JP2002307499A - Method and equipment for injection-molding thermoplastic resin molded product - Google Patents

Method and equipment for injection-molding thermoplastic resin molded product

Info

Publication number
JP2002307499A
JP2002307499A JP2001108843A JP2001108843A JP2002307499A JP 2002307499 A JP2002307499 A JP 2002307499A JP 2001108843 A JP2001108843 A JP 2001108843A JP 2001108843 A JP2001108843 A JP 2001108843A JP 2002307499 A JP2002307499 A JP 2002307499A
Authority
JP
Japan
Prior art keywords
foaming agent
screw
blowing agent
injection molding
agent supply
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Withdrawn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
JP2001108843A
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 JP2001108843A priority Critical patent/JP2002307499A/en
Publication of JP2002307499A publication Critical patent/JP2002307499A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for injection-molding a thermoplastic resin molded product capable of stably and continuously supplying a foaming agent, especially non-reactive gas such as carbon dioxide, nitrogen gas or the like to a thermoplastic resin under lower pressure to infiltrate the same into the thermoplastic resin in large quantities, and an injection molding equipment using the method. SOLUTION: The foaming agent sent into the foaming agent supply passage 5a, which is provided in a screw 3a from the rear end of the screw 3a to the front end thereof, from the rear end of the screw 3a is supplied to the molten resin from a plurality of the foaming agent supply ports 52 opened in the outer peripheral surface of the screw 3a in a cylinder 2 to be infiltrated into the molten resin.

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、熱可塑性樹脂成形
品の射出成形方法および射出成形装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for injection molding a thermoplastic resin molded article.

【0002】[0002]

【従来の技術】発泡剤となる二酸化炭素ガスや窒素ガス
などの非反応性ガスを射出される溶融樹脂中に含浸さ
せ、非反応性ガス含浸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(米国特許5158986号参照)などが公知である。
2. Description of the Related Art Thermoplastic resin in which a non-reactive gas such as carbon dioxide gas or nitrogen gas as a foaming agent is impregnated into a molten resin to be injected, and the non-reactive gas impregnated resin is injected into a mold and foamed. As a method of injection molding of a foam, 1) a method in which a non-reactive gas is previously impregnated with a non-reactive gas under a high pressure into a solid-state raw material resin before being charged into a cylinder; A method of impregnating with a reactive gas (see US Pat. No. 5,158,986) is known.

【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 non-reactive gas into a raw material resin in a solid state, it is possible to obtain a thermoplastic resin foam, but in order to impregnate the non-reactive gas, for example, a molding machine is used. Since it is necessary to stop supplying the resin to the chamber and 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 implement industrially.

【0004】一方、従来のシリンダー内で溶融状態の樹
脂に非反応性ガスを含浸させる後者の方法は、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、
シリンダー内のスクリューの回転により溶融するととも
に、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、シリンダーの一か所に設け
られたガス供給口からシリンダー内へ非反応性ガスを供
給するようになっている。したがって、高圧状態の計量
中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。しかも、高圧ガスを用い
るには、装置自体を高圧ガスに耐える耐圧構造にしなけ
ればならず製造コストが増大するという問題がある。
[0004] On the other hand, the conventional method of impregnating a resin in a molten state with a non-reactive gas in a cylinder is based on resin pellets or the like supplied from a raw material supply port into the cylinder.
While melting by rotation of the screw in the cylinder, while the screw is retracted and the molten resin is measured at the tip measuring section of the cylinder, non-reactive gas enters the cylinder from the gas supply port provided in one place of the cylinder It is designed to supply gas. Therefore, since the non-reactive gas is supplied to the molten resin being measured in the high pressure state, it is difficult to inject the gas into the molten resin unless the pressure of the supply gas is higher than the pressure of the molten resin. In addition, the use of a high-pressure gas has a problem in that the apparatus itself must have a pressure-resistant structure capable of withstanding the high-pressure gas, thereby increasing the manufacturing cost.

【0005】そこで、本発明の発明者らは、非反応性ガ
スを比較的低圧でシリンダー内の樹脂に安定的にかつ連
続的に含浸させることができる方法として、射出成形機
のシリンダー内にてスクリュー回転によって溶融状態に
なった計量部に達する前の樹脂圧の低い溶融樹脂に、非
反応性ガス等の発泡剤をスクリューの後端部から前端方
向に向かってスクリュー内部に設けられた発泡剤供給路
の、シリンダー内でスクリュー外周面に開口する発泡剤
供給口より非反応性ガスを溶融樹脂に供給し、発泡剤を
溶融樹脂に含浸させたのちの発泡剤含浸樹脂を計量部で
計量して射出する方法を既に提案している(特願200
0−70724号)。
The inventors of the present invention have proposed a method for stably and continuously impregnating a resin in a cylinder with a non-reactive gas at a relatively low pressure by using a method in an injection molding machine cylinder. A foaming agent, such as a non-reactive gas, is provided inside the screw from the rear end to the front end of the screw in the molten resin having a low resin pressure before reaching the measuring section in a molten state by the rotation of the screw. A non-reactive gas is supplied to the molten resin from a foaming agent supply port opened in the outer peripheral surface of the screw in the cylinder in the supply path, and the foaming agent-impregnated resin after impregnating the foaming agent into the molten resin is measured by the measuring unit. Has already proposed a method of injecting (Japanese Patent Application 200)
0-70724).

【0006】しかし、先に発明者らが提案した方法にお
いても、発泡剤供給口が1つであるため発泡剤の含浸速
度に従来の方法よりは低圧にできても含浸速度を上げる
にはある程度ガス圧を上げざるを得ず、完全な改善には
到っていない。
However, even in the method proposed by the present inventors, since the number of the blowing agent supply ports is one, even if the impregnation rate of the blowing agent can be made lower than that of the conventional method, it is necessary to increase the impregnation rate to some extent. The gas pressure had to be increased and the improvement had not been completed.

【0007】[0007]

