JPS6223544Y2 - - Google Patents

Info

Publication number
JPS6223544Y2
JPS6223544Y2 JP1983177286U JP17728683U JPS6223544Y2 JP S6223544 Y2 JPS6223544 Y2 JP S6223544Y2 JP 1983177286 U JP1983177286 U JP 1983177286U JP 17728683 U JP17728683 U JP 17728683U JP S6223544 Y2 JPS6223544 Y2 JP S6223544Y2
Authority
JP
Japan
Prior art keywords
section
kneading
feed
feed section
kneading machine
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
Application number
JP1983177286U
Other languages
Japanese (ja)
Other versions
JPS6083039U (en
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 filed Critical
Priority to JP1983177286U priority Critical patent/JPS6083039U/en
Priority to KR1019840005149A priority patent/KR850004019A/en
Publication of JPS6083039U publication Critical patent/JPS6083039U/en
Application granted granted Critical
Publication of JPS6223544Y2 publication Critical patent/JPS6223544Y2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/92Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with helices or screws
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Accessories For Mixers (AREA)

Description

【考案の詳細な説明】 本考案は、摩擦係数の小さい材料、嵩比重の小
さい材料を生産量の低下を伴なわずに混練する連
続式混練機に関する。
[Detailed Description of the Invention] The present invention relates to a continuous kneading machine that kneads materials with a small coefficient of friction and materials with a small bulk specific gravity without reducing production volume.

単軸押出機、二軸スクリユー式押出機の一部で
は、従来から摩擦係数の小さい滑りやすい材料、
嵩比重の小さい材料を対象とする場合、材料を強
制的に押出機に押込む装置が使用されてきたが、
高速回転する二軸連続式の混練機では、材料を混
練機の供給ホツパーに充満させると、材料の喰込
みが良く過負荷になることがあつた。従つて、通
常は、フイーダ部の前段に定量供給装置を設けて
供給量を制御し、混練部のロータの回転数とは別
個に生産量をコントロールするのが一般的であ
る。即ち、混練機の混練部の処理能力に比べて材
料の供給量は少な目にして、所謂スターブ状態で
運転する。しかし、硬質塩化ビニールやカーボン
ブラツク等の粉末材料を混練する場合には、材料
の摩擦係数が小さいためにフイード部の送り能力
が低下したり、材料の嵩比重が小さいために送り
能力が不足する状態が起こり、混練機の生産能力
が十分に増加しないことがある。
Some single-screw extruders and twin-screw extruders have traditionally used slippery materials with a low coefficient of friction,
When targeting materials with low bulk specific gravity, devices that force the material into an extruder have been used;
In a two-shaft continuous kneading machine that rotates at high speed, when the feed hopper of the kneading machine is filled with material, the material is often eaten into the kneading machine, resulting in an overload. Therefore, it is common practice to control the supply amount by providing a quantitative feeding device upstream of the feeder section, and to control the production amount separately from the rotation speed of the rotor of the kneading section. That is, the amount of material supplied is small compared to the processing capacity of the kneading section of the kneader, and the kneader is operated in a so-called starved state. However, when kneading powder materials such as hard vinyl chloride or carbon black, the feeding capacity of the feed section decreases because the friction coefficient of the material is small, or the feeding capacity is insufficient because the bulk specific gravity of the material is small. A situation may occur in which the production capacity of the kneader does not increase sufficiently.

そこで、このように混練機の送り能力が不足す
るのを防止するために、混練部のロータの回転数
を上げるか、フイード部のスクリユーの長さを延
ばす等の対策が考えられている。しかし、ロータ
の回転数を上げると材料の発熱が増し、熱的に不
安定で温度に制限のある材料では分解し易い等の
問題がある。またフイード部のスクリユーの寸法
を大きくすることは、機械全体の寸法が大型化し
コストアツプにつながると同時に、ロータに加わ
る曲げ応力も増加するため、機械の寿命が短かく
なり、高粘度の材料が混練できない制約がある。
Therefore, in order to prevent such insufficient feeding capacity of the kneading machine, countermeasures have been considered, such as increasing the rotational speed of the rotor in the kneading section or increasing the length of the screw in the feed section. However, increasing the rotational speed of the rotor increases heat generation of the material, and there are problems such as thermally unstable and temperature-limited materials that are likely to decompose. In addition, increasing the size of the screw in the feed section increases the overall size of the machine and increases costs. At the same time, the bending stress applied to the rotor also increases, shortening the life of the machine and kneading high-viscosity materials. There are restrictions that prevent it.

