JPH054207B2 - - Google Patents

Info

Publication number
JPH054207B2
JPH054207B2 JP60078190A JP7819085A JPH054207B2 JP H054207 B2 JPH054207 B2 JP H054207B2 JP 60078190 A JP60078190 A JP 60078190A JP 7819085 A JP7819085 A JP 7819085A JP H054207 B2 JPH054207 B2 JP H054207B2
Authority
JP
Japan
Prior art keywords
temperature
cylinder
resin
thermocouple
hopper
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 - Lifetime
Application number
JP60078190A
Other languages
Japanese (ja)
Other versions
JPS61235120A (en
Inventor
Koji Kubota
Takashi Mizuno
Kenichi Terao
Kyoshi Kinoshita
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP60078190A priority Critical patent/JPS61235120A/en
Publication of JPS61235120A publication Critical patent/JPS61235120A/en
Publication of JPH054207B2 publication Critical patent/JPH054207B2/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
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/76Measuring, controlling or regulating
    • B29C45/78Measuring, controlling or regulating of temperature
    • 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
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/72Heating or cooling
    • B29C45/74Heating or cooling of the injection unit
    • 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
    • B29C48/501Extruder feed section
    • 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
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/793Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling upstream of the plasticising zone, e.g. heating in the hopper
    • 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
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/793Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling upstream of the plasticising zone, e.g. heating in the hopper
    • B29C48/797Cooling
    • 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
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/80Thermal 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
    • B29C48/83Heating or cooling the cylinders
    • 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
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/80Thermal 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
    • B29C48/83Heating or cooling the cylinders
    • B29C48/832Heating
    • 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
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/86Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the nozzle zone
    • B29C48/865Heating
    • 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
    • B29C48/03Extrusion 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

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は射出成形機、押出成形機に利用できる
温調装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a temperature control device that can be used in injection molding machines and extrusion molding machines.

(従来の技術) 第4図に示す従来の射出成形機は、シリンダ1
の左方にノズル2を取付けてあり、同シリンダ1
の右方はホツパジヤケツト3の中に挿入し、2つ
割りのリテーナリング4とボルト5により固定さ
れている。リテーナリング4の前のシリンダ1の
外周には、ヒータ12が設けてあり、熱電対11
を検出器として、温調計10により適温に制御さ
れている。ヒータ12の前方のシリンダ外周のヒ
ータ18及びノズル外周のヒータ19は、図示さ
れていない温調計により、それぞれ適温に制御さ
れている。
(Prior art) The conventional injection molding machine shown in FIG.
Nozzle 2 is installed on the left side of cylinder 1.
The right side is inserted into the hot spring jacket 3 and fixed with a two-piece retainer ring 4 and bolts 5. A heater 12 is provided on the outer periphery of the cylinder 1 in front of the retainer ring 4, and a thermocouple 11
The temperature is controlled to an appropriate temperature using a temperature controller 10 as a detector. The heater 18 on the outer periphery of the cylinder in front of the heater 12 and the heater 19 on the outer periphery of the nozzle are each controlled at appropriate temperatures by a temperature controller (not shown).