【発明が解決しようとする課題】本発明の目的は、発泡
剤、特に二酸化炭素ガスや窒素ガスなどの非反応性ガス
をより低圧で熱可塑性樹脂に安定的かつ連続的に供給
し、大量に含浸させることができる、熱可塑性樹脂成形
品の射出成形方法、及びこの方法を用いる射出成形装置
を提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to supply a blowing agent, particularly a non-reactive gas such as a carbon dioxide gas or a nitrogen gas, to a thermoplastic resin stably and continuously at a lower pressure and to produce a large amount of the same. An object of the present invention is to provide an injection molding method of a thermoplastic resin molded article which can be impregnated, and an injection molding apparatus using the method.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
に、本発明の請求項1に係る熱可塑性樹脂成形品の射出
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にてスクリュー回転によって
溶融状態になった溶融樹脂に、発泡剤供給口から発泡剤
を供給して、発泡剤を溶融樹脂に混合し含浸させる発泡
剤含浸工程と、得られた発泡剤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発泡成形品
を得る射出成形工程とを含む熱可塑性樹脂成形品の射出
成形方法であって、スクリューの後端部から前端方向に
向かってスクリュー内部に設けられた発泡剤供給路の、
シリンダー内でスクリュー外周面に開口する複数の発泡
剤供給口よりスクリューの後端部から発泡剤供給路に送
り込まれた前記発泡剤を溶融樹脂に供給し、発泡剤を溶
融樹脂に含浸させるようにした。
Means for Solving the Problems In order to achieve the above object, an injection molding method for a thermoplastic resin molded product according to the first aspect of the present invention (hereinafter referred to as "the molding method of the first aspect") is as follows.
A foaming agent impregnating step of supplying a foaming agent from a foaming agent supply port to a molten resin melted by a screw rotation in a cylinder of an injection molding machine, and mixing and impregnating the foaming agent with the molten resin; An injection molding step of injecting the measured resin into the mold cavity after measuring the blowing agent-impregnated molten resin to obtain a foamed molded product, wherein the rear end of the screw Of the blowing agent supply path provided inside the screw from the front end direction,
The foaming agent fed into the foaming agent supply path from the rear end of the screw through a plurality of foaming agent supply ports opened to the screw outer peripheral surface in the cylinder is supplied to the molten resin, and the foaming agent is impregnated in the molten resin. did.

【0009】本発明の請求項2に係る熱可塑性樹脂成形
品の射出成形方法(以下、「請求項2の成形方法」と記
す)は、請求項1の成形方法において、発泡剤をスクリ
ュー軸の前後方向にずれた位置に設けられた複数の発泡
剤供給口から供給するようにした。
According to a second aspect of the present invention, there is provided an injection molding method for a thermoplastic resin molded article (hereinafter referred to as a “method of the second aspect”). The foaming agent was supplied from a plurality of blowing agent supply ports provided at positions shifted in the front-rear direction.

【0010】本発明の請求項3に係る熱可塑性樹脂成形
品の射出成形方法(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、
発泡剤を個別の発泡剤供給路を経た各発泡剤供給口から
供給するようにした。
According to a third aspect of the present invention, there is provided a method for injection-molding a thermoplastic resin article (hereinafter referred to as a “third molding method”) according to the first or second aspect.
The blowing agent was supplied from each blowing agent supply port via a separate blowing agent supply passage.

【0011】本発明の請求項4に係る熱可塑性樹脂成形
品の射出成形方法(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、発泡剤として熱可塑性樹脂に対する非反応性ガス
を用いるようにした。
According to a fourth aspect of the present invention, an injection molding method for a thermoplastic resin molded article (hereinafter, referred to as “a molding method according to a fourth aspect”) is a method according to any one of the first to third aspects. A non-reactive gas for the thermoplastic resin is used as a foaming agent.

【0012】本発明の請求項5に係る熱可塑性樹脂成形
品の射出成形装置(以下、「請求項5の成形装置」と記
す)は、スクリューの後端部から前端方向に向かってス
クリュー内部に設けられた発泡剤供給路の、シリンダー
内でスクリュー外周面に開口する発泡剤供給口よりスク
リューの後端部から発泡剤供給路に送り込まれた前記発
泡剤を溶融樹脂に供給し、発泡剤を溶融樹脂に含浸させ
たのちの発泡剤含浸樹脂が計量部で計量されて射出され
るようになっている射出成形装置であって、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発泡剤含浸ゾーンを形成する拡大発
泡剤含浸ゾーン形成部がスクリューの先端近くに設けら
れ、拡大発泡剤含浸ゾーン形成部に発泡剤供給口が複数
個開口している構成とした。
According to a fifth aspect of the present invention, there is provided an injection molding apparatus for a thermoplastic resin molded article (hereinafter referred to as a "molding apparatus of the fifth aspect"). In the provided foaming agent supply path, the foaming agent fed into the foaming agent supply path from the rear end of the screw from the foaming agent supply port opening to the screw outer peripheral surface in the cylinder is supplied to the molten resin, and the foaming agent is supplied. An injection molding apparatus in which the blowing agent-impregnated resin after being impregnated into the molten resin is weighed and injected by the measuring section, and the pitch of the front and rear screw flights is increased,
And / or, by the screw shaft diameter is made smaller, the expanded foaming agent impregnated zone forming portion forming an expanded foaming agent impregnated zone having a larger internal volume in the inter-flight space than the inter-flight space is closer to the tip of the screw. , And a plurality of foaming agent supply ports are opened in the enlarged foaming agent impregnation zone forming portion.

【0013】本発明の請求項6に係る熱可塑性樹脂成形
品の射出成形装置(以下、「請求項6の成形装置」と記
す)は、請求項5の成形装置において、少なくとも1つ
の発泡剤供給口が他の発泡剤供給口に対しスクリュー軸
の前後方向にずれた位置に設けられている構成とした。
According to a sixth aspect of the present invention, an injection molding apparatus for a thermoplastic resin molded article (hereinafter referred to as a “molding apparatus of the sixth aspect”) is a molding apparatus of the fifth aspect, wherein at least one foaming agent is supplied. The port was provided at a position shifted in the front-rear direction of the screw shaft with respect to the other blowing agent supply ports.

【0014】本発明の請求項7に係る熱可塑性樹脂成形
品の射出成形装置(以下、「請求項7の成形装置」と記
す)は、請求項5または請求項6の成形装置において、
スクリュー内に互いに隔絶された複数の発泡剤供給路を
備え、各発泡剤供給路ごとに発泡剤供給口を備えている
構成とした。
According to a seventh aspect of the present invention, there is provided an injection molding apparatus for a thermoplastic resin molded article (hereinafter referred to as a “molding apparatus of the seventh aspect”).
A plurality of foaming agent supply paths separated from each other were provided in the screw, and a foaming agent supply port was provided for each foaming agent supply path.

【0015】本発明の請求項8に係る熱可塑性樹脂成形
品の射出成形装置(以下、「請求項8の成形装置」と記
す)は、請求項7の成形装置において、少なくとも1つ
の発泡剤供給路の一部が、他の発泡剤供給路の内部を貫
通するパイプ状に設けられている構成とした。
An injection molding apparatus for a thermoplastic resin molded product according to claim 8 of the present invention (hereinafter referred to as “molding apparatus of claim 8”) is a molding apparatus according to claim 7, wherein at least one foaming agent is supplied. A part of the passage was provided in a pipe shape penetrating the inside of another blowing agent supply passage.

【0016】本発明の射出成形方法において、発泡剤供
給口の位置は、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であれ
ば、特に限定されないが、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。
In the injection molding method of the present invention, the position of the blowing agent supply port is not particularly limited as long as the pressure of the molten resin is lower at the rear end side of the screw tip than at the measuring section. However, a portion where the molten resin is not yet completely filled between the screw and the cylinder is preferable.

