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JP2003062892A - Extrusion-molding method for expansion-molding by double-screw extruder - Google Patents

Extrusion-molding method for expansion-molding by double-screw extruder

Info

Publication number
JP2003062892A
JP2003062892A JP2001259270A JP2001259270A JP2003062892A JP 2003062892 A JP2003062892 A JP 2003062892A JP 2001259270 A JP2001259270 A JP 2001259270A JP 2001259270 A JP2001259270 A JP 2001259270A JP 2003062892 A JP2003062892 A JP 2003062892A
Authority
JP
Japan
Prior art keywords
resin material
screw
foaming agent
molten resin
screw extruder
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.)
Pending
Application number
JP2001259270A
Other languages
Japanese (ja)
Inventor
Kuniaki Endo
邦昭 遠藤
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.)
Shibaura Machine Co Ltd
Original Assignee
Toshiba Machine 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 Toshiba Machine Co Ltd filed Critical Toshiba Machine Co Ltd
Priority to JP2001259270A priority Critical patent/JP2003062892A/en
Publication of JP2003062892A publication Critical patent/JP2003062892A/en
Pending 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/68Barrels or cylinders
    • B29C48/682Barrels or cylinders for twin screws
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/51Screws with internal flow passages, e.g. for molten material
    • B29C48/515Screws with internal flow passages, e.g. for molten material for auxiliary fluids, e.g. foaming agents
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/57Screws provided with kneading disc-like elements, e.g. with oval-shaped elements

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Abstract

(57)【要約】 【課題】 1台の押出機で発泡成形が出来る完全噛合形
同方向回転二軸押出機による発泡押出成形方法を提供す
る。 【解決手段】 先端部にダイを取付けた完全噛合形同
方向回転二軸押出機の材料供給口より樹脂材料を供給
し、加熱・溶融した後、発泡剤を注入し、先端の前記ダ
イから押出す発泡成形の押出成形方法において、スクリ
ュ溝内を樹脂材料で充満・溶融させた後、更に下流にス
クリュ溝内を空隙の有る状態にした領域で発泡させるた
めの発泡剤を注入し混合して、発泡剤入りの溶融樹脂を
ダイ方向に移送させながらバレルやスクリュ軸の冷却手
段により発泡剤入り溶融樹脂材料を冷却して前記ダイか
ら押出す前記二軸押出機による発泡成形の押出成形方法
とした。
PROBLEM TO BE SOLVED: To provide a foaming extrusion molding method using a completely meshing co-rotating twin-screw extruder capable of foaming molding with one extruder. SOLUTION: A resin material is supplied from a material supply port of a fully meshing co-rotating twin-screw extruder having a die attached to a tip, heated and melted, a foaming agent is injected, and a push is made from the die at the tip. In the extrusion molding method of foaming out, after filling and melting the inside of the screw groove with a resin material, a foaming agent for foaming in a region where the inside of the screw groove has a space further downstream is injected and mixed. An extrusion molding method of foam molding by the twin-screw extruder, in which the molten resin containing a foaming agent is cooled by means of a barrel or screw shaft while the molten resin containing a foaming agent is transferred in a die direction, and is extruded from the die. did.

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】本発明は先端部にダイを取付
けた完全噛合形同方向回転二軸押出機による押出し方法
に係り、特に樹脂材料を加熱溶融した後発泡剤を注入
し、先端のダイから押出す二軸押出機による発泡成形の
押出成形方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an extrusion method using a completely meshing type co-rotating twin-screw extruder having a die attached to the tip, and in particular, a resin material is heated and melted, and then a foaming agent is injected to the die at the tip. TECHNICAL FIELD The present invention relates to an extrusion molding method for foam molding using a twin-screw extruder that extrudes from a sheet.

