JPH06293021A - Deaerating method of powder molding machine and vent device for molding powder - Google Patents

Deaerating method of powder molding machine and vent device for molding powder

Info

Publication number
JPH06293021A
JPH06293021A JP5104947A JP10494793A JPH06293021A JP H06293021 A JPH06293021 A JP H06293021A JP 5104947 A JP5104947 A JP 5104947A JP 10494793 A JP10494793 A JP 10494793A JP H06293021 A JPH06293021 A JP H06293021A
Authority
JP
Japan
Prior art keywords
resin
screw
vacuum pump
vent
volatile matter
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
JP5104947A
Other languages
Japanese (ja)
Inventor
Hideaki Nakajima
英昭 中島
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works 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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP5104947A priority Critical patent/JPH06293021A/en
Publication of JPH06293021A publication Critical patent/JPH06293021A/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
    • B29C48/78Thermal 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
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/67Screws having incorporated mixing devices not provided for in groups B29C48/52 - B29C48/66
    • 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
    • B29C48/76Venting, drying means; Degassing means
    • B29C48/765Venting, drying means; Degassing means in the extruder apparatus
    • B29C48/766Venting, drying means; Degassing means in the extruder apparatus in 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
    • B29C48/92Measuring, controlling or regulating
    • 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
    • B29C48/365Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pumps, e.g. piston pumps

Abstract

PURPOSE:To suck moisture and a volatile matter from a resin forcibly and prevent suction to the outside of a powder resin under an unmelted state fowarded to a vent by reducing the suction force of a vacuum pump when the torque value of a screw reaches a specified value or less when moisture, the volatile matter, etc., produced from the resin in a vent section are sucked and exhausted by the vacuum pump. CONSTITUTION:When an initial stage passes and a resin is supplied at every fixed quantity, the torque value of a screw 10 rises because specified shearing force, frictional force, etc., work, and the on signal of a vacuum pump 4 is output when the torque value is larger than a set value. A space not filled with the resin can be formed during the flight of a vent section 13, and the specific degree of vacuum works. Consequently, moisture, a volatile matter, etc., produced from the resin are sucked and exhausted by the pump 4. Driving torque is made smaller than the set value though the supply of the resin is stopped, the quantity of the resin fed to a supply section is decreased, melting is delayed and the resin under an unmelted state reaches the vent section 13, the pump 4 is turned off, then preventing suction to the pump 4 of the resin under the unmelted state.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、シリンダと、該シリン
ダ内に設けられているスクリューとからなり、該スクリ
ューを駆動すると、樹脂がスクリューの溝にそって前方
に送られる過程で溶融・混練され、そしてベント部にお
いて樹脂から生じる水分、揮発分等を吸引排気するパウ
ダー成形機の脱気方法および該方法の実施に供されるパ
ウダー成形用ベント装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention comprises a cylinder and a screw provided in the cylinder. When the screw is driven, the resin is melted and kneaded in the process of being forwardly fed along the groove of the screw. The present invention relates to a deaeration method of a powder molding machine for sucking and exhausting water, volatile matter, and the like generated from a resin in a vent portion, and a vent apparatus for powder molding used for carrying out the method.

【0002】[0002]