本考案は、このような従来の問題点を解消する
ことを目的として提供されたものであつて、その
特徴とする処は、フイード部、混練部、絞り部及
び排出部を備えると共に、混練部には送り翼と戻
し翼とを有する有翼ロータを設け、混練部での材
料に対する軸方向の平均の力は絞り部より材料を
押出すには不十分とし、かつ混練部を通る材料の
全体的移動はフイード部からの材料の送り量に依
存するようにした連続式混練機において、フイー
ド部とその前段の定量供給装置との間に、定量供
給装置から供給された材料を強制的にフイード部
へ押込む強制押込装置を具備した点にある。
The present invention was provided for the purpose of solving such conventional problems, and its features include a feed section, a kneading section, a squeezing section, and a discharge section, and a kneading section. is equipped with a winged rotor having sending blades and returning blades, and the average force in the axial direction on the material in the kneading section is insufficient to extrude the material from the constriction section, and the entire material passing through the kneading section is In a continuous kneading machine, the material movement depends on the amount of material fed from the feed section, the material fed from the metering device is forcibly fed between the feed section and the metering device in the preceding stage. The main feature is that it is equipped with a forcible pushing device that pushes it into the section.

以下、図示の実施例について本考案を詳述する
と、第1図及び第2図において、1は二軸連続式
混練機の混練機本体で、これにはフイード部2、
混練部3、絞り部4及び排出部5が備えられてい
る。フイード部2は供給口6から供給された材料
を混練部3側へと送るためのものであつて、スク
リユー7を有する。混練部3はスクリユー7と一
体回転する有翼ロータ8を具備し、そのロータ8
には送り翼と戻し翼とが軸方向に形成されてお
り、この混練部3での材料に対する軸方向の平均
の力は絞り部4より材料を押出すには不十分な程
度に設定され、従つて、混練部3を通る材料の全
体的移動はフイード部2からの材料の送り量に依
存するようになつている。絞り部4は混練部3で
の混練度を調整するためのものであつて、上下一
対の絞り板9,10を有し、その各絞り板9,1
0はシリンダ11,12により上下調整可能であ
る。混練機本体1のフイード部2側上部には供給
ホツパー13が設けられ、またこの供給ホツパー
13は、材料ホツパー14,15からの材料が定
量供給装置16,17を介して定量ずつ供給され
るようになつている。供給ホツパー13内にはそ
の内部の材料をフイード部2に強制的に押込む強
制押込装置18が設けられている。この強制押込
装置18は上端部側で支持された縦方向の回転軸
19と、この回転軸19に設けられた撹拌用突起
20及びスクリユー21とを備え、その回転軸1
9はモータ22により回転駆動されている。
Hereinafter, the present invention will be described in detail with reference to the illustrated embodiment. In FIGS. 1 and 2, 1 is a kneader main body of a two-screw continuous kneader, which includes a feed section 2,
A kneading section 3, a squeezing section 4, and a discharge section 5 are provided. The feed section 2 is for feeding the material supplied from the supply port 6 to the kneading section 3 side, and has a screw 7. The kneading section 3 is equipped with a winged rotor 8 that rotates integrally with the screw 7.
A feed blade and a return blade are formed in the axial direction, and the average force in the axial direction on the material in the kneading section 3 is set to an extent insufficient to extrude the material from the constriction section 4. The overall movement of the material through the kneading section 3 is therefore dependent on the amount of material fed from the feed section 2. The throttle section 4 is for adjusting the degree of kneading in the kneading section 3, and has a pair of upper and lower throttle plates 9, 10, each of which
0 can be adjusted up and down using cylinders 11 and 12. A supply hopper 13 is provided at the upper part of the feed section 2 side of the kneading machine main body 1, and this supply hopper 13 is configured so that the material from the material hoppers 14 and 15 is supplied in fixed quantities via quantitative supply devices 16 and 17. It's getting old. A forced pushing device 18 is provided in the supply hopper 13 to forcibly push the material therein into the feed section 2 . This forced pushing device 18 includes a vertical rotating shaft 19 supported on the upper end side, a stirring protrusion 20 and a screw 21 provided on the rotating shaft 19, and the rotating shaft 1
9 is rotationally driven by a motor 22.

