JPH0550425A - Apparatus for controlling degree of kneading in continuous kneading machine - Google Patents
Apparatus for controlling degree of kneading in continuous kneading machineInfo
- Publication number
- JPH0550425A JPH0550425A JP3217414A JP21741491A JPH0550425A JP H0550425 A JPH0550425 A JP H0550425A JP 3217414 A JP3217414 A JP 3217414A JP 21741491 A JP21741491 A JP 21741491A JP H0550425 A JPH0550425 A JP H0550425A
- Authority
- JP
- Japan
- Prior art keywords
- kneading
- pressure
- rotor
- blade
- blade portion
- 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.)
- Granted
Links
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
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/465—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft each shaft comprising rotor parts of the Banbury type in addition to screw parts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/48—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
- B29B7/488—Parts, e.g. casings, sealings; Accessories, e.g. flow controlling or throttling devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7476—Systems, i.e. flow charts or diagrams; Plants
- B29B7/7495—Systems, i.e. flow charts or diagrams; Plants for mixing rubber
-
- 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
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/375—Plasticisers, homogenisers or feeders comprising two or more stages
- B29C48/39—Plasticisers, homogenisers or feeders comprising two or more stages a first extruder feeding the melt into an intermediate location of a second extruder
-
- 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
- B29C48/40—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/41—Intermeshing counter-rotating screws
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、プラスチック、ゴム等
の可塑性材料を、連続的に可塑化溶融して、添加剤、充
填材等を練り込む連続混練機の混練度制御装置に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a kneading degree control device for a continuous kneading machine in which a plastic material such as plastic or rubber is continuously plasticized and melted to knead additives, fillers and the like.
【0002】[0002]
【従来の技術】この種の従来技術としては、特開平2ー
263609号公報に開示されたものがある。この技術
は図5に示すように、供給口16及び排出口17を有す
るチャンバ6と、混練翼部3を有してチャンバ6内に平
行に配置されていて可変モータ10によって駆動される
2本のロータ5と、チャンバ6の供給口16と排出口1
7との間でロータ5に対して遠近位置調整自在に設けら
れた可動ダム8と、排出口17の下流側に配置されたギ
ヤポンプ18とを備えている。2. Description of the Related Art A conventional technique of this type is disclosed in Japanese Patent Laid-Open No. 2-263609. As shown in FIG. 5, this technique includes a chamber 6 having a supply port 16 and a discharge port 17 and two chambers having a kneading blade part 3 arranged in parallel in the chamber 6 and driven by a variable motor 10. Rotor 5, supply port 16 and discharge port 1 of chamber 6
7, a movable dam 8 provided so as to be able to adjust the far and near position with respect to the rotor 5, and a gear pump 18 arranged downstream of the discharge port 17.
【0003】前記可動ダム8はロータ5の混練翼部3の
下流側に形成した断面円形部19に対向していて、ロー
タ5との間に間隙7を形成しており、駆動装置(モー
タ)11を駆動することにより間隙7を調整可能にして
いる。ロータ5には断面円形部19の下流側に送り翼部
4が形成されていて、ギヤポンプ18へ混練材料を強制
押動可能になっている。The movable dam 8 faces a circular section 19 formed on the downstream side of the kneading blade portion 3 of the rotor 5 and forms a gap 7 between the movable dam 8 and the rotor 5, thus forming a drive unit (motor). The gap 7 can be adjusted by driving 11. The rotor 5 is provided with the feed blade portion 4 on the downstream side of the circular section 19 so that the kneaded material can be forcibly pushed to the gear pump 18.
【0004】前記可動ダム8には間隙7を通過する樹脂
の圧力と温度とを測定する圧力センサ20と温度センサ
21とを有し、これらから得られた測定値をもとにして
駆動装置11を制御するように構成されている。また、
ギヤポンプ18の入口には圧力センサ22が設けられて
いて、入口圧力を測定してギヤポンプ18のモータ23
を制御し、後処理装置への混練材料の供給量を調整する
ように構成されている。The movable dam 8 has a pressure sensor 20 and a temperature sensor 21 for measuring the pressure and temperature of the resin passing through the gap 7, and the drive unit 11 is based on the measured values obtained from these. Is configured to control. Also,
A pressure sensor 22 is provided at the inlet of the gear pump 18, measures the inlet pressure, and measures the motor 23 of the gear pump 18.
