JPS62288025A - Control of extruding temprature in synthetic resin extrusion molder - Google Patents
Control of extruding temprature in synthetic resin extrusion molderInfo
- Publication number
- JPS62288025A JPS62288025A JP61132185A JP13218586A JPS62288025A JP S62288025 A JPS62288025 A JP S62288025A JP 61132185 A JP61132185 A JP 61132185A JP 13218586 A JP13218586 A JP 13218586A JP S62288025 A JPS62288025 A JP S62288025A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- cylinder
- head
- dice
- thermometer
- 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
Links
- 238000001125 extrusion Methods 0.000 title claims description 47
- 229920003002 synthetic resin Polymers 0.000 title claims description 11
- 239000000057 synthetic resin Substances 0.000 title claims description 11
- 229920005989 resin Polymers 0.000 claims abstract description 21
- 239000011347 resin Substances 0.000 claims abstract description 21
- 239000013307 optical fiber Substances 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 abstract description 7
- 239000011247 coating layer Substances 0.000 abstract description 6
- 239000011521 glass Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 238000010292 electrical insulation Methods 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 description 12
- 239000002994 raw material Substances 0.000 description 9
- 229920005992 thermoplastic resin Polymers 0.000 description 4
- 238000000465 moulding Methods 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- 238000002845 discoloration Methods 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 238000004891 communication Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000004043 responsiveness Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/78—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
- B29C48/86—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the nozzle zone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/78—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
- B29C48/80—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the plasticising zone, e.g. by heating cylinders
- B29C48/83—Heating or cooling the cylinders
- B29C48/832—Heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/78—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
- B29C48/86—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the nozzle zone
- B29C48/865—Heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
Landscapes
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Radiation Pyrometers (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
3、発明の詳細な説明
[発明の利用分野1
本発明は、熱可塑性樹脂等の合成樹脂押出成形機におけ
る押出温度の制御方法に関するものであり、特に押出成
形機における押出部所の温度を光ファイバ型赤外線温度
計を使用して測定し、それによって制御する方法に関す
るものである。Detailed Description of the Invention 3. Detailed Description of the Invention [Field of Application of the Invention 1 The present invention relates to a method for controlling extrusion temperature in an extrusion molding machine for synthetic resins such as thermoplastic resins, and in particular to a method for controlling extrusion temperature in an extrusion molding machine. The present invention relates to a method for measuring the temperature at an extrusion site using an optical fiber type infrared thermometer and controlling the temperature accordingly.
[従来技術]
ポリエチレンやポリ塩化ビニル樹脂のごとき熱可塑性樹
脂の押出成形は、押出成形機のシリンダー内に配置され
た押出スクリューを回転させて供給した原料樹脂を加圧
しつつ搬送し、他方シリンダーあるいはダイスヘッドに
巻かれた例えば帯状電熱器(バンドヒーター)に通電し
、発熱させることによりシリンダーあるいはダイスヘッ
ドを加熱し、それによって加熱されたシリンダー内の原
料樹脂を加熱し軟化させ、これをダイスヘッドから押し
出してダイスヘッドの形状に対応した形状に成形するこ
とによって行われる。従来、このヒーターの温度制御は
、事前の温度設定によって行われていた。[Prior art] Extrusion molding of thermoplastic resins such as polyethylene and polyvinyl chloride resin involves rotating an extrusion screw placed in the cylinder of an extrusion molding machine to convey the supplied raw material resin while pressurizing it. For example, a band-shaped electric heater (band heater) wrapped around the die head is energized to generate heat, thereby heating the cylinder or the die head, which heats and softens the raw material resin in the heated cylinder, which is then heated to the die head. This is done by extruding it from a mold and molding it into a shape that corresponds to the shape of the die head. Conventionally, the temperature of this heater has been controlled by setting the temperature in advance.