【0002】[0002]

【従来の技術】従来、この種の発泡成形の押出成形方法
を図4により説明すると、単軸スクリュの第一押出機1
の材料供給口2より樹脂材料を供給し、加熱・溶融した
後、この溶融樹脂に液状の発泡剤をポンプ3により注入
し溶融樹脂材料に混合した後、単軸スクリュの第二押出
機4の材料供給口5内へ導入し、この第二押出機4内で
発泡剤入り溶融樹脂を冷却して、ダイ6で賦形し、ダイ
からでた大気中で発泡させて発泡製品7として押出すよ
うな成形方法である。
2. Description of the Related Art Conventionally, an extrusion molding method of this type of foam molding will be described with reference to FIG.
After the resin material is supplied from the material supply port 2 and heated and melted, the liquid foaming agent is injected into the molten resin by the pump 3 and mixed with the molten resin material, and then the second extruder 4 of the single screw is used. Introduced into the material supply port 5, the molten resin containing the foaming agent is cooled in the second extruder 4, shaped by the die 6, foamed in the atmosphere from the die and extruded as a foamed product 7. Such a molding method.

【0003】[0003]

【発明が解決しょうとする課題】しかしながら、前述の
従来方法は単軸押出機を2台使用するために設備費用が
大きく掛り、また据付面積も大きくなり、省エネルギ、
省スペース化が実現出来なかった。
However, the above-mentioned conventional method requires a large equipment cost because it uses two single-screw extruders, and also requires a large installation area, resulting in energy saving,
Space saving could not be realized.

【0004】本発明の目的は押出機を2台使用し設備費
用が大きく掛り、また据付面積も大きくなるという欠点
を取除き、1台の押出機で、省エネルギ、省スペース化
が実現できる完全噛合形同方向回転二軸押出機による発
泡成形の押出成形方法を提供することにある。
The object of the present invention is to eliminate the drawbacks that two extruders are used, the facility cost is large, and the installation area is large. One extruder can realize energy saving and space saving. An object of the present invention is to provide an extrusion molding method of foam molding by a mesh type co-rotating twin-screw extruder.

【0005】[0005]

【課題を解決するための手段】前述の目的を達成するた
め本発明は、先端部にダイを取付けた完全噛合形同方向
回転二軸押出機の材料供給口より樹脂材料を供給し、加
熱・溶融した後、発泡剤を注入し、先端の前記ダイから
押出す発泡成形の押出成形方法において、スクリュ溝内
を樹脂材料で充満・溶融させた後、更に下流にスクリュ
溝内を空隙の有る状態にした領域で発泡させるための発
泡剤を注入し混合して、発泡剤入りの溶融樹脂材料をダ
イ方向に移送させながらバレルやスクリュ軸の冷却手段
により発泡剤入り溶融樹脂材料を冷却してダイから押出
す前記二軸押出機による発泡成形の押出成形方法とし
た。
In order to achieve the above-mentioned object, the present invention supplies a resin material through a material supply port of a completely meshing type co-rotating twin-screw extruder having a die attached to its tip, and heats it. In the extrusion molding method of foam molding in which a foaming agent is injected after being melted and extruded from the die at the tip, after the screw groove is filled and melted with a resin material, there is a void in the screw groove further downstream. Injecting and mixing the foaming agent for foaming in the area, the molten resin material containing the foaming agent is cooled by the cooling means of the barrel or screw shaft while transferring the molten resin material containing the foaming agent in the die direction. The extrusion molding method of foam molding using the twin-screw extruder is used.