【従来の技術】射出成形機の射出装置は、周知のよう
に、シリンダと該シリンダ内で駆動されるスクリューと
から、概略構成されてる。樹脂を溶融・混練する過程で
樹脂から生じる水分、揮発分等を外部に逃すことのでき
るベント式射出装置も、同様に、シリンダと該シリンダ
内で駆動されるスクリューとを備えている。そしてシリ
ンダあるいはスクリューは、ホッパから粉末材料が供給
される供給部、該供給部の下流側に位置する第1メタリ
ング部、この第1メタリング部の下流側のベント部、そ
の下流側の第2メタリング部と区分され、第2メタリン
グ部の先端にスクリューヘッドが設けられている。ベン
ト部に位置するスクリューの溝は、深くなっている。あ
るいはベント部のスクリューの軸径は小さくなってい
る。また、供給部と第1メタリング部とからなる第1ス
テージにおける樹脂の送り量は、ベント部と第2メタリ
ング部からなる第2ステージの樹脂の送り量より小さく
なるように構成されている。そしてベント部に位置する
シリンダにはベント孔が設けられ、このベント孔には真
空ポンプが接続されている。
2. Description of the Related Art As is well known, an injection device of an injection molding machine is generally composed of a cylinder and a screw driven in the cylinder. A vent type injection device capable of releasing moisture, volatile matter and the like generated from the resin to the outside in the process of melting and kneading the resin also includes a cylinder and a screw driven in the cylinder. The cylinder or screw includes a supply unit to which the powder material is supplied from the hopper, a first metal ring unit located on the downstream side of the supply unit, a vent unit on the downstream side of the first metal ring unit, and a second metal ring on the downstream side. A screw head is provided at the tip of the second metering portion. The groove of the screw located at the vent is deep. Alternatively, the shaft diameter of the screw in the vent portion is smaller. Further, the resin feed amount in the first stage including the supply unit and the first metalling unit is configured to be smaller than the resin feed amount in the second stage including the vent unit and the second metalling unit. A vent hole is provided in the cylinder located at the vent portion, and a vacuum pump is connected to the vent hole.

【0003】したがって、ホッパから供給部に樹脂を供
給してスクリューを回転駆動すると、樹脂は、外部から
加えられる熱と、スクリューの回転による剪断、摩擦等
による発熱作用で可塑化混練されてスクリューの先端部
に送られる。このとき、第2ステージの樹脂の送り量
は、第1ステージの送り量より大きいので、ベント部で
はフライト内には、溶融樹脂で満たされていない空間が
できる。このように空間ができるので、樹脂から生じる
水分、揮発分等を、溶融樹脂を外部に漏らすことなく、
ベント孔から真空ポンプにより外部に強制的に吸引排気
することができる。
Therefore, when the resin is supplied from the hopper to the supply portion and the screw is driven to rotate, the resin is plasticized and kneaded by the heat applied from the outside and the exothermic action due to shearing, friction, etc. due to the rotation of the screw to cause the screw to rotate. Sent to the tip. At this time, the feed amount of the resin in the second stage is larger than the feed amount in the first stage, so that a space not filled with the molten resin is formed in the flight at the vent portion. Since a space is created in this way, moisture, volatile matter, etc. generated from the resin can be prevented without leaking the molten resin to the outside.
A vacuum pump can be used to forcibly suck and exhaust air from the vent hole.

【0004】[0004]

【発明が解決しようとする課題】上記のように、従来の
ベント式シリンダによっても、樹脂から生じる水分、揮
発分等のみを外部に吸引排気することはできる。しかし
ながら、従来の真空ポンプは、溶融・混練動作と連動し
て起動するようになっているので、場合によっては粉末
樹脂がベント孔から配管系、真空ポンプ等に吸引される
欠点がある。さらに詳しく説明すると、ホッパから充分
の粉末樹脂が供給されていると、粉末樹脂はスクリュー
の回転による剪断力、摩擦力等の発熱作用で得られる熱
と、外部から加えられる熱とにより溶融してベント部に
送られるが、供給量が減少すると、充分な剪断力、摩擦
力等が得られなくなるので、溶融化が遅れ、パウダーの
ままベント部に送られることがある。そうすると、パウ
ダー状の樹脂は軽いので、真空ポンプに吸引される。一
旦吸引されると、配管系をふくめ真空ポンプにパウダー
状の樹脂が付着し面倒な清掃が必要となる。したがっ
て、本発明は、樹脂から生じる水分、揮発分等を外部に
強制的に吸引することができると共に、粉末樹脂が未溶
融の状態でベント部まで送られても、未溶融状態の樹脂
が外部に吸引されない、パウダー成形機の脱気方法用お
よび該方法の実施に供されるパウダー成形用ベント装置
を提供することを目的としている。
As described above, even with the conventional vent type cylinder, it is possible to suck and exhaust only water, volatile matter and the like generated from the resin. However, since the conventional vacuum pump is adapted to be activated in association with the melting / kneading operation, there is a drawback in some cases that the powdered resin is sucked from the vent hole into the piping system, the vacuum pump or the like. More specifically, when a sufficient amount of powder resin is supplied from the hopper, the powder resin is melted by heat obtained by heat generating action such as shearing force and frictional force due to rotation of the screw and heat applied from the outside. Although it is sent to the vent part, if the supply amount is reduced, sufficient shearing force, frictional force, etc. cannot be obtained, so that melting may be delayed and powder may be sent to the vent part as it is. Then, since the powdery resin is light, it is sucked by the vacuum pump. Once sucked, powdery resin adheres to the vacuum pump including the piping system, which requires troublesome cleaning. Therefore, according to the present invention, moisture, volatile matter, etc. generated from the resin can be forcibly sucked to the outside, and even if the powdered resin is sent to the vent portion in the unmelted state, the unmelted resin remains outside. It is an object of the present invention to provide a deaeration method for a powder molding machine, which is not sucked into the air, and a powder molding vent apparatus used for carrying out the method.

