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JPS6153931B2 - - Google Patents
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JPS6153931B2 - - Google Patents

Info

Publication number
JPS6153931B2
JPS6153931B2 JP56089136A JP8913681A JPS6153931B2 JP S6153931 B2 JPS6153931 B2 JP S6153931B2 JP 56089136 A JP56089136 A JP 56089136A JP 8913681 A JP8913681 A JP 8913681A JP S6153931 B2 JPS6153931 B2 JP S6153931B2
Authority
JP
Japan
Prior art keywords
cylinder
thermoplastic resin
injection
injection molding
sub
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP56089136A
Other languages
Japanese (ja)
Other versions
JPS57203524A (en
Inventor
Masao Shizawa
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.)
Orion Kasei KK
Original Assignee
Orion Kasei KK
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 Orion Kasei KK filed Critical Orion Kasei KK
Priority to JP56089136A priority Critical patent/JPS57203524A/en
Publication of JPS57203524A publication Critical patent/JPS57203524A/en
Publication of JPS6153931B2 publication Critical patent/JPS6153931B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/02Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
    • B29C44/04Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles consisting of at least two parts of chemically or physically different materials, e.g. having different densities
    • B29C44/0492Devices for feeding the different materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor

Landscapes

  • Injection Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、発泡成形品の射出成形方法とその装
置、特に成形品の内部が発泡体で外部表面が発泡
していない合成樹脂からなる発泡成形品の射出成
形方法とその装置に関する。 一般に合成樹脂の低発泡射出成形(以下SF成
形と称する)による製品は、剛性、遮音性、断熱
性に優れ、かつ製品のデザイン上の変化に富む等
の特徴があるが、反面発泡によつて表面に渦巻状
の模様を生じるために外的美感を損ね、商品によ
つては成形後に表面塗装を施こさなければならな
い欠点があつた。これらの欠点を解消するため
に、従来からSF成形法としての各種の装置や方
法が開発され、その一つとして二組の同容量の射
出成形ユニツトを備え、これらより二種の合成樹
脂をバルブ切換えにより交互に或いは同時に射出
する方法もあつたが、その基本となるものは金型
内における樹脂流の特性である。 即ち、キヤビテイ内に射出された樹脂流を観察
すると、まずはじめに射出された樹脂はキヤビテ
イ壁面に触れて、その温度が下るために粘度も下
り、ゲート付近のキヤビテイ壁面に停滞しなが
ら、引き続き射出される樹脂は、その内側を通り
その先の壁面に停滞し次々と同じ状態を連続的に
繰り返し充填が完了する。従つて、1回に射出さ
れる樹脂のうち、はじめの方に射出される樹脂は
キヤビテイの壁面に(製品の表面に)、そしてあ
との方に射出される樹脂は肉厚の中央部に充填さ
れることは公知の通りである。 然し乍ら、これが理論通りに行なわれるために
は一回に射出される樹脂の粘度が出来るだけ均一
で且つ流速も間断なく一定であることが必要であ
る。 然るに従来行なわれている方法は、2組の射出
ユニツトによつて夫々状態の異る樹脂を射出する
ため両樹脂の粘度を一定に保つことは困難であ
り、且つ間断なく連続的に射出することは難し
い。そのため交互射出のためのバルブの切換によ
つてヘジテーシヨンマークを生じたり、或いはや
や複雑な形状の成形品の場合は発泡層が表面に露
出したり又は末端まで発泡層が行き渡らないとい
う欠点があつた。 本発明は終始シリンダーによつて射出される樹
脂の粘度を一定に保ち乍ら間断なく連続的に射出
を行うことによつて複雑な形状の成形品でも内部
を発泡層とし、表面(スキン層)は発泡剤を全く
含まない樹脂で成形することができ塗装不用な成
形品を得んとしたもので、その目的とするところ
は従来の射出成形機に僅かな補助装置を加え、こ
れによつて外観良好な発泡成形品を連続的に得る
方法を提供せんとするものである。 即ち、本発明者は従来のスクリユーを内設した
シリンダーからなる射出成形機を用い、これに副
シリンダーを連設し、金型に当接したミキシング
ノズルを用いてシリンダーからの熱可塑性樹脂を
金型内へシヨツトすると共に前記副シリンダーか
らの熱可塑性樹脂と発泡剤の混合物を前記シリン
ダーからの射出工程中の任意の時期に射出し、ミ
キシングノズルで混練して、金型へシヨツトする
ことができる発泡成形品の射出成形方法とその装
置を提供せんとする。 以下本発明の実施例を添付図面によつて詳細に
説明する。第1図は本発明装置の一実施態様を示
す一部断面図であり、ホツパー1は熱可塑性樹脂
Aをシリンダー2内に供給するためのもので、シ
リンダー2には電動機とこれに連結する変速機に
よつて回転しながら進退するスクリユー3を内蔵
する。シリンダーヘツド4と樹脂成形用の金型7
間は、左ひねりと右ひねりのエレメントからなる
各種スタテイツクミキサー5を内蔵したミキシン
グノズル6を介在して設け、スクリユー3により
熱可塑性樹脂Aを金型7内へ射出(シヨツト)す
るようにしている。しかして、シリンダーヘツド
4には、射出容量がシリンダー2の射出容量の3
%〜20%、好ましくは5〜10%の副シリンダー8
を連結管9によつて連結し、副シリンダー8にホ
ツパー(図示せず)等により供給した熱可塑性合
成樹脂Bと発泡剤Cの混合物Dを副シリンダーに
内設した副スクリユー14によつてシリンダーヘ
ツド4内へ射出するようにしている。なお、ここ
でシリンダーヘツド4とはスクリユー3が位置す