上記構成において、摩擦係数の小さい材料、嵩
比重の小さい材料等を混練する場合には、強制押
込装置18を使用し、これによつて供給ホツパー
13内の材料を軽く強制的にフイード部2へと押
込んでやる。これによつてフイード部2でのスク
リユー7に対する材料の喰込みが著しく改善さ
れ、混練機の生産能力を増大しつつ、前述の如き
材料を混練できる。この場合、強制押込装置18
のスクリユー21の回転数を制御して生産量を増
減させるが、ロータ8が速い速度で回転する混練
機では、材料を多量に送込むと過負荷状態となつ
て停止する。従つて、これを防止するためにはス
クリユー21の回転数を制御する他、定量供給装
置16,17により材料の供給量を制御し、安定
して一定の混練条件にすることが望ましい。また
定量供給装置16,17があれば、スクリユー2
1の回転数はある程度の幅をもつて選択すること
が可能となり、過負荷や生産量の変動を伴なうこ
となく一定の品質の混練物を安定して得ることが
できる。
In the above configuration, when kneading a material with a small friction coefficient, a material with a small bulk specific gravity, etc., the forced pushing device 18 is used to lightly force the material in the supply hopper 13 into the feed section 2. I'll push it in. As a result, the feeding of the material into the screw 7 in the feed section 2 is significantly improved, and the above-mentioned materials can be kneaded while increasing the production capacity of the kneader. In this case, the forced pushing device 18
The production volume is increased or decreased by controlling the rotational speed of the screw 21. However, in a kneading machine where the rotor 8 rotates at a high speed, if a large amount of material is fed, the kneading machine becomes overloaded and stops. Therefore, in order to prevent this, in addition to controlling the rotational speed of the screw 21, it is desirable to control the amount of material supplied by the quantitative supply devices 16 and 17 to maintain stable and constant kneading conditions. Also, if there are quantitative supply devices 16 and 17, the screw 2
1 can be selected within a certain range, and a kneaded material of constant quality can be stably obtained without overload or fluctuation in production.

因みに強制押込装置18を具備した本考案と従
来のものとを比較すると、次の通りであつた。
Incidentally, a comparison between the present invention equipped with the forced pushing device 18 and the conventional one was as follows.

即ち、粉末状の硬質塩化ビニールコンパウンド
を混練機本体1のチヤンバー内径120mm〓の混練
機にて混練した処、従来は、ロータ回転数
300rpmで生産量が300Kg/hが上限であつた。こ
の時の混練機本体1の供給口6をみると、粉末材
料が溜つており、フイード部2での材料の送り力
が不足し、材料が混練部3に送り込まれず、逆流
していることが判かつた。
That is, when powdered hard vinyl chloride compound is kneaded in a kneader with a chamber inner diameter of 120 mm in the kneader body 1, conventionally, the rotor rotation speed is
The upper limit of production was 300Kg/h at 300rpm. At this time, if you look at the supply port 6 of the kneading machine main body 1, you will notice that the powder material has accumulated, and that the feeding force of the material in the feed section 2 is insufficient, so that the material is not fed into the kneading section 3 and is flowing backwards. I got it.