【0017】例えば、請求項5の成形装置のように、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発泡剤含浸ゾーンを形成す
る拡大発泡剤含浸ゾーン形成部がスクリューの先端近く
に設けられた構造とするとともに、スクリューのこの拡
大発泡剤含浸ゾーン形成部に発泡剤供給口を開口させる
ようにすることが好ましく、この拡大発泡剤含浸ゾーン
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, when the pitch of the front and rear screw flights is increased and / or the screw shaft diameter is reduced as in the molding apparatus of claim 5, the space between the front and rear flights is set in the inter-flight space. The expanded foaming agent impregnated zone forming part which forms an expanded foaming agent impregnated zone having a larger internal volume than the space is provided near the tip of the screw, and the blowing agent is supplied to this expanded foaming agent impregnated zone forming part of the screw. It is preferable to open the mouth, and it is more preferable to open the mouth at a position facing the non-resin-filled portion near the front flight in the expanded foaming agent impregnation zone.

【0018】また、スクリューの発泡剤供給路には、発
泡剤供給口近傍に発泡剤供給口からスクリュー内の発泡
剤供給路への溶融樹脂の入り込みを防ぐ樹脂逆流防止弁
が設けられているようにしても構わない。
In the blowing agent supply path of the screw, a resin check valve is provided near the blowing agent supply port to prevent molten resin from entering the blowing agent supply path from the blowing agent supply port into the screw. It does not matter.

【0019】樹脂逆流防止弁としては、発泡剤圧力が溶
融樹脂圧力より大きくなった場合に開くものであれば、
特に限定されないが、例えば、発泡剤非供給時に、弁が
スプリング力で閉鎖されており、発泡剤供給路からの導
入発泡剤圧力がスプリングの付勢力より大のときに弁が
開いて、発泡剤供給口よりシリンダー内へ発泡剤が供給
され、溶融樹脂が発泡剤供給口から逆流しようとすると
スプリングの付勢力で弁が閉じ、発泡剤供給路への進入
(逆流)が防止されるばね式やボールチェック式のもの
など動作が確実なものが好ましいが、溶融樹脂の圧力を
検出し、予め設定された発泡剤圧力より溶融樹脂圧力が
低くなった場合に開く電磁バルブでも構わない。
As the resin check valve, if it opens when the pressure of the blowing agent becomes higher than the pressure of the molten resin,
Although not particularly limited, for example, when the blowing agent is not supplied, the valve is closed by a spring force, and when the pressure of the blowing agent introduced from the blowing agent supply passage is larger than the urging force of the spring, the valve opens, and the blowing agent is opened. When the foaming agent is supplied from the supply port into the cylinder and the molten resin tries to flow backward from the foaming agent supply port, the valve is closed by the biasing force of the spring, and a spring type that prevents entry into the foaming agent supply path (backflow) or Although it is preferable to use a ball check type or the like that ensures operation, an electromagnetic valve that detects the pressure of the molten resin and opens when the pressure of the molten resin becomes lower than a predetermined foaming agent pressure may be used.

【0020】なお、樹脂逆流防止弁の材質は200℃以
上の耐熱性を有するものであれば特定されるものではな
いが、強度、耐熱性、摺動性、加工性の面から金属、特
にステンレス鋼が好ましい。
The material of the resin check valve is not specified as long as it has a heat resistance of 200 ° C. or higher. However, from the viewpoints of strength, heat resistance, slidability and workability, metals, especially stainless steel, are used. Steel is preferred.

【0021】本発明に使用される熱可塑性樹脂は特に限
定されないが、たとえば、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 thermoplastic resin used in the present invention is not particularly limited. Examples thereof include a resin having a high melt viscosity, which is difficult to melt-mold, a resin which is easily decomposed by heat, an additive having a low boiling point or an additive which is easily decomposed by heat. And the like.

【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 resins that are difficult to melt-mold because of their high melt viscosities include resins for engineering plastics such as ultrahigh molecular weight polyethylene, ultrahigh polymerization degree polyvinyl chloride, polytetrafluoroethylene, and polyimide.

【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。
Examples of resins that are easily thermally decomposed include biodegradable resins such as polylactic acid and polyhydroxybutyrate, and polyvinyl chloride and polyacrylonitrile having a high degree of chlorination.

【0024】本発明で用いられる発泡剤は、樹脂と反応
を起こさず、さらに樹脂を劣化させるなどの悪影響を樹
脂に与えないものであれば特に限定されないが、請求項
4のように成形しようとする樹脂に対して非反応性ガス
が好ましく、たとえば、二酸化炭素、窒素、アルゴン、
ネオン、ヘリウム、酸素等の無機系ガス、フロン、低分
子量の炭化水素などの有機系ガスが挙げられる。
The foaming agent used in the present invention is not particularly limited as long as it does not react with the resin and does not adversely affect the resin such as deteriorating the resin. Non-reactive gases are preferred for the resin to be used, for example, carbon dioxide, nitrogen, argon,
Examples include inorganic gases such as neon, helium, and oxygen, and organic gases such as chlorofluorocarbon and low molecular weight hydrocarbons.

【0025】これらのうち、環境に与える悪影響が低
く、そしてガスの回収が必要でない点で無機ガスが好ま
しく、難成形樹脂に対する溶解度が高く、樹脂の溶融効
果が大きく、そして直接大気中に放出してもほとんど害
がないという観点から、二酸化炭素ガスがより好まし
い。なお、発泡剤は、単独で用いてもよく、あるいは2
種類以上のガスを併用してもよい。
Of these, inorganic gases are preferred in that they have a low adverse effect on the environment and do not require gas recovery, have high solubility in difficult-to-mold resins, have a high melting effect for resins, and are directly released into the atmosphere. Carbon dioxide gas is more preferable from the viewpoint that there is almost no harm. The blowing agent may be used alone, or 2
More than one type of gas may be used in combination.

【0026】[0026]

【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
に係る射出成形装置の第1の実施の形態を示すものであ
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below.
This will be described in detail with reference to the drawings. 1 to 4 show a first embodiment of an injection molding apparatus according to the present invention.

【0027】図1に示すように、射出成形装置Aは、射
出成形機1と、これに発泡剤としてのガスを送るガス注
入装置9とからなる。
As shown in FIG. 1, the injection molding apparatus A comprises an injection molding machine 1 and a gas injection device 9 for feeding a gas as a foaming agent thereto.

【0028】射出成形機1は、図1〜図3に示すよう
に、シリンダー2と、その内部に配されたスクリュー3
aと、シールボックス4とから主に構成され、他の部分
より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発泡剤含
浸ゾーン11がシリンダー2とスクリュー3aとの間に
形成されるようになっている。図1中、12は計量部、
13は樹脂供給ホッパー、14はユニット、15はシー
ルボックス4の接続アームである。拡大発泡剤含浸ゾー
ン11は、図2および図3に示すように、スクリュー3
aの先端(下流端)近く(先端からやや後端寄り、すな
わちホッパー寄り)に拡大発泡剤含浸ゾーン形成部31
が設けられることによって形成されるようになってい
る。
As shown in FIGS. 1 to 3, the injection molding machine 1 includes a cylinder 2 and a screw 3 arranged inside the cylinder.
and an expansion foaming agent impregnated zone 11 mainly composed of a seal box 4 and having a larger inter-flight space volume than other parts and a higher resin feeding speed than the upstream side. It is formed between the screw 3a. In FIG. 1, 12 is a measuring section,
13 is a resin supply hopper, 14 is a unit, and 15 is a connection arm of the seal box 4. As shown in FIGS. 2 and 3, the expanded blowing agent impregnation zone 11
a near the front end (downstream end) of (a) (slightly near the rear end from the front end, that is, near the hopper);
Are formed by being provided.