[発明が解決しようとする問題点]
しかしながら上述した従来技術において、押出機のシリ
ンダーあるいはダイスヘッド内では、押出スクリューに
よる押圧により樹脂の圧力が高まり、押出機に対する設
定温度と樹脂の瀉麿とは必ずしも一致せず、通常この設
定温度よりも樹脂の温度の方が高くなりがちである。そ
のため例えば架橋剤を含有するポリエチレンを押出成形
する場合、架橋剤の反応湯度を越えるような温度で樹脂
を押し出すと、押出成形中に架橋反応が進み、ヤケを生
ずることになる。例えばこの押出成形品が高電圧用ケー
ブルの被覆層である場合には、このヤケが被覆層に混入
して被覆層の電気絶縁性を低下させる。このようにケー
ブル被覆層用の押出成形の場合には、特にシリンダー内
の原料樹脂の温度管理を厳密に行うことが必要である。[Problems to be Solved by the Invention] However, in the above-mentioned conventional technology, the pressure of the resin increases in the cylinder or die head of the extruder due to pressure by the extrusion screw, and the set temperature for the extruder and the melting rate of the resin are They do not necessarily match, and the resin temperature usually tends to be higher than this set temperature. Therefore, for example, when extruding polyethylene containing a crosslinking agent, if the resin is extruded at a temperature exceeding the reaction temperature of the crosslinking agent, the crosslinking reaction will proceed during extrusion, resulting in discoloration. For example, when this extrusion molded product is a coating layer of a high-voltage cable, this discoloration is mixed into the coating layer and reduces the electrical insulation properties of the coating layer. In this way, in the case of extrusion molding for a cable coating layer, it is necessary to strictly control the temperature of the raw resin in the cylinder.
[問題点を解決するだめの手段及び作用]本発明は、上
述した従来技術における問題点を解決するためになされ
たものであって、合成樹脂の押出成形機におりる押出樹
脂の真の押出温度を測定かつ制御し、安定した押出温度
を維持し得るようにすることを目的とするものである。[Means and operations for solving the problems] The present invention has been made to solve the problems in the prior art described above, and it is possible to achieve true extrusion of extruded resin into a synthetic resin extrusion molding machine. The purpose is to measure and control the temperature and maintain a stable extrusion temperature.
すなわち本発明は、合成樹脂押出成形機に33けるダイ
スヘッド部を流れる押出樹脂の温度を光ファイバ型赤外
線温度計により検出し、それによって上記シリンダーあ
るいはダイスヘッドの渇麿を制御することを特徴とする
合成樹脂押出成形機における押出温度の制御方法である
。That is, the present invention is characterized in that the temperature of the extruded resin flowing through the die head section 33 of the synthetic resin extrusion molding machine is detected by an optical fiber type infrared thermometer, and the drying temperature of the cylinder or the die head is thereby controlled. This is a method for controlling extrusion temperature in a synthetic resin extrusion molding machine.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
まず本発明において使用される合成樹脂押出成形機につ
いてその概要を説明する。押出成形機は基本的には筒状
をなし成形容器となる゛シリンダー内′、その内部に配
置される゛押出スクリュー″、該シリンダーの先端に取
り付けられた″゛ダイスヘツド″該シリンダーの後方に
かつ該シリンダーに連通して配置され、樹脂原料を供給
するための″ホッパー″、該押出スクリコーを回転させ
る回転駆動機構、該シリンダーを加熱づるための加熱装
置及びその温麿制御I1機構からなる。この押出成形機
において、該シリンダーの内部には押出スクリコーが回
転駆動機構の駆動力により回転覆るように配置されてい
る。通常、シリンダーの内部は、その先端にゆくに従っ
てやや細くなる形状となっており、また押出スクリュー
のピッチはその先端にゆくに従って次第に小さくなるよ
うに形成されている。その結果シリンダーの内壁と押出
スクリューの谷で形成される空隙はその先端にゆくに従
って小さくなるので、ホッパーから供給され、続いて押
出スクリューの回転に伴ってその先端に向かって運ばれ
る樹脂原料は、その先端にゆくに従って加圧される。さ
らにシリンダーには、それを加熱する加熱装置とその温
度制御III機構が取り付けられており、それらの作動
により樹脂原料は、必要かつ十分な温度に加熱されるよ
うになっている。First, the outline of the synthetic resin extrusion molding machine used in the present invention will be explained. An extrusion molding machine basically has a cylindrical shape and a molded container, an "extrusion screw" placed inside the cylinder, a "dice head" attached to the tip of the cylinder, and a "dice head" located behind the cylinder. It is arranged in communication with the cylinder and consists of a "hopper" for supplying the resin raw material, a rotation drive mechanism for rotating the extrusion screw, a heating device for heating the cylinder, and its temperature control I1 mechanism. In an extrusion molding machine, an extrusion screw is placed inside the cylinder so as to be rotated and covered by the driving force of a rotational drive mechanism.Usually, the inside of the cylinder has a shape that tapers slightly toward its tip. Also, the pitch of the extrusion screw is formed so that it gradually becomes smaller toward the tip.As a result, the gap formed between the inner wall of the cylinder and the valley of the extrusion screw becomes smaller toward the tip, so that the pitch of the extrusion screw becomes smaller as it goes toward the tip. Then, as the extrusion screw rotates, the resin raw material is conveyed toward the tip and is pressurized as it moves toward the tip.Furthermore, the cylinder is equipped with a heating device to heat it and its temperature control III mechanism. The resin raw materials are heated to a necessary and sufficient temperature by their operation.