るスクリユー2の先端部を含む意である。また前
記ミキシングノズル6の後部、すなわちシリンダ
ーヘツド4を含む副シリンダー8の連結部には、
前記シリンダー2により熱可塑性樹脂Aを射出す
る工程中の任意の時期に前記副シリンダー8より
の混合物Dを射出あるいは停止する制御機構を備
えている。この制御機構は、第1図及び第2図に
示すようにスクリユー3の後部において連動する
カム10とリミツトスイツチLS−1,LS−2、
により電気的に作動するようにした油圧シリンダ
ー11とニードル弁12を前記連結管9の反対側
のシリンダーヘツド4に設けてなるもので、ニー
ドル弁により副シリンダー8からの混合物Dの射
出あるいは停止を制御できるように設けている。 つぎに本発明方法である発泡成形品の射出成形
方法を説明すると、ホツパー1より主シリンダー
2内に熱可塑性樹脂Aを供給すると共に別途設け
た小容量の副シリンダー8内に熱可塑性樹脂Bと
発泡剤Cの混合物Dを供給する。熱可塑性樹脂A
とBは、例えばポリエチレン、ポリプロピレン、
ポリスチレン、ABS樹脂、変性ポリフエニレン
オキサイド(GE社製 商品名ノリル)、グラフト
化ポリフエニレンエーテル(旭ダウ社製商品名ザ
イロン)、ポリアミド(ナイロン6、ナイロン66
等)又はポリカーボネート等から選ばれたもので
ある。また、熱可塑性樹脂AとBは互いに相溶性
のあるものであれば異種のものであつてもよく、
相溶性のあるものの例としてはポリプロピレンと
ポリエチレン、ABS樹脂とポリスチレン、変性
ポリフエニレンオキサイドとポリスチレン、グラ
フト化ポリフエニレンエーテルとポリスチレン、
ナイロン66とナイロン6又はポリカーボネートと
ABS樹脂等が挙げられる。熱可塑性樹脂Bと混
合する発泡剤Cとしては、アゾヂカルボンアミド
(ADCA)、アゾビスイソブチロニトリル
(AZDN)、P・P′−オキシビスベンゼンスルホニ
ルヒドラジツド(OBSH)、N・N′−ジニトロソ
ペンタメチレンテトラミン(DPT)、P−トルエ
ンスルホニルセミカルバジツド(TSSC)等が考
えられる。しかして、前記シリンダー2内に供給
した熱可塑性樹脂Aは、スクリユー3の前進によ
りシリンダーヘツド4からミキシングノズル6を
通してスプルー15より金型7内へ所要量シヨツ
トされる(第3図)。この際、スクリユー3の後
部のカム10はリミツトスイツチLS−3よりス
タートとし、スクリユー3と共にカム10は前進
するが、カム10がリミツトスイツチLS−1に
至るまで油圧シリンダー11のニードル弁はミキ
シングノズル6の後部に位置する副シリンダー8
の連結部、即ちシリンダー2と副シリンダー8に
介在する連結管9のシリンダーヘツド4内への出
口13において閉じられている。さらに、スクリ
ユー3が前進してカム10がリミツトスイツチ
LS−1を押すと、油圧シリンダー11が解放さ
れてニードル弁12は出口13において開き、こ
れと同時に副スクリユー14が前進を開始して熱
可塑性樹脂Bと発泡剤Cの混合物Dはシリンダー
ヘツド4内へ射出する。このようにして混合物D
は、熱可塑性樹脂Aと一体になつてミキシングノ
ズル6内で混合されスプルー15より金型7内へ
シヨツトする。この場合、発泡剤の重量比は、熱
可塑性樹脂AとBを加えた重量に対して0.2〜0.8
%が適性な発泡状態を得るために望ましい。この
場合、熱可塑性樹脂Aと混合物Dとの混練物Eは
樹脂Aに対する混合物の比が後述するよう僅かで
あり、且つミキシングノズル内で十分に混練され
るためにもとの樹脂Aと混練物Eとの粘度差は殆
んどなく理想的溶融樹脂流の原則によつて、先の
シヨツトされた熱可塑性樹脂Aの内側を流れて金
型7内にシヨツトされ、樹脂1内において微細な
独立気泡状に発泡層を形成する(第4図)。つい
で、スクリユー3がさらに前進することによりカ
ム10がリミツトスイツチLS−2を押すと、副
スクリユー14は停止して混合物Dをシリンダー
ヘツド4に送入停止すると同時に油圧シリンダー
によりニードル弁12は閉じ、金型7内には再び
熱可塑性樹脂Aのみをシヨツトする。こうしてミ
キシングノズル6内及びスプルー15内が合成樹
脂Aで充填された状態となり、カム10はリミツ
トスイツチLS−4を押して射出を完了する。次
に、スクリユー3は回転し、リミツトスイツチ
LS−3まで後退して停止し、次の工程を連続し
て行なうことが可能となる。 なお、以上の工程説明は本発明の一実施態様で
あつて、例えばスプルー15とミキシングノズル
6内に熱可塑性樹脂を充填された状態から副シリ
ンダー8より混合物を射出することから工程を開
始することもでき、従つて本発明はシリンダー2
からの射出中の任意の時期に副シリンダーの混合
物を射出するものであればいずれの方法でも目的
が達成できる。 このようにして得た発泡成形品は、内部が合成
樹脂の発泡体(コア層樹脂)で外部表面が合成樹
脂の表皮(スキン層樹脂)からなるために外観が
美しいばかりでなく、剛性、這音性及び断熱性の
優れたものが本発明のきわめて簡単な改良装置と
容易な操作によつて得られる。 実施例 1 射出容量3600gのシリンダー2と射出容量200
gの副シリンダー8を用いた。 シリンダー2にはポリスチレンを供給し、副シ
リンダー8には下記比率で予備混合した混合物を
供給した。
The present invention relates to a method and apparatus for injection molding a foam molded article, and more particularly to a method and apparatus for injection molding a foam molded article, in which the inside of the molded article is made of foam and the outer surface is made of an unfoamed synthetic resin. In general, products made by low-foaming injection molding (hereinafter referred to as SF molding) of synthetic resins have characteristics such as excellent rigidity, sound insulation, and heat insulation, and a wide variety of product designs. The spiral pattern formed on the surface impairs the external appearance, and some products have the disadvantage that the surface must be painted after molding. In order to eliminate these drawbacks, various devices and methods have been developed for the SF molding method, one of which is equipped with two sets of injection molding units of the same capacity, and from these two sets of injection molding units are used to mold two