これに対し本考案に係る混練機では、強制押込
装置18により800Kg/hの割合で硬質塩化ビニ
ールコンパウンドを供給した処、供給ホツパー1
3に材料が溜まることなく安定して運転できた。
従つて本考案によれば、生産量が800Kg/hまで
増加できることが判かる。また可遡化された材料
の温度は約180℃であつた。但し、混練機のロー
タ回転数は400rpm、強制押込装置18は150mm〓
の単軸スクリユー式で、回転数300rpmで運転し
た。
In contrast, in the kneader according to the present invention, the forced pushing device 18 fed the hard vinyl chloride compound at a rate of 800 kg/h, and the supply hopper 1
3. Stable operation was achieved without material accumulating.
Therefore, it is found that the production amount can be increased to 800 kg/h by this invention. The temperature of the recycled material was about 180°C. However, the rotor speed of the kneader was 400 rpm, and the forced pushing device 18 had a diameter of 150 mm.
It was a single-shaft screw type and was operated at a rotation speed of 300 rpm.

強制押込装置18は第3図に示す如く押込体2
3をエアシリンダ24により往復駆動するように
しても良く、この場合にも前記同様の混練機を使
用して実験すると、生産量を従来の300Kg/hか
ら600Kg/h程度まで増加することが可能であつ
た。但し、押込体23の加圧部面積は100mm×150
mm、ストロークは300mmとし、2Kg/cm2のエアー
シリンダ24で駆動した。なお、この場合には、
スクリユー式に比べて負荷の変動が若干大になる
が、問題はない。
As shown in FIG. 3, the forced pushing device 18
3 may be reciprocated by the air cylinder 24, and in this case, when experimenting using the same kneading machine as described above, it is possible to increase the production amount from the conventional 300 Kg/h to about 600 Kg/h. It was hot. However, the area of the pressing part of the pushing body 23 is 100mm x 150mm.
mm, the stroke was 300 mm, and it was driven by a 2 Kg/cm 2 air cylinder 24. In this case,
Load fluctuations are slightly larger than with the screw type, but this is not a problem.

以上実施例に詳述したように本考案によれば、
強制押込装置により材料を強制的にフイード部に
押込むようにしているので、ロータ回転数を低速
に保つても材料を確実にフイード部で喰込むこと
ができ、従つて、摩擦係数の小さいスリツプのし
易い材料、嵩比重の小さい材料でも安定して均一
に混練でき、十分な生産能力を維持しつつ均一な
混練物が得られる。また発熱し易い材料、熱分解
し易い材料も安定して混練できる。しかも、混練
機のフイード部を長くする必要がないので、ロー
タ軸を短かくでき、機械的強度の向上により高粘
度の材料の混練が可能であり、更にはコンパクト
化による製作コストのダウン、生産性のアツプ等
が可能である。
As detailed in the embodiments above, according to the present invention,
Since the material is forcibly pushed into the feed section by the forced pushing device, the material can be reliably bitten into the feed section even if the rotor rotational speed is kept at a low speed.Therefore, the coefficient of friction is small, making it easy to slip. Even materials with low bulk specific gravity can be stably and uniformly kneaded, and a uniform kneaded product can be obtained while maintaining sufficient production capacity. In addition, materials that easily generate heat and materials that are easily thermally decomposed can be stably kneaded. Moreover, since there is no need to lengthen the feed section of the kneader, the rotor shaft can be shortened, and the improved mechanical strength makes it possible to knead high-viscosity materials.Furthermore, the compactness reduces manufacturing costs and production. Sexual enhancement is possible.

