JP2601645B2 - Kneading control device for continuous kneading machine - Google Patents

Kneading control device for continuous kneading machine

Info

Publication number
JP2601645B2
JP2601645B2 JP7139607A JP13960795A JP2601645B2 JP 2601645 B2 JP2601645 B2 JP 2601645B2 JP 7139607 A JP7139607 A JP 7139607A JP 13960795 A JP13960795 A JP 13960795A JP 2601645 B2 JP2601645 B2 JP 2601645B2
Authority
JP
Japan
Prior art keywords
kneading
gear pump
rotor
discharge port
chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP7139607A
Other languages
Japanese (ja)
Other versions
JPH0899313A (en
Inventor
二志 福井
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP7139607A priority Critical patent/JP2601645B2/en
Publication of JPH0899313A publication Critical patent/JPH0899313A/en
Application granted granted Critical
Publication of JP2601645B2 publication Critical patent/JP2601645B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/72Measuring, controlling or regulating
    • B29B7/728Measuring data of the driving system, e.g. torque, speed, power, vibration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/465Mixing; 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/48Mixing; 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
    • B29B7/482Mixing; 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 provided with screw parts in addition to other mixing parts, e.g. paddles, gears, discs
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/48Mixing; 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
    • B29B7/488Parts, e.g. casings, sealings; Accessories, e.g. flow controlling or throttling devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/48Mixing; 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
    • B29B7/488Parts, e.g. casings, sealings; Accessories, e.g. flow controlling or throttling devices
    • B29B7/489Screws
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/582Component parts, details or accessories; Auxiliary operations for discharging, e.g. doors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/72Measuring, controlling or regulating
    • B29B7/726Measuring properties of mixture, e.g. temperature or density
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7495Systems, i.e. flow charts or diagrams; Plants for mixing rubber
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/60Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92333Raw material handling or dosing, e.g. active hopper or feeding device
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92361Extrusion unit
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92514Pressure
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/9258Velocity
    • B29C2948/926Flow or feed rate
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • 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
    • B29C48/255Flow control means, e.g. valves
    • B29C48/2552Flow control means, e.g. valves provided in the feeding, melting, plasticising or pumping zone, e.g. screw, barrel, gear-pump or ram
    • 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
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/387Plasticisers, homogenisers or feeders comprising two or more stages using a screw extruder and a gear pump
    • 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
    • B29C48/395Means 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
    • B29C48/40Means 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
    • B29C48/402Means 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 the screws having intermeshing parts
    • 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

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、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制御装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a kneading control device for a continuous kneader for continuously plasticizing and melting plastic materials such as plastics and rubber and kneading additives and fillers.

【0002】[0002]

【従来の技術】例えばプラスチックの連続混練機は、供
給口及び排出口を有するチャンバ内に、混練翼部を有す
る2本のロータを平行に配置し、供給口から供給された
混練材料添加剤及び充填材等を、ロータで混練して可塑
化溶融しながら排出口から排出する。
2. Description of the Related Art In a continuous kneader for plastics, for example, two rotors having kneading blades are arranged in parallel in a chamber having a supply port and a discharge port, and a kneading material additive supplied from a supply port and The filler and the like are kneaded by the rotor and plasticized and melted, and are discharged from the discharge port.

【0003】この混練製品の品質を向上するために、混
練作用中の混練度、圧力又は温度を制御する各種の混練
制御装置が開発されている。この混練制御装置の従来技
術として、まず、特公昭56−3091号公報に開示さ
れたものがある。この第1技術は、チャンバの排出口の
下流側に後処理装置へ混練材料を送給するためのギヤポ
ンプを直結して、このギヤポンプを可変モータで回転速
度を制御し、ギヤポンプの入口の圧力を制御すること
で、チャンバ内の材料の充満度を変化させて、混練度を
調整するようにしている。
In order to improve the quality of the kneaded product, various kneading control devices for controlling the kneading degree, pressure or temperature during the kneading operation have been developed. As a prior art of the kneading control device, there is a device disclosed in Japanese Patent Publication No. 56-3091. In the first technique, a gear pump for feeding the kneading material to a post-processing device is directly connected to a downstream side of a discharge port of a chamber, and the rotational speed of the gear pump is controlled by a variable motor to reduce the pressure at the inlet of the gear pump. By controlling, the kneading degree is adjusted by changing the filling degree of the material in the chamber.