types of synthetic resin into valves. There have been methods of alternately or simultaneously injecting resin by switching, but the basis of this method is the characteristics of the resin flow within the mold. In other words, when observing the flow of resin injected into the cavity, the injected resin first touches the cavity wall, its temperature decreases, the viscosity decreases, and the resin continues to be injected while remaining on the cavity wall near the gate. The resin passes through the inside and stagnates on the wall beyond, and the same state is repeated one after another until the filling is completed. Therefore, of the resin injected at one time, the resin injected earlier will fill the wall of the cavity (on the surface of the product), and the resin injected later will fill the center of the wall thickness. It is well known that this is the case. However, in order for this to be carried out according to theory, it is necessary that the viscosity of the resin injected at one time be as uniform as possible, and that the flow rate be constant without interruption. However, in the conventional method, two sets of injection units inject resins in different states, so it is difficult to keep the viscosity of both resins constant, and it is difficult to continuously inject resins without interruption. is difficult. Therefore, switching of the valve for alternate injection may cause hesitation marks, or in the case of a molded product with a somewhat complicated shape, the foam layer may be exposed to the surface or the foam layer may not reach the ends. It was hot. The present invention maintains the viscosity of the resin injected by a cylinder from beginning to end and performs continuous injection without interruption, thereby creating a foam layer inside even complex-shaped molded products, and forming a foam layer on the surface (skin layer). The aim was to create a molded product that could be molded from a resin that did not contain any foaming agents and did not require painting.The aim was to add a small amount of auxiliary equipment to a conventional injection molding machine, and thereby It is an object of the present invention to provide a method for continuously obtaining foamed molded products with good appearance. That is, the present inventor used a conventional injection molding machine consisting of a cylinder with a screw inside, connected a sub-cylinder to this, and used a mixing nozzle in contact with the mold to mold thermoplastic resin from the cylinder. The mixture of thermoplastic resin and foaming agent from the sub-cylinder can be injected from the cylinder at any time during the injection process, mixed with a mixing nozzle, and shot into the mold. We aim to provide an injection molding method and apparatus for foam molded products. Embodiments of the present invention will be described in detail below with reference to the accompanying drawings. FIG. 1 is a partial cross-sectional view showing one embodiment of the device of the present invention, in which a hopper 1 is for supplying thermoplastic resin A into a cylinder 2, and the cylinder 2 is equipped with an electric motor and a speed changer connected thereto. It has a built-in screw 3 that moves forward and backward while rotating depending on the machine. Cylinder head 4 and mold 7 for resin molding