Is controlled to adjust the supply amount of the kneading material to the post-treatment device.
【0005】[0005]
【発明が解決しようとする課題】前記従来技術において
は、混練度制御は可動ダム8とギヤポンプ18入口とで
樹脂圧力又は温度を測定して行うようになっているが、
これらの部分は実質的な混練が終了した部分であり、マ
クロ的な混練度の制御には役立つが、ミクロ的な混練品
質の制御には効果が期待し難い。In the above prior art, the kneading degree control is performed by measuring the resin pressure or temperature at the movable dam 8 and the inlet of the gear pump 18.
These parts are the parts where the substantial kneading is completed, and they are useful for macroscopic kneading degree control, but it is difficult to expect an effect for microscopic kneading quality control.
【0006】即ち、添加剤の分散性、樹脂のホモジナイ
ジング等の混練品質は、樹脂に最も大きい剪断力が加わ
る溶融開始点で決定されるものであり、この溶融開始点
から離れた下流側で圧力等を測定して混練度を制御して
も、要求品質を得るための圧力は得難く且つ時間的ずれ
もあって、より厳格な制御は困難である。ところで、フ
ィッシユ・アイを消去するためのホモジナイジングは、
分子のからまりをほぐすためにからまり力以上の最大剪
断応力が必要であり、添加剤の凝集塊を分散させる場合
には、その凝集力以上の最大剪断応力が必要であり、そ
のような最大剪断応力が作用するのは溶融開始点付近で
あり、前記従来技術のような連続混練機では、通常、折
り返し点Cの前後、より詳しくは送り翼Aの3分の1か
ら戻し翼Bの3分の1までの範囲である。That is, the kneading quality such as the dispersibility of the additive and the homogenizing of the resin is determined by the melting start point where the largest shearing force is applied to the resin, and the downstream side away from the melting start point. Even if the kneading degree is controlled by measuring the pressure and the like with, it is difficult to obtain the pressure for obtaining the required quality and there is a time lag, so that more strict control is difficult. By the way, the homogenizing method to erase the fish eye is
The maximum shear stress above the entanglement force is required to loosen the entanglement of the molecules, and when dispersing the aggregates of additives, the maximum shear stress above the cohesive force is required. The shear stress acts near the melting start point, and in the continuous kneader such as the above-mentioned conventional technique, it is usually before and after the turning point C, more specifically, one-third of the feeding blade A to three of the returning blade B. The range is up to one-third.
【0007】そして、この最大剪断応力τmaxは樹脂
の粘度、添加剤の種類等によって値が異なり、最大剪断
応力τmaxを得るための最大樹脂圧力Pmax/ma
x(円周方向の最大圧力Pmaxの内の軸方向最大圧
力)から算出することができる。即ち、Pmax/ma
x=C(定数)・τmaxの関係がある。従って、要求
品質を満足するための必要な最大剪断応力τmaxは、
溶融開始点付近で最大樹脂圧力Pmax/maxが必要
値になるように、可動ダム8等を制御することにより得
られる。The maximum shear stress τmax varies depending on the viscosity of the resin, the type of additives, etc., and the maximum resin pressure Pmax / ma for obtaining the maximum shear stress τmax.
It can be calculated from x (maximum axial pressure within the maximum pressure Pmax in the circumferential direction). That is, Pmax / ma
There is a relationship of x = C (constant) · τmax. Therefore, the maximum shear stress τmax required to satisfy the required quality is
It can be obtained by controlling the movable dam 8 so that the maximum resin pressure Pmax / max becomes a required value near the melting start point.
