JPH10329200A - Method and apparatus for controlling composite extrusion molding machine - Google Patents
Method and apparatus for controlling composite extrusion molding machineInfo
- Publication number
- JPH10329200A JPH10329200A JP9140440A JP14044097A JPH10329200A JP H10329200 A JPH10329200 A JP H10329200A JP 9140440 A JP9140440 A JP 9140440A JP 14044097 A JP14044097 A JP 14044097A JP H10329200 A JPH10329200 A JP H10329200A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- extruder
- gear pump
- fixed
- pass filter
- 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 24
- 239000002131 composite material Substances 0.000 title claims description 10
- 238000000034 method Methods 0.000 title claims description 9
- 239000000463 material Substances 0.000 claims abstract description 15
- 239000000284 extract Substances 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims description 19
- 150000001875 compounds Chemical class 0.000 claims description 5
- 230000000737 periodic effect Effects 0.000 claims 2
- 238000010586 diagram Methods 0.000 description 5
- 230000000295 complement effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 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
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means 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
-
- 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
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/365—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pumps, e.g. piston pumps
- B29C48/37—Gear pumps
-
- 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
- B29C48/92—Measuring, controlling or regulating
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92019—Pressure
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92361—Extrusion unit
- B29C2948/9238—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/9239—Screw or gear
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
- B29C2948/9259—Angular velocity
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92885—Screw or gear
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、押出機のスクリュ
により混練された合成樹脂成形材料をギヤポンプによっ
て吐出するようにした複合形押出成形装置における制御
方法及び制御装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a control method and a control apparatus for a composite extrusion molding apparatus in which a synthetic resin molding material kneaded by a screw of an extruder is discharged by a gear pump.
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】従来、
上述の如き複合形押出成形装置においては、上記ギヤポ
ンプの吐出量を安定化して、成形品の寸法精度を向上さ
せるため、ギヤポンプの吸入圧によって押出機のスクリ
ュの回転速度を制御するとともに、押出機への材料供給
量を制御するようにすることが提案されている。2. Description of the Related Art
In the compound extrusion molding apparatus as described above, in order to stabilize the discharge amount of the gear pump and improve the dimensional accuracy of the molded product, the rotational speed of the screw of the extruder is controlled by the suction pressure of the gear pump, and the extruder is controlled. It has been proposed to control the amount of material supplied to the system.
【0003】しかしながら、この種装置では押出機内に
材料が滞溜する時間が長いため、上述のように、単にギ
ヤポンプの吸入圧のみによって押出機への材料供給量の
制御を行なう場合には、その材料供給量の変化の影響が
長時間にわたって残り、圧力変動を取り除くことが難し
いとともに、上記ギヤポンプの吸入圧によって押出機の
スクリュの回転速度を制御したとしても、上記圧力検出
値には長周期分の圧力変動信号が含まれているので、短
周期の圧力変動に対して必ずしも応答が早くなるとは限
らない等の問題がある。[0003] However, in this type of apparatus, since the material stays in the extruder for a long time, as described above, when the amount of material supplied to the extruder is controlled only by the suction pressure of the gear pump, it is difficult to control the amount of material supplied to the extruder. The influence of the change in the material supply amount remains for a long time, it is difficult to remove the pressure fluctuation, and even if the rotation speed of the screw of the extruder is controlled by the suction pressure of the gear pump, the detected pressure value is longer than the long period. , The response to short-period pressure fluctuations is not always fast.
【0004】本発明はこのような点に鑑み、上述の如き
不都合がなく複合形押出成形装置の的確な制御を行い、
製品の精度を一定に保つことができるようにした制御方
法及び制御装置を得ることを目的とする。[0004] In view of the above, the present invention provides an accurate control of a composite extrusion molding apparatus without the above-mentioned disadvantages.
It is an object of the present invention to obtain a control method and a control device capable of keeping the accuracy of a product constant.