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

第1図は本考案の一実施例を示す構成図、第2
図はその絞り部の構成図、第3図は他の実施例を
示す構成図である。 1……混練機本体、2……フイード部、3……
混練部、4……絞り部、5……排出部、8……有
翼ロータ、13……供給ホツパー、16,17…
…定量供給装置、18……強制押込装置。
Fig. 1 is a configuration diagram showing one embodiment of the present invention;
The figure is a block diagram of the aperture section, and FIG. 3 is a block diagram showing another embodiment. 1... Kneading machine main body, 2... Feed section, 3...
Kneading section, 4... Squeezing section, 5... Discharge section, 8... Winged rotor, 13... Supply hopper, 16, 17...
...Quantitative supply device, 18... Forced pushing device.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] フイード部、混練部、絞り部及び排出部を備え
ると共に、混練部には送り翼と戻し翼とを有する
有翼ロータを設け、混練部での材料に対する軸方
向の平均の力は絞り部より材料を押出すには不十
分とし、かつ混練部を通る材料の全体的移動はフ
イード部からの材料の送り量に依存するようにし
た連続式混練機において、フイード部とその前段
の定量供給装置との間に、定量供給装置から供給
された材料を強制的にフイード部へ押込む強制押
込装置を具備したことを特徴とする連続式混練
機。
The kneading section is equipped with a feed section, a kneading section, a constriction section, and a discharge section, and the kneading section is equipped with a winged rotor having sending blades and return vanes. In a continuous kneading machine, the amount of material is insufficient to extrude the material, and the overall movement of the material through the kneading section depends on the amount of material fed from the feed section. 1. A continuous kneading machine characterized in that the continuous kneading machine is equipped with a forcible pushing device that forcibly pushes the material supplied from the quantitative feeding device into a feed section.
JP1983177286U 1983-11-15 1983-11-15 Continuous kneading machine Granted JPS6083039U (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP1983177286U JPS6083039U (en) 1983-11-15 1983-11-15 Continuous kneading machine
KR1019840005149A KR850004019A (en) 1983-11-15 1984-08-24 Continuous mixer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1983177286U JPS6083039U (en) 1983-11-15 1983-11-15 Continuous kneading machine

Publications (2)

Publication Number Publication Date
JPS6083039U JPS6083039U (en) 1985-06-08
JPS6223544Y2 true JPS6223544Y2 (en) 1987-06-16

Family

ID=30385201

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1983177286U Granted JPS6083039U (en) 1983-11-15 1983-11-15 Continuous kneading machine

Country Status (2)

Country Link
JP (1) JPS6083039U (en)
KR (1) KR850004019A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100751837B1 (en) * 2006-09-26 2007-08-29 최종호 Continuous and multipurpose mixer

Also Published As

Publication number Publication date
KR850004019A (en) 1985-07-01
JPS6083039U (en) 1985-06-08

Similar Documents

Publication Publication Date Title
JP3868757B2 (en) Rubber composition kneading apparatus and kneading method
CN100500413C (en) Metering feeder, kneading and extruding equipment
JP3816282B2 (en) Compound manufacturing method using biaxial continuous kneader
JP2546880B2 (en) Screw extruder
CS9101348A2 (en) Delivery worm
CN102205619A (en) Exhaust-type differential double-screw extruder
CN102205620A (en) Differential-speed conical twin-screw extruder
Mollan Historical overview
JP3803457B2 (en) Biaxial continuous kneading extrusion equipment
JPS6223544Y2 (en)
JPS59164124A (en) Continuous kneading and extruding device with gear pump
JP3330126B2 (en) Rubber composite extrusion apparatus and unvulcanized rubber extrusion method
JPS5850533B2 (en) Two-screw continuous kneader
JP3812964B2 (en) Twin screw extruder
CN202155160U (en) Conical dual-rotor continuous mixing unit
EP3814080B1 (en) Mixing process for producing an elastomeric composition
JP2601336B2 (en) Kneading extruder
JP3113879B2 (en) Continuous kneading extruder
JP3187920B2 (en) Co-rotating twin screw extruder
JP3530334B2 (en) Continuous kneader and rotor of continuous kneader
JPS6321381Y2 (en)
JP2002355879A (en) Conical screw for twin-screw extruder and extrusion molding method using the same
CN214820760U (en) Miniature double screw extruder
CN218777070U (en) Parallel counter-rotating double-screw mixing extruder
CN219946840U (en) Banbury mixer for producing thermoplastic elastomer