【0005】[0005]

【課題を解決するための手段】本発明は、上記目的を達
成するために、スクリューを駆動して、樹脂を前記スク
リューの溝にそって前方に送りながら溶融・混練し、そ
してベント部において樹脂から生じる水分、揮発分等を
真空ポンプで吸引排気するとき、前記スクリューのトル
ク値が所定値以下のときは、前記真空ポンプの吸引力を
減らすように構成される。請求項2記載の発明は、シリ
ンダと、該シリンダ内に設けられているスクリューとか
らなり、樹脂が前記スクリューの溝にそって前方に送ら
れる過程で溶融・混練され、そしてベント装置によって
樹脂から生じる水分、揮発分等が吸引排気されるように
なっている、射出成形機用のベント装置であって、前記
ベント装置は、前記シリンダに設けられているベント孔
と、該ベント孔に接続され、樹脂から生じる水分、揮発
分等を強制的に吸引する真空ポンプと、該真空ポンプの
吸引力を制御する制御手段と、前記スクリューのトルク
を検知するトルク検知手段とからなり、前記制御手段
は、前記トルク検知手段で検知されるトルク値が所定値
より低いと、前記真空ポンプの真空度が小さくなるよう
に制御する。
In order to achieve the above-mentioned object, the present invention is to drive a screw to melt and knead the resin while sending the resin forward along the groove of the screw, and to perform resin melting at the vent portion. When sucking and exhausting water, volatile matter, and the like generated from the vacuum pump with a vacuum pump and the torque value of the screw is a predetermined value or less, the suction force of the vacuum pump is reduced. The invention according to claim 2 comprises a cylinder and a screw provided in the cylinder, wherein the resin is melted and kneaded in the process of being forwardly fed along the groove of the screw, and the resin is melted and kneaded by a vent device. A vent device for an injection molding machine, wherein generated water, volatile matter, and the like are sucked and exhausted, wherein the vent device is connected to the vent hole provided in the cylinder and the vent hole. A vacuum pump for forcibly sucking water, volatile matter, etc. generated from the resin, a control means for controlling the suction force of the vacuum pump, and a torque detection means for detecting the torque of the screw. When the torque value detected by the torque detection means is lower than a predetermined value, the vacuum degree of the vacuum pump is controlled to be small.

【0006】[0006]

【作用】請求項2記載の発明は、次のように作用する。
すなわち樹脂を供給すると共に、スクリューを駆動す
る。そうすると、樹脂はスクリューの溝にそって前方に
送られる過程で溶融・混練される。このとき制御装置に
は、トルク検知手段からスクリューのトルク値が入力さ
れる。そうして制御装置は、入力されるトルク値が所定
値に達していると、真空ポンプの、例えばオン状態を保
つ。しがって、溶融・混練される過程で樹脂から生じる
水分、揮発分等は真空ポンプにより強制的に吸引排気さ
れる。これに対し、樹脂の供給量が減るなどして入力さ
れるトルク値が所定値より小さいと、制御装置は真空ポ
ンプの真空度が小さくなるように、例えば真空ポンプを
オフするように制御する。これにより、未溶融状態の樹
脂がベント部に達しても真空ポンプに吸引されることは
ない。
The invention according to claim 2 operates as follows.
That is, the resin is supplied and the screw is driven. Then, the resin is melted and kneaded in the process of being sent forward along the groove of the screw. At this time, the torque value of the screw is input to the control device from the torque detection means. Then, when the input torque value has reached the predetermined value, the control device keeps the vacuum pump, for example, in the ON state. Therefore, water, volatile matter and the like generated from the resin in the process of melting and kneading are forcibly sucked and exhausted by the vacuum pump. On the other hand, when the input torque value is smaller than the predetermined value due to a decrease in the resin supply amount, the control device controls so that the vacuum degree of the vacuum pump becomes smaller, for example, the vacuum pump is turned off. As a result, even if the unmelted resin reaches the vent portion, it is not sucked by the vacuum pump.