【0005】[0005]
【課題を解決するための手段】本願の第1の発明は、定
量制御して原料を押出機に供給する定量フィーダと、定
量フィーダから原料を供給される押出機と、その押出機
の押出側に連結されるギヤポンプとを有する複合形押出
成形装置の制御方法において、上記ギヤポンプの入口側
の圧力を検出し、その圧力の変動を長周期成分と短周期
成分とに分離し、上記長周期成分の圧力変動によってギ
ヤポンプの入口側圧力が設定圧力になるように定量フィ
ーダの材料供給量を制御するとともに、短周期成分の圧
力変動によって押出機のスクリュ回転速度を制御するこ
とを特徴とする。Means for Solving the Problems A first invention of the present application is directed to a quantitative feeder for supplying a raw material to an extruder under quantitative control, an extruder for supplying the raw material from the quantitative feeder, and an extrusion side of the extruder. A method for controlling a compound extrusion molding apparatus having a gear pump connected to a gear pump, comprising detecting a pressure at an inlet side of the gear pump, separating a change in the pressure into a long-period component and a short-period component, The amount of material supplied to the fixed-quantity feeder is controlled so that the pressure on the inlet side of the gear pump becomes the set pressure by the pressure fluctuation, and the screw rotation speed of the extruder is controlled by the pressure fluctuation of the short-period component.
【0006】第2の発明は、また定量制御して原料を押
出機に供給する定量フィーダと、定量フィーダから原料
を供給される押出機と、その押出機の押出側に連結され
るギヤポンプとを有する複合形押出成形装置の制御方法
において、上記ギヤポンプの入口側圧力及び出口側の圧
力を検出し、その差圧の変動を長周期成分と短周期成分
とに分離し、上記長周期成分の差圧変動によってギヤポ
ンプの入口側圧力が設定圧力になるように定量フィーダ
の材料供給量を制御するとともに、短周期成分の差圧変
動によって押出機のスクリュ回転速度を制御することを
特徴とする。According to a second aspect of the present invention, there is provided a quantitative feeder for supplying a raw material to an extruder under quantitative control, an extruder for supplying the raw material from the quantitative feeder, and a gear pump connected to the extrusion side of the extruder. In the control method of the compound extrusion molding apparatus having the above, detecting the pressure on the inlet side and the pressure on the outlet side of the gear pump, separating the fluctuation of the differential pressure into a long-period component and a short-period component, It is characterized in that the material supply amount of the fixed-quantity feeder is controlled so that the pressure on the inlet side of the gear pump becomes a set pressure by the pressure fluctuation, and the screw rotation speed of the extruder is controlled by the fluctuation of the differential pressure of the short-period component.
【0007】さらに第3の発明は、定量制御して原料を
押出機に供給する定量フィーダと、定量フィーダから原
料を供給される押出機と、その押出機の押出側に連結さ
れたギヤポンプとを有する複合形押出成形装置の制御装
置において、上記ギヤポンプの入口側の圧力を検出する
圧力検出器と、上記圧力検出器で検出された圧力の変動
信号の長周期成分を取り出すローパスフィルタと、上記
圧力の変動信号の短周期成分を取り出すハイパスフィル
ターと、ローパスフィルタにより抽出された圧力変動信
号により定量のフィーダの材料供給量を制御する第1の
制御装置と、ハイパスフィルターにより抽出された圧力
変動信号により押出機のスクリュ回転速度を制御する第
2の制御装置とを有することを特徴とする。In a third aspect of the present invention, there is provided a quantitative feeder for supplying a raw material to an extruder under quantitative control, an extruder for supplying the raw material from the quantitative feeder, and a gear pump connected to the extrusion side of the extruder. A control device for the compound extrusion molding apparatus, comprising: a pressure detector for detecting a pressure on the inlet side of the gear pump; a low-pass filter for extracting a long-period component of a fluctuation signal of the pressure detected by the pressure detector; A high-pass filter that extracts a short-period component of the fluctuation signal of the first control device, a first control device that controls a fixed amount of material supplied to the feeder by the pressure fluctuation signal extracted by the low-pass filter, and a pressure fluctuation signal that is extracted by the high-pass filter. A second control device for controlling the screw rotation speed of the extruder.