次に樹脂の可塑化工程と温調の関係を説明する
と、シリンダ1の中のスクリユ6(図示のものは
フライトの一部のみを示す)は、深い一定の溝深
さを有する供給部7、溝深さが順次浅くなる圧縮
部8、浅い一定の溝深さである計量部9から構成
されている。ホツパ13からペレツト状(又は粉
体)の樹脂が供給されると、供給部7において、
樹脂とシリンダ1の内面との摩擦係数とシリンダ
内圧及びシリンダ内面の表面積との積である摩擦
力と、樹脂と供給部7の谷底表面との摩擦係数と
シリンダ内圧及びスクリユ谷底表面積の積である
摩擦力との差により、スクリユ6の回転に伴い、
樹脂が前方へ搬送され、同時に樹脂は、シリンダ
1からの伝熱により予熱される。
Next, to explain the relationship between the resin plasticization process and temperature control, the screw 6 in the cylinder 1 (the illustrated one shows only a part of the flight) has a supply part 7 having a deep and constant groove depth, It is composed of a compression section 8 whose groove depth gradually becomes shallower and a measuring section 9 whose groove depth is shallow and constant. When pellet-like (or powder) resin is supplied from the hopper 13, in the supply section 7,
The friction force is the product of the friction coefficient between the resin and the inner surface of the cylinder 1, the cylinder internal pressure, and the surface area of the cylinder inner surface, and the product of the friction coefficient between the resin and the bottom surface of the supply section 7, the cylinder internal pressure, and the screw bottom surface area. Due to the difference in frictional force, as the screw 6 rotates,
The resin is transported forward, and at the same time, the resin is preheated by heat transfer from the cylinder 1.

またヒータ12からの伝熱によりホツパ穴17
の付近の温度が上がると、(一般に90℃〜100℃以
上)、ペレツト状の樹脂の表面が融けておこし状
になり、スクリユ供給部7へ落下しにくくなるの
で、それを防ぐ為、ホツパジヤケツト3に冷却水
を通水する。その冷却水流量は、手動操作弁16
を用いて、作業者の経験や勘により調整される。
なお、冷却水は、入口配管14からホツパジヤケ
ツト3内の通路20を通り、出口配管15へ流れ
る。スクリユ供給部7と接するシリンダ1の範囲
は、ホツパ穴17からヒータ12までの部分であ
る。ここでヒータ12以後のシリンダ部分をシリ
ンダ基部1aと呼ぶことにする。またシリンダ基
部1aの温度は、ヒータ12からの伝熱とホツパ
ジヤケツト3の冷却水による吸熱、樹脂への伝熱
のバランスにより決定される。
In addition, due to heat transfer from the heater 12, the hopper hole 17
When the temperature around the area rises (generally above 90°C to 100°C), the surface of the pellet-like resin melts and becomes rough, making it difficult for it to fall into the screw supply section 7. Cooling water is passed through. The cooling water flow rate is determined by the manually operated valve 16.
It is adjusted based on the operator's experience and intuition.
Note that the cooling water flows from the inlet pipe 14 through the passage 20 in the hopper jacket 3 to the outlet pipe 15. The range of the cylinder 1 that comes into contact with the screw supply section 7 is the part from the hopper hole 17 to the heater 12. Here, the cylinder portion after the heater 12 will be referred to as a cylinder base portion 1a. The temperature of the cylinder base 1a is determined by the balance between heat transfer from the heater 12, heat absorption by the cooling water in the hopper jacket 3, and heat transfer to the resin.

次に供給部7により搬送された樹脂は、圧縮部
8により機械的エネルギーによる剪断、圧縮及び
ヒータ18からの伝熱により溶融される。溶融さ
れた樹脂は、逆流防止弁10を通り、スクリユ先
端に貯蔵される。
Next, the resin conveyed by the supply section 7 is melted by the compression section 8 by shearing and compression by mechanical energy and heat transfer from the heater 18 . The molten resin passes through the check valve 10 and is stored at the tip of the screw.

ここで溶融樹脂の品質、特に樹脂温度の均一性
は、成形品品質と密接な関係がある。すなわち、
樹脂温度の一部の過熱による焼け、過小によるシ
ヨートシヨツト、温度が不均一な樹脂同志が冷却
時、組織的に結合しないことによるデラミネーシ
ヨン(層間はくり)、不均一な樹脂温度層が表面
に出るフローマーク等の成形不良を生じる。従つ
て樹脂温度の均一を実現する為に、スクリユ形状
の改良、スクリユ回転数、背圧のフイードバツク
制御やプログラム制御、シリンダヒータのPID制
御が試みられ、一応の成果が得られている。
The quality of the molten resin, particularly the uniformity of the resin temperature, is closely related to the quality of the molded product. That is,
Burning due to overheating of a part of the resin temperature, short shot due to too low temperature, delamination due to resins with uneven temperature not bonding systematically when cooled, uneven resin temperature layer on the surface This causes molding defects such as flow marks. Therefore, in order to achieve uniform resin temperature, attempts have been made to improve the screw shape, screw rotation speed, feedback control and program control of the screw rotation speed, back pressure, and PID control of the cylinder heater, and some results have been obtained.