【0007】[0007]

【実施例】以下、本発明の実施例を説明する。図1は、
本発明の1実施例を示す断面図である。同図に示されて
いるように、本実施例に係わる射出機も、筒状のシリン
ダ1と、その内部に回転方向と軸方向とに駆動自在に設
けられているスクリュー10とを備えている。スクリュ
ー10は、図において右方から左方に向かって供給部1
1、第1メタリング部12、ベント部13、第2メタリ
ング部14と構成上区分され、第2メタリング部14の
前方部にスクリューヘッド15が設けられている。また
供給部11と第1メタリング部12は、第1ステージS
T1に、そしてベント部13と第2メタリング部14は
第2ステージST2に区分される。本実施例において
も、第1ステージST1における樹脂の送り量は、第2
ステージST2の送り量より小さい。またベント部13
のスクリュー10の溝は、他の部分に比較して深くなっ
ている。
EXAMPLES Examples of the present invention will be described below. Figure 1
It is sectional drawing which shows 1 Example of this invention. As shown in the figure, the injection machine according to the present embodiment also includes a cylindrical cylinder 1 and a screw 10 provided inside the cylinder 1 so as to be rotatable in the rotational direction and the axial direction. . The screw 10 corresponds to the supply unit 1 from the right to the left in the figure.
1, the first metering part 12, the vent part 13, and the second metering part 14 are structurally divided, and a screw head 15 is provided in the front part of the second metering part 14. Further, the supply unit 11 and the first metering unit 12 are connected to the first stage S
The vent portion 13 and the second metering portion 14 are divided into the second stage ST2 at T1. Also in this embodiment, the resin feed amount in the first stage ST1 is
It is smaller than the feed amount of stage ST2. In addition, the vent portion 13
The groove of the screw 10 is deeper than the other portions.

【0008】ベント部13に相当するシリンダ1には、
ベント管2が設けられ、このベント管2に、吸引管3が
接続されている。そして吸引管3には真空ポンプ4が介
装されている。真空ポンプ4は、本実施例では電動モー
タで駆動され、この電動モータは制御装置5により制御
されるようになっている。スクリュー10を回転駆動す
るために、図において右方に電動モータ7が設けられて
いる。電動モータ7は、減速機構を介してスクリュー1
0を回転駆動するが、スクリュー10のトルクは、電動
モータ7の電流値で計測され、制御装置5にライン8で
入力されるようになっている。制御装置5は、射出成形
に必要な構成要素を制御すると共に、スクリュー10の
トルク値を予め設定でき、設定されたトルク値と、電動
モータ7の電流値で計測されたトルク値とを比較し、計
測されたトルク値が設定されたトルク値より小さいとき
は、ライン6により真空ポンプ4のモータをオフする信
号を出力する機能も有する。
In the cylinder 1 corresponding to the vent portion 13,
A vent pipe 2 is provided, and a suction pipe 3 is connected to the vent pipe 2. A vacuum pump 4 is installed in the suction pipe 3. The vacuum pump 4 is driven by an electric motor in this embodiment, and the electric motor is controlled by the control device 5. To drive the screw 10 to rotate, an electric motor 7 is provided on the right side of the drawing. The electric motor 7 is a screw 1 via a reduction mechanism.
Although 0 is rotationally driven, the torque of the screw 10 is measured by the current value of the electric motor 7 and input to the control device 5 via the line 8. The control device 5 controls the components necessary for injection molding, and can preset the torque value of the screw 10, and compares the set torque value with the torque value measured by the electric current value of the electric motor 7. When the measured torque value is smaller than the set torque value, the line 6 also has a function of outputting a signal for turning off the motor of the vacuum pump 4.