【0004】この第1技術は、高粘度でない樹脂の混練
には利用できるに充分な効果を有するが、高粘度樹脂の
混練には、ロータの押込力が小さいためギヤポンプの歯
への喰い込み効率が悪くなることがあり、圧力のハンチ
ング現象を生じ、樹脂の溶融開始点がふらついて、不安
定運転になることがある。このような第1技術の問題点
を解決すべく改良したものとして、供給口への材料供給
量を調整して混練度を制御する第2技術と、排出口の近
傍に材料の軸方向流れを遮る固定ダムを設けて圧力及び
温度を制御する第3技術(特開昭58−183210号
公報参照)とがある。
The first technique has a sufficient effect that can be used for kneading a resin having a low viscosity. However, the kneading of a high-viscosity resin requires a small pushing force of a rotor, so that the efficiency of biting into teeth of a gear pump is reduced. Of the resin, the hunting phenomenon of the pressure may occur, and the melting start point of the resin may fluctuate, resulting in unstable operation. As an improvement to solve such a problem of the first technique, a second technique of controlling the kneading degree by adjusting a material supply amount to a supply port and an axial flow of the material near the discharge port are disclosed. There is a third technique (see Japanese Patent Application Laid-Open No. 58-183210) in which a pressure and a temperature are controlled by providing a fixed dam for shielding.

【0005】前記第2技術は、混練作用に対する悪影響
は少ないが、効果も少なく、また、制御応答性が悪いと
いう問題を有し、第3技術はある一定の粘度の樹脂には
効果があるが、樹脂の粘度が異なれば対応し難い等の問
題を有している。これら第1〜第3技術の長所を有機的
に結合して問題点を解決したのが、図5に示す第4技術
(特開昭60−107999号明細書及び図面)であ
る。
[0005] The second technique has a problem that the adverse effect on the kneading action is small, but the effect is small and the control response is poor. The third technique is effective for a resin having a certain viscosity. In addition, there is a problem that it is difficult to cope with a difference in the viscosity of the resin. The fourth technique (JP-A-60-107999 and the drawings) shown in FIG. 5 solves the problem by organically combining the advantages of the first to third techniques.

【0006】この第4技術は、チャンバ4の排出口3の
下流側にギヤポンプ7を配置し、供給口2の上方にフィ
ード装置6を配置し、排出口3の近傍に可動ダム8’を
設けて構成し、ギヤポンプ7は入口における圧力をセン
サP1Cで検出して、ギヤポンプ7を安定運転できる範
囲内で可変モータM4を制御し、フィード装置6による
フィード条件を常に一定にし、排出口3の温度センサT
1C、ロータ用モータM2の回転数及びフィード条件等
をダムコントローラ14に入力して、チャンバ4内のシ
ャー面積、充満度等を可動ダム8’で変化させることに
よって、広範囲の粘度の樹脂を、安定且つ効果的に混練
できるようにしている。
According to the fourth technique, a gear pump 7 is disposed downstream of a discharge port 3 of a chamber 4, a feed device 6 is disposed above a supply port 2, and a movable dam 8 'is provided near the discharge port 3. The gear pump 7 detects the pressure at the inlet with the sensor P1C, controls the variable motor M4 within a range in which the gear pump 7 can be operated stably, always keeps the feed condition by the feed device 6 constant, Sensor T
1C, the number of rotations of the motor M2 for the rotor, the feed conditions, and the like are input to the dam controller 14, and the area of the shear in the chamber 4, the degree of filling, and the like are changed by the movable dam 8 '. Kneading is performed stably and effectively.