ところが、樹脂の摩擦係数と温度の関係は、一
般に第5図に示すように2種類ある。それを実線
と点線で示す。特に実線で示す特性の樹脂は、ス
クリユ供給部7に対応するシリンダ基部1aの温
度により著しく摩擦係数が変化し、搬送力が変動
する。この為、次工程である圧縮部8を通過する
樹脂量が変化するので、同一回転数、背圧であつ
ても、剪断力、圧縮力が変化し、樹脂温度が変動
する。ちなみに実線の特性を持つ樹脂は、ABS、
PMMA、PA66、PETであり、点線の特性を持
つ樹脂は、PP、LDPEである。最近前記実線の
特性を持つ樹脂は、レンズ等の精密光学部品や工
業部品に使用されており、成形品質の安定化の
為、樹脂温度均一性の高度化が要求されている。
However, there are generally two types of relationships between the friction coefficient of resin and temperature, as shown in FIG. This is shown by solid and dotted lines. In particular, for resins having the characteristics shown by the solid line, the coefficient of friction changes significantly depending on the temperature of the cylinder base 1a corresponding to the screw supply section 7, and the conveying force fluctuates. For this reason, the amount of resin passing through the compression section 8, which is the next step, changes, so even if the rotation speed and back pressure are the same, the shear force and compression force change, and the resin temperature fluctuates. By the way, the resins with the characteristics shown in the solid line are ABS,
These are PMMA, PA66, and PET, and the resins with the characteristics indicated by the dotted line are PP and LDPE. Recently, resins having the characteristics shown in the solid line have been used for precision optical parts such as lenses and industrial parts, and in order to stabilize molding quality, a high level of resin temperature uniformity is required.

ところが従来のシリンダ基部1aは、リテーナ
リング4とボルト5に干渉するため、ヒータが取
付けられないリテーナリング下部のシリンダ外周
がある。そこでの放熱等の外乱により、温度変動
が生じる。またホツパジヤケツト3の冷却水の通
水を作業者の勘によつて調整している為、温度変
動を押える制御がなされていないので、樹脂温度
の均一性を悪化させていた。
However, since the conventional cylinder base 1a interferes with the retainer ring 4 and the bolts 5, there is a portion of the cylinder outer periphery below the retainer ring where the heater cannot be attached. Temperature fluctuations occur due to disturbances such as heat radiation there. Furthermore, since the passage of cooling water through the hot spring jacket 3 is adjusted by the operator's intuition, there is no control to suppress temperature fluctuations, which deteriorates the uniformity of resin temperature.

また他の欠点として、ホツパジヤケツト3に冷
却水を通水し続けることにより、ホツパジヤケツ
トを冷し過ぎる場合がある。この一例として実機
でのシリンダ基部温度分布を第6図の実線に示
す。これを見ると熱電対11を過ぎたところか
ら、温度が急激に下がつている。ヒータ12があ
つても、このように急激に温度が下がつているの
は、ホツパジヤケツト3を冷却水の通水により過
冷にして、ヒータ12の伝熱を奪つているからで
ある。
Another drawback is that by continuing to flow cooling water through the hot pad jacket 3, the hot pad jacket 3 may become too cool. As an example of this, the cylinder base temperature distribution in an actual machine is shown by the solid line in FIG. As you can see, the temperature drops rapidly after passing thermocouple 11. Even with the heater 12, the temperature decreases rapidly like this because the hot spring jacket 3 is supercooled by the cooling water flowing through it, which deprives the heater 12 of heat transfer.