【0009】次に上記実施例の作用について説明する。
制御装置5に、樹脂が溶融されてベント部13に送られ
るときの、スクリュー10のトルク値を予め設定する。
ホッパ16から粉末状の樹脂を供給部11に供給すると
共に、電動モータ7によりスクリュー10を回転駆動す
る。そうすると、周知のように、樹脂は第1ステージS
T1から第2ステージST2に送られる過程で、シリン
ダ1の外周部に設けられているヒータ17、17、…に
よる加熱と、スクリュー10の回転駆動による剪断力、
摩擦力等による発熱作用とにより溶融・混練され、前方
に蓄積される。所定量蓄積されたら、スクリュー10を
駆動してノズルから金型19に射出する。冷却固化を待
って型開きして成形品を取り出す。型締めして、以下同
様な操作を繰り返して成形品を得る。
Next, the operation of the above embodiment will be described.
The torque value of the screw 10 when the resin is melted and sent to the vent portion 13 is preset in the control device 5.
The powdery resin is supplied from the hopper 16 to the supply unit 11, and the screw 10 is rotationally driven by the electric motor 7. Then, as is well known, the resin is the first stage S
In the process of being transferred from T1 to the second stage ST2, heating by the heaters 17, 17, ... Provided on the outer peripheral portion of the cylinder 1 and shearing force by rotational driving of the screw 10,
It is melted and kneaded by the heat generated by frictional force, etc., and accumulated in the front. When a predetermined amount is accumulated, the screw 10 is driven to inject from the nozzle into the mold 19. After cooling and solidification, the mold is opened and the molded product is taken out. The mold is clamped, and the same operation is repeated thereafter to obtain a molded product.

【0010】上記のようにして成形品を得るとき、例え
ば成形機を起動した初期の段階では、樹脂はスクリュー
10のフライト間に満たされていないので、大きな剪断
力、摩擦力等は作用しない。したがって、スクリュー1
0の回転駆動トルクも小さい。それゆえ、電動モータ7
の電流値で計測されるスクリュー10のトルク値は、制
御装置5に予め設定されている設定値より小さく、制御
装置5はライン6により真空ポンプ4の電動モータをオ
フする信号を出力する。そうすると、真空ポンプ4は起
動しないので、未溶融状態の粉末樹脂がベント部13に
例え送られても、粉末樹脂はベント管2から吸引管3、
真空ポンプ4等に吸引されることはない。
When the molded product is obtained as described above, for example, at the initial stage when the molding machine is started, the resin is not filled between the flights of the screw 10, so that large shearing force, frictional force, etc. do not act. Therefore, screw 1
The rotational drive torque of 0 is also small. Therefore, the electric motor 7
The torque value of the screw 10 measured by the current value is smaller than the preset value set in the control device 5, and the control device 5 outputs a signal for turning off the electric motor of the vacuum pump 4 through the line 6. Then, since the vacuum pump 4 does not start, even if the unmelted powdered resin is sent to the vent portion 13, the powdered resin flows from the vent pipe 2 to the suction pipe 3,
It is not sucked by the vacuum pump 4 or the like.