A mixing nozzle 6 incorporating various static mixers 5 consisting of left-handed and right-handed elements is interposed between the mixing nozzles 6 and the screw 3 to inject the thermoplastic resin A into the mold 7. There is. Therefore, the injection capacity of the cylinder head 4 is 3 of the injection capacity of the cylinder 2.
%~20%, preferably 5~10% secondary cylinder 8
are connected by a connecting pipe 9, and a mixture D of thermoplastic synthetic resin B and foaming agent C, which is supplied to the sub-cylinder 8 by a hopper (not shown), etc., is transferred to the cylinder by a sub-screw 14 installed in the sub-cylinder. The liquid is ejected into the head 4. Note that the cylinder head 4 here includes the tip of the screw 2 where the screw 3 is located. In addition, at the rear of the mixing nozzle 6, that is, at the connection part of the sub-cylinder 8 including the cylinder head 4,
A control mechanism is provided for injecting or stopping the mixture D from the sub-cylinder 8 at any time during the process of injecting the thermoplastic resin A from the cylinder 2. This control mechanism consists of a cam 10 and limit switches LS-1, LS-2, which are interlocked at the rear of the screw 3, as shown in FIGS. 1 and 2.
A hydraulic cylinder 11 and a needle valve 12 which are electrically actuated are provided in the cylinder head 4 on the opposite side of the connecting pipe 9, and the injection or stopping of the mixture D from the auxiliary cylinder 8 is performed by the needle valve. It is set up so that it can be controlled. Next, to explain the injection molding method for foam molded products, which is the method of the present invention, thermoplastic resin A is supplied from the hopper 1 into the main cylinder 2, and thermoplastic resin B is supplied into the separately provided small-capacity sub-cylinder 8. Supply mixture D of blowing agent C. Thermoplastic resin A
and B are, for example, polyethylene, polypropylene,
Polystyrene, ABS resin, modified polyphenylene oxide (manufactured by GE, product name Noryl), grafted polyphenylene ether (product name Zylon, manufactured by Asahi Dow), polyamide (nylon 6, nylon 66)
etc.) or polycarbonate. Furthermore, the thermoplastic resins A and B may be different types as long as they are compatible with each other.
Examples of compatible materials include polypropylene and polyethylene, ABS resin and polystyrene, modified polyphenylene oxide and polystyrene, grafted polyphenylene ether and polystyrene,
Nylon 66 and nylon 6 or polycarbonate
Examples include ABS resin. The blowing agent C mixed with the thermoplastic resin B includes azodicarbonamide (ADCA), azobisisobutyronitrile (AZDN), P.P'-oxybisbenzenesulfonylhydrazide (OBSH), N.N. Possible examples include '-dinitrosopentamethylenetetramine (DPT) and P-toluenesulfonyl semicarbazide (TSSC). As the screw 3 moves forward, the thermoplastic resin A supplied into the cylinder 2 is shot in a required amount from the cylinder head 4 through the mixing nozzle 6 and into the mold 7 from the sprue 15 (FIG. 3). At this time, the cam 10 at the rear of the screw 3 starts from the limit switch LS-3, and the cam 10 moves forward together with the screw 3, but until the cam 10 reaches the limit switch LS-1, the needle valve of the hydraulic cylinder 11 closes the mixing nozzle 6. Secondary cylinder 8 located at the rear