【0006】また、前記発泡剤の注入域は樹脂材料を溶
融させた後、前記溶融樹脂材料で前記スクリュ溝内を充
満状態にした領域であることを特徴とする前記二軸押出
機による発泡成形の押出成形方法とした。更にまた、前
記発泡剤の注入域は樹脂材料を溶融させた後、前記溶融
樹脂材料でスクリュ溝内を充満状態にした領域と更にそ
の下流にあるスクリュ溝内を溶融樹脂材料が空隙の有る
状態にした領域であることを特徴とする前記二軸押出機
による発泡成形の押出成形方法とした。そして、前記冷
却手段は前記バレル内に冷却媒体を導入するバレル冷却
孔を設けたことを特徴とする前記二軸押出機による発泡
成形の押出成形方法とした。そしてまた、前記冷却手段
は前記スクリュ軸内に冷却媒体を導入するスクリュ冷却
孔を設けたことを特徴とする前記二軸押出機による発泡
成形の押出成形方法とした。
Further, the injection area of the foaming agent is an area in which the screw groove is filled with the molten resin material after the resin material is melted, and the foam molding by the twin-screw extruder is performed. The extrusion molding method of Furthermore, in the injection region of the foaming agent, after the resin material is melted, the molten resin material has voids in the region where the screw groove is filled with the molten resin material and in the screw groove further downstream thereof. In the extrusion molding method of foam molding using the twin-screw extruder, The cooling means is provided with a barrel cooling hole for introducing a cooling medium into the barrel, which is an extrusion molding method for foam molding by the twin-screw extruder. The cooling means is provided with a screw cooling hole for introducing a cooling medium into the screw shaft, which is an extrusion molding method for foam molding by the twin-screw extruder.

【0007】これにより完全噛合形同方向回転二軸押出
機一台で発泡成形が可能となり、設備費用の低減と据付
面積の縮小も可能となり省エネルギ、省スペース化が実
現された。
As a result, foam molding can be performed with one completely meshing type co-rotating twin-screw extruder, and the equipment cost and the installation area can be reduced, thus saving energy and space.

【0008】[0008]

【発明の実施の形態】以下本発明の実施の形態を図1の
(イ)、(ロ)、および図2、図3により説明する。完
全噛合形同方向回転二軸押出機10のバレル組立11の
内径部には完全に噛合って同方向回転するスクリュ組立
12が回転自在に挿入されており、また、バレル組立1
1の基部には材料供給口13が設けてあり、樹脂材料を
連続的に一定量ずつ供給する材料供給装置14が設置さ
れ、樹脂材料15を定量ずつ連続的にバレル組立11内
に有るスクリュ組立12へ供給する。スクリュ組立12
は図1(ロ)のA部分で樹脂材料15を搬送させ、B部
分で樹脂材料15を溶融させる。このB部分はニーディ
ングディスク16から構成され、樹脂材料15の混練・
溶融部分を受け持つ。また、B部分ではバレル11の内
部のスクリュ溝内は材料樹脂15で完全に充満されてい
る。その充満状態を図1の(ロ)のB部分で示す。そし
て溶融樹脂材料15aで完全に充満されたB部分は材料
供給口13側との間でポリマーシール(樹脂シール)の
役目を果たし、C部分で発生したガス等はB部分の前述
のポリマーシールの遮断壁で完全にA側へ行かない様に
している。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to (a) and (b) of FIG. 1, and FIGS. A screw assembly 12 that completely meshes and rotates in the same direction is rotatably inserted into an inner diameter portion of a barrel assembly 11 of a completely meshing type co-rotating twin-screw extruder 10.
A material supply port 13 is provided at the base of No. 1 and a material supply device 14 for continuously supplying a constant amount of a resin material is installed. Supply to 12. Screw assembly 12
1 conveys the resin material 15 at the portion A in FIG. 1B and melts the resin material 15 at the portion B. This part B is composed of a kneading disc 16 and is used for kneading and mixing the resin material 15.
Responsible for the molten part. In the portion B, the screw groove inside the barrel 11 is completely filled with the resin material 15. The filled state is indicated by B in FIG. The portion B completely filled with the molten resin material 15a serves as a polymer seal (resin seal) with the material supply port 13 side, and the gas or the like generated in the portion C is of the polymer seal of the portion B described above. The blocking wall prevents you from going to the A side completely.