【0007】一方、混練度調整方法は異なるが、同じく
混練度が調整できて、ギヤポンプによって高能率の混練
ができるようにした技術として、特開昭61−2335
08号(第5技術)に開示されたものがある。この第5
技術は、供給口及び排出口を有して軸方向に移動可能な
シリンダと、混練翼部を有してシリンダ内に平行に配置
された片持ち支持の2本のスクリュと、シリンダの供給
口と排出口との間に配置されていてシリンダとスクリュ
とで形成されるスロットと、シリンダ軸線方向に開口さ
れた排出口の下流側に配置されたギヤポンプとを備え、
前記スロットはスクリュに対してシリンダを軸方向に位
置調整することによりスロット調整加納になっており、
前記スクリュはスロットから排出口の手前まで混練翼部
より小径の先端スクリュが形成されている。
On the other hand, although the kneading degree adjusting method is different, a technique for adjusting the kneading degree and enabling highly efficient kneading with a gear pump is disclosed in Japanese Patent Application Laid-Open No. 61-2335.
No. 08 (fifth technology). This fifth
The technology includes an axially movable cylinder having a supply port and a discharge port, two cantilevered screws having kneading blades and arranged in parallel in the cylinder, and a cylinder supply port. And a slot formed between the cylinder and the screw and disposed between the discharge port, and a gear pump disposed downstream of the discharge port opened in the cylinder axis direction,
The slot is slot adjusted by adjusting the position of the cylinder in the axial direction with respect to the screw,
The screw is formed with a tip screw having a smaller diameter than the kneading blade from the slot to just before the discharge port.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、前記第
4技術においても、可動ダム8’はロータ5の軸方向に
長いが断面積の小さい混練翼部Bに対向しているため、
材料の遮蔽変化量が少なく、排出口3側の樹脂温度又は
圧力は余り変化し難く、逆に、ギヤポンプ7の制御の影
響を受けて、可動ダム8’通過時の材料の圧力又は温度
が変化するために、制御が困難又は不正確になることが
ある。また、排出口3の近傍ではロータ5自体に押出能
力がないので高粘度樹脂のギヤポンプ7への喰い込み不
良は解消し難いものである。
However, also in the fourth technique, the movable dam 8 'faces the kneading wing portion B which is long in the axial direction of the rotor 5 but has a small sectional area.
The amount of change in shielding of the material is small, and the temperature or pressure of the resin at the discharge port 3 is hardly changed. On the contrary, the pressure or temperature of the material when passing through the movable dam 8 ′ changes under the influence of the control of the gear pump 7. Control can be difficult or inaccurate. Further, since the rotor 5 itself does not have an extruding ability near the discharge port 3, it is difficult to eliminate poor biting of the high-viscosity resin into the gear pump 7.

【0009】第5技術においては、先端スクリュ部は混
練材料をギヤポンプに強制的に送り、ギヤポンプにおけ
る喰い込みを良好にするのに有効であるが、スクリュに
スロット部を形成すると必然的に混練翼部より小径にな
り、しかもシリンダが軸方向移動すると、先端スクリュ
部とギヤポンプとの間の距離が変化し、シリンダとオー
バラップする先端スクリュ部の長さ及び先端スクリュ部
の先端からギヤポンプまでの長さの変動は、ギヤポンプ
のサクション圧を変動することになる。しかも前記シリ
ンダを移動自在にするという構成は、シリンダだけでな
くギヤポンプ及びその下流側の後処理装置等も移動可能
に構成する必要があり、極めて大きなコストを占め、し
かも高精度が要求されるわりに微細な混練調整を困難に
している。
In the fifth technique, the tip screw portion is effective for forcibly feeding the kneading material to the gear pump to improve the bite in the gear pump. However, if a slot portion is formed in the screw, the kneading blade is inevitably formed. When the diameter becomes smaller than that of the section and the cylinder moves in the axial direction, the distance between the tip screw section and the gear pump changes, and the length of the tip screw section overlapping the cylinder and the length from the tip of the tip screw section to the gear pump are changed. Variations in the magnitude will vary the suction pressure of the gear pump. In addition, in order to move the cylinder freely, not only the cylinder but also the gear pump and a post-processing device downstream thereof need to be movable, which occupies an extremely large cost and requires high precision. Fine kneading adjustment is difficult.