The connection between the cylinder 2 and the auxiliary cylinder 8 is closed at the outlet 13 of the connecting pipe 9 into the cylinder head 4. Furthermore, the screw 3 moves forward and the cam 10 switches the limit switch.
When LS-1 is pressed, the hydraulic cylinder 11 is released and the needle valve 12 opens at the outlet 13, and at the same time the secondary screw 14 starts moving forward and the mixture D of the thermoplastic resin B and the blowing agent C flows into the cylinder head 4. Eject inward. In this way, mixture D
is mixed with the thermoplastic resin A in the mixing nozzle 6 and shot into the mold 7 through the sprue 15. In this case, the weight ratio of the blowing agent to the weight of the thermoplastic resins A and B is 0.2 to 0.8.
% is desirable to obtain suitable foaming conditions. In this case, the kneaded product E of the thermoplastic resin A and the mixture D has a small ratio of the mixture to the resin A, as will be described later, and is sufficiently kneaded in the mixing nozzle, so that there is a difference between the original resin A and the kneaded product. There is almost no difference in viscosity from E, and according to the principle of ideal molten resin flow, it flows inside the previously shot thermoplastic resin A and is shot into the mold 7, forming fine independent particles within the resin 1. A foam layer is formed in the form of bubbles (Fig. 4). Next, when the screw 3 moves further forward and the cam 10 pushes the limit switch LS-2, the sub-screw 14 stops and stops feeding the mixture D to the cylinder head 4. At the same time, the needle valve 12 is closed by the hydraulic cylinder and the metal Only the thermoplastic resin A is shot into the mold 7 again. In this way, the inside of the mixing nozzle 6 and the inside of the sprue 15 are filled with the synthetic resin A, and the cam 10 pushes the limit switch LS-4 to complete the injection. Next, screw 3 rotates and the limit switch
It is possible to move back to LS-3 and stop, and then perform the next process continuously. The above process description is one embodiment of the present invention, and for example, the process starts by injecting the mixture from the sub cylinder 8 from a state in which the sprue 15 and the mixing nozzle 6 are filled with thermoplastic resin. Therefore, the present invention can also be used for cylinder 2.
The purpose can be achieved by any method that injects the mixture in the secondary cylinder at any time during injection from the secondary cylinder. The foam molded product obtained in this way has a synthetic resin foam inside (core layer resin) and an outer surface made of synthetic resin skin (skin layer resin), so it not only has a beautiful appearance but also has good rigidity and elasticity. Excellent acoustic and thermal insulation properties are obtained by the very simple improved device and easy operation of the present invention. Example 1 Cylinder 2 with injection capacity 3600g and injection capacity 200
A secondary cylinder 8 of g was used. Polystyrene was supplied to cylinder 2, and a mixture premixed at the following ratio was supplied to sub-cylinder 8.