このような場合、供給部7での樹脂の予熱が不
十分となる。そして圧縮部8に冷たい樹脂が搬送
されると、供給される機械的エネルギーやシリン
ダの伝熱に対して不十分となり、未溶融樹脂が生
じ、樹脂温度が不均一になる。それと同時に、圧
縮部8の溝深さの減少に対して溶融が追従できな
くなり、固体樹脂の詰りが発生し、スクリユ駆動
力が増加する。従つて樹脂の搬送時は、圧縮部8
に入るまでに溶融寸前の温度まで予熱が必要であ
る。以上の様に従来のシリンダ基部1aは、リテ
ーナリング4の下部のシリンダ外周の放熱や、ホ
ツパジヤケツト3を過冷却にすることから、樹脂
の予熱が不十分になり、樹脂温度の不均一やスク
リユ駆動力の増加を生じていた。
In such a case, preheating of the resin in the supply section 7 becomes insufficient. When the cold resin is conveyed to the compression section 8, it becomes insufficient for the mechanical energy supplied and the heat transfer of the cylinder, resulting in unmelted resin and uneven resin temperature. At the same time, the melting cannot follow the decrease in the groove depth of the compressed portion 8, clogging of the solid resin occurs, and the screw driving force increases. Therefore, when transporting the resin, the compression section 8
It is necessary to preheat to a temperature just before melting. As described above, the conventional cylinder base 1a dissipates heat from the outer periphery of the cylinder under the retainer ring 4 and overcools the hot spring jacket 3, resulting in insufficient preheating of the resin, resulting in uneven resin temperature and screw drive. It was causing an increase in power.

(発明が解決しようとする問題点) 本発明は従来の射出成形機における樹脂温度の
不均一やスクリユ駆動力の増加等の問題点を解決
しようとするものである。
(Problems to be Solved by the Invention) The present invention attempts to solve problems in conventional injection molding machines, such as uneven resin temperature and increased screw driving force.

(問題点を解決するための手段) このため本発明は、ホツパ穴からのスクリユの
供給部までに対応する範囲のシリンダ基部をホツ
パジヤケツトの冷却と、シリンダ外周のヒータか
らの加熱により温調する射出成形機等のシリンダ
の温調装置において、ホツパジヤケツトとシリン
ダを固定するためのリテーナリングの下部に加熱
装置を設けると共に、同加熱装置の温度制御装置
を設け、かつ同ホツパジヤケツト内のシリンダ温
度を検出する熱電対と、同ホツパジヤケツト内に
通す冷却水の流量を調節する電磁弁を備え、同電
磁弁を前記熱電対の信号により制御してホツパ穴
の樹脂温度を制御するようにしたもので、これを
問題点解決のための手段とするものである。
(Means for Solving the Problems) Therefore, the present invention provides an injection system in which the temperature of the cylinder base in the range from the hopper hole to the screw supply section is controlled by cooling the hopper jacket and heating from the heater on the outer circumference of the cylinder. In a temperature control device for a cylinder of a molding machine, etc., a heating device is provided at the bottom of a retainer ring for fixing the hopper jacket and the cylinder, a temperature control device for the heating device is provided, and the temperature of the cylinder in the hopper jacket is detected. It is equipped with a thermocouple and a solenoid valve that adjusts the flow rate of cooling water passed through the hopper jacket, and the solenoid valve is controlled by the signal from the thermocouple to control the resin temperature in the hopper hole. It is intended as a means to solve problems.