【0010】本発明は、ロータをシリンダに対して軸線
方向位置固定し、ロータの混練翼部の下流側に断面円形
部と送り翼部とを形成し、可動ダムに断面円形部に略沿
う対向縁を形成して材料通過面積を大きく変更できるよ
うにすると共に、送り翼部でギヤポンプへ材料を強制的
に送って、ギヤポンプでの制御が可動ダムでの制御に影
響しないようにすると共に安価に製作できるようにした
連続混練機の混練制御装置を提供することを目的とす
る。
According to the present invention, the rotor is axially fixed with respect to the cylinder, a circular section and a feed blade are formed downstream of the kneading blade of the rotor, and the movable dam is opposed to the movable dam substantially along the circular section. An edge is formed so that the material passage area can be greatly changed, and the material is forcibly fed to the gear pump at the feed wing so that the control by the gear pump does not affect the control by the movable dam and the cost is low. An object of the present invention is to provide a kneading control device for a continuous kneader that can be manufactured.

【0011】[0011]

【課題を解決するための手段】本発明における課題を解
決するための具体的構成は、供給口2及び排出口3を有
するチャンバ4と、混練翼部Bを有してチャンバ4内に
平行に配置され且つチャンバ4に対して軸線方向位置固
定の2本のロータ5と、チャンバ4の供給口2と排出口
3との間でロータ5に対して径方向遠近位置調整自在に
設けられた可動ダム8と、排出口3の下流側に配置され
たギヤポンプ7とを備えており、前記可動ダム8はロー
タ5の混練翼部Bの下流側に形成した断面円形部Cに対
向し且つ略沿う対向縁12を有し、前記ロータ5にはギ
ヤポンプ7へ混練材料を強制押動させるべく断面円形部
Cの下流側から排出口3まで延設された送り翼部Dが形
成されていることにある。
The concrete structure for solving the problems of the present invention is as follows: a chamber 4 having a supply port 2 and a discharge port 3; Two rotors 5 arranged and fixed in the axial direction with respect to the chamber 4, and a movable member provided between the supply port 2 and the discharge port 3 of the chamber 4 so that the position in the radial direction can be adjusted with respect to the rotor 5. The movable dam 8 includes a dam 8 and a gear pump 7 disposed downstream of the discharge port 3. The movable dam 8 faces and substantially follows a circular section C formed downstream of the kneading blade B of the rotor 5. The rotor 5 has a feed wing portion D extending from the downstream side of the circular section C to the discharge port 3 for forcibly pushing the kneading material to the gear pump 7. is there.

【0012】[0012]

【作用】フィード装置6によって供給口2から供給され
た材料は、チャンバ4内で軸線方向相対位置不動の2本
のロータ5のスクリュ部Aによって混練翼部Bへ送ら
れ、混練、剪断作用を受けて、可塑化溶融される。可塑
化溶融された材料は混練翼部Bの下流側の断面円形部C
と可動ダム8との間を通過して、送り翼部Dによって排
出口3へ強力に押出され、ギヤポンプ7によって所要圧
力で後処理装置へ排出される。
The material supplied from the supply port 2 by the feed device 6 is sent to the kneading blade portion B by the screw portions A of the two rotors 5 which are stationary relative to each other in the axial direction in the chamber 4, and the kneading and shearing operations are performed. It is plasticized and melted. The plasticized and melted material has a circular section C on the downstream side of the kneading blade section B.
, And is strongly pushed out to the discharge port 3 by the feed blade portion D, and discharged to the post-processing device by the gear pump 7 at a required pressure.