【0008】また、混練品質は一時点の最大剪断応力τ
maxが決定的要因であるが、最大剪断応力τmaxの
総計によっても影響される場合があり、この最大剪断応
力τmaxの総計が必要値になるように制御するのも有
効である。本発明の第1の目的は、混練翼部3の送り翼
Aと戻し翼Bとの折り返し点C付近の最大樹脂圧力Pm
ax/maxを圧力センサ9で測定して、ロータ5の可
変モータ10と可動ダム8の駆動装置11との少なくと
もどちらか一方を制御することにより、混練品質のより
厳格且つ迅速な制御ができるようにした連続混練機の混
練度制御装置を提供することにある。The kneading quality depends on the maximum shear stress τ at one point.
Although max is a decisive factor, it may be influenced by the total maximum shear stress τmax, and it is also effective to control the total maximum shear stress τmax to a required value. The first object of the present invention is to provide a maximum resin pressure Pm in the vicinity of a turning point C between the feeding blade A and the returning blade B of the kneading blade portion 3.
By measuring ax / max with the pressure sensor 9 and controlling at least one of the variable motor 10 of the rotor 5 and the drive device 11 of the movable dam 8, more precise and quick control of the kneading quality can be achieved. Another object of the present invention is to provide a kneading degree control device for the continuous kneading machine.
【0009】本発明の第2の目的は、混練翼部3の送り
翼Aと戻し翼Bとの折り返し点Cを含むその前後一定範
囲D、E内の最大圧力Pmaxを複数の圧力センサ9で
測定して、この複数の圧力測定値の総計を演算部14で
演算して、ロータ5の可変モータ10と可動ダム8の駆
動装置11との少なくともどちらか一方を制御すること
により、混練品質のより厳格且つ迅速な制御ができるよ
うにした連続混練機の混練度制御装置を提供することに
ある。A second object of the present invention is to use a plurality of pressure sensors 9 to determine the maximum pressure Pmax within a certain range D and E before and after the turning point C between the feeding blade A and the returning blade B of the kneading blade portion 3. The kneading quality is measured by measuring and totaling the plurality of pressure measurement values by the calculation unit 14 to control at least one of the variable motor 10 of the rotor 5 and the drive device 11 of the movable dam 8. An object of the present invention is to provide a kneading degree control device for a continuous kneading machine, which enables more rigorous and quick control.
【0010】[0010]
【課題を解決するための手段】本発明における課題解決
のための第1の具体的手段は、混練翼部3と送り翼部4
とを有する2本のロータ5をチャンバ6内に配置し、こ
のチャンバ6に混練翼部3と送り翼部4との間でロータ
5との間隙7を調整する可動ダム8を設け、樹脂圧力を
圧力センサ9で測定してロータ5の可変モータ10と可
動ダム8の駆動装置11との少なくともどちらか一方を
制御する制御機構12を設けた連続混練機の混練度制御
装置において、前記制御機構12の圧力センサ9を、混
練翼部3の送り翼Aと戻し翼Bとの折り返し点C付近に
設けていることである。The first concrete means for solving the problems in the present invention is the kneading blade portion 3 and the feeding blade portion 4.
Two rotors 5 each having a rotor are arranged in a chamber 6, and a movable dam 8 for adjusting a gap 7 between the kneading blade portion 3 and the feeding blade portion 4 with the rotor 5 is provided in the chamber 6, and a resin pressure is applied. In the kneading degree control device of the continuous kneading machine, which is provided with a control mechanism 12 for controlling at least one of the variable motor 10 of the rotor 5 and the drive device 11 of the movable dam 8 by measuring the pressure sensor 9 The pressure sensor 9 of 12 is provided in the vicinity of the turning point C between the feeding blade A and the returning blade B of the kneading blade portion 3.