【0011】初期の段階が過ぎ、所定量宛供給されるよ
うになると、所定の大きさの剪断力、摩擦力等が作用す
るようになるので、スクリュー10のトルク値は上昇す
る。トルク値はライン8により制御装置5に入力されて
いるので、設定値より大きくなると、真空ポンプ4の電
動モータをオンする信号を出力する。第1ステージST
1における樹脂の送り量は、第2ステージST2の送り
量より小さく、またベント部13のスクリュー10の溝
は、他の部分に比較して深くなっているので、ベント部
13のフライト間には樹脂が満たされない空間ができ、
この空間にベント管2および吸引管3を介して所定の真
空度が作用する。したがって、溶融・混練の過程で樹脂
から生じる水分、揮発分等は、真空ポンプ4により吸引
排気される。何らかの原因でホッパ16への樹脂の供給
が途絶え、供給部11に供給される樹脂の量が減少する
と、すなわちスクリュー10のフライト間に樹脂が満た
されないようになると、剪断力、摩擦力等による充分な
発熱作用が得られないので、溶融が遅れ、未溶融状態の
樹脂がベント部13に達するようになる。この時は前述
したようにスクリュー10の回転駆動トルクが設定値よ
り小さくなるので、制御装置5は真空ポンプ4の電動モ
ータをオフする信号を出力する。したがって、未溶融状
態の樹脂がベント部13に達しても真空ポンプ4等に吸
引されることはない。
When the initial amount is passed and a predetermined amount is supplied, a shearing force, a frictional force, etc. having a predetermined magnitude come to act, so that the torque value of the screw 10 increases. Since the torque value is input to the control device 5 through the line 8, when it becomes larger than the set value, a signal for turning on the electric motor of the vacuum pump 4 is output. First stage ST
The feed amount of the resin in 1 is smaller than the feed amount of the second stage ST2, and the groove of the screw 10 of the vent portion 13 is deeper than the other portions, so that between the flights of the vent portion 13, There is a space not filled with resin,
A predetermined degree of vacuum acts on this space through the vent pipe 2 and the suction pipe 3. Therefore, water, volatile matter and the like generated from the resin in the process of melting and kneading are sucked and exhausted by the vacuum pump 4. If the supply of the resin to the hopper 16 is interrupted for some reason and the amount of the resin supplied to the supply unit 11 is reduced, that is, if the resin is not filled during the flight of the screw 10, the shearing force, the frictional force, etc. are sufficient. Since such a heat-generating effect cannot be obtained, melting is delayed, and unmelted resin reaches the vent portion 13. At this time, since the rotational driving torque of the screw 10 becomes smaller than the set value as described above, the control device 5 outputs a signal to turn off the electric motor of the vacuum pump 4. Therefore, even if the unmelted resin reaches the vent portion 13, it is not sucked by the vacuum pump 4 or the like.

【0012】上記実施例では、スクリュー10の回転駆
動トルク値により、真空ポンプ4の電動モータがオン、
オフされているが、未溶融状態の樹脂が真空ポンプ4等
に吸引されない程度に真空ポンプ4の真空度を制御する
こともできる。例えば、スクリュー10の回転駆動トル
クと設定値とを比較して、その差に応じて真空ポンプ4
の電動モータの回転数を位相制御することもできる。ま
た、図に示されているように、真空ポンプ4の上流側の
吸引管3に、分岐管3’を設け、この分岐管3’に流量
制御弁あるいは開閉弁9を設け、そしてこの開閉弁9を
制御装置5で制御することもできる。例えば前述したよ
うに、電動モータ7の電流値で計測されるスクリュー1
0のトルク値と、制御装置5に予め設定されている設定
値とを比較して、その差に応じて制御装置5が開閉弁9
を開閉するように、あるいは開度を調節するように実施
することもできる。開閉弁9を開にすると、あるいは開
度を大きくすると、真空ポンプ4には外気が吸引される
ので、ベント部13には大きな負圧は作用しないように
なる。したがって、未溶融状態の樹脂が送られても真空
ポンプ4等に吸引されることはない。さらには、吸引管
3に開閉弁9’を設け、スクリュー10のトルク値が設
定値以下の時は、開閉弁9’で吸引管3を遮断し、真空
ポンプ4の吸引力がベント部13に及ばないようにする
こともできる。このように実施すると、真空ポンプ4の
電動モータをオン・オフする場合に比較して、電動モー
タの寿命が長くなる効果が得られる。
In the above embodiment, the electric motor of the vacuum pump 4 is turned on according to the rotational driving torque value of the screw 10.
Although turned off, the vacuum degree of the vacuum pump 4 can be controlled to such an extent that the unmelted resin is not sucked by the vacuum pump 4 or the like. For example, the rotation driving torque of the screw 10 is compared with a set value, and the vacuum pump 4 is operated according to the difference.
The number of rotations of the electric motor can also be phase-controlled. Further, as shown in the figure, a branch pipe 3'is provided on the suction pipe 3 on the upstream side of the vacuum pump 4, a flow control valve or an on-off valve 9 is provided on the branch pipe 3 ', and the on-off valve is provided. 9 can also be controlled by the control device 5. For example, as described above, the screw 1 measured by the current value of the electric motor 7
The torque value of 0 is compared with a preset value set in the control device 5, and the control device 5 causes the open / close valve 9 to operate according to the difference.
It is also possible to carry out so as to open and close or to adjust the opening degree. When the on-off valve 9 is opened or the opening is increased, the vacuum pump 4 sucks the outside air, so that a large negative pressure does not act on the vent portion 13. Therefore, even if the unmelted resin is sent, it is not sucked by the vacuum pump 4 or the like. Further, the suction pipe 3 is provided with an opening / closing valve 9 ', and when the torque value of the screw 10 is equal to or less than the set value, the suction pipe 3 is shut off by the opening / closing valve 9', and the suction force of the vacuum pump 4 is applied to the vent portion 13. You can choose not to exceed it. By carrying out in this way, compared with the case where the electric motor of the vacuum pump 4 is turned on / off, the effect of extending the life of the electric motor can be obtained.