【表】 これらの原料を前記方法により発泡成形品を製
造した。
[Table] Foam molded products were manufactured using these raw materials according to the method described above.

【表】 このようにして本発明により出来たSF成形品
は、渦巻状の模様又は銀条等の全くない塗装不要
の外観を呈した。 実施例 2 実施例1と同一の装置及び金型を使用し、主シ
リンダーには変性ポリフエニレンオキサイド(商
品名ノリルFN−215)を供給し、副シリンダーに
は下記比率で予備混合した混合物を供給した。
[Table] The SF molded product thus produced according to the present invention exhibited an appearance without any spiral pattern or silver stripes, and did not require painting. Example 2 Using the same equipment and mold as in Example 1, modified polyphenylene oxide (trade name Noryl FN-215) was supplied to the main cylinder, and a mixture premixed in the following ratio was supplied to the sub cylinder. supplied.

【表】 このようにして出来た成形品は、実施例1と同
様に渦巻状の模様又は銀条等が全くない塗装不要
の外観を呈した。
[Table] Similar to Example 1, the molded product thus produced had an appearance without any spiral pattern or silver stripes, and did not require painting.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明による射出装置の主要部分の断
面図、第2図はリミツトスイツチの配置図、第
3,4,5図は金型内の樹脂流を示す断面図であ
る。 1……ホツパー、2……主シリンダー、3……
主スクリユー、4……シリンダーヘツド、6……
ミキシングノズル、7……金型、8……副シリン
ダー、9……連結管、10……カム、11……油
圧シリンダー、12……ニードル弁、14……副
スクリユー、LS−1……副シリンダーの射出開
始用リミツトスイツチ、LS−2……副シリンダ
ーの射出停止用リミツトスイツチ、LS−3……
主シリンダーの計量完了用リミツトスイツチ、
LS−4……主シリンダーの射出完了用リミツト
スイツチ、A,B……合成樹脂、C……発泡剤、
D……BとCの混合物、E……A,BとCの発泡
混練物。
FIG. 1 is a sectional view of the main parts of an injection device according to the present invention, FIG. 2 is a layout diagram of a limit switch, and FIGS. 3, 4, and 5 are sectional views showing resin flow within a mold. 1...Hopper, 2...Main cylinder, 3...
Main screw, 4... Cylinder head, 6...
Mixing nozzle, 7... Mold, 8... Sub cylinder, 9... Connecting pipe, 10... Cam, 11... Hydraulic cylinder, 12... Needle valve, 14... Sub screw, LS-1... Sub Cylinder injection start limit switch, LS-2...Sub-cylinder injection stop limit switch, LS-3...
Limit switch for main cylinder metering completion;
LS-4... Limit switch for main cylinder injection completion, A, B... Synthetic resin, C... Foaming agent,
D...Mixture of B and C, E...Foam kneaded product of A, B and C.