【0011】本発明における課題解決のための第2の具
体的手段は、混練翼部3と送り翼部4とを有する2本の
ロータ5をチャンバ6内に配置し、このチャンバ6に混
練翼部3と送り翼部4との間でロータ5との間隙7を調
整する可動ダム8を設け、樹脂圧力を圧力センサ9で測
定してロータ5の可変モータ10と可動ダム8の駆動装
置11との少なくともどちらか一方を制御する制御機構
12を設けた連続混練機の混練度制御装置において、前
記制御機構12は圧力センサ9を混練翼部3の送り翼A
と戻し翼Bとの折り返し点Cを含むその前後一定範囲
D、E内に軸方向複数設けると共に、複数の圧力センサ
9からの圧力測定値の総計を演算する演算部14を設け
ていることである。A second specific means for solving the problem in the present invention is to arrange two rotors 5 having a kneading blade portion 3 and a feeding blade portion 4 in a chamber 6, and to the chamber 6, kneading blades. A movable dam 8 for adjusting a gap 7 with the rotor 5 is provided between the portion 3 and the feed blade portion 4, and a variable motor 10 of the rotor 5 and a drive device 11 for the movable dam 8 are provided by measuring a resin pressure with a pressure sensor 9. In the kneading degree control device of the continuous kneading machine, which is provided with a control mechanism 12 for controlling at least one of the above, the control mechanism 12 controls the pressure sensor 9 to feed the blade A of the kneading blade part 3.
By providing a plurality of axial directions within a certain range D and E before and after the turning point C between the return vane B and the return vane B, and providing a computing unit 14 for computing the total of the pressure measurement values from the plurality of pressure sensors 9. is there.
【0012】[0012]
【作用】プラスチック、ゴム等の可塑性材料を添加剤、
充填材等と共に供給口16から供給すると、可変モータ
10によるロータ5の回転により、スクリュウ部24か
ら混練翼部3へ送られ、混練、剪断作用を受けて可塑化
溶融される。可塑化溶融された樹脂材料は、混練翼部3
の下流側の断面円形部19と可動ダム8との間の間隙7
を通過して、送り翼部4によって排出口17へ強力に押
し出され、ギヤポンプによって所要圧力で後処理装置へ
排出される。[Function] Addition of plastic materials such as plastic and rubber,
When supplied from the supply port 16 together with the filler and the like, the rotor 5 is rotated by the variable motor 10 to be sent from the screw portion 24 to the kneading blade portion 3 and subjected to kneading and shearing action to be plasticized and melted. The plasticized and melted resin material is mixed with the kneading blade portion 3.
7 between the circular section 19 and the movable dam 8 on the downstream side of the
Is strongly pushed out to the discharge port 17 by the feed blade portion 4, and is discharged to the post-processing device at a required pressure by the gear pump.
【0013】前記樹脂材料は混練翼部3に入るとロータ
5とチャンバ6から剪断力を受ける。この剪断力は送り
翼Aの先端から次第に大きくなり、折り返し点Cで最大
となり、戻し翼Bの後端にいくに従って減少する。制御
機構12は折り返し点C付近に設けた圧力センサ9で最
大樹脂圧力Pmax/maxを測定し、樹脂材料の必要
品質を得るに要求される最大剪断応力τmaxが発生し
ているかを演算部13で比較演算して、発生していない
場合には、ロータ5の可変モータ10を制御してロータ
5回転数を変更し、及び/又は、可動ダム8の駆動装置
11を駆動して間隙7の大きさを調整し、必要な最大剪
断応力τmaxを発生する最大樹脂圧力Pmax/ma
x以上に変更する。When the resin material enters the kneading blade portion 3, it receives a shearing force from the rotor 5 and the chamber 6. This shearing force gradually increases from the tip of the feed blade A, reaches its maximum at the turning point C, and decreases toward the rear end of the return blade B. The control mechanism 12 measures the maximum resin pressure Pmax / max with the pressure sensor 9 provided in the vicinity of the turning point C, and the arithmetic unit 13 determines whether the maximum shear stress τmax required to obtain the required quality of the resin material is generated. If a comparison calculation is performed and no occurrence occurs, the variable motor 10 of the rotor 5 is controlled to change the rotation speed of the rotor 5, and / or the drive device 11 of the movable dam 8 is driven to increase the size of the gap 7. The maximum resin pressure Pmax / ma that adjusts the height to generate the required maximum shear stress τmax.