(作用) ホツパ穴付近がシリンダからの伝熱により過熱
されようとすると、第2熱電対により温度を検出
している制御器は信号を出し、電磁弁を動作さ
せ、入口配管からホツパジヤケツト内に流入する
冷却水の流量を調節してホツパ穴付近の温度を適
温に制御する。次にリテーナリングの下部のシリ
ンダの中に取付けられた第1熱電対を検出器とす
る温調計により、加熱装置が温度制御されるの
で、この部分のシリンダ温度は適温に制御され
る。
(Function) When the area around the hopper hole is about to become overheated due to heat transfer from the cylinder, the controller that detects the temperature using the second thermocouple issues a signal, operates the solenoid valve, and causes the flow of water from the inlet pipe into the hopper jacket. The temperature near the hopper hole is controlled to an appropriate temperature by adjusting the flow rate of cooling water. Next, the temperature of the heating device is controlled by a temperature controller having a first thermocouple as a detector installed in the cylinder at the bottom of the retainer ring, so that the cylinder temperature in this part is controlled to an appropriate temperature.

(実施例) 以下本発明の実施例を図面について説明する
と、第1図〜第3図は本発明の実施例を示す。先
ず第1図〜第2図の実施例について説明すると、
シリンダホツパ穴17からヒータ12の取付位置
までのシリンダ1の中に、熱電対21を検出器と
する温調計22で制御されるカートリツジヒータ
23を設置する。またホツパ穴17下部のシリン
ダ1に挿入された熱電対24を検出器とし、冷却
水量を制御する電磁比例流量弁(又は電磁切換
弁)25の制御器26を設置する。なお、以上の
構成以外の各部の構造は前記第4図と同一であ
る。
(Example) Examples of the present invention will be described below with reference to the drawings. FIGS. 1 to 3 show examples of the present invention. First, the embodiment shown in FIGS. 1 and 2 will be explained.
A cartridge heater 23 is installed in the cylinder 1 from the cylinder hopper hole 17 to the mounting position of the heater 12, which is controlled by a temperature controller 22 having a thermocouple 21 as a detector. A thermocouple 24 inserted into the cylinder 1 at the bottom of the hopper hole 17 is used as a detector, and a controller 26 of an electromagnetic proportional flow valve (or electromagnetic switching valve) 25 for controlling the amount of cooling water is installed. The structure of each part other than the above structure is the same as that shown in FIG. 4 above.

次に以上の如く構成された実施例について作用
を説明する。先ずホツパ穴17付近が、シリンダ
1からの伝熱により過熱されようとすると、熱電
対24により温度を検出している制御器26は信
号を出し、電磁比例流量弁25を動作させ、入口
配管14からホツパジヤケツト3内に流入する冷
却水の流量を調節してホツパ穴17付近の温度を
適温に制御する。従つてホツパ穴17の樹脂が、
おこし状にならない適度な予熱(80℃以下)が可
能となる。
Next, the operation of the embodiment configured as above will be explained. First, when the vicinity of the hopper hole 17 is about to become overheated due to heat transfer from the cylinder 1, the controller 26, which detects the temperature using the thermocouple 24, outputs a signal, operates the electromagnetic proportional flow valve 25, and closes the inlet pipe 14. The temperature near the hopper hole 17 is controlled to an appropriate temperature by adjusting the flow rate of cooling water flowing into the hopper jacket 3 from the hopper jacket 3. Therefore, the resin in the hopper hole 17 is
Moderate preheating (below 80℃) is possible without causing overheating.