さらにシリンダーの先端には、その加熱により可塑化し
た樹脂原料を押し出しつつ成形する型となるダイスヘッ
ドが取り付けられている。Furthermore, a die head is attached to the tip of the cylinder, which serves as a mold for extruding and molding the resin raw material that has been plasticized by heating.
基本的には上述のように構成された押出成形機は、まず
押出スクリュー回転駆動機構を作動させて押出スクリュ
ーを所定の速度で回転させ、またシリンダーに取り付け
られた加熱装置に通電し、と共にその温度制御機構を作
動させてシリンダーを加熱し、合成樹脂を成形するに適
した温度に維持する。そして通常はペレット状に一次的
に成形した合成樹脂原料がホッパーから連続的に投入さ
れる。原料ベレットは、押出スクリコーの回転と共にシ
リンダー内を次第に先端に向かって移動して(搬送され
て)ゆく。シリンダーは、前述したように樹脂が可塑化
するに適当な温度に加熱されており、また押出スクリュ
ーの回転により、原料ペレットは搬送と共に加熱されて
シリンダー内の先端部では可塑化して流動し、ダイスヘ
ッドの孔部から押し出される。この時、樹脂はダイスヘ
ッドの孔の形状に対応した形状に成形されるのである。Basically, an extrusion molding machine configured as described above first operates the extrusion screw rotation drive mechanism to rotate the extrusion screw at a predetermined speed, and also energizes the heating device attached to the cylinder. The temperature control mechanism is activated to heat the cylinder and maintain it at a temperature suitable for molding the synthetic resin. Usually, synthetic resin raw materials that have been primarily formed into pellets are continuously fed from a hopper. The raw material pellet is gradually moved (transported) inside the cylinder toward the tip as the extrusion screw rotates. As mentioned above, the cylinder is heated to an appropriate temperature for plasticizing the resin, and as the extrusion screw rotates, the raw material pellets are heated as they are conveyed, plasticize and flow at the tip of the cylinder, and then pass through the die. It is pushed out from the hole in the head. At this time, the resin is molded into a shape that corresponds to the shape of the hole in the die head.
本発明は、特にこの加熱装置に伴う加熱制御機構を特徴
とするものである。すなわち上述した合成樹脂用押出成
形機のダイスヘッド部を流れる押出樹脂の温度を光ファ
イバ型赤外線温度計により検出し、それによってシリン
ダーあるいはダイスヘッドの温度を制御するのである。The present invention is particularly characterized by a heating control mechanism associated with this heating device. That is, the temperature of the extruded resin flowing through the die head of the above-mentioned synthetic resin extrusion molding machine is detected by an optical fiber type infrared thermometer, and the temperature of the cylinder or the die head is thereby controlled.
ここで[光ファイバ型赤外線温度計]は、測定物(押出
樹脂)から放射される赤外線エネルギーを収束、伝達す
る光ファイバと、この赤外線エネルギーを電気信号に変
換し温度信号として取り出す赤外線検出部から成る。[Optical fiber type infrared thermometer] consists of an optical fiber that converges and transmits the infrared energy emitted from the object to be measured (extruded resin), and an infrared detector that converts this infrared energy into an electrical signal and extracts it as a temperature signal. Become.
この光ファイバ型赤外線温度計は、その温度制御機構に
連動しており、押出成形機のシリンダーあるいはダイス
ヘッドを加熱しつつ、温度制御機横の作用によりこれら
を所定の湿度に維持し、また外気の温度変化に対しても
十分に忠実にかつ迅速に対応して所定の温度を維持する
。この温度制御機構は、基本的には赤外線温度制御器に
よって取り出されて、温度信号を押出成形機の加熱系温
度制御器にフィードバックし、設定温度と比較し、加熱
電源を開閉することにより行う。制御系にPIDコント
ロール、ザイリスタ制御等を採用することにより加熱系
の応答性を良好にすることが可能である。This optical fiber type infrared thermometer is linked to its temperature control mechanism, and while heating the cylinder or die head of the extrusion molding machine, it maintains them at a predetermined humidity by the action on the side of the temperature controller. To maintain a predetermined temperature by sufficiently faithfully and quickly responding to temperature changes. This temperature control mechanism is basically taken out by an infrared temperature controller, feeds back a temperature signal to the heating system temperature controller of the extrusion molding machine, compares it with a set temperature, and turns on and off the heating power source. By employing PID control, Zyristor control, etc. in the control system, it is possible to improve the responsiveness of the heating system.