【0008】第4の発明は、上記定量制御して原料を押
出機に供給する定量フィーダと、定量フィーダから原料
を供給される押出機と、その押出機の押出側に連結され
たギヤポンプとを有する複合形押出成形装置の制御装置
において、上記ギヤポンプの入口側の圧力を検出する第
1の圧力検出器と、ギヤポンプの出口側の圧力を検出す
る第2の圧力検出器と、両圧力検出器で検出された圧力
の差圧の変動信号の長周期成分を取り出すローパスフィ
ルタと、上記差圧の変動信号の短周期成分を取り出すハ
イパスフィルタと、ローパスフィルタにより抽出された
圧力変動信号により定量フィーダの材料供給量を制御す
る第1の制御装置と、ハイパスフィルタにより抽出され
た圧力変動信号により押出機のスクリュ回転速度を制御
する第2の制御装置とを有することを特徴とする。[0010] A fourth aspect of the present invention provides a quantitative feeder for supplying a raw material to an extruder under the above-mentioned quantitative control, an extruder for supplying the raw material from the quantitative feeder, and a gear pump connected to the extrusion side of the extruder. A first pressure detector for detecting a pressure on an inlet side of the gear pump, a second pressure detector for detecting a pressure on an outlet side of the gear pump, and both pressure detectors. A low-pass filter for extracting a long-period component of the fluctuation signal of the differential pressure of the pressure detected in the above, a high-pass filter for extracting a short-period component of the fluctuation signal of the differential pressure, and a pressure fluctuation signal extracted by the low-pass filter. A first control device for controlling a material supply amount, and a second control device for controlling a screw rotation speed of an extruder based on a pressure fluctuation signal extracted by a high-pass filter. Characterized in that it has and.
【0009】[0009]
【発明の実施の形態】以下、添付図面を参照して本発明
の実施の形態について説明する。図1は本発明における
複合形押出成形装置の制御装置のブロック図であって、
定量フィーダ1から2軸押出機2に供給された原料は、
その2軸押出機で混練されながら加熱、溶融されてギヤ
ポンプ3に送り込まれ、そこで上記2軸押出機2から連
続的に搬送されてくる原料が一定量づつ計量され、フィ
ルタ4を経てダイ5に供給される。Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a block diagram of a control device of a composite extrusion molding apparatus according to the present invention,
The raw material supplied from the fixed-quantity feeder 1 to the twin-screw extruder 2 is:
The mixture is heated and melted while being kneaded by the twin-screw extruder and fed to the gear pump 3, where the raw material continuously conveyed from the twin-screw extruder 2 is measured by a fixed amount, and is passed through the filter 4 to the die 5. Supplied.
【0010】上記ギヤポンプ3の入口側には圧力検出器
6が設けられており、その圧力検出器6で検出されたギ
ヤポンプ入口側の圧力P1がローパスフィルタ7及びハ
イパスフィルタ8にそれぞれ入力される。上記ローパス
フィルタ7では、上記ギヤポンプ入口側圧力P1の長周
期成分の圧力変動信号が抽出され、その長周期成分の圧
力変動信号が第1の制御装置9に入力される。そしてそ
の第1の制御装置9から上記ギヤポンプ入口側の圧力が
設定圧力になるような制御信号が出力され、その制御信
号が定量フィーダ1の駆動モータ10に入力され、駆動
モータ10の制御によって定量フィーダ1から2軸押出
機2に供給される原料供給量が制御される。A pressure detector 6 is provided on the inlet side of the gear pump 3, and the pressure P1 on the gear pump inlet side detected by the pressure detector 6 is input to a low-pass filter 7 and a high-pass filter 8, respectively. The low-pass filter 7 extracts a long-period component pressure fluctuation signal of the gear pump inlet-side pressure P <b> 1, and inputs the long-period pressure fluctuation signal to the first controller 9. Then, a control signal is output from the first control device 9 so that the pressure on the gear pump inlet side becomes the set pressure, and the control signal is input to the drive motor 10 of the fixed-quantity feeder 1. The amount of raw materials supplied from the feeder 1 to the twin-screw extruder 2 is controlled.