【0009】次にB部分でポリマーシールの役目を果た
した溶融樹脂材料15aは図1(ロ)のC部分に移送さ
れる。その場合、溶融樹脂材料15aはC部分ではスク
リュ17の溝内は空隙の有る状態になっている。次に図
1(ロ)のD部分へ移送されるが、D部分の領域では先
端のダイなどを通過する流動抵抗に打ち勝つだけの昇圧
が必要であり、溶融樹脂材料15aは自動的にスクリュ
17の溝内が完全に充満状態となる。その結果、C部分
はB部分とD部分で完全に遮断された蜜閉状態となる。
そして、D部分を通過した溶融材料樹脂15は最終的に
ダイ18で賦形されて押し出され、空気中に開放された
直後に発泡して発泡製品19となる。
Next, the molten resin material 15a which has functioned as a polymer seal at the portion B is transferred to the portion C of FIG. In this case, the molten resin material 15a has voids in the groove of the screw 17 at the portion C. Next, it is transferred to the D portion of FIG. 1B, but in the region of the D portion, it is necessary to raise the pressure so as to overcome the flow resistance passing through the die at the tip, and the molten resin material 15a automatically moves to the screw 17 The inside of the groove will be completely filled. As a result, the C portion is in a tightly closed state in which the B portion and the D portion are completely blocked.
Then, the molten material resin 15 that has passed through the portion D is finally shaped by the die 18 and extruded, and immediately after being released into the air, foams to become a foamed product 19.

【0010】以上、スクリュ組立12の樹脂材料の充満
状態を図1(ロ)のグラフで示した。
The filling state of the resin material of the screw assembly 12 is shown in the graph of FIG.

【0011】材料供給口13からバレル組立11内に供
給された樹脂材料15は前述したようにB部分で発熱・
溶融されるが、その時、発泡剤20をポンプ21により
B部分のニーディングディスク16面上の溶融樹脂材料
15aに注入する場合もあり、また、B部分の直後のC
部分で注入される場合もある。また、B部分とC部分の
2個所から発泡剤20を注入することもある。この場合
発泡剤20の注入はB部分では液体状で注入され、ニー
ディングディスク16上で溶融樹脂材料15aと効率良
く攪拌・混合される。また、C部分へ発泡剤20を注入
する場合はスクリュ溝内は空隙部が有る為、バレル内径
面の注入直前までは液体状態であっても、注入された後
は空間に噴射され、しかも雰囲気が高い温度である為に
発泡剤20の液体はガス体に変化し、そのガス状の発泡
剤20は拡散速度も早くなり、また、完全噛合形同方向
回転二軸押出機のスクリュは、片方のスクリュが他方の
スクリュ表面をセルフワイピングしながら回転し、スク
リュ同士の噛合部分では溶融樹脂材料15aは表面更新
効果が行なわれて、いつも新しい溶融樹脂材料15aの
表面がガス状態の発泡剤20に晒されるので、ガス状の
発泡剤20は溶融樹脂材料15aに活発に含浸されてい
くことになる。
The resin material 15 supplied from the material supply port 13 into the barrel assembly 11 generates heat in the portion B as described above.
It is melted, but at that time, the foaming agent 20 may be injected into the molten resin material 15a on the surface of the kneading disk 16 in the B portion by the pump 21, and C immediately after the B portion may be injected.
It may be injected in parts. In addition, the foaming agent 20 may be injected from two locations, the B portion and the C portion. In this case, the foaming agent 20 is injected in a liquid state at the portion B, and is efficiently stirred and mixed with the molten resin material 15a on the kneading disk 16. Further, when the foaming agent 20 is injected into the C portion, since there is a void in the screw groove, even if it is in a liquid state until just before the injection of the barrel inner diameter surface, it is injected into the space after injection, and the atmosphere Because of the high temperature, the liquid of the foaming agent 20 changes into a gas body, the diffusion speed of the gaseous foaming agent 20 also increases, and the screw of the complete meshing co-rotating twin-screw extruder has one side. Screw rotates while self-wiping the surface of the other screw, and the surface of the molten resin material 15a is renewed at the meshing portions of the screws, so that the surface of the new molten resin material 15a always becomes the foaming agent 20 in the gas state. As it is exposed, the gaseous foaming agent 20 is actively impregnated into the molten resin material 15a.

