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JPS6246208B2 - - Google Patents
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JPS6246208B2 - - Google Patents

Info

Publication number
JPS6246208B2
JPS6246208B2 JP56073294A JP7329481A JPS6246208B2 JP S6246208 B2 JPS6246208 B2 JP S6246208B2 JP 56073294 A JP56073294 A JP 56073294A JP 7329481 A JP7329481 A JP 7329481A JP S6246208 B2 JPS6246208 B2 JP S6246208B2
Authority
JP
Japan
Prior art keywords
kneading
rotor
barrel
section
discharge
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
JP56073294A
Other languages
Japanese (ja)
Other versions
JPS57187022A (en
Inventor
Kimio Inoe
Futashi Fukui
Shinichi Fukumizu
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 JP56073294A priority Critical patent/JPS57187022A/en
Publication of JPS57187022A publication Critical patent/JPS57187022A/en
Publication of JPS6246208B2 publication Critical patent/JPS6246208B2/ja
Granted 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
    • B29B7/34Mixing; 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
    • B29B7/465Mixing; 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
    • 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
    • B29C48/268Throttling of the flow, e.g. for cooperating with plasticising elements or for degassing
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Description

【発明の詳細な説明】 本発明は、混練物の均一度を向上させ、分散が
不充分なまゝ充填剤等が排出されるのを防止する
ことを目的とした二軸連続式混練機の改良に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is directed to a twin-screw continuous kneader for the purpose of improving the uniformity of a kneaded material and preventing fillers from being discharged without sufficient dispersion. It is about improvement.

合成樹脂等の高分子物質を混練する装置には、
大別して単軸又は二軸のロータをチヤンバー内に
装備した連続式混練機、バンバリーミキサー等の
バツチ式(回分式)混練機、及びスクリユー押出
機があり、このうち、特に二軸連続混練機は高い
せん断速度により短時間で材料を可塑化して効率
の良い混練を可能にしている。
Equipment for kneading polymeric substances such as synthetic resins includes
Broadly divided, there are continuous kneading machines equipped with a single-screw or twin-screw rotor in the chamber, batch-type kneading machines such as Banbury mixers, and screw extruders. The high shear rate plasticizes the material in a short time, enabling efficient kneading.

すなわち、第1図のグラフに定性的に示す如
く、混練機のせん断速度と一定品質の混練物を得
るために必要な混練時間とは反比例する関係にあ
り、また同図にブロツクで表わした範囲Aは連続
式混練機の場合、同Bはバツチ式混練機の場合、
同Cはスクリユー押出機の場合の各特性領域を示
す。二軸連続式混練機の場合、せん断速度は最大
1000sec-1混練時間は10〜40sec程度で、スクリユ
ー押出機等に比べて著しく高いせん断速度で短時
間の混練を行うため、効率が良く、小型化が可能
であり、また、合成樹脂に多量の無機質充填剤を
混合する等複合材料の混練にもすぐれた能力を発
揮する。
In other words, as shown qualitatively in the graph of Figure 1, the shear rate of the kneader and the kneading time required to obtain a kneaded product of a constant quality are inversely proportional, and the range represented by the block in the figure A is for a continuous kneader, B is for a batch kneader,
C shows each characteristic range in the case of a screw extruder. For twin-screw continuous kneading machines, the shear rate is maximum
1000sec -1 The kneading time is about 10 to 40 seconds, and the kneading is performed in a short time at a significantly higher shear rate than screw extruders, etc., so it is efficient and can be made smaller. It also exhibits excellent ability for kneading composite materials such as mixing inorganic fillers.

ところが、近年、合成樹脂産業の発達に伴い樹
脂の用途も多様化し、単一種の合成樹脂のほかに
二種以上の合成樹脂を混合したブレンドポリマー
や各種添加剤を混合した複合材料も含めて品種が
著しく増加しており、これに対応して、連続式混
練機においても混練する材料によつては混練時間
の延長を必要とする場合があり、混練機内部にお
ける材料の滞溜時間を広範囲に調節し得ることが
要求されている。この場合、従来のこの種連続混
練機によると、調節要素として吐出口における吐
出オリフイスの開度、生産量等が考えられるが、
各種材料に応じた範囲にわたる滞溜時間の調節に
は、なお問題が残されていた。
However, in recent years, with the development of the synthetic resin industry, the uses of resin have diversified, and in addition to a single type of synthetic resin, there are various types including blended polymers that are a mixture of two or more types of synthetic resins and composite materials that are a mixture of various additives. In response to this, even in continuous kneading machines, depending on the material to be kneaded, it may be necessary to extend the kneading time, and the residence time of the material inside the kneading machine may have to be extended over a wide range. It is required to be adjustable. In this case, according to the conventional continuous kneading machine of this type, the opening degree of the discharge orifice at the discharge port, the production volume, etc. can be considered as adjustment factors.
Problems still remain in adjusting the residence time over a range depending on the various materials.