【0011】一方、ハイパスフィルタ8では、上記ギヤ
ポンプ入口側圧力P1の短周期成分の圧力変動信号が抽
出され、その短周期成分の圧力変動信号が第2の制御装
置11に入力される。そして、上記第2の制御装置11
から前期ギヤポンプ入口側の圧力が設定圧力になるよう
な制御信号が出力され、その制御信号が2軸押出機2の
駆動モータ12に入力され、2軸押出機のスクリュ回転
速度が制御される。図2に上記制御装置における制御フ
ローを示す。On the other hand, the high-pass filter 8 extracts a short-period component pressure fluctuation signal of the gear pump inlet-side pressure P 1, and inputs the short-period pressure fluctuation signal to the second controller 11. Then, the second control device 11
Outputs a control signal such that the pressure on the inlet side of the gear pump becomes the set pressure, the control signal is input to the drive motor 12 of the twin-screw extruder 2, and the screw rotation speed of the twin-screw extruder is controlled. FIG. 2 shows a control flow in the control device.
【0012】しかして、ギヤポンプの入口側圧力の長周
期成分の圧力変動信号によって定量フィーダが制御さ
れ、定量フィーダの特性変化による外乱に対する修正が
行なわれるとともに、短周期成分の圧力変動信号によっ
て2軸押出機のスクリュ回転速度が制御され、押出機の
スクリュ回転速度が上記圧力変動に速やかに応答し、変
動幅が小さく制御される。すなわち、長周期成分の圧力
変動信号と短周期成分の圧力変動信号によって定量フィ
ーダ及び2軸押出機を制御することによって、長周期の
変動及び短周期の変動の両者をそれぞれ取り除くことが
でき、圧力変動が小さくなるように制御される。Thus, the fixed-quantity feeder is controlled by the pressure fluctuation signal of the long-period component of the pressure on the inlet side of the gear pump, and the disturbance due to the change in the characteristic of the fixed-quantity feeder is corrected. The screw rotation speed of the extruder is controlled, the screw rotation speed of the extruder quickly responds to the pressure fluctuation, and the fluctuation width is controlled to be small. That is, by controlling the fixed-quantity feeder and the twin-screw extruder with the pressure fluctuation signal of the long-period component and the pressure fluctuation signal of the short-period component, both the long-period fluctuation and the short-period fluctuation can be eliminated, respectively. Control is performed so that the fluctuation is reduced.
【0013】ところで、上記実施の形態においては、ギ
ヤポンプ3の入口側圧力によって定量フィーダ1及び2
軸押出機2のスクリュ回転速度を制御するようにしたも
のを示したが、ギヤポンプ3の入口側及び出口側の圧力
差によって定量フィーダ及び2軸押出機のスクリュ回転
速度を制御するようしてもよい。すなわち、定量フィー
ダの供給量変動は必ずギヤポンプ前後の差圧の変化とし
て現われる。したがって、この差圧によって定量フィー
ダ等を制御することによって外乱に対処することができ
る。In the above embodiment, the fixed-quantity feeders 1 and 2 are controlled by the pressure on the inlet side of the gear pump 3.
The screw rotation speed of the screw extruder 2 is controlled. However, the screw rotation speed of the fixed feeder and the twin screw extruder may be controlled by the pressure difference between the inlet side and the outlet side of the gear pump 3. Good. That is, the change in the supply amount of the fixed amount feeder always appears as a change in the differential pressure before and after the gear pump. Therefore, by controlling the fixed-quantity feeder and the like by the differential pressure, it is possible to cope with the disturbance.