【0013】[0013]

【発明の効果】以上のように本発明によると、ベント装
置には、真空ポンプが設けられているので、スクリュー
を駆動して、樹脂をスクリューの溝にそって前方に送り
ながら溶融・混練するとき樹脂から生じる水分、揮発分
等を真空ポンプで強制的に吸引排気することができる。
しかも、スクリューのトルク値が所定値以下のときは、
すなわち粉末状態の樹脂が送られる可能性のあるとき
は、制御装置は真空ポンプの吸引力を減らすので、未溶
融状態の樹脂が例え送られても、真空ポンプに吸引され
ることがない、という本発明特有の効果が得られる。
As described above, according to the present invention, since the vent device is provided with the vacuum pump, the screw is driven to melt and knead the resin while feeding the resin forward along the groove of the screw. At this time, water, volatile matter, etc. generated from the resin can be forcibly sucked and exhausted by a vacuum pump.
Moreover, when the torque value of the screw is less than or equal to the predetermined value,
That is, when powdery resin may be sent, the controller reduces the suction force of the vacuum pump, so even if unmelted resin is sent, it is not sucked by the vacuum pump. The effect peculiar to the present invention can be obtained.

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

【図1】本発明の1実施例を一部断面にして示す模式図
である。
FIG. 1 is a schematic view showing an embodiment of the present invention with a partial cross section.

【符号の説明】[Explanation of symbols]

1 シリンダ 2 ベント
管(ベント孔) 4 真空ポンプ 5 制御装
置 10 スクリュー 13 ベント
1 cylinder 2 vent pipe (vent hole) 4 vacuum pump 5 controller 10 screw 13 vent part