すなわち、一般にこの種連続式混練機の操作は
生産量、ミキシングロータの回転数、吐出口にお
ける吐出オリフイスの開度、ミキシングチヤンバ
ー及びロータの冷却条件等に基づいて行われ、生
産量、ロータ回転数及び冷却条件を一定にした場
合はオリフイス開度によつて混練物の温度や混練
度が調節でき、オリフイス開度(θ)と混練機内
部における材料の滞溜時間(t)との関係は第2
図のグラフに示す如くなる。つまり、オリフイス
開度が小さくなると、吐出抵抗の増加により混練
機中での材料充填率が増して滞溜時間が長くな
り、これによつて混練度が増し、混練物の温度も
上昇する。また、同グラフで生産量Q1の場合と
同Q2の場合(Q1>Q2)について示した如
く、生産量を減少することによつても滞溜時間を
延長し得るが、この場合は混練機の能率を下げる
ことになる。このほかロータを長くすることによ
つても滞溜時間が増加するが、混練物の温度も上
昇するため、混練物の温度に制限がある場合はオ
リフイス開度を大きくしなければならず、必ずし
も滞溜時間を延長することにはならない。
In other words, the operation of this type of continuous kneading machine is generally performed based on the production volume, the rotation speed of the mixing rotor, the opening degree of the discharge orifice at the discharge port, the cooling conditions of the mixing chamber and the rotor, etc. When the number and cooling conditions are kept constant, the temperature and degree of kneading can be adjusted by the orifice opening, and the relationship between the orifice opening (θ) and the residence time (t) of the material inside the kneader is Second
The result will be as shown in the graph in the figure. That is, when the orifice opening becomes smaller, the material filling rate in the kneader increases due to the increase in discharge resistance, and the residence time becomes longer, thereby increasing the degree of kneading and increasing the temperature of the kneaded material. In addition, as shown in the same graph for the case of production volume Q1 and the case of production volume Q2 (Q1>Q2), the residence time can also be extended by reducing the production volume, but in this case, the residence time can be extended by reducing the production volume. This will reduce efficiency. In addition, lengthening the rotor will also increase the residence time, but this will also increase the temperature of the kneaded material, so if there is a limit to the temperature of the kneaded material, the orifice opening degree must be increased. It does not extend the residence time.

また、混練にあたつては、混練物の平均的な混
練度を向上することのほかに均一な混練を行うこ
とがさらに重要となる場合が多い。すなわち、例
えばフイルムグレードのポリオレフイン樹脂のフ
イツシユアイの問題やカーボンブラツク等の添加
については、全体的にフイルシユアイの数やカー
ボンブラツクの未分散粒子数を少なくすることも
大切であるが、少量であつても混練の不充分なも
のが混入して一定サイズ以上のフイツシユアイや
カーボン粒子が残ると、混練物の性質に悪影響を
与える。これを防止するには混練機中での材料の
滞溜時間を均一化し、材料が部分的にほとんどせ
ん断仕事を受けないで混練機を通過する所謂シヨ
ートパスを防がなければならないが、従来のこの
種連続式混練機では、シヨートパスを避け難く、
材料の部分的な滞溜時間のばらつきが大きくて、
前記の問題点を解消することができなかつた。こ
の問題点の解消を図るために、出願人は、バレル
内に装設される混練ロータの混練翼部に相当する
バレルの一部に該ロータに向つて移動する際に該
ロータとの接線方向の間隙を変化し得るように構
成した絞り機構を設け、該絞り機構によりバレル
内部空間を調節可能にしてなる構成の連続式混練
機を提案し(特開昭55−139825号)、その解決を
図つた。
Furthermore, during kneading, in addition to improving the average degree of kneading of the kneaded product, it is often even more important to perform uniform kneading. In other words, for example, regarding the problem of film-grade polyolefin resins and the addition of carbon black, it is important to reduce the overall number of film-eyes and the number of undispersed particles of carbon black, but even in small amounts, If insufficiently kneaded materials are mixed in and fisheye or carbon particles larger than a certain size remain, the properties of the kneaded product will be adversely affected. To prevent this, it is necessary to equalize the residence time of the material in the kneader and prevent the so-called short pass, where the material partially passes through the kneader with little shearing work. In continuous seed kneading machines, short passes are difficult to avoid.
There is a large variation in the local residence time of the material,
The above problems could not be solved. In order to solve this problem, the applicant has proposed that a portion of the barrel corresponding to the kneading blade of the kneading rotor installed in the barrel be moved in the tangential direction to the rotor when moving toward the rotor. We proposed a continuous kneading machine with a constriction mechanism configured to change the gap, and the internal space of the barrel could be adjusted by the constriction mechanism (Japanese Patent Application Laid-open No. 139825/1982), and found a solution to this problem. Figure.