【0012】一方、バレル組立11は図2のバレルブロ
ック26等を目的に応じて複数個組合わせる構成になっ
ている。また、図1(ロ)C部分では高温度の溶融樹脂
材料15aを最適温度まで冷却して、ダイ18の出口で
発泡体形成に必要な最適粘度になるように調整する必要
がある。そのためにバレルブロック26にバレル冷却孔
22を設けて、そこに冷却水や冷却油等の冷却媒体を通
してバレルブロック26全体を冷やし、バレル内径面よ
り溶融樹脂材料15aの過剰発熱量を奪い溶融樹脂材料
15aの温度を下げ、最適粘度に調整する。また、スク
リュ組立12は図3に示すようにスクリュ軸25のスク
リュ冷却孔23に冷却パイプ24をスクリュ軸25の基
部を支点とする片持ち状態で設置し、冷却水や冷却油等
の冷却媒体を矢印aのようにパイプ24の内径部からス
クリュ孔径部23に導き、スクリュ組立12を内部から
冷却することにより、スクリュ組立12のスクリュ外表
面を通過する溶融樹脂材料15aの過剰発熱量を除去
し、溶融樹脂材料15aの温度を発泡成形の最適温度に
冷却調整するようになっている。溶融樹脂材料15aの
過剰発熱量に対し、バレル組立11とスクリュ組立12
の上記冷却装置を同時に使用しても良いし、或いは片方
づつ別々に使用しても良い。
On the other hand, the barrel assembly 11 is constructed by combining a plurality of barrel blocks 26, etc. of FIG. 2 according to the purpose. Further, in the portion C of FIG. 1B, it is necessary to cool the molten resin material 15a having a high temperature to the optimum temperature and adjust the viscosity of the molten resin material 15a at the outlet of the die 18 to the optimum viscosity required for foam formation. To this end, the barrel cooling holes 22 are provided in the barrel block 26, and the entire barrel block 26 is cooled by passing a cooling medium such as cooling water or cooling oil therethrough to deprive the excessive heat generation amount of the molten resin material 15a from the inner diameter surface of the barrel to melt the molten resin material. Lower the temperature of 15a and adjust to the optimum viscosity. In the screw assembly 12, as shown in FIG. 3, a cooling pipe 24 is installed in a screw cooling hole 23 of a screw shaft 25 in a cantilever state with a base of the screw shaft 25 as a fulcrum, and a cooling medium such as cooling water or cooling oil is provided. Is guided from the inner diameter portion of the pipe 24 to the screw hole diameter portion 23 as indicated by the arrow a, and the screw assembly 12 is cooled from the inside, thereby removing the excessive heat generation amount of the molten resin material 15a passing through the screw outer surface of the screw assembly 12. Then, the temperature of the molten resin material 15a is cooled and adjusted to the optimum temperature for foam molding. The barrel assembly 11 and the screw assembly 12 against the excessive heating value of the molten resin material 15a.
The above cooling devices may be used simultaneously, or one of them may be used separately.

【0013】[0013]

【発明の効果】以上説明したように本発明の押出し方法
は、押出機を2台使用し設備費用が大きく掛り、また据
付面積も大きくなるという欠点を取除き、1台の押出機
で省エネルギ、省スペース化が実現できる完全噛合形同
方向回転二軸押出機による発泡成形の押出成形方法を提
供出来た。
As described above, the extrusion method of the present invention eliminates the drawbacks of using two extruders, which requires a large equipment cost and requires a large installation area. Thus, we have been able to provide an extrusion molding method for foam molding using a complete mesh type co-rotating twin-screw extruder that can save space.

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

【図1】(イ)は本発明の1実施形態例を示す二軸押出
機による発泡成形の押出成形方法の説明図、(ロ)はス
クリュ組立の樹脂材料の充満状態を説明した図である。
FIG. 1A is an explanatory view of an extrusion molding method of foam molding by a twin-screw extruder showing one embodiment of the present invention, and FIG. 1B is a view explaining a filled state of a resin material for screw assembly. .

【図2】本発明の1実施形態例を示す二軸押出機による
発泡成形の押出成形方法の説明図で、バレルブロックに
設けたバレル冷却の説明図である。
FIG. 2 is an explanatory diagram of an extrusion molding method of foam molding by a twin-screw extruder showing an embodiment of the present invention, and is an explanatory diagram of barrel cooling provided in a barrel block.