【0013】可動ダム8は断面円形部Cの外周面11に
略沿う対向縁12を有していて、径方向に遠近位置調整
することによって、断面円形部Cとその間の材料通過面
積を、略零からチャンバ4内全開まで大きく変化可能で
あり、この材料通過面積を変化して、材料の温度、圧力
を制御する。ギヤポンプ7は混練翼部Bと略同径の送り
翼部Dによって材料が強制的に押込まれるため、喰い込
み不良を生じることがなく、能力が抑えられることもな
く、また、ギヤポンプ7による後処理装置への材料供給
制御は送り翼部Dによって遮断され、可動ダム8による
制御に影響を与えることはない。
The movable dam 8 has an opposing edge 12 substantially along the outer peripheral surface 11 of the circular section C. By adjusting the radial position of the movable dam 8, the area of the circular section C and the material passing area therebetween can be substantially reduced. The temperature and pressure of the material can be controlled by changing the material passage area from zero to the fully open state of the chamber 4. Since the material is forcibly pushed into the gear pump 7 by the feed wing portion D having substantially the same diameter as the kneading wing portion B, no biting failure occurs, the capacity is not suppressed, and The control of the material supply to the processing apparatus is interrupted by the feed wing D, and does not affect the control by the movable dam 8.

【0014】[0014]

【実施例】以下、本発明の実施例を図面に基いて説明す
る。図1〜4において、連続混練機1は供給口2と排出
口3とを有するチャンバ4内に、2本のロータ5を平行
に配置し、供給口2の上方にフィード装置6を、排出口
3の下方にギヤポンプ7を、供給口2と排出口3の中途
部に可動ダム8を夫々配置している。
Embodiments of the present invention will be described below with reference to the drawings. 1 to 4, in a continuous kneader 1, two rotors 5 are disposed in parallel in a chamber 4 having a supply port 2 and a discharge port 3, and a feed device 6 is provided above the supply port 2 and a discharge port is provided. 3, a gear pump 7 is arranged below, and a movable dam 8 is arranged in the middle of the supply port 2 and the discharge port 3 respectively.

【0015】フィード装置6はフィードスクリュ10を
可変モータM1で駆動する形式のものを示しており、プ
ラスチック、ゴム等の混練材料、添加剤、充填材等を所
要量ずつ供給口2へ供給する。2本のロータ5は同一形
状で噛合状態に隣接して、モータM2によって同期回転
されており、チャンバ4に対して軸線方向位置固定され
ていて、供給口2側に位置するスクリュ部Aから下流側
へ順次混練翼部B、断面円形部C及び送り翼部Dが形成
されている。
The feed device 6 is of a type in which a feed screw 10 is driven by a variable motor M1, and supplies a kneading material such as plastic and rubber, an additive, a filler and the like to the supply port 2 by a required amount. The two rotors 5 have the same shape and are adjacent to each other in a meshing state, are synchronously rotated by a motor M2, are axially fixed with respect to the chamber 4, and are downstream from the screw portion A located on the supply port 2 side. A kneading wing portion B, a circular cross-section portion C and a feed wing portion D are sequentially formed on the side.

【0016】前記スクリュ部A及び混練翼部Bは図3、
4に示す断面略三角形状で、材料を送りながら混練し、
圧力及び発熱で可塑化溶融し、断面円形部Cを通過する
際には混練作業は略完了し、送り翼部Dは主に溶融材料
を排出口3へ押動させるだけとなる。この送り翼部Dは
図1に示すようにスクリュ部Aと略同一形状で且つ混練
翼部Bとも略同径に形成されており、断面円形部Cの下
流側から排出口3まで延設されている。なお、本実施例
では、図1に示すようにチャンバ4の下面側に開口した
排出口3にギヤポンプ7が接続されているため、前記送
り翼部Dの更に下流側(ロータ5の最下流部)に、溶融
樹脂をその排出口3へ落とし込むための平行翼部Eが形
成されている。
The screw section A and the kneading blade section B are shown in FIG.
4 has a substantially triangular cross section, and kneading while feeding the material,
The kneading operation is substantially completed when plasticizing and melting by the pressure and heat and passing through the circular section C, and the feed wing section D mainly only pushes the molten material to the discharge port 3. As shown in FIG. 1, the feed wing portion D has substantially the same shape as the screw portion A and has substantially the same diameter as the kneading wing portion B. The feed wing portion D extends from the downstream side of the circular section C to the discharge port 3. ing. In this embodiment,
Then, as shown in FIG. 1, the chamber 4 was opened on the lower surface side.
Since the gear pump 7 is connected to the discharge port 3,
Further downstream of the wing portion D (the most downstream portion of the rotor 5),
The parallel wing E for dropping the resin into the outlet 3 is shaped
Has been established.