【0029】すなわち、拡大発泡剤含浸ゾーン形成部3
1は、スクリュー3aの他の部分より、スクリュー溝が
深くなされ、且つ、前後スクリューフライト間のピッチ
が大きくなされることによってシリンダー2との間に拡
大発泡剤含浸ゾーン11を形成するようになっている。
また、スクリュー3aは、内部に発泡剤供給路5aを備
えている。
That is, the expanded foaming agent impregnated zone forming section 3
1 is such that the screw groove is made deeper than the other part of the screw 3a, and the pitch between the front and rear screw flights is made larger so that the expanded foaming agent impregnation zone 11 is formed with the cylinder 2; I have.
The screw 3a has a foaming agent supply passage 5a inside.

【0030】発泡剤供給路5a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つの発泡剤導入口51と、拡大発泡剤含浸ゾーン
形成部31の外壁面に前後に1対ずつずれて開口する4
つの発泡剤供給口52と、発泡剤供給口52の近傍に、
発泡剤供給口52からの溶融樹脂の逆流を防止するばね
式の逆流防止弁7とを備えている。
As shown in FIGS. 2 to 4, the foaming agent supply passage 5a has one foaming agent introduction port 51 opened on the outer wall surface on the screw rear end outside the cylinder 2 and an expanded foaming agent impregnation zone forming portion 31. 4 open one pair on the outer wall of
Two blowing agent supply ports 52, and in the vicinity of the blowing agent supply port 52,
A spring-type check valve 7 for preventing the backflow of the molten resin from the blowing agent supply port 52 is provided.

【0031】逆流防止弁7は、通常、弁本体71がスプ
リング72によって閉弁方向(図3の矢印X方向)に付
勢されて閉じられていて発泡剤供給路5a側に溶融樹脂
が流入しないようになっているが、発泡剤供給路5aに
ガスが供給されて来ると、発泡剤圧力のよって弁本体7
1がスプリング8の付勢力に抗して開弁方向(図3の矢
印Xと逆方向)に移動するようになっている。すなわ
ち、発泡剤が逆流防止弁7を通過し、更に発泡剤供給口
52を経て、拡大発泡剤含浸ゾーン11の溶融樹脂に供
給されるようになっている。
Normally, the check valve 7 is closed by the valve body 71 being urged by a spring 72 in the valve closing direction (the direction of arrow X in FIG. 3) so that the molten resin does not flow into the blowing agent supply passage 5a. However, when gas is supplied to the blowing agent supply passage 5a, the valve body 7
1 moves in the valve opening direction (the direction opposite to the arrow X in FIG. 3) against the urging force of the spring 8. That is, the blowing agent is supplied to the molten resin in the expanded blowing agent impregnation zone 11 through the check valve 7 and further through the blowing agent supply port 52.

【0032】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,発泡剤導入口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の発泡剤導入
口51形成部分を囲繞している。また、シールボックス
4は、発泡剤導入口51が臨む位置にリング状の凹溝4
1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 is fixed to the drive unit 14 of the injection molding machine 1 by a connection arm 15 so that the position of the seal box 4 does not shift with respect to the forward and backward rotation and rotation of the screw 3a. 3a surrounds the portion where the foaming agent introduction port 51 is formed. The seal box 4 has a ring-shaped groove 4 at a position facing the foaming agent introduction port 51.
1, and a pair of seal members 42 are provided so as to elastically contact the screw peripheral surface so as to sandwich the concave groove 41 from both front and rear sides of the screw 3a and to prevent gas leakage from inside the concave groove 41. .

【0033】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
される発泡剤としての二酸化炭素ガスの注入口43が穿
設されている。
In the groove 41 of the seal box 4,
An injection port 43 for carbon dioxide gas as a foaming agent injected from a gas injection device 9 opened outside the seal box 4 is provided.

【0034】シリンダー2は、スクリュー3aの回転停
止時にシリンダー2内のガス含浸溶融樹脂がガス圧力に
より樹脂供給ホッパー13側へ逆流することを防止する
ために、図4に示すように、スクリュー3aの拡大発泡
剤含浸ゾーン形成部31からやや後端寄りに、チェック
リング21が取り付けられている。チェックリング21
は、特に、発泡剤供給口52からのガス圧力が高いとき
に、樹脂の逆流防止に好適に用いられる。また、シリン
ダー2の先端には、図1に示すように、シャットオフ弁
24が設けられている。
When the rotation of the screw 3a is stopped, the cylinder 2 prevents the gas-impregnated molten resin in the cylinder 2 from flowing back to the resin supply hopper 13 due to the gas pressure, as shown in FIG. A check ring 21 is attached slightly to the rear end from the expanded foaming agent impregnation zone forming portion 31. Check ring 21
Is preferably used to prevent the resin from flowing back, especially when the gas pressure from the blowing agent supply port 52 is high. A shut-off valve 24 is provided at the tip of the cylinder 2 as shown in FIG.

【0035】射出成形装置A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。溶融混練された樹脂はチェック
リング21を経て圧力開放部、即ち、拡大発泡剤含浸ゾ
ーン11へ送られる。
Since the injection molding apparatus A is configured as described above, when the raw resin is supplied from the hopper 13 into the cylinder 2 through the raw material supply port, the raw resin is melted and kneaded by the rotation of the screw 3a. Cylinder 2
Is sent toward the tip. The melt-kneaded resin is sent through the check ring 21 to the pressure release section, that is, the expanded foaming agent impregnation zone 11.

【0036】一方、ガス注入装置9を出たガスは、導入
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発泡剤導
入口51からガス供給路5a内に入り逆流防止弁7を経
て4つの発泡剤供給口52から拡大発泡剤含浸ゾーン1
1に供給され、拡大発泡剤含浸ゾーン11内に充填され
た溶融樹脂に含浸させられる。
On the other hand, the gas that has exited the gas injection device 9 enters the groove 41 of the seal box 4 via the introduction pipe 91 and the injection port 43, and from the blowing agent introduction port 51 opening at a position facing the groove 41. The expanded foaming agent impregnated zone 1 enters the gas supply passage 5a and enters the four blowing agent supply ports 52 through the check valve 7.
1 and is impregnated with the molten resin filled in the expanded foaming agent impregnation zone 11.