【0014】図3は上記差圧による制御を行うようにし
た実施の態様を示す図であり、ギヤポンプ3の入口側及
び出口側に第1の圧力検出器6及び第2の圧力検出器1
3をそれぞれ設け、第1の圧力検出器6及び第2の圧力
検出器13で検出された両圧力信号が差圧演算器14で
比較演算され、その差圧がそれぞれローパスフィルタ7
及びハイパスフィルタ8に入力され、上記差圧変動の長
周期成分により定量フィーダ1が制御されるとともに短
周期成分により2軸押出機2のスクリュ回転速度が制御
される。FIG. 3 is a diagram showing an embodiment in which the control based on the differential pressure is performed. A first pressure detector 6 and a second pressure detector 1 are provided on the inlet side and the outlet side of the gear pump 3.
The two pressure signals detected by the first pressure detector 6 and the second pressure detector 13 are compared with each other by a differential pressure calculator 14, and the differential pressure is calculated by a low-pass filter 7.
The high-pass filter 8 controls the fixed-quantity feeder 1 by the long-period component of the differential pressure fluctuation, and controls the screw rotation speed of the twin-screw extruder 2 by the short-period component.
【0015】しかして、この場合もギヤポンプ3の入口
側と出口側との圧力差の長周期成分によりフィーダ供給
量が制御され、短周期成分によりスクリュ回転速度が制
御され、長周期成分の制御と短周期成分の制御とが分担
実行され、相互の補完機能が生かされ、広範囲にわたる
正確な制御が行われる。In this case, too, the feeder supply amount is controlled by the long-period component of the pressure difference between the inlet side and the outlet side of the gear pump 3, the screw rotation speed is controlled by the short-period component, and the long-period component is controlled. The control of the short-period component is executed in a shared manner, the mutual complement function is utilized, and accurate control over a wide range is performed.
【0016】[0016]
【発明の効果】以上説明したように、本発明はギヤポン
プの入口側圧力の変動或は入口側と出口側との圧力差の
変動を長周期成分と短周期成分とに分け、それぞれによ
って定量フィーダ及び2軸押出機のスクリュ回転速度を
制御するようしたので、長周期成分の制御と短周期成分
の制御の両制御をそれぞれ分担実行してともに行うこと
ができ両周期の変動を互いに補完して確実に取り除くこ
とができてギヤポンプの入口における圧力変動を小さく
することができ、製品精度を向上させることができる。As described above, according to the present invention, the fluctuation of the pressure on the inlet side of the gear pump or the fluctuation of the pressure difference between the inlet side and the outlet side is divided into a long-period component and a short-period component. And the screw rotation speed of the twin-screw extruder is controlled, so that both the control of the long-period component and the control of the short-period component can be shared and executed together, and the fluctuations of both periods can be complemented by each other. As a result, the pressure fluctuation at the inlet of the gear pump can be reduced, and the product accuracy can be improved.
【図1】本発明の一実施の形態を示すブロック図。FIG. 1 is a block diagram showing one embodiment of the present invention.
【図2】図1に示す装置の制御フローを示す図。FIG. 2 is a diagram showing a control flow of the apparatus shown in FIG.
【図3】本発明の他の実施の形態を示すブロック図。FIG. 3 is a block diagram showing another embodiment of the present invention.