【0017】この送り翼部Dに対向しているチャンバ4
の部位にはベント9が形成されており、混練途中に材料
から発生する揮発分を排出可能にしている。このベント
9によって揮発分が供給口2へ逆流することにより生じ
るフィード阻害を防止している。可動ダム8は断面円形
部Cに対向して上下1対設けられている。断面円形部C
の外周面11の径はチャンバ4の内径より若干小さく、
上下各可動ダム8は外周面11に略沿う対向縁12を有
している。
The chamber 4 facing the feed wing portion D
A vent 9 is formed at the portion (1), so that volatiles generated from the material during kneading can be discharged. This vent 9 prevents feed obstruction caused by the backflow of volatiles to the supply port 2. The movable dam 8 is provided in a pair of upper and lower portions facing the circular section C. Circular section C
Is slightly smaller than the inner diameter of the chamber 4,
Each of the upper and lower movable dams 8 has an opposing edge 12 substantially along the outer peripheral surface 11.

【0018】即ち、対向縁12は外周面11と同一又は
若干大きい曲率の円弧面を横並びに形成したものであ
り、モータM3によって断面円形部Cに対して径方向に
遠近位置調整可能となっている。尚、上下可動ダム8の
モータM3は1個又は同調された2個で構成され、ラッ
クピニオン機構又はネジジャッキ機構を介して、上下可
動ダム8を対向方向に同一量移動できるようになってい
る。また、上下可動ダム8は油圧シリンダで駆動しても
良い。
That is, the opposing edge 12 is formed by arranging circular arc surfaces having the same or slightly larger curvature as the outer peripheral surface 11 side by side, and can be adjusted in the radial direction with respect to the circular section C by the motor M3. I have. The motor M3 of the vertically movable dam 8 is constituted by one or two tuned motors so that the vertically movable dam 8 can be moved in the opposite direction by the same amount via a rack and pinion mechanism or a screw jack mechanism. . Further, the vertically movable dam 8 may be driven by a hydraulic cylinder.

【0019】前記上下可動ダム8は断面円形部Cに対し
て遠近位置調整することによって、材料通過面積を略零
からチャンバ4内全開状態まで変化させることができ、
面積を絞ることによって、材料の流動抵抗が増加され、
温度及び圧力は上昇される。TIC,PICは通過材料
の温度及び圧力を夫々測定し、モータM3を制御する温
度センサと圧力センサである。従って材料の温度又は圧
力を測定し、所要の混練度になっていない場合はモータ
M3が作動され、可動ダム8が断面円形部Cとの間のゲ
ートを調整して、混練度を制御(溶融開始点を調整)す
る。
The upper and lower movable dams 8 can change the material passage area from substantially zero to a fully open state in the chamber 4 by adjusting the far and near positions with respect to the circular section C.
By reducing the area, the flow resistance of the material is increased,
Temperature and pressure are increased. TIC and PIC are a temperature sensor and a pressure sensor which measure the temperature and the pressure of the passing material, respectively, and control the motor M3. Therefore, the temperature or pressure of the material is measured, and if the required kneading degree is not attained, the motor M3 is operated, and the movable dam 8 adjusts the gate between the movable dam 8 and the circular section C to control the kneading degree (melting). Adjust the starting point).