Claims (1)

【特許請求の範囲】 1 シリンダーに内設したスクリユーにより熱可
塑性樹脂をシリンダーヘツドから金型へシヨツト
する射出成形機において、前記シリンダーヘツド
と金型間にはミキシングノズルを介在して設け、
前記ミキシングノズルの後部には熱可塑性樹脂と
発泡剤の混合物を前記シリンダーの射出工程中の
任意の時期に射出あるいは停止する制御機構を備
えた副シリンダーを連設したことを特徴とする発
泡成形品の射出成形装置。 2 前記ミキシングノズルの後部に連設した副シ
リンダーが、連結管を介在して前記シリンダーヘ
ツドに連結したものであることを特徴とする特許
請求の範囲第1項記載の発泡成形品の射出成形装
置。 3 前記シリンダーの射出工程中の任意の時期に
副シリンダーの混合物をミキシングノズルの後部
に送入あるいは停止する制御機構が、前記スクリ
ユーと電気的に連動して作動するようにした弁で
あることを特徴とする特許請求の範囲第1項又は
第2項に記載の発泡成形品の射出成形装置。 4 前記副シリンダーが、混合物を射出する副ス
クリユーを内設し、射出容量が前記シリンダーの
射出容量の5〜10%であることを特徴とする特許
請求の範囲第1項乃至第3項のいずれかに記載の
発泡成形品の射出成形装置。 5 熱可塑性樹脂をシリンダーのスクリユーでシ
リンダーヘツドより金型へシヨツトする射出成形
法において、予め用意した副シリンダー内に前記
熱可塑性樹脂と同一種類の熱可塑性樹脂と発泡剤
の混合物を供給し、前記シリンダーの射出工程中
の任意の時期に前記副シリンダーの熱可塑性樹脂
と発泡剤の混合物を射出し、前記シリンダヘツド
と金型間に介在したミキシングノズルにより前記
シリンダーからの熱可塑性樹脂と前記混合物を混
練しながら連続的に金型内にシヨツトすることを
特徴とする発泡成形品の射出成形方法。 6 前記シリンダーの射出工程中の任意の時期
が、前記シリンダーからの熱可塑性樹脂の射出中
の最初、途中或いは最後のいずれかから選ばれた
ものであることを特徴とする特許請求の範囲第5
項に記載する発泡成形品の射出成形方法。 7 熱可塑性樹脂をシリンダーのスクリユーでシ
リンダーヘツドより金型へシヨツトする射出成形
法において、予め用意した副シリンダー内に前記
熱可塑性樹脂と相溶性を有する異種の熱可塑性樹
脂と発泡剤を供給し、前記シリンダーの射出中の
任意の時期に前記副シリンダーの熱可塑性樹脂と
発泡剤の混合物を射出し、前記シリンダーヘツド
と金型間に介在したミキシングノズルにより前記
シリンダーからの熱可塑性樹脂と前記混合物を混
練しながら連続的に金型内へシヨツトすることを
特徴とする発泡成形品の射出成形方法。 8 前記シリンダーの射出工程中の任意の時期
が、前記シリンダーからの熱可塑性樹脂の射出中
の最初、途中或いは最後のいずれかから選ばれた
ものであることを特徴とする特許請求の範囲第7
項に記載する発泡成形品の射出成形方法。
[Scope of Claims] 1. An injection molding machine in which thermoplastic resin is shot from a cylinder head to a mold by a screw installed in a cylinder, with a mixing nozzle interposed between the cylinder head and the mold,
A foam molded product characterized in that a sub-cylinder is connected to the rear of the mixing nozzle and is equipped with a control mechanism for injecting or stopping the mixture of thermoplastic resin and foaming agent at any time during the injection process of the cylinder. injection molding equipment. 2. The injection molding apparatus for foam molded products according to claim 1, wherein a sub-cylinder connected to the rear of the mixing nozzle is connected to the cylinder head via a connecting pipe. . 3. The control mechanism for feeding or stopping the mixture in the sub-cylinder to the rear of the mixing nozzle at any time during the injection process of the cylinder is a valve that operates in electrical conjunction with the screw. An injection molding apparatus for a foam molded product according to claim 1 or 2. 4. Any one of claims 1 to 3, characterized in that the sub-cylinder is provided with a sub-screw for injecting the mixture, and the injection capacity is 5 to 10% of the injection capacity of the cylinder. An injection molding device for a foam molded product according to claim 1. 5 In an injection molding method in which a thermoplastic resin is shot from a cylinder head into a mold using a cylinder screw, a mixture of a thermoplastic resin of the same type as the thermoplastic resin and a blowing agent is supplied into a sub-cylinder prepared in advance, and the The mixture of thermoplastic resin and foaming agent in the secondary cylinder is injected at any time during the injection process of the cylinder, and the mixture is mixed with the thermoplastic resin from the cylinder by a mixing nozzle interposed between the cylinder head and the mold. A method for injection molding foam molded products, which is characterized by continuously shooting into a mold while kneading. 6. Claim 5, wherein the arbitrary timing during the injection process of the cylinder is selected from the beginning, middle, or end of the injection of the thermoplastic resin from the cylinder.
Injection molding method for foam molded products described in Section. 7. In an injection molding method in which a thermoplastic resin is shot from a cylinder head into a mold using a cylinder screw, a different type of thermoplastic resin and a blowing agent that are compatible with the thermoplastic resin are supplied into a sub-cylinder prepared in advance, The mixture of thermoplastic resin and foaming agent in the sub-cylinder is injected at any time during injection of the cylinder, and the mixture is mixed with the thermoplastic resin from the cylinder by a mixing nozzle interposed between the cylinder head and the mold. An injection molding method for foam molded products characterized by continuously shooting into a mold while kneading. 8. Claim 7, wherein the arbitrary time during the injection process of the cylinder is selected from the beginning, middle, or end of the injection of the thermoplastic resin from the cylinder.
Injection molding method for foam molded products described in Section.
JP56089136A 1981-06-10 1981-06-10 Method and apparatus for injection molding of expanded molding Granted JPS57203524A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56089136A JPS57203524A (en) 1981-06-10 1981-06-10 Method and apparatus for injection molding of expanded molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56089136A JPS57203524A (en) 1981-06-10 1981-06-10 Method and apparatus for injection molding of expanded molding