前示の混練機では混練材料の滞溜時間及び混練
度を広範囲に調整することができ、また、平均滞
溜時間を延長することができるので、混練材料の
シヨートパスを防止することが可能となつて混練
物の品質を旧来機に増して向上し得る等の利点を
有していたが、本発明者等がさらに研究を重ねた
結果、先に提案した混練機より品質の向上が図れ
る混練機を見いだした。
In the above-mentioned kneading machine, the residence time and degree of kneading of the kneaded materials can be adjusted over a wide range, and the average residence time can be extended, making it possible to prevent short passes of the kneaded materials. However, as a result of further research by the present inventors, a kneading machine that can improve the quality of the kneaded product compared to the previously proposed kneading machine has been developed. I found it.

即ち、前示の混練機では、混練開始時では、絞
り機構のみでは、ロータと絞り部材との金属接触
のために焼付きなどのトラブルの原因になり、樹
脂洩れをおこして混練開始時の材料のロスが多く
なることが判明した。
In other words, in the above-mentioned kneading machine, when starting kneading, using only the squeezing mechanism causes problems such as seizure due to the metal contact between the rotor and the squeezing member, which causes resin leakage and reduces the quality of the material at the start of kneading. It was found that the loss of

本発明は、以上の諸点に鑑み発明されたもの
で、混練開始時とそれ以降に於ける混練性状を主
副のオリフイスにより行なうことを特徴とするも
ので、以下、図示の実施例に基づき詳述する。
The present invention was invented in view of the above points, and is characterized in that the kneading properties at the start of kneading and thereafter are controlled by main and sub-orifices. Describe.

第1図は混練機の混練時間と剪断速度との関係
を示すグラフ、第2図は連続混練機の吐出オリフ
イスの開度と材料滞溜時間との関係を示すグラ
フ、第3図乃至第10図は本発明連続式混練機の
実施例を示すもので、第3図は連続混練機全体を
示す縦断面図、第4図は第3図のA−A線に沿う
断面図、第5図乃至第7図は副オリフイス機構の
実施例を示す断面図、第8図は混練ロータの排出
部断面を示す拡大断面図、第9図及び第10図は
混練翼部分を示す断面図、第11図は、副オリフ
イス開度と混練押出物温度及びカーボン分散度指
数との関係を示すグラフである。
Figure 1 is a graph showing the relationship between the kneading time and shear rate of the kneading machine, Figure 2 is a graph showing the relationship between the opening degree of the discharge orifice of the continuous kneader and material residence time, and Figures 3 to 10 The figures show an embodiment of the continuous kneading machine of the present invention, in which Fig. 3 is a longitudinal sectional view showing the entire continuous kneading machine, Fig. 4 is a sectional view taken along line A-A in Fig. 3, and Fig. 5 7 to 7 are cross-sectional views showing an embodiment of the sub-orifice mechanism, FIG. 8 is an enlarged cross-sectional view showing a cross section of the discharge part of the kneading rotor, FIGS. 9 and 10 are cross-sectional views showing the kneading blade portion, and FIG. The figure is a graph showing the relationship between the opening degree of the sub-orifice, the temperature of the kneaded extrudate, and the carbon dispersion index.