【図3】本発明の1実施形態例を示す二軸押出機による
発泡成形の押出成形方法の説明図で、スクリュ軸に設け
たスクリュ冷却の説明図である。
FIG. 3 is an explanatory diagram of an extrusion molding method of foam molding by a twin-screw extruder showing one embodiment of the present invention, and is an explanatory diagram of screw cooling provided on a screw shaft.

【図4】従来の発泡成形の内、押出成形方法の1実施例
の説明図である。
FIG. 4 is an explanatory diagram of one example of an extrusion molding method among conventional foam molding.

【符号の説明】[Explanation of symbols]

10 完全噛合形同方向回転二軸押出機 11 バレル組立 12 スクリュ組立 13 材料供給口 14 材料供給装置 15 樹脂材料 15a 溶融樹脂材料 16 ニーディングディスク 17 スクリュ 18 ダイ 19 発泡製品 20 発泡剤 21 ポンプ 22 バレル冷却孔 23 スクリュ冷却孔 24 冷却パイプ 25 スクリュ軸 26 バレルブロック 10 Perfect mesh type co-rotating twin screw extruder 11 barrel assembly 12 screw assembly 13 Material supply port 14 Material supply device 15 Resin material 15a Molten resin material 16 kneading disc 17 screws 18 dies 19 Foam products 20 Foaming agent 21 pumps 22 barrel cooling holes 23 Screw cooling hole 24 Cooling pipe 25 screw shaft 26 barrel block

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 先端部にダイを取付けた完全噛合形同方
向回転二軸押出機の材料供給口より樹脂材料を供給し、
加熱・溶融した後、発泡剤を注入し、先端の前記ダイか
ら押出す発泡成形の押出成形方法において、スクリュ溝
内を樹脂材料で充満・溶融させた後、更に下流にスクリ
ュ溝内を空隙の有る状態にした領域で発泡させるための
発泡剤を注入し混合して、発泡剤入りの溶融樹脂材料を
ダイ方向に移送させながらバレルやスクリュ軸の冷却手
段により発泡剤入り溶融樹脂材料を冷却してダイから押
出す前記二軸押出機による発泡成形の押出成形方法。
1. A resin material is supplied from a material supply port of a completely meshing type co-rotating twin-screw extruder having a die attached to its tip,
In the extrusion molding method of foam molding in which a foaming agent is injected after heating and melting and extruded from the die at the tip, after the screw groove is filled and melted with a resin material, there is a void in the screw groove further downstream. Injecting and mixing the foaming agent for foaming in the existing state, and cooling the foaming agent-containing molten resin material by the cooling means of the barrel and screw shaft while transferring the foaming agent-containing molten resin material in the die direction. Extrusion molding method of foam molding by the twin-screw extruder.
【請求項2】 前記発泡剤の注入域は樹脂材料を溶融さ
せた後、前記溶融樹脂でスクリュ溝内を充満状態にした
領域であることを特徴とする請求項1記載の二軸押出機
による発泡成形の押出成形方法。
2. The twin-screw extruder according to claim 1, wherein the injection area of the foaming agent is an area in which the screw groove is filled with the molten resin after the resin material is melted. Extrusion molding method for foam molding.
【請求項3】 前記発泡剤の注入域は樹脂材料を溶融さ
せた後、前記溶融樹脂材料でスクリュ溝内を充満状態に
した領域と更にその下流にあるスクリュ溝内を溶融樹脂
材料が空隙の有る状態にした領域であることを特徴とす
る請求項1記載の二軸押出機による発泡成形の押出成形
方法。
3. The molten resin material is melted in the injection region of the foaming agent, and then a region in which the screw groove is filled with the molten resin material and a screw groove located further downstream of the region are filled with the molten resin material. The extrusion molding method for foam molding by a twin-screw extruder according to claim 1, wherein the region is an existing region.
【請求項4】 前記冷却手段は前記バレル内に冷却媒体
を導入するバレル冷却孔を設けたことを特徴とする請求
項1、2、3の内いずれか一記載の二軸押出機による発
泡成形の押出成形方法。
4. The foam molding by a twin-screw extruder according to claim 1, wherein the cooling means is provided with a barrel cooling hole for introducing a cooling medium into the barrel. Extrusion method.
【請求項5】 前記冷却手段は前記スクリュ軸内に冷却
媒体を導入するスクリュ冷却孔を設けたことを特徴とす
る請求項1、2、3の内いずれか一記載の二軸押出機に
よる発泡成形の押出成形方法。
5. The foaming by the twin-screw extruder according to claim 1, wherein the cooling means is provided with a screw cooling hole for introducing a cooling medium into the screw shaft. Extrusion molding method.
JP2001259270A 2001-08-29 2001-08-29 Extrusion-molding method for expansion-molding by double-screw extruder Pending JP2003062892A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001259270A JP2003062892A (en) 2001-08-29 2001-08-29 Extrusion-molding method for expansion-molding by double-screw extruder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001259270A JP2003062892A (en) 2001-08-29 2001-08-29 Extrusion-molding method for expansion-molding by double-screw extruder