【0037】そして、溶融樹脂が続けて送られて来るに
伴って拡大発泡剤含浸ゾーン11で二酸化炭素ガスが含
浸された発泡剤含浸溶融樹脂がシリンダー2の先端の計
量部に送られる。計量部12に発泡剤含浸溶融樹脂が送
り込まれるに伴って、図1に示すように、スクリュー3
a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にて所定量の発泡剤含浸溶融樹脂が
計量される。
Then, as the molten resin is continuously sent, the blowing agent-impregnated molten resin impregnated with carbon dioxide gas in the expanded foaming agent impregnation zone 11 is sent to the measuring section at the tip of the cylinder 2. As the blowing agent-impregnated molten resin is fed into the measuring section 12, as shown in FIG.
“a” gradually retreats in accordance with the amount of the fed resin, and a predetermined amount of the molten resin impregnated with the blowing agent is measured by the tip measuring section 12 of the cylinder 2.

【0038】このようにして、計量が終了したガス含浸
溶融樹脂は射出金型(図示せず)内に射出され、発泡成
形品が得られる。
In this way, the gas-impregnated molten resin that has been measured is injected into an injection mold (not shown) to obtain a foam molded product.

【0039】以上のように構成された射出成形装置Aを
用いた成形方法によれば、計量部12より低圧の拡大発
泡剤含浸ゾーン11部分で二酸化炭素ガスを溶融樹脂に
含浸させるようにしたので、二酸化炭素ガスの供給圧を
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。しかも、複数の発泡剤供
給口52から供給するようにしたので、単数の発泡剤供
給口から供給する場合よりも溶融樹脂との接触面積が増
大し、より短時間で二酸化炭素ガスを含浸させることが
できる。その結果、高い生産性をもって、均質で微細な
発泡成形体を提供することができる。
According to the molding method using the injection molding apparatus A configured as described above, the molten resin is impregnated with the carbon dioxide gas in the expanded foaming agent impregnation zone 11 at a lower pressure than the measuring section 12. Even if the supply pressure of the carbon dioxide gas is not so high, the molten resin can be uniformly impregnated with the gas in a short time. In addition, since the gas is supplied from the plural foaming agent supply ports 52, the contact area with the molten resin is increased as compared with the case where the gas is supplied from a single foaming agent supply port, and the carbon dioxide gas can be impregnated in a shorter time. Can be. As a result, a uniform and fine foamed molded article can be provided with high productivity.

【0040】また、上記射出成形装置Aは、スクリュー
3aの先端近くに、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、および、スクリュー軸径が小さく
なされることによって、前後フライト間空間にこれより
後端側のフライト間空間よりも内容積が大きい溶融樹脂
が低圧で非充満状態になるようにするとともに、スクリ
ュー3a内に設けられた発泡剤供給路5aの発泡剤供給
口52を拡大発泡剤含浸ゾーン11に臨むように設けた
ので、二酸化炭素ガスの供給をスクリュー3a部分で行
なえるとともに、より低圧で効率よく溶融樹脂に含浸さ
せることができ、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。
In addition, the injection molding apparatus A is arranged such that the pitch of the front and rear screw flights is increased near the tip of the screw 3a and the diameter of the screw shaft is reduced, so that the space between the front and rear flights is increased. The molten resin having an inner volume larger than the inter-flight space at the end side is made to be in a non-filled state at a low pressure, and the blowing agent supply port 52 of the blowing agent supply path 5a provided in the screw 3a is impregnated with an expanded blowing agent. Since it is provided so as to face the zone 11, the supply of carbon dioxide gas can be performed at the screw 3a portion, and the molten resin can be impregnated with the molten resin more efficiently at a lower pressure. Manufacturing cost can be reduced.

【0041】また、発泡剤供給路5aの発泡剤供給口5
2の近傍に、発泡剤供給口52からの溶融樹脂の逆流を
防止するばね式の逆流防止弁7を設けたので、よりガス
圧を低く設定することができる。
The blowing agent supply port 5 of the blowing agent supply passage 5a
Since the spring-type check valve 7 for preventing the backflow of the molten resin from the foaming agent supply port 52 is provided in the vicinity of 2, the gas pressure can be set lower.

【0042】図5は、本発明に係る射出成形装置の第2
の実施の形態を示すものである。図5に示すように、こ
の射出成形装置Bは、スクリュー3b内に2本の発泡剤
供給路5b,5cが設けられていて、両発泡剤供給路5
b,5cの発泡剤導入口51が同じシールボックス4の
凹溝41を臨む位置に開口し、一方の発泡剤供給路5b
の発泡剤供給口52と他方の発泡剤供給路5cの発泡剤
供給口52とが拡大発泡剤含浸ゾーン11の前後方向に
ずれた位置に開口している以外は上記射出成形装置Aと
同様になっている。
FIG. 5 shows a second embodiment of the injection molding apparatus according to the present invention.
1 shows an embodiment of the present invention. As shown in FIG. 5, this injection molding apparatus B has two blowing agent supply paths 5b and 5c in a screw 3b.
The foaming agent introduction ports 51 b and 5 c open at positions facing the concave groove 41 of the same seal box 4, and one of the foaming agent supply paths 5 b
In the same manner as the injection molding apparatus A, except that the blowing agent supply port 52 and the blowing agent supply port 52 of the other blowing agent supply passage 5c are opened at positions shifted in the front-rear direction of the expanded blowing agent impregnation zone 11. Has become.

【0043】すなわち、この射出成形装置Bを用いた成
形方法によれば、各発泡剤供給口52が個別の発泡剤供
給路5b(5c)ごとに設けられているので、射出成形
装置Aの効果に加えて、各発泡剤供給口52からの二酸
化炭素ガスの供給量を安定させることができるという効
果を備えている。
That is, according to the molding method using the injection molding apparatus B, since each foaming agent supply port 52 is provided for each individual foaming agent supply path 5b (5c), the effect of the injection molding apparatus A is obtained. In addition to this, there is an effect that the supply amount of carbon dioxide gas from each blowing agent supply port 52 can be stabilized.