[実施例]
以下、本発明をその一実施例を示す図面に基づいて具体
的に説明する。[Example] Hereinafter, the present invention will be specifically described based on drawings showing one example thereof.
第1図は本発明の方法を実施した熱可塑性樹脂用押出成
形機のシリンダーの先端部分の概要を示す断面図である
。図中、1はシリンダー(先端部分)、2はダイスヘッ
ド、3は押出スクリュ−−(先端部分)、4はスクリー
ンメツシュ、5はブレカープレート、6はバンドヒータ
ー、7は光ファイバ型赤外線温度計、8は耐熱性ガラス
である。FIG. 1 is a sectional view schematically showing the tip of a cylinder of an extrusion molding machine for thermoplastic resin in which the method of the present invention is carried out. In the figure, 1 is a cylinder (tip part), 2 is a die head, 3 is an extrusion screw (tip part), 4 is a screen mesh, 5 is a breaker plate, 6 is a band heater, 7 is an optical fiber type infrared temperature A total of 8 is heat-resistant glass.
すでに詳細に説明したごとく、シリンダー1の先端には
スクリーンメツシュ4及びそれを支えるブレーカ−プレ
ート5が重ねられて配置され、それを押圧するようにダ
イスヘッド2が重ねられてシリンダー1に取り付けられ
ている。そしてシリンダー1の内部には、押出スクリュ
−3が回転可能に配置されており、図示されていない押
出シリンダー回転駆動機構の作動により回転するように
なっている。またシリンダー1及びダイスヘッド2の外
部には、バンドヒーター6が巻かれており、通電される
と発熱してシリンダー1及びダイスヘッド2を加熱する
ようになっている。本図においては、ダイスヘッド2に
は、その微小な一部に孔が穿けられており、ダイスヘッ
ド2の内面を形成するように耐熱性ガラス8が填められ
ている。そしてその孔部には、外部から本発明において
最も特徴的な光ファイバ型赤外線温度計7が挿入されて
いる。温度計7は図示されていない温度制御機構に接続
されており、その温度制tII機構は温度計7によって
検出された情報によりシリンダー1やダイスヘッド2が
所定の温度に加熱されるように(通電)条件を決め、自
動的に作動し、バンドヒーター6を加熱する。As already explained in detail, the screen mesh 4 and the breaker plate 5 that support it are stacked at the tip of the cylinder 1, and the die head 2 is stacked and attached to the cylinder 1 so as to press it. ing. An extrusion screw 3 is rotatably disposed inside the cylinder 1 and is rotated by the operation of an extrusion cylinder rotation drive mechanism (not shown). A band heater 6 is wound around the outside of the cylinder 1 and the die head 2, and when energized, generates heat to heat the cylinder 1 and the die head 2. In this figure, the die head 2 has a hole formed in a small portion thereof, and a heat-resistant glass 8 is filled so as to form the inner surface of the die head 2. An optical fiber type infrared thermometer 7, which is the most characteristic feature of the present invention, is inserted into the hole from the outside. The thermometer 7 is connected to a temperature control mechanism (not shown), and the temperature control tII mechanism heats the cylinder 1 and the die head 2 to a predetermined temperature based on the information detected by the thermometer 7. ) The conditions are determined and the band heater 6 is heated automatically.
[発明の効果1
本発明によれば、押出成形機におりるダイスヘッド部を
流れる押出樹脂の温度を光ファイバ型赤外線温度計によ
り直接検出し、それによってシリンダーあるいはダイス
ヘッドの温度を制御することから、従来の問題点を一掃
することができる。[Effect of the invention 1 According to the present invention, the temperature of the extruded resin flowing through the die head portion of the extrusion molding machine is directly detected by an optical fiber type infrared thermometer, and the temperature of the cylinder or the die head is thereby controlled. Therefore, conventional problems can be eliminated.
というきわめて優れた効果が奏せられる。An extremely excellent effect can be achieved.