【0020】ギヤポンプ7は従来技術と同様にモータM
4で駆動されていて、ポンプ入口の圧力を圧力センサP
ICで測定して、モータM4を制御し、後処理装置への
混練材料の供給量を調整する。このギヤポンプ7は、送
り翼部Dによる送り出しだけでは後処理装置へ供給し難
い高粘度材料のときに特に有用であり、その制御による
圧力変化は、送り翼部Dで材料が強制送りされてくるた
め、混練作用中の材料には伝播されなく、可動ダム8に
よる制御とギヤポンプ7による制御とは独立している。
The gear pump 7 has a motor M as in the prior art.
4 and is driven by a pressure sensor P
The measurement is performed by an IC, and the motor M4 is controlled to adjust the supply amount of the kneading material to the post-processing device. The gear pump 7 is particularly useful for a high-viscosity material that is difficult to supply to a post-processing apparatus by only sending it out by the feed wing D, and the pressure change due to the control causes the material to be forcibly fed by the feed wing D. Therefore, the control by the movable dam 8 and the control by the gear pump 7 are independent from each other during the kneading operation.

【0021】[0021]

【発明の効果】以上詳述した本発明によれば、可動ダム
8はロータ5の断面円形部Cに対向し且つ略沿う対向線
12を有しているので、ロータ5とチャンバ4との間の
材料通過面積を略零から全開まで変化させることが可能
になり、材料の流動抵抗を変えて混練度を制御する範囲
を大きくすることができ、効果的な混練制御が可能にな
る。また、ロータ5には混練材料を排出口3へ強制的に
押動する送り翼部Dを設けているので、ギヤポンプ7で
の材料喰い込み不良を減少させることができると共に、
材料を後処理装置へ円滑に供給するためにギヤポンプ7
を制御しても、その制御は可動ダム8による混練制御に
影響することがなく、混練制御を正確且つ容易に行なう
ことができ、高粘度材料の混練であっても、安定的な運
転ができる。
According to the present invention described in detail above, since the movable dam 8 has the opposing line 12 which is opposed to and substantially along the circular section C of the rotor 5, the movable dam 8 is located between the rotor 5 and the chamber 4. It is possible to change the material passage area from substantially zero to full open, to increase the range of controlling the kneading degree by changing the flow resistance of the material, and to enable effective kneading control.
You. Further, since the rotor 5 is provided with the feed wing portion D for forcibly pushing the kneaded material to the discharge port 3, it is possible to reduce a material biting defect in the gear pump 7, and
Gear pump 7 to supply the material to the after-treatment device smoothly
Does not affect the kneading control by the movable dam 8, the kneading control can be performed accurately and easily, and stable operation can be performed even when kneading high-viscosity materials. .

【0022】その上にチャンバ4を軸線方向に移動して
スロット調整をする従来技術に比して、径方向遠近位置
調整自在な可動ダム8を設けることにより、ギヤポンプ
7のサクション圧を変動することなく混練度を調整でき
るようにし、あわせてロータ5をチャンバ4に対して軸
線方向位置固定してチャンバ4及びギヤポンプ7を移動
しない定置式にしていることにより、混練機全体の大幅
なコストダウン及び高精度化が実現される。
The suction pressure of the gear pump 7 can be varied by providing a movable dam 8 whose position in the radial direction can be adjusted as compared with the prior art in which the chamber 4 is moved in the axial direction to adjust the slot. In addition, the kneading degree can be adjusted without any trouble, and the rotor 5 is fixed in the axial direction with respect to the chamber 4 so that the chamber 4 and the gear pump 7 are not moved. High accuracy is realized.

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

【図1】本発明の実施例を示す全体説明図である。FIG. 1 is an overall explanatory diagram showing an embodiment of the present invention.

【図2】図1のII−II線断面図である。FIG. 2 is a sectional view taken along line II-II of FIG.

【図3】図1のIII −III 線断面図である。FIG. 3 is a sectional view taken along line III-III of FIG.

【図4】図1のIV−IV線断面図である。FIG. 4 is a sectional view taken along line IV-IV of FIG. 1;

【図5】第4従来技術を示す説明図である。FIG. 5 is an explanatory diagram showing a fourth conventional technique.