1 定量フィーダ 2 2軸押出機 3 ギヤポンプ 4 フィルタ 5 ダイ 6 圧力検出器 7 ローパスフィルタ 8 ハイパスフィルタ 9 第1の制御装置 11 第2の制御装置 13 第2の圧力検出器 14 差圧演算器 REFERENCE SIGNS LIST 1 fixed-quantity feeder 2 twin-screw extruder 3 gear pump 4 filter 5 die 6 pressure detector 7 low-pass filter 8 high-pass filter 9 first control device 11 second control device 13 second pressure detector 14 differential pressure calculator
Claims (4)
フィーダと、定量フィーダから原料を供給される押出機
と、その押出機の押出側に連結されるギヤポンプとを有
する複合形押出成形装置の制御方法において、上記ギヤ
ポンプの入口側の圧力を検出し、その圧力の変動を長周
期成分と短周期成分とに分離し、上記長周期成分の圧力
変動によってギヤポンプの入口側圧力が設定圧力になる
ように定量フィーダの材料供給量を制御するとともに、
短周期成分の圧力変動によって押出機のスクリュ回転速
度を制御することを特徴とする、複合形押出成形装置の
制御方法。1. A composite extrusion molding apparatus comprising: a fixed-quantity feeder for supplying a raw material to an extruder under quantitative control; an extruder for supplying the raw material from the fixed-quantity feeder; and a gear pump connected to an extrusion side of the extruder. In the control method of the device, the pressure on the inlet side of the gear pump is detected, and the fluctuation of the pressure is separated into a long-period component and a short-period component. Control the material feed rate of the fixed-quantity feeder so that
A method for controlling a compound extrusion molding apparatus, wherein a screw rotation speed of an extruder is controlled by a pressure fluctuation of a short-period component.
フィーダと、定量フィーダから原料を供給される押出機
と、その押出機の押出側に連結されるギヤポンプとを有
する複合形押出成形装置の制御方法において、上記ギヤ
ポンプの入口側の圧力及び出口側の圧力を検出し、その
差圧の変動を長周期成分と短周期成分とに分離し、上記
長周期成分の差圧変動によってギヤポンプの入口側圧力
が設定圧力になるように定量フィーダの材料供給量を制
御するとともに、短周期成分の差圧変動によって押出機
のスクリュ回転速度を制御することを特徴とする、複合
形押出成形装置の制御方法。2. A composite extrusion molding machine comprising: a fixed-quantity feeder for supplying a raw material to an extruder under quantitative control; an extruder for supplying the raw material from the fixed-quantity feeder; and a gear pump connected to the extrusion side of the extruder. In the control method of the device, the pressure on the inlet side and the pressure on the outlet side of the gear pump are detected, and the fluctuation of the differential pressure is separated into a long-period component and a short-period component. Type extrusion molding machine characterized by controlling the amount of material supplied to the fixed-quantity feeder so that the inlet pressure of the extruder becomes the set pressure, and controlling the screw rotation speed of the extruder by the fluctuation of the differential pressure of the short-period component. Control method.
フィーダと、定量フィーダから原料を供給される押出機
と、その押出機の押出側に連結されたギヤポンプとを有
する複合形押出成形装置の制御装置において、上記ギヤ
ポンプの入口側の圧力を検出する圧力検出器と、上記圧
力検出器で検出された圧力の変動信号の長周期成分を取
り出すローパスフィルタと、上記圧力の変動信号の短周
期成分を取り出すハイパスフィルターと、ローパスフィ
ルタにより抽出された圧力変動信号により定量のフィー
ダの材料供給量を制御する第1の制御装置と、ハイパス
フィルターにより抽出された圧力変動信号により押出機
のスクリュ回転速度を制御する第2の制御装置とを有す
ることを特徴とする、複合形押出成形装置の制御装置。3. A composite extrusion molding machine comprising: a fixed-quantity feeder for supplying a raw material to an extruder under quantitative control; an extruder for supplying the raw material from the fixed-quantity feeder; and a gear pump connected to the extrusion side of the extruder. In the control device of the apparatus, a pressure detector for detecting the pressure on the inlet side of the gear pump, a low-pass filter for extracting a long-period component of the fluctuation signal of the pressure detected by the pressure detector, A high-pass filter for extracting a periodic component, a first controller for controlling a fixed amount of material supplied to a feeder based on a pressure fluctuation signal extracted by a low-pass filter, and a screw rotation of an extruder based on a pressure fluctuation signal extracted by the high-pass filter. A control device for controlling the speed, the control device for a composite extrusion molding device.