第1図は本発明の方法による一実施例の熱可塑性樹脂用
押出成形機の先端部分の概要を示す断面図である。
図中、1ニジリンダ−(先端部分)、
2 ; ダ イ ス ヘ ッ ド
、3:押出スクリュー(先端部分)、
4ニスクリーンメツシユ、
5 : ブ し カ − プ し −
ト 、6 : バ ン ド ヒ −
タ − 、−〇−
7:光ファイバ型赤外線i i y4.8 : 耐
熱 性 ガ ラ ス。FIG. 1 is a sectional view schematically showing the tip portion of an extrusion molding machine for thermoplastic resin according to an embodiment of the method of the present invention. In the figure, 1. Niji cylinder (tip part), 2: die head, 3: extrusion screw (tip part), 4. Nijiri mesh, 5: book cup.
G, 6: Band He -
7: Optical fiber type infrared ray 4.8: Resistance
Thermal glass.
Claims (1)
出樹脂の温度を光ファイバ型赤外線温度計により検出し
、それによって上記シリンダーあるいはダイスヘッドの
温度を制御することを特徴とする合成樹脂押出成形機に
おける押出温度の制御方法。Extrusion in a synthetic resin extrusion molding machine, characterized in that the temperature of the extruded resin flowing through a die head in the synthetic resin extrusion molding machine is detected by an optical fiber type infrared thermometer, and the temperature of the cylinder or the die head is controlled thereby. How to control temperature.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61132185A JPS62288025A (en) | 1986-06-06 | 1986-06-06 | Control of extruding temprature in synthetic resin extrusion molder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61132185A JPS62288025A (en) | 1986-06-06 | 1986-06-06 | Control of extruding temprature in synthetic resin extrusion molder |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62288025A true JPS62288025A (en) | 1987-12-14 |
Family
ID=15075376
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61132185A Pending JPS62288025A (en) | 1986-06-06 | 1986-06-06 | Control of extruding temprature in synthetic resin extrusion molder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62288025A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05154894A (en) * | 1991-12-03 | 1993-06-22 | Japan Steel Works Ltd:The | Method and device for continuously examining molten resin |
US5322654A (en) * | 1989-10-14 | 1994-06-21 | The Queen's University Of Belfast | Rotational moulding apparatus and process |
WO2000059707A1 (en) * | 1999-03-31 | 2000-10-12 | Barmag Ag | Extrusion device |
-
1986
- 1986-06-06 JP JP61132185A patent/JPS62288025A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5322654A (en) * | 1989-10-14 | 1994-06-21 | The Queen's University Of Belfast | Rotational moulding apparatus and process |
JPH05154894A (en) * | 1991-12-03 | 1993-06-22 | Japan Steel Works Ltd:The | Method and device for continuously examining molten resin |
WO2000059707A1 (en) * | 1999-03-31 | 2000-10-12 | Barmag Ag | Extrusion device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2692346C2 (en) | Granules / liquid flow control device for a printing head of a 3d printer, into which granules and / or liquid are fed | |
US3733059A (en) | Plastic extruder temperature control system | |
JP3758682B2 (en) | Block element continuous extrusion method and apparatus | |
US3630802A (en) | Method and apparatus for producing a coated substrate and a laminated product | |
KR20190062664A (en) | modular smart nozzle prevents unmelting | |
US3758001A (en) | Extruder | |
JP2020157760A (en) | Method for operating extruder in three-dimensional (3d) object printer to improve layer formation | |
JPS62288025A (en) | Control of extruding temprature in synthetic resin extrusion molder | |
GB1056133A (en) | Improvements in or relating to methods of and apparatus for extrusion | |
US6409491B1 (en) | Extrusion die assembly | |
CN111231356A (en) | Preparation method for controlling mixed color flow lines of wood-plastic composite material | |
JPH07241851A (en) | Method of feeding indeterminately formed material to be extruded | |
JPH04316823A (en) | Raw material push-in apparatus | |
RU2745944C1 (en) | 3d printer extruder with convection heating | |
CN212949009U (en) | Glue filling device for plastic mould | |
EP0586205A1 (en) | Variable width film die | |
CN111070623B (en) | Preparation method of wood-grain-like co-extrusion color-mixing wood-plastic composite material | |
KR102020359B1 (en) | modular pressure control smart nozzle | |
JPH071559A (en) | Synthetic resin extrusion molding machine | |
CA1068061A (en) | Plastics extrusion die head improvement | |
JPH10156907A (en) | Heating of plasticizing material | |
JPH08238653A (en) | Thermo-plasticizing apparatus | |
JPH0725132B2 (en) | Inflation molding method and apparatus therefor | |
JPH10109349A (en) | Screw extruder | |
CN211251120U (en) | Injection molding raw material drying device |