Change to x or higher.
【0014】また、前記制御機構12は折り返し点Cを
含むその前後一定範囲D、E内に設けた軸方向複数の圧
力センサ9で、その範囲D、E内の複数個所の最大圧力
Pmaxを測定し、それらの測定値を積分して圧力の総
計(面積)を演算部14で演算し、且つその圧力の総計
が樹脂材料の必要品質を得るに要求される大きさになっ
ているかを比較演算して、なっていない場合には、ロー
タ5の可変モータ10を制御してロータ5回転数を変更
し、及び/又は、可動ダム8の駆動装置11を駆動して
間隙7の大きさを調整し、圧力の総計が必要量以上の剪
断力を発生するように変更する。Further, the control mechanism 12 measures a maximum pressure Pmax at a plurality of positions within the ranges D and E by a plurality of axial pressure sensors 9 provided within a predetermined range D and E before and after the turning point C. Then, the measured values are integrated to calculate the total pressure (area) by the calculation unit 14, and the total pressure is compared and calculated to determine whether the total pressure is large enough to obtain the required quality of the resin material. If not, the variable motor 10 of the rotor 5 is controlled to change the rotational speed of the rotor 5, and / or the drive device 11 of the movable dam 8 is driven to adjust the size of the gap 7. Then, change the total pressure so as to generate more shear force than necessary.
【0015】[0015]
【実施例】以下、本発明の実施例を図面に基づいて説明
する。図1、2において、1は従来技術と同様な構成の
連続混練機で、混練翼部3と送り翼部4とを有する2本
のロータ5をチャンバ6内に配置し、このチャンバ6に
混練翼部3と送り翼部4との間でロータ5との間隙7を
調整する可動ダム8を設け、樹脂圧力を圧力センサ9で
測定してロータ5の可変モータ10と可動ダム8の駆動
装置11との少なくともどちらか一方を制御する制御機
構12を設けている。Embodiments of the present invention will be described below with reference to the drawings. In FIGS. 1 and 2, reference numeral 1 denotes a continuous kneader having the same structure as that of the prior art. A movable dam 8 that adjusts a gap 7 with the rotor 5 is provided between the wing portion 3 and the feed wing portion 4, and a variable motor 10 of the rotor 5 and a drive device of the movable dam 8 are measured by measuring a resin pressure with a pressure sensor 9. A control mechanism 12 for controlling at least one of 11 and 11 is provided.
【0016】前記混練翼部3はチップが軸方向中央で曲
がり方向が反対になっていて、混練翼部3の先端から中
央までが送り翼A、中央から後端までが戻し翼Bとなっ
ており、樹脂材料に剪断力を与えるための圧力を発生す
る。樹脂材料に与える最大圧力Pmaxの発生は、混練
翼部3のチップ数によって異なり、6チップの場合は図
3のようになり、4チップの場合は図4のようになり、
それぞれ最大圧力Pmaxが測定できる位置に圧力セン
サ9を配置する。The tip of the kneading blade portion 3 is bent at the center in the axial direction and the bending directions are opposite to each other. The tip of the kneading blade portion 3 is a feeding blade A from the center to the rear end thereof is a returning blade B. And generate a pressure for applying a shearing force to the resin material. The generation of the maximum pressure Pmax applied to the resin material depends on the number of chips of the kneading blade portion 3, and is 6 in the case of 6 chips and 4 in the case of 4 chips,
The pressure sensor 9 is arranged at a position where the maximum pressure Pmax can be measured.