Publications (1)

Publication Number Publication Date
JP2003062892A true JP2003062892A (en) 2003-03-05

Family

ID=19086667

Family Applications (1)

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

Country Link
JP (1) JP2003062892A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101809421B1 (en) * 2017-09-06 2017-12-14 거원산업 주식회사 Apparatus for finishing edge of trunk mat
KR101815833B1 (en) * 2016-04-18 2018-01-05 이응기 An extruder for extruding porous plastics
CN108943643A (en) * 2018-08-06 2018-12-07 南京欧纳壹有机光电有限公司 A kind of raw material premix device of modified plastics double helix extrusion molding system
JP2019171845A (en) * 2018-03-27 2019-10-10 パナソニック株式会社 Manufacturing apparatus of composite resin composition and manufacturing method
JP2023154008A (en) * 2018-03-27 2023-10-18 パナソニックホールディングス株式会社 Apparatus and method for producing composite resin composition

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5269469A (en) * 1975-12-05 1977-06-09 Bayer Ag Device for extrusion molding temperature sensitive thermoplastic to semiiproduct
JPS52133381A (en) * 1976-05-04 1977-11-08 Teijin Ltd Process for expansion molding by 22shaft extruder
JP2001179808A (en) * 1999-12-22 2001-07-03 Toshiba Mach Co Ltd Foam continuous molding method and apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5269469A (en) * 1975-12-05 1977-06-09 Bayer Ag Device for extrusion molding temperature sensitive thermoplastic to semiiproduct
JPS52133381A (en) * 1976-05-04 1977-11-08 Teijin Ltd Process for expansion molding by 22shaft extruder
JP2001179808A (en) * 1999-12-22 2001-07-03 Toshiba Mach Co Ltd Foam continuous molding method and apparatus

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101815833B1 (en) * 2016-04-18 2018-01-05 이응기 An extruder for extruding porous plastics
KR101809421B1 (en) * 2017-09-06 2017-12-14 거원산업 주식회사 Apparatus for finishing edge of trunk mat
JP2019171845A (en) * 2018-03-27 2019-10-10 パナソニック株式会社 Manufacturing apparatus of composite resin composition and manufacturing method
JP2023154008A (en) * 2018-03-27 2023-10-18 パナソニックホールディングス株式会社 Apparatus and method for producing composite resin composition
JP7372741B2 (en) 2018-03-27 2023-11-01 パナソニックホールディングス株式会社 Manufacturing device and method for composite resin composition
JP7587648B2 (en) 2018-03-27 2024-11-20 パナソニックホールディングス株式会社 Apparatus and method for producing composite resin composition
JP2025016782A (en) * 2018-03-27 2025-02-04 パナソニックホールディングス株式会社 Apparatus and method for producing composite resin composition
CN108943643A (en) * 2018-08-06 2018-12-07 南京欧纳壹有机光电有限公司 A kind of raw material premix device of modified plastics double helix extrusion molding system

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