【符号の説明】[Explanation of symbols]

1 連続混練機 2 供給口 3 排出口 4 チャンバ 5 ロータ 6 フィード装置 7 ギヤポンプ 8 可動ダム 12 対向縁 A スクリュ部 B 混練翼部 C 断面円形部 D 送り翼部 DESCRIPTION OF SYMBOLS 1 Continuous kneader 2 Supply port 3 Discharge port 4 Chamber 5 Rotor 6 Feed device 7 Gear pump 8 Movable dam 12 Opposite edge A Screw part B Kneading wing part C Round section D Feed wing part

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 供給口(2)及び排出口(3)を有する
チャンバ(4)と、混練翼部(B)を有してチャンバ
(4)内に平行に配置され且つチャンバ(4)に対して
軸線方向位置固定の2本のロータ(5)と、チャンバ
(4)の供給口(2)と排出口(3)との間でロータ
(5)に対して径方向遠近位置調整自在に設けられた可
動ダム(8)と、排出口(3)の下流側に配置されたギ
ヤポンプ(7)とを備えており、前記可動ダム(8)は
ロータ(5)の混練翼部(B)の下流側に形成した断面
円形部(C)に対向し且つ略沿う対向縁(12)を有
し、前記ロータ(5)にはギヤポンプ(7)へ混練材料
を強制押動させるべく断面円形部(C)の下流側から排
出口(3)まで延設された送り翼部(D)が形成されて
いることを特徴とする連続混練機の混練制御装置。
1. A chamber (4) having a supply port (2) and a discharge port (3), and a kneading wing (B) arranged parallel to and inside the chamber (4) with a kneading blade (B). On the other hand, between the two rotors (5) fixed in the axial direction and the supply port (2) and the discharge port (3) of the chamber (4), the radial distance position of the rotor (5) can be adjusted freely. It has a movable dam (8) provided and a gear pump (7) arranged downstream of the discharge port (3), and the movable dam (8) is a kneading blade (B) of a rotor (5). The rotor (5) has an opposing edge (12) opposed to and substantially along the circular section (C) formed on the downstream side of the rotor. The rotor (5) has a circular section for forcibly pushing the kneading material to the gear pump (7). discharging from the downstream side of the (C)
A kneading control device for a continuous kneader, wherein a feed wing portion (D) extending to an outlet (3) is formed.
JP7139607A 1995-06-06 1995-06-06 Kneading control device for continuous kneading machine Expired - Lifetime JP2601645B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7139607A JP2601645B2 (en) 1995-06-06 1995-06-06 Kneading control device for continuous kneading machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7139607A JP2601645B2 (en) 1995-06-06 1995-06-06 Kneading control device for continuous kneading machine

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP1086184A Division JPH0641135B2 (en) 1989-04-04 1989-04-04 Kneading control device for continuous kneader

Publications (2)

Publication Number Publication Date
JPH0899313A JPH0899313A (en) 1996-04-16
JP2601645B2 true JP2601645B2 (en) 1997-04-16

Family

ID=15249228

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7139607A Expired - Lifetime JP2601645B2 (en) 1995-06-06 1995-06-06 Kneading control device for continuous kneading machine

Country Status (1)

Country Link
JP (1) JP2601645B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009057753A1 (en) 2007-11-02 2009-05-07 Kabushiki Kaisha Kobe Seiko Sho Mechanism for regulating kneadability, extruder, continuous kneading machine, method for regulating kneadability and kneading method

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5822800B2 (en) * 2012-08-21 2015-11-24 株式会社神戸製鋼所 Kneading rotor and kneading machine
JP6308907B2 (en) * 2013-08-13 2018-04-11 株式会社神戸製鋼所 Continuous kneader

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Publication number Priority date Publication date Assignee Title
JPS565719A (en) * 1979-06-29 1981-01-21 Kobe Steel Ltd Continuous type kneading device
JPS5850533A (en) * 1981-09-21 1983-03-25 Fuji Photo Film Co Ltd Color photosensitive silver halide material
JPS61233508A (en) * 1986-04-08 1986-10-17 Japan Steel Works Ltd:The Continuous kneading and granulating apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009057753A1 (en) 2007-11-02 2009-05-07 Kabushiki Kaisha Kobe Seiko Sho Mechanism for regulating kneadability, extruder, continuous kneading machine, method for regulating kneadability and kneading method

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