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 スクリュー10を駆動して、樹脂を前記
スクリューの溝にそって前方に送りながら溶融・混練
し、そしてベント部13において樹脂から生じる水分、
揮発分等を真空ポンプ4で吸引排気するとき、 前記スクリュー10のトルク値が所定値以下のときは、
前記真空ポンプ4の吸引力を減らすことを特徴とするパ
ウダー成形機の脱気方法。
1. A screw 10 is driven to melt and knead resin while feeding the resin forward along a groove of the screw, and water generated from the resin in the vent portion 13
When the volatile matter and the like are sucked and exhausted by the vacuum pump 4, and when the torque value of the screw 10 is less than or equal to a predetermined value,
A deaeration method for a powder molding machine, comprising reducing the suction force of the vacuum pump 4.
【請求項2】シリンダ1と、該シリンダ内に設けられて
いるスクリュー10とからなり、樹脂が前記スクリュー
10の溝にそって前方に送られる過程で溶融・混練さ
れ、そしてベント装置によって樹脂から生じる水分、揮
発分等が吸引排気されるようになっている、射出成形機
用のベント装置であって、 前記ベント装置は、前記シリンダ1に設けられているベ
ント孔2と、該ベント孔に接続され、樹脂から生じる水
分、揮発分等を強制的に吸引する真空ポンプ4と、該真
空ポンプの吸引力を制御する制御手段5と、前記スクリ
ュー10のトルク値を検知するトルク検知手段とからな
り、 前記制御手段5は、前記トルク検知手段で検知されるト
ルク値が所定値より低いと、前記真空ポンプ4のベント
部13に作用する真空度が小さくなるように制御するこ
とを特徴とするパウダー成形用ベント装置。
2. A cylinder 1 and a screw 10 provided in the cylinder, wherein the resin is melted and kneaded in the process of being forwardly fed along the groove of the screw 10, and is vented from the resin by a vent device. A vent device for an injection molding machine, wherein generated water, volatile matter, and the like are sucked and exhausted, and the vent device includes a vent hole 2 provided in the cylinder 1 and a vent hole. A vacuum pump 4 which is connected and forcibly sucks water, volatile matter, etc. generated from the resin, control means 5 for controlling the suction force of the vacuum pump, and torque detection means for detecting the torque value of the screw 10. When the torque value detected by the torque detection means is lower than a predetermined value, the control means 5 reduces the degree of vacuum acting on the vent portion 13 of the vacuum pump 4. Control Powder molding vent apparatus, characterized by.
JP5104947A 1993-04-08 1993-04-08 Deaerating method of powder molding machine and vent device for molding powder Pending JPH06293021A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5104947A JPH06293021A (en) 1993-04-08 1993-04-08 Deaerating method of powder molding machine and vent device for molding powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5104947A JPH06293021A (en) 1993-04-08 1993-04-08 Deaerating method of powder molding machine and vent device for molding powder

Publications (1)

Publication Number Publication Date
JPH06293021A true JPH06293021A (en) 1994-10-21

Family

ID=14394295

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5104947A Pending JPH06293021A (en) 1993-04-08 1993-04-08 Deaerating method of powder molding machine and vent device for molding powder

Country Status (1)

Country Link
JP (1) JPH06293021A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6187229B1 (en) 1995-11-10 2001-02-13 Nissei Plastic Industrial Co., Ltd. Process for injection molding information recording disks
WO2004067244A1 (en) * 2003-01-30 2004-08-12 Hitachi Chemical Co., Ltd. Semiconductor-sealing-purpose epoxy resin compound producing method
JP2007331304A (en) * 2006-06-16 2007-12-27 Nippon Steel Corp High density volume reducing molding machine of waste plastic and exhaust method therefor
KR100924081B1 (en) * 2007-11-09 2009-11-02 (주)이앤페트로테크놀러지 Oil manufacturing device for high polymer waste
JP2014141034A (en) * 2013-01-25 2014-08-07 Japan Steel Works Ltd:The Vacuum degree control device and method by electromotive valve of pusher

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6187229B1 (en) 1995-11-10 2001-02-13 Nissei Plastic Industrial Co., Ltd. Process for injection molding information recording disks
WO2004067244A1 (en) * 2003-01-30 2004-08-12 Hitachi Chemical Co., Ltd. Semiconductor-sealing-purpose epoxy resin compound producing method
CN100364744C (en) * 2003-01-30 2008-01-30 日立化成工业株式会社 Semiconductor-sealing-purpose epoxy resin compound producing method
US7521011B2 (en) 2003-01-30 2009-04-21 Hitachi Chemical Company, Ltd. Semiconductor-sealing-purpose epoxy resin compound producing method
JP2007331304A (en) * 2006-06-16 2007-12-27 Nippon Steel Corp High density volume reducing molding machine of waste plastic and exhaust method therefor
KR100924081B1 (en) * 2007-11-09 2009-11-02 (주)이앤페트로테크놀러지 Oil manufacturing device for high polymer waste
JP2014141034A (en) * 2013-01-25 2014-08-07 Japan Steel Works Ltd:The Vacuum degree control device and method by electromotive valve of pusher

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