【0044】図6は、本発明に係る射出成形装置の第3
の実施の形態を示すものである。図6に示すように、こ
の射出成形装置Cは、スクリュー3c内に2本の発泡剤
供給路5d,5eが設けられていて、両発泡剤供給路5
d,5eの発泡剤導入口51がスクリュー3cの前後方
向にずれた位置に開口していて、それぞれ個別のシール
ボックス4の凹溝41を臨む位置に開口している以外は
上記射出成形装置Bと同様になっている。
FIG. 6 shows a third embodiment of the injection molding apparatus according to the present invention.
1 shows an embodiment of the present invention. As shown in FIG. 6, this injection molding apparatus C has two blowing agent supply paths 5d and 5e in a screw 3c.
The injection molding apparatus B described above, except that the foaming agent introduction ports 51 d and 5 e are opened at positions shifted in the front-rear direction of the screw 3 c and open at positions facing the concave grooves 41 of the individual seal boxes 4. Is similar to

【0045】すなわち、この射出成形装置Cを用いた成
形方法によれば、射出成形装置Bの効果に加えて、シー
ルボックス4ごとにガス圧を変更することが容易で、溶
融樹脂への二酸化炭素ガスの含浸量を容易にコントロー
ル可能であるとともに、発泡剤供給口52が溶融樹脂で
詰まった場合でも詰まった発泡剤供給路5d(5e)側
のみに高圧ガスを送り込める。すなわち、高圧ガスによ
って溶融樹脂をシリンダー2内に押し戻すことができメ
ンテナンスが容易となる。
That is, according to the molding method using the injection molding apparatus C, in addition to the effect of the injection molding apparatus B, it is easy to change the gas pressure for each seal box 4 and to reduce the carbon dioxide to the molten resin. The gas impregnation amount can be easily controlled, and even when the blowing agent supply port 52 is clogged with the molten resin, the high-pressure gas can be sent only to the clogged blowing agent supply passage 5d (5e). That is, the molten resin can be pushed back into the cylinder 2 by the high-pressure gas, so that maintenance is facilitated.

【0046】図7は、本発明に係る射出成形装置の第4
の実施の形態を示すものである。図7に示すように、こ
の射出成形装置Dは、スクリュー3d内の2本の発泡剤
供給路5f,5gのうち短い側の発泡剤供給路5fの発
泡剤導入口51近傍から発泡剤供給口52の近傍部分
が、長い発泡剤供給路5gの内部をパイプ状に貫通して
設けられている以外は上記射出成形装置Cと同様になっ
ている。
FIG. 7 shows a fourth embodiment of the injection molding apparatus according to the present invention.
1 shows an embodiment of the present invention. As shown in FIG. 7, the injection molding apparatus D includes a blowing agent supply port 5 near the blowing agent supply port 51 of the shorter one of the two blowing agent supply paths 5 f and 5 g in the screw 3 d. The configuration is the same as that of the injection molding apparatus C except that a portion near 52 is provided so as to penetrate the inside of the long foaming agent supply path 5g in a pipe shape.

【0047】すなわち、この射出成形装置Dを用いた成
形方法によれば、射出成形装置Cの効果に加えて、スク
リュー内の発泡剤供給路の占める割合を小さくしてスク
リュー3dを小型化することができる。
That is, according to the molding method using the injection molding apparatus D, in addition to the effect of the injection molding apparatus C, the ratio of the foaming agent supply passage in the screw is reduced to reduce the size of the screw 3d. Can be.

【0048】本発明は、上記の実施の形態に限定されな
い。たとえば、上記の射出成形装置B(C,D)では発
泡剤供給路がそれぞれ2本ずつであったが、3本以上で
も構わない。
The present invention is not limited to the above embodiment. For example, in the above injection molding apparatus B (C, D), the number of the foaming agent supply paths is two each, but may be three or more.

【0049】[0049]

【実施例】以下に、本発明の実施例を詳しく説明する。 (実施例1)図8に示す4つの発泡剤供給口52をスク
リューの拡大発泡剤含浸ゾーン形成部31に備えた成形
装置Aを肉厚6mm,直径25cmの円盤状キャビティ
61を有する金型6にセットした。そして、成形装置A
のホッパーからポリプロピレン樹脂をシリンダー2内に
供給するとともに、発泡剤供給路5aを介して5.5M
Paのガス圧で二酸化炭素ガスを拡大発泡剤含浸ゾーン
11に供給し、50mm/sec,100mm/se
c,200mm/sec,300mm/secの4種の
射出速度で金型6内に二酸化炭素ガス含浸溶融樹脂を射
出し、それぞれ肉厚6mm,直径25cmの円盤状発泡
成形体を得た。
Embodiments of the present invention will be described below in detail. (Example 1) A molding apparatus A having four foaming agent supply ports 52 shown in FIG. 8 in an enlarged foaming agent impregnated zone forming section 31 of a screw is a mold 6 having a disk-shaped cavity 61 having a thickness of 6 mm and a diameter of 25 cm. Set to And the molding device A
Of the polypropylene resin into the cylinder 2 from the hopper, and 5.5M through the blowing agent supply path 5a.
A carbon dioxide gas is supplied to the expanded foaming agent impregnation zone 11 at a gas pressure of Pa, and is supplied at 50 mm / sec and 100 mm / sec.
The molten resin impregnated with carbon dioxide gas was injected into the mold 6 at four injection speeds of c, 200 mm / sec, and 300 mm / sec to obtain disk-shaped foamed molded articles each having a thickness of 6 mm and a diameter of 25 cm.

【0050】(比較例1)図9に示すように、スクリュ
ー3pの拡大発泡剤含浸ゾーン形成部31に1つしか発
泡剤供給口52が設けられていない以外、実施例1と同
様の成形装置Pおよび実施例1と同様の金型6を用い
て、成形装置Pのホッパーからポリプロピレン樹脂をシ
リンダー2内に供給するとともに、発泡剤供給路5pを
介して5.5MPaのガス圧で二酸化炭素ガスを拡大発
泡剤含浸ゾーン11に供給し、50mm/sec,10
0mm/sec,200mm/sec,300mm/s
ecの4種の射出速度で金型6内に二酸化炭素ガス含浸
溶融樹脂を射出し、それぞれ肉厚6mm,直径25cm
の円盤状発泡成形体を得た。
Comparative Example 1 As shown in FIG. 9, the same molding apparatus as in Example 1 except that only one foaming agent supply port 52 is provided in the enlarged foaming agent impregnation zone forming portion 31 of the screw 3p. Using the mold P and the same mold 6 as in Example 1, a polypropylene resin is supplied into the cylinder 2 from the hopper of the molding apparatus P, and carbon dioxide gas is supplied at a gas pressure of 5.5 MPa through the blowing agent supply passage 5p. Is supplied to the expanded foaming agent impregnation zone 11 and is supplied at 50 mm / sec.
0mm / sec, 200mm / sec, 300mm / s
The molten resin impregnated with carbon dioxide gas is injected into the mold 6 at four injection speeds of ec, each having a thickness of 6 mm and a diameter of 25 cm.
Was obtained.

【0051】そして、実施例1および比較例1の各射出
速度ごとに得られた各発泡成形体の発泡倍率を調べた結
果、図10に示すように、実施例1で得られた発泡成形
体の方がいずれの射出速度においても、比較例1のもの
より発泡倍率が高くなっていた。すなわち、この結果か
ら発泡剤供給口を複数設けるようにすれば、短時間で発
泡剤を溶融樹脂に含浸させることができ、射出速度を上
げることができることがわかる。
Then, as a result of examining the expansion ratio of each foam molded article obtained at each injection speed in Example 1 and Comparative Example 1, as shown in FIG. 10, the foam molded article obtained in Example 1 was obtained. In each of the injection speeds, the expansion ratio was higher than that of Comparative Example 1. That is, from this result, it can be seen that if a plurality of blowing agent supply ports are provided, the blowing agent can be impregnated into the molten resin in a short time, and the injection speed can be increased.