【0017】ロータ5の軸方向における最大圧力Pma
xの分布は、中央の折り返し点Cで略最大となる。そこ
で、この折り返し点Cでの最大圧力Pmaxを圧力セン
サ9で測定すれば、連続混練機1内での最大圧力である
最大樹脂圧力Pmax/maxが測定できる。この折り
返し点Cの前後一定範囲D、Eは、混練品質に重大な影
響を与える剪断力が発生する範囲であり、範囲Dは送り
翼Aの約3分の1(先端から)の位置から折り返し点C
まで、範囲Eは折り返し点Cから戻し翼Bの約3分の1
(先端から)の位置までである。Maximum pressure Pma in the axial direction of the rotor 5
The distribution of x becomes approximately maximum at the turning point C in the center. Therefore, if the maximum pressure Pmax at the turning point C is measured by the pressure sensor 9, the maximum resin pressure Pmax / max, which is the maximum pressure in the continuous kneading machine 1, can be measured. The constant ranges D and E before and after the turning point C are ranges in which shearing force that seriously affects the kneading quality is generated, and the range D is folded from a position of about 1/3 (from the tip) of the feed blade A. Point C
Range E is about 1/3 of the return wing B from the turning point C
Up to the position (from the tip).
【0018】前記制御機構12は、混練翼部3の送り翼
Aと戻し翼Bとの折り返し点Cとその前後一定範囲D、
E内に複数(4個)の圧力センサ9a,9b,9c,9
dを設けている。これらの圧力センサ9a,9b,9
c,9dは並列に配置され、演算部13、14に接続さ
れ、両演算部13、14は図外の駆動部を介して可変モ
ータ10と駆動装置11とに接続されている。The control mechanism 12 has a turning point C between the feeding blade A and the returning blade B of the kneading blade portion 3 and a certain range D before and after the turning point.
Plural (four) pressure sensors 9a, 9b, 9c, 9 in E
d is provided. These pressure sensors 9a, 9b, 9
c and 9d are arranged in parallel and connected to the arithmetic units 13 and 14, and both arithmetic units 13 and 14 are connected to the variable motor 10 and the drive device 11 via a drive unit (not shown).
【0019】図2において、演算部13はPmax/m
ax検出部、Pmax/max設定部及び比較演算部等
を有し、圧力センサ9a,9b,9c,9dが測定した
最大圧力Pmaxの中から軸方向の最大圧力を選別し、
その最大樹脂圧力Pmax/maxを設定値と比較し
て、高低を演算し、低ければ可変モータ10、駆動装置
11等に修正指令信号を発する。In FIG. 2, the calculation unit 13 has Pmax / m.
It has an ax detection unit, a Pmax / max setting unit, a comparison calculation unit, and the like, and selects the maximum pressure in the axial direction from the maximum pressures Pmax measured by the pressure sensors 9a, 9b, 9c, 9d,
The maximum resin pressure Pmax / max is compared with a set value to calculate the height, and if it is low, a correction command signal is issued to the variable motor 10, the drive device 11 and the like.
【0020】但し、最大樹脂圧力Pmax/maxは略
折り返し点Cで発生するので、この折り返し点Cに圧力
センサ9aを設けておけば、Pmax/max検出部は
不要であり、単一位置の最大圧力を測定するだけで制御
ができる。演算部14はPmax積分部、Pmax積分
値設定部及び比較演算部等を有し、圧力センサ9a,9
b,9c,9dが測定した最大圧力Pmaxの総てを積
分して圧力総計(面積)を算し、その圧力総計を設定値
と比較して、高低を演算し、低ければ可変モータ10、
駆動装置11等に修正指令信号を発する。However, since the maximum resin pressure Pmax / max is generated substantially at the turning point C, if the pressure sensor 9a is provided at the turning point C, the Pmax / max detecting section is not required, and the maximum value of a single position can be obtained. It can be controlled simply by measuring the pressure. The calculation unit 14 includes a Pmax integration unit, a Pmax integration value setting unit, a comparison calculation unit, and the like, and the pressure sensors 9a and 9a.
b, 9c, 9d integrates all the maximum pressures Pmax measured to calculate the total pressure (area), and compares the total pressure with a set value to calculate the high and low, and if it is low, the variable motor 10,
A correction command signal is issued to the drive device 11 and the like.
