoplastic resin foam
JP2001150504A (en) * 1999-12-01 2001-06-05 Japan Steel Works Ltd:The Method and apparatus for forming cellular plastic resin

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000334764A (en) * 1999-05-25 2000-12-05 Sekisui Chem Co Ltd Injection molding method and apparatus for thermoplastic resin molded article
JP2001001379A (en) * 1999-06-18 2001-01-09 Japan Steel Works Ltd:The Plasticizing device for molding thermoplastic resin foam
JP2001150504A (en) * 1999-12-01 2001-06-05 Japan Steel Works Ltd:The Method and apparatus for forming cellular plastic resin

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005074794A (en) * 2003-08-29 2005-03-24 Mitsui Chemicals Inc Apparatus for molding foamed thermoplastic resin composition molding
JP2009166463A (en) * 2008-01-21 2009-07-30 Toyo Mach & Metal Co Ltd Gas foam injection molding machine

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