【0052】[0052]

【発明の効果】本発明の熱可塑性樹脂成形品の射出成形
方法は、以上のように構成されているので、溶融樹脂の
ガス含浸に長時間を要することがなく、比較的低圧で安
定して連続的に発泡剤を供給して溶融樹脂に含浸させる
ことができる。しかも、複数の発泡剤供給口から発泡剤
を供給するようにしたので、単数の発泡剤供給口から供
給する場合よりも溶融樹脂との接触面積が増大し、より
短時間で発泡剤を含浸させることができる。
The injection molding method for a thermoplastic resin molded article of the present invention is configured as described above, so that it does not require a long time for gas impregnation of the molten resin, and is stable at a relatively low pressure. The blowing agent can be continuously supplied to impregnate the molten resin. Moreover, since the blowing agent is supplied from a plurality of blowing agent supply ports, the contact area with the molten resin is increased as compared with the case where the blowing agent is supplied from a single blowing agent supply port, and the blowing agent is impregnated in a shorter time. be able to.

【0053】したがって、生産性が高いと共に、均質で
微細な高機能(断熱、緩衝、計量)の発泡成形体を射出
成形で安価に提供することができる。
Therefore, it is possible to provide a homogeneous and fine high-performance (insulated, buffered, metered) foam molded article at a low cost by injection molding, while having high productivity.

【0054】特に、請求項2の成形方法のようにすれ
ば、より効率よく溶融樹脂を含浸させることができる。
In particular, according to the molding method of the second aspect, the molten resin can be impregnated more efficiently.

【0055】請求項3の成形方法のようにすれば、発泡
剤の供給量を個別に調整でき、より効率よく溶融樹脂に
発泡剤を含浸できる。また、発泡剤供給口に溶融樹脂等
によるつまりが生じた場合も、個別に高圧ガスを発泡剤
供給路内に圧入して取り除くことができる。
According to the molding method of the third aspect, the supply amount of the blowing agent can be adjusted individually, and the blowing agent can be more efficiently impregnated into the molten resin. In addition, even when the blowing agent supply port is clogged with the molten resin or the like, the high-pressure gas can be individually pressed into the blowing agent supply path and removed.

【0056】請求項4の成形方法のようにすれば、樹脂
と反応を起こさず、さらに樹脂を劣化させるなどの悪影
響を樹脂に与えることなく、均質で微細な高機能(断
熱、緩衝、計量)の発泡成形体を射出成形で安価に提供
することができる。
According to the molding method of the fourth aspect, the resin does not react with the resin, and does not adversely affect the resin, such as deteriorating the resin. Can be provided at low cost by injection molding.

【0057】本発明の熱可塑性樹脂成形品の射出成形装
置は、以上のように構成されているので、より低圧で効
率よく溶融樹脂に含浸させることができ、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 the injection molding apparatus for a thermoplastic resin molded article of the present invention is configured as described above, it is possible to impregnate the molten resin with lower pressure and more efficiently, and it is necessary to make the entire apparatus a pressure-resistant structure. Therefore, the manufacturing cost of the device can be reduced.

【0058】請求項7の成形装置のようにすれば、発泡
剤の供給量を個別に調整でき、ようにより効率よく溶融
樹脂に発泡剤を含浸できる。また、発泡剤供給口に溶融
樹脂等によるつまりが生じた場合も、個別に高圧ガスを
発泡剤供給路内に圧入して取り除くことができ、メンテ
ナンスが容易である。
According to the molding apparatus of the seventh aspect, the supply amount of the blowing agent can be individually adjusted, and the blowing agent can be more efficiently impregnated into the molten resin. In addition, even when the blowing agent supply port is clogged with a molten resin or the like, the high-pressure gas can be individually pressed into the blowing agent supply path and removed, thereby facilitating maintenance.

【0059】請求項8の成形装置のようにすれば、スク
リュー内の発泡剤供給路が占める割合を最小限にするこ
とができ、装置の小型化を図ることができる。
According to the molding apparatus of the eighth aspect, the ratio occupied by the blowing agent supply passage in the screw can be minimized, and the apparatus can be downsized.

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

【図1】本発明にかかる射出成形装置の第1の実施の形
態を示し、その全体をあらわす切欠側面図である。
FIG. 1 shows a first embodiment of an injection molding apparatus according to the present invention, and is a cutaway side view showing the whole thereof.

【図2】図1の射出成形装置の射出成形機の全体概要を
示す切欠側面図である。
FIG. 2 is a cutaway side view showing the general outline of the injection molding machine of the injection molding apparatus of FIG.

【図3】図2の射出成形機を模式的にあらわす断面図で
ある。
FIG. 3 is a sectional view schematically showing the injection molding machine of FIG. 2;

【図4】図2の射出成形機の要部拡大断面図である。FIG. 4 is an enlarged sectional view of a main part of the injection molding machine of FIG.

【図5】本発明にかかる射出成形装置の第2の実施の形
態を示し、その射出成形機を模式的にあらわす断面図で
ある。
FIG. 5 is a cross-sectional view schematically showing an injection molding machine according to a second embodiment of the injection molding apparatus according to the present invention.

【図6】本発明にかかる射出成形装置の第3の実施の形
態を示し、その射出成形機を模式的にあらわす断面図で
ある。
FIG. 6 is a cross-sectional view schematically showing an injection molding machine according to a third embodiment of the present invention;

【図7】本発明にかかる射出成形装置の第4の実施の形
態を示し、その射出成形機を模式的にあらわす断面図で
ある。
FIG. 7 is a cross-sectional view schematically showing an injection molding machine according to a fourth embodiment of the injection molding apparatus according to the present invention.

【図8】実施例1で使用した成形装置および金型を模式
的にあらわす断面図である。
FIG. 8 is a cross-sectional view schematically showing a molding apparatus and a mold used in Example 1.

【図9】比較例1で使用した成形装置および金型を模式
的にあらわす断面図である。
FIG. 9 is a cross-sectional view schematically showing a molding apparatus and a mold used in Comparative Example 1.

【図10】実施例1および比較例1で得られた発泡成形
体の射出速度毎の発泡倍率の変化をあらわすグラフであ
る。
FIG. 10 is a graph showing a change in expansion ratio for each injection speed of the foamed molded products obtained in Example 1 and Comparative Example 1.