【0021】前記演算部13、14はどちらか一方でも
又は両方同時に使用しても良く、また、可変モータ10
及び駆動装置11もどちらか一方でも又は両方同時に制
御するようにしても良い。尚、供給口16へ材料を供給
するためのフィーダのモータを制御する方法もあるが、
処理量が変化するため、下流設備(例えば造粒装置)に
悪影響がでるので望ましくない。Either one of the arithmetic units 13 or 14 may be used, or both of them may be used at the same time.
The drive device 11 may be controlled either or both simultaneously. Although there is a method of controlling the motor of the feeder for supplying the material to the supply port 16,
Since the throughput varies, downstream equipment (for example, a granulator) is adversely affected, which is not desirable.
【0022】[0022]
【発明の効果】以上詳述した本発明によれば、制御機構
12の圧力センサ9を、混練翼部3の送り翼Aと戻し翼
Bとの折り返し点C付近に設けているので、樹脂材料の
略溶融開始点の圧力を測定することができ、そしてこの
圧力をロータ5の可変モータ10と可動ダム8の駆動装
置11との少なくともどちらか一方で制御するので、混
練品質のより厳格且つ迅速な制御ができようになる。According to the present invention described in detail above, since the pressure sensor 9 of the control mechanism 12 is provided in the vicinity of the turning point C between the feeding blade A and the returning blade B of the kneading blade portion 3, the resin material is used. Since the pressure at the melting start point can be measured, and this pressure is controlled by at least one of the variable motor 10 of the rotor 5 and the drive device 11 of the movable dam 8, the kneading quality can be stricter and quicker. Can be controlled.
【0023】また、本発明によれば、制御機構12は圧
力センサ9を、混練翼部3の送り翼Aと戻し翼Bとの折
り返し点Cを含むその前後一定範囲D、E内に軸方向複
数設けると共に、複数の圧力測定値の総計を演算する演
算部14を設けているので、樹脂材料の略溶融開始点を
含むその近傍の圧力を複数個所で測定することができ、
そしてこの複数の圧力測定値の総計をロータ5の可変モ
ータ10と可動ダム8の駆動装置11との少なくともど
ちらか一方で制御するので、混練品質のより厳格且つ迅
速な制御ができるようになる。Further, according to the present invention, the control mechanism 12 causes the pressure sensor 9 to axially fall within a certain range D and E before and after the turning point C between the feeding blade A and the returning blade B of the kneading blade portion 3. Along with providing a plurality, the arithmetic unit 14 for calculating the total of the plurality of pressure measurement values is provided, so that the pressure in the vicinity thereof including the substantially melting start point of the resin material can be measured at a plurality of points,
Further, since the total of the plurality of pressure measurement values is controlled by at least one of the variable motor 10 of the rotor 5 and the drive device 11 of the movable dam 8, it becomes possible to control the kneading quality more strictly and quickly.
【0024】尚、本発明は特に、ブロックコポリマーの
ポリプロピレンのゴム分散性や、高密度ポリエチレンの
フィッシュアイ消去性等を向上するのに有用である。The present invention is particularly useful for improving the rubber dispersibility of polypropylene, which is a block copolymer, and the fish-eye erasing property of high-density polyethylene.
【図1】本発明の実施例を示す説明図である。FIG. 1 is an explanatory diagram showing an embodiment of the present invention.
【図2】同制御機構のブロック線図である。FIG. 2 is a block diagram of the control mechanism.
【図3】6チップロータの最大圧力発生状況を示す説明
図である。FIG. 3 is an explanatory diagram showing a maximum pressure generation state of a 6-chip rotor.
【図4】4チップロータの最大圧力発生状況を示す説明
図である。FIG. 4 is an explanatory diagram showing a maximum pressure generation state of a 4-chip rotor.
【図5】従来技術の連続混練機の混練度制御装置の全体
を示す説明図である。FIG. 5 is an explanatory view showing an entire kneading degree control device of a conventional kneading machine.