Publications (2)

Publication Number Publication Date
JPS57203524A JPS57203524A (en) 1982-12-13
JPS6153931B2 true JPS6153931B2 (en) 1986-11-20

Family

ID=13962457

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56089136A Granted JPS57203524A (en) 1981-06-10 1981-06-10 Method and apparatus for injection molding of expanded molding

Country Status (1)

Country Link
JP (1) JPS57203524A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5276373B2 (en) * 2008-07-24 2013-08-28 花王株式会社 Filling dish for powder cosmetics
JP2022552840A (en) 2019-10-15 2022-12-20 ビーエーエスエフ ソシエタス・ヨーロピア Method and Apparatus for Producing Marbled Molded Parts and Method for Producing the Apparatus

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2241002B2 (en) * 1971-09-07 1975-04-30 Hanning, Robert, Campinone D'italia (Italien) Method and device for the injection molding of plastic molded parts with a smooth shell and a porous core
CH566207A5 (en) * 1972-12-07 1975-09-15 Siemag Siegener Masch Bau
DE2500972A1 (en) * 1975-01-11 1976-07-15 Schloemann Siemag Ag Injection mouldings of thermoplastics with expansion agents - mixing head between plasticiser and buffer chamber improves product quality
DE2623308C3 (en) * 1976-05-25 1980-07-31 Schloemann-Siemag Ag, 4000 Duesseldorf Device for the discontinuous production of molded parts from thermoplastic material
JPS5356258A (en) * 1976-11-01 1978-05-22 Asahi Dow Ltd Injection molding machine nozzle
JPS6016326B2 (en) * 1977-04-27 1985-04-25 旭化成株式会社 Multilayer molded body and its molding method and device
JPS5314759A (en) * 1976-07-27 1978-02-09 Asahi Dow Ltd Method and device for injection molding multiilayer molded article
JPS5378262A (en) * 1976-12-23 1978-07-11 Asahi Dow Ltd Composite shapes molding apparatus
DE2705291A1 (en) * 1977-02-09 1978-08-10 Schloemann Siemag Ag METHOD AND DEVICE FOR THE PRODUCTION OF MOLDED PARTS FROM THERMOPLASTIC PLASTIC

Also Published As

Publication number Publication date
JPS57203524A (en) 1982-12-13

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