【符号の説明】 A,B,C,D 射出成形装置 1 射出成形機 11 拡大発泡剤含浸ゾーン 12 計量部 2 シリンダー 3a,3b,3c,3d スクリュー 31 拡大発泡剤含浸ゾーン形成部 4 シールボックス 5a,5b,5c,5d,5e,5f,5g 発泡剤供
給路 51 発泡剤導入口 52 発泡剤供給口
[Description of Signs] A, B, C, D Injection molding apparatus 1 Injection molding machine 11 Expanded foaming agent impregnated zone 12 Measuring section 2 Cylinder 3a, 3b, 3c, 3d Screw 31 Expanded foaming agent impregnated zone forming section 4 Seal box 5a , 5b, 5c, 5d, 5e, 5f, 5g Blowing agent supply path 51 Blowing agent introduction port 52 Blowing agent supply port

フロントページの続き Fターム(参考) 4F206 AA11 AB02 AG20 JA04 JD03 JF04 JF13 JF21 JL02 JM01 JN03 JQ11 Continued on the front page F term (reference) 4F206 AA11 AB02 AG20 JA04 JD03 JF04 JF13 JF21 JL02 JM01 JN03 JQ11

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】射出成形機のシリンダー内にてスクリュー
回転によって溶融状態になった溶融樹脂に、発泡剤供給
口から発泡剤を供給して、発泡剤を溶融樹脂に混合し含
浸させる発泡剤含浸工程と、得られた発泡剤含浸溶融樹
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
て発泡成形品を得る射出成形工程とを含む熱可塑性樹脂
成形品の射出成形方法であって、スクリューの後端部か
ら前端方向に向かってスクリュー内部に設けられた発泡
剤供給路の、シリンダー内でスクリュー外周面に開口す
る複数の発泡剤供給口よりスクリューの後端部から発泡
剤供給路に送り込まれた前記発泡剤を溶融樹脂に供給
し、発泡剤を溶融樹脂に含浸させることを特徴とする熱
可塑性樹脂成形品の射出成形方法。
1. A foaming agent impregnation for supplying a foaming agent from a foaming agent supply port to a molten resin melted by screw rotation in a cylinder of an injection molding machine, and mixing and impregnating the foaming agent with the molten resin. Step and an injection molding method of a thermoplastic resin molded article including an injection molding step of injecting the measured resin into the mold cavity after measuring the obtained foaming agent impregnated molten resin to obtain a foam molded article, From the rear end of the screw to the blowing agent supply path, from the plurality of blowing agent supply ports that open to the outer peripheral surface of the screw in the cylinder of the blowing agent supply path provided inside the screw from the rear end of the screw toward the front end A method for injection-molding a thermoplastic resin molded product, characterized in that the blowing agent supplied is supplied to a molten resin, and the blowing agent is impregnated in the molten resin.
【請求項2】発泡剤をスクリュー軸の前後方向にずれた
位置に設けられた複数の発泡剤供給口から供給する請求
項1に記載の熱可塑性樹脂成形品の射出成形方法。
2. The injection molding method of a thermoplastic resin molded product according to claim 1, wherein the blowing agent is supplied from a plurality of blowing agent supply ports provided at positions shifted in the front-rear direction of the screw shaft.
【請求項3】発泡剤を個別の発泡剤供給路を経た各発泡
剤供給口から供給する請求項1または請求項2に記載の
熱可塑性樹脂成形品の射出成形方法。
3. The method of injection molding a thermoplastic resin article according to claim 1, wherein the blowing agent is supplied from each blowing agent supply port through a separate blowing agent supply path.
【請求項4】発泡剤が熱可塑性樹脂に対する非反応性ガ
スである請求項1〜請求項3のいずれかに記載の熱可塑
性樹脂成形品の射出成形方法。
4. The injection molding method for a thermoplastic resin molded product according to claim 1, wherein the foaming agent is a non-reactive gas for the thermoplastic resin.
【請求項5】スクリューの後端部から前端方向に向かっ
てスクリュー内部に設けられた発泡剤供給路の、シリン
ダー内でスクリュー外周面に開口する発泡剤供給口より
スクリューの後端部から発泡剤供給路に送り込まれた前
記発泡剤を溶融樹脂に供給し、発泡剤を溶融樹脂に含浸
させたのちの発泡剤含浸樹脂が計量部で計量されて射出
されるようになっている射出成形装置であって、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発泡剤含浸ゾーンを形成する拡
大発泡剤含浸ゾーン形成部がスクリューの先端近くに設
けられ、拡大発泡剤含浸ゾーン形成部に発泡剤供給口が
複数個開口していることを特徴とする射出成形装置。
5. A foaming agent supply passage provided inside the screw from the rear end of the screw toward the front end thereof, and a foaming agent from a rear end of the screw through a foaming agent supply port opened in the outer peripheral surface of the screw in the cylinder. In the injection molding apparatus, the blowing agent fed into the supply path is supplied to the molten resin, and the blowing agent-impregnated resin after the blowing agent is impregnated in the molten resin is measured and injected by the measuring unit. There, by increasing the pitch of the front and rear screw flights, and / or by reducing the screw shaft diameter, the expanded foaming agent impregnated zone having a larger internal volume in the inter-flight space than the inter-flight space. The expanded foaming agent impregnated zone forming part for forming is provided near the tip of the screw, and a plurality of foaming agent supply ports are opened in the expanded foaming agent impregnated zone forming part. An injection molding apparatus characterized by the above-mentioned.
【請求項6】少なくとも1つの発泡剤供給口が他の発泡
剤供給口に対しスクリュー軸の前後方向にずれた位置に
設けられている請求項5に記載の射出成形装置。
6. The injection molding apparatus according to claim 5, wherein at least one blowing agent supply port is provided at a position shifted from the other blowing agent supply ports in the front-rear direction of the screw shaft.
【請求項7】スクリュー内に互いに隔絶された複数の発
泡剤供給路を備え、各発泡剤供給路ごとに発泡剤供給口
を備えている請求項5または請求項6に記載の射出成形
装置。
7. The injection molding apparatus according to claim 5, further comprising a plurality of foaming agent supply paths separated from each other in the screw, and a foaming agent supply port provided for each of the foaming agent supply paths.
【請求項8】少なくとも1つの発泡剤供給路の一部が、
他の発泡剤供給路の内部を貫通するパイプ状に設けられ
ている請求項7に記載の射出成形装置。
8. A part of at least one blowing agent supply path,
The injection molding apparatus according to claim 7, wherein the injection molding apparatus is provided in a pipe shape penetrating the inside of another blowing agent supply path.
JP2001108843A 2001-04-06 2001-04-06 Method and equipment for injection-molding thermoplastic resin molded product Withdrawn JP2002307499A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001108843A JP2002307499A (en) 2001-04-06 2001-04-06 Method and equipment for injection-molding thermoplastic resin molded product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001108843A JP2002307499A (en) 2001-04-06 2001-04-06 Method and equipment for injection-molding thermoplastic resin molded product

Publications (1)

Publication Number Publication Date
JP2002307499A true JP2002307499A (en) 2002-10-23

Family

ID=18960904

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001108843A Withdrawn JP2002307499A (en) 2001-04-06 2001-04-06 Method and equipment for injection-molding thermoplastic resin molded product

Country Status (1)

Country Link
JP (1) JP2002307499A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007054995A (en) * 2005-08-23 2007-03-08 Ube Machinery Corporation Ltd Injection divice

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007054995A (en) * 2005-08-23 2007-03-08 Ube Machinery Corporation Ltd Injection divice

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