1 連続混練機 2 混練度制御装置 3 混練翼部 4 送り翼部 5 ロータ 6 チャンバ 7 間隙 8 可動ダム 9 圧力センサ 10 可変モータ 11 駆動装置 12 制御機構 13 演算部 14 演算部 A 送り翼 B 戻し翼 C 折り返し点 D 範囲 E 範囲 1 continuous kneading machine 2 kneading degree control device 3 kneading blade part 4 feeding blade part 5 rotor 6 chamber 7 gap 8 movable dam 9 pressure sensor 10 variable motor 11 drive device 12 control mechanism 13 computing unit 14 computing unit A feeding blade B return blade C Folding point D range E range
Claims (2)
のロータ5をチャンバ6内に配置し、このチャンバ6に
混練翼部3と送り翼部4との間でロータ5との間隙7を
調整する可動ダム8を設け、樹脂圧力を圧力センサ9で
測定してロータ5の可変モータ10と可動ダム8の駆動
装置11との少なくともどちらか一方を制御する制御機
構12を設けた連続混練機の混練度制御装置において、 前記制御機構12の圧力センサ9を、混練翼部3の送り
翼Aと戻し翼Bとの折り返し点C付近に設けていること
を特徴とする連続混練機の混練度制御装置。1. Two rotors 5 having a kneading blade portion 3 and a feeding blade portion 4 are arranged in a chamber 6, and a rotor 5 and a rotor 5 are provided in the chamber 6 between the kneading blade portion 3 and the feeding blade portion 4. Is provided with a movable dam 8 for adjusting the gap 7, and a control mechanism 12 is provided for measuring at least one of the variable motor 10 of the rotor 5 and the drive device 11 of the movable dam 8 by measuring the resin pressure with the pressure sensor 9. In the kneading degree control device of the continuous kneading machine, the pressure sensor 9 of the control mechanism 12 is provided in the vicinity of the turning point C between the feeding blade A and the returning blade B of the kneading blade part 3. Machine kneading degree control device.
のロータ5をチャンバ6内に配置し、このチャンバ6に
混練翼部3と送り翼部4との間でロータ5との間隙7を
調整する可動ダム8を設け、樹脂圧力を圧力センサ9で
測定してロータ5の可変モータ10と可動ダム8の駆動
装置11との少なくともどちらか一方を制御する制御機
構12を設けた連続混練機の混練度制御装置において、 前記制御機構12は圧力センサ9を混練翼部3の送り翼
Aと戻し翼Bとの折り返し点Cを含むその前後一定範囲
D、E内に軸方向複数設けると共に、複数の圧力センサ
9からの圧力測定値の総計を演算する演算部14を設け
ていることを特徴とする連続混練機の混練度制御装置。2. Two rotors 5 having a kneading blade portion 3 and a feeding blade portion 4 are arranged in a chamber 6, and a rotor 5 and a rotor 5 are provided in the chamber 6 between the kneading blade portion 3 and the feeding blade portion 4. Is provided with a movable dam 8 for adjusting the gap 7, and a control mechanism 12 is provided for measuring at least one of the variable motor 10 of the rotor 5 and the drive device 11 of the movable dam 8 by measuring the resin pressure with the pressure sensor 9. In the kneading degree control device of the continuous kneading machine, the control mechanism 12 causes the pressure sensor 9 to axially fall within a certain range D and E before and after the turning point C between the feeding blade A and the returning blade B of the kneading blade portion 3. A kneading degree control device for a continuous kneading machine, wherein a plurality of the kneading degree control devices are provided and a calculation unit 14 that calculates the total of the pressure measurement values from the plurality of pressure sensors 9 is provided.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3217414A JP2813256B2 (en) | 1991-08-28 | 1991-08-28 | Kneading degree control device for continuous kneading machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3217414A JP2813256B2 (en) | 1991-08-28 | 1991-08-28 | Kneading degree control device for continuous kneading machine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0550425A true JPH0550425A (en) | 1993-03-02 |
JP2813256B2 JP2813256B2 (en) | 1998-10-22 |
Family
ID=16703833
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3217414A Expired - Fee Related JP2813256B2 (en) | 1991-08-28 | 1991-08-28 | Kneading degree control device for continuous kneading machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2813256B2 (en) |
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