次にリテーナリング4の下部のシリンダの中に
取付けられた熱電対21の検出器とする温調計2
2により、カートリツジヒータ23が温度制御さ
れるので、この部分のシリンダ温度は適温に制御
される。また両者の制御により理想的なシリンダ
基部の温度分布を実現できる。この一例を第6図
の点線に示す。この温度分布は、ホツパ穴17の
位置が、樹脂がおこし状にならないで十分予熱で
きる温度として、80℃に設定する。そして熱電対
11の位置まで樹脂が十分予熱される為、リテー
ナリング4の下部、すなわち熱電対21の位置で
の温度を140℃に、熱電対11の位置での温度を
180℃に設定した例である。また温度制御により、
この温度分布は安定する。
Next, a temperature controller 2 is used as a detector for a thermocouple 21 installed in the cylinder at the bottom of the retainer ring 4.
2, the temperature of the cartridge heater 23 is controlled, so the cylinder temperature in this area is controlled to an appropriate temperature. Furthermore, by controlling both, an ideal temperature distribution at the cylinder base can be achieved. An example of this is shown by the dotted line in FIG. This temperature distribution is set at 80° C., which is a temperature at which the position of the hopper hole 17 can be sufficiently preheated without causing the resin to rise. Since the resin is sufficiently preheated to the thermocouple 11 position, the temperature at the lower part of the retainer ring 4, that is, the thermocouple 21 position, is 140°C, and the temperature at the thermocouple 11 position is 140°C.
This is an example where the temperature is set to 180℃. In addition, temperature control allows
This temperature distribution becomes stable.

次に第3図に示す他の実施例について説明する
と、第3図に示すようにリテーナリング4の下部
に巻かれた油配管31とホツパジヤケツト3とシ
リンダ1との間に設けた円筒状の隙間32に、高
温の油を流すことによりシリンダ基部1aを加熱
する。なお、33は熱電対24を検出器とし、油
の温度と流量を制御する制御器、34は、ホツパ
穴17へ油が漏れるのを防ぐシールである。
Next, another embodiment shown in FIG. 3 will be described. As shown in FIG. 32, the cylinder base 1a is heated by flowing high temperature oil. Note that 33 is a controller that uses the thermocouple 24 as a detector to control the temperature and flow rate of oil, and 34 is a seal that prevents oil from leaking into the hopper hole 17.

(発明の効果) 以上詳細に説明した如く本発明は構成されてい
るので、シリンダ基部の温度の安定により、樹脂
の摩擦係数が安定するため、搬送能力の変動が低
減する。これにより樹脂温度が均一化し、成形品
の不良が低減できる。またホツパ穴からスクリユ
圧縮部に対応するシリンダは、過熱や過冷却がな
い適度な温度分布に制御されるので、樹脂を搬送
中に予熱できる。これにより、樹脂温の均一化及
びスクリユの駆動力の低減ができる。
(Effects of the Invention) Since the present invention is configured as described above in detail, the temperature at the base of the cylinder is stabilized, and the friction coefficient of the resin is stabilized, so that fluctuations in conveying capacity are reduced. This makes the resin temperature uniform and reduces molded product defects. Further, since the cylinder corresponding to the screw compression part from the hopper hole is controlled to have an appropriate temperature distribution without overheating or overcooling, the resin can be preheated during transportation. This makes it possible to equalize the resin temperature and reduce the driving force of the screw.

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

第1図は本発明の実施例を示す射出成形機にお
ける温調装置の側断面図、第2図は第1図の〜
断面図、第3図は第1図と異なる実施例を示す
温調装置の側断面図、第4図は従来の射出成形機
の側断面図、第5図は従来の温度と摩擦係数との
関係を示す線図、第6図は従来と本発明における
位置とシリンダ温度との関係を示す線図である。 図の主要部分の説明 1……シリンダ、3……
ホツパジヤケツト、4……リテーナリング、17
……ホツパ穴、21……熱電対(第1熱電対)、
22……温調計、23……カートリツジヒータ
(加熱装置)、24……熱電対(第2熱電対)、2
5……電磁比例流量弁(電磁弁)、26……制御
器。
FIG. 1 is a side sectional view of a temperature control device in an injection molding machine showing an embodiment of the present invention, and FIG.
3 is a side sectional view of a temperature control device showing an embodiment different from that shown in FIG. 1, FIG. 4 is a side sectional view of a conventional injection molding machine, and FIG. Diagram showing the relationship. FIG. 6 is a diagram showing the relationship between position and cylinder temperature in the conventional method and the present invention. Explanation of main parts of the diagram 1...Cylinder, 3...
Hot spring jacket, 4... Retainer ring, 17
... Hopper hole, 21 ... Thermocouple (first thermocouple),
22... Temperature controller, 23... Cartridge heater (heating device), 24... Thermocouple (second thermocouple), 2
5... Solenoid proportional flow valve (electromagnetic valve), 26... Controller.