フィーダと、定量フィーダから原料を供給される押出機
と、その押出機の押出側に連結されたギヤポンプとを有
する複合形押出成形装置の制御装置において、上記ギヤ
ポンプの入口側の圧力を検出する第1の圧力検出器と、
ギヤポンプの出口側の圧力を検出する第2の圧力検出器
と、両圧力検出器で検出された圧力の差圧の変動信号の
長周期成分を取り出すローパスフィルタと、上記差圧の
変動信号の短周期成分を取り出すハイパスフィルタと、
ローパスフィルタにより抽出された圧力変動信号により
定量フィーダの材料供給量を制御する第1の制御装置
と、ハイパスフィルタにより抽出された圧力変動信号に
より押出機のスクリュ回転速度を制御する第2の制御装
置とを有することを特徴とする、複合形押出成形装置の
制御装置。4. A composite extrusion molding machine comprising: a fixed-quantity feeder for supplying a raw material to an extruder under quantitative control; an extruder for supplying the raw material from the fixed-quantity feeder; and a gear pump connected to the extrusion side of the extruder. A first pressure detector for detecting a pressure on the inlet side of the gear pump;
A second pressure detector for detecting the pressure on the outlet side of the gear pump; a low-pass filter for extracting a long-period component of a fluctuation signal of the differential pressure of the pressures detected by the two pressure detectors; A high-pass filter that extracts the periodic component,
A first control device for controlling the material supply amount of the fixed-quantity feeder based on the pressure fluctuation signal extracted by the low-pass filter, and a second control device for controlling the screw rotation speed of the extruder based on the pressure fluctuation signal extracted by the high-pass filter. A control device for a composite extrusion molding device, comprising:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9140440A JPH10329200A (en) | 1997-05-29 | 1997-05-29 | Method and apparatus for controlling composite extrusion molding machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9140440A JPH10329200A (en) | 1997-05-29 | 1997-05-29 | Method and apparatus for controlling composite extrusion molding machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10329200A true JPH10329200A (en) | 1998-12-15 |
Family
ID=15268701
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9140440A Pending JPH10329200A (en) | 1997-05-29 | 1997-05-29 | Method and apparatus for controlling composite extrusion molding machine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10329200A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101136017B1 (en) * | 2008-10-16 | 2012-04-18 | 파우엠이-아체트 엑스트루지온 게엠베하 | Extrusion conveying device |
| EP2636504A1 (en) * | 2012-03-05 | 2013-09-11 | Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) | Kneading/extruding equipment and operation control method thereof |
| CN106762617A (en) * | 2017-03-31 | 2017-05-31 | 四川凯创机电设备有限公司 | Screw pump flow feedback governing system |
| JP2022048765A (en) * | 2020-09-15 | 2022-03-28 | 住友化学株式会社 | Method for producing acrylic resin film and apparatus for producing acrylic resin film |
-
1997
- 1997-05-29 JP JP9140440A patent/JPH10329200A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101136017B1 (en) * | 2008-10-16 | 2012-04-18 | 파우엠이-아체트 엑스트루지온 게엠베하 | Extrusion conveying device |
| EP2636504A1 (en) * | 2012-03-05 | 2013-09-11 | Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) | Kneading/extruding equipment and operation control method thereof |
| US9333674B2 (en) | 2012-03-05 | 2016-05-10 | Kobe Steel, Ltd. | Kneading/extruding equipment with feedforward control of latter stage pump |
| CN106762617A (en) * | 2017-03-31 | 2017-05-31 | 四川凯创机电设备有限公司 | Screw pump flow feedback governing system |
| JP2022048765A (en) * | 2020-09-15 | 2022-03-28 | 住友化学株式会社 | Method for producing acrylic resin film and apparatus for producing acrylic resin film |
| JP2025020462A (en) * | 2020-09-15 | 2025-02-12 | 住友化学株式会社 | Acrylic resin film manufacturing method and acrylic resin film manufacturing device |
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