Claims (1)

【特許請求の範囲】[Claims] ホツパ穴からのスクリユの供給部までに対応す
る範囲のシリンダ貴部をホツパジヤケツトの冷却
と、シリンダ外周のヒータからの加熱により温調
する射出成形機等のシリンダの温調装置におい
て、ホツパジヤケツトとシリンダを固定するため
のリテーナリングの下部に加熱装置を設けると共
に、同加熱装置の温度制御装置を設け、かつ同ホ
ツパジヤケツト内のシリンダ温度を検出する熱電
対と、同ホツパジヤケツト内に通す冷却水の流量
を調節する電磁弁を備え、同電磁弁を前記熱電対
の信号により制御してホツパ穴の樹脂温度を制御
するようにしたことを特徴とする温調装置。
In a temperature control device for a cylinder such as an injection molding machine, the temperature of the cylinder head in the range from the hopper hole to the screw supply section is controlled by cooling the hopper jacket and heating from a heater around the cylinder. A heating device is installed at the bottom of the retainer ring for fixing, and a temperature control device is installed for the heating device, and a thermocouple is installed to detect the cylinder temperature in the hot spring jacket, and the flow rate of cooling water passing through the hot spring jacket is adjusted. 1. A temperature control device comprising a solenoid valve for controlling the resin temperature in the hopper hole by controlling the solenoid valve by a signal from the thermocouple.
JP60078190A 1985-04-12 1985-04-12 Temperature regulating device Granted JPS61235120A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60078190A JPS61235120A (en) 1985-04-12 1985-04-12 Temperature regulating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60078190A JPS61235120A (en) 1985-04-12 1985-04-12 Temperature regulating device

Publications (2)

Publication Number Publication Date
JPS61235120A JPS61235120A (en) 1986-10-20
JPH054207B2 true JPH054207B2 (en) 1993-01-19

Family

ID=13655065

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60078190A Granted JPS61235120A (en) 1985-04-12 1985-04-12 Temperature regulating device

Country Status (1)

Country Link
JP (1) JPS61235120A (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0494915A (en) * 1990-08-10 1992-03-27 Nissei Plastics Ind Co Control method for injection molding machine
JP3057159B1 (en) * 1999-04-13 2000-06-26 ファナック株式会社 Heating cylinder base temperature control device of injection molding machine
WO2012142152A2 (en) * 2011-04-12 2012-10-18 Zimmer, Inc. Modified injection molding unit and method of delivering cooled molding material
JP6158102B2 (en) * 2014-01-21 2017-07-05 住友重機械工業株式会社 Injection molding machine
AT519152B1 (en) * 2016-10-10 2018-09-15 Engel Austria Gmbh Injection unit
JP7400410B2 (en) * 2019-11-29 2023-12-19 セイコーエプソン株式会社 plasticizing equipment
JP7516869B2 (en) 2020-05-28 2024-07-17 セイコーエプソン株式会社 Plasticizing device, injection molding device, and three-dimensional modeling device
JP7683334B2 (en) 2021-06-07 2025-05-27 セイコーエプソン株式会社 Plasticizing equipment, injection molding equipment, and 3D modeling equipment
JP2024148095A (en) * 2023-04-04 2024-10-17 住友重機械工業株式会社 Injection molding machine management device, injection molding machine, and injection molding machine management method

Also Published As

Publication number Publication date
JPS61235120A (en) 1986-10-20

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