第3図に示す通り、1,1は二軸のミキシング
用有翼ロータ、2は該両ロータ1,1を取囲むミ
キシングバレルである。上記ロータ1は材料移送
用のスクリユー部1aと混練翼部1bとを有し、
両ロータ1,1は適宜の駆動装備にて互いに異方
向に回転せしめられるように構成している。ま
た、バレル2は、両ロータ1,1に対応する実質
的に円筒状の並列な二つの室を連通一体化してな
る。該バレル2の装入端側には材料供給用のホツ
パー3を設け、他端側には、下向きに開口した開
度調節可能な吐出オリフイス4等を具備する吐出
口5が設けられている。
As shown in FIG. 3, 1, 1 is a biaxial mixing winged rotor, and 2 is a mixing barrel surrounding both rotors 1, 1. The rotor 1 has a screw part 1a for material transfer and a kneading blade part 1b,
Both rotors 1, 1 are configured to be rotated in mutually different directions by appropriate drive equipment. Further, the barrel 2 is formed by integrating two substantially cylindrical parallel chambers corresponding to the two rotors 1, 1 in communication with each other. A hopper 3 for supplying material is provided at the charging end of the barrel 2, and a discharge port 5 is provided at the other end, including a discharge orifice 4 which opens downward and whose opening degree can be adjusted.

更に、前記ロータ1,1の混練翼部1bに後続
して該ロータの外径に等しいかまた小径の断面円
形の絞り部1cと断面円形の排出部1dを設けて
いる。
Further, following the kneading blade portions 1b of the rotors 1, 1, there are provided a constriction portion 1c with a circular cross section and a discharge portion 1d with a circular cross section, each having a diameter equal to or smaller than the outer diameter of the rotor.

6は、前記ロータの絞り部1cに相応するバレ
ル2に配備された可動体であり、バレル2の他の
部分との間でシール状態を保ちながら、ロータ
1,1の軸方向と直角な接続方向へ移動可能に、
換言すれば、ロータ1,1に対して近接離間可能
に構成されている。
Reference numeral 6 denotes a movable body disposed in the barrel 2 corresponding to the constricted portion 1c of the rotor, and connects the rotors 1, 1 at right angles to the axial direction while maintaining a sealed state with other parts of the barrel 2. be able to move in the direction of
In other words, it is configured to be able to approach and separate from the rotors 1, 1.

可動体6の内面は、両ロータの外周に対応させ
て二つの円弧状部分が幅方向に連なる形状とな
す。
The inner surface of the movable body 6 has a shape in which two arcuate portions are connected in the width direction, corresponding to the outer peripheries of both rotors.

7は、前示の主オリフイス機構に於けるオリフ
イス4の開閉用の油圧シリンダである。
7 is a hydraulic cylinder for opening and closing the orifice 4 in the main orifice mechanism described above.

可動体6は、第4図乃至第7図に示す如く、バ
レル2の上部及び下部に設けることが絞り調節範
囲を広くする意味で良好である。
It is preferable to provide the movable body 6 at the upper and lower parts of the barrel 2, as shown in FIGS. 4 to 7, in order to widen the aperture adjustment range.

即ち、第4図の実施例では、絞り部6をバレル
2の上下位置に別体6a,6bとして配設すると
共に各々の可動体6の両側端にフランジ部8を形
成してなり、これらフランジ部8に先端部分だけ
ねじを刻設し、かつその他は平滑な部分を有する
締結ボルト9が貫通してバレル2に取付けられて
なり、更に、その近傍にバレル2の上部,下部に
先端が当接する如く距離調節用ボルト10が螺着
されてなるものであり、これらにより副オリフイ
ス機構を構成する。
That is, in the embodiment shown in FIG. 4, the throttle parts 6 are arranged as separate parts 6a and 6b at the upper and lower positions of the barrel 2, and flange parts 8 are formed at both ends of each movable body 6, and these flanges A fastening bolt 9 having a screw threaded only at the tip portion of the portion 8 and having a smooth portion on the other portion is passed through and attached to the barrel 2, and furthermore, the tips are attached to the upper and lower portions of the barrel 2 near the bolt 9. A distance adjusting bolt 10 is screwed so as to be in contact with each other, and these constitute a sub-orifice mechanism.

第5図は、副オリフイス機構の可動体6a,6
bを上下同時に連動させる場合の実施例であり、
上下の可動体6a,6bに相当する箇所のみねじ
11aを上下反対方向の移動する如く形成し、そ
の他は平滑とした調節ボルト11を上下の可動体
6a,6b並びにバレル2を貫通して両側に設け
てなり、これら調節ボルト11,11の上端部に
夫々プーリ12,12を固着すると共にこれらプ
ーリ相互間にチエーン、ベルト等の伝動帯13を
張架してある。
FIG. 5 shows movable bodies 6a, 6 of the sub-orifice mechanism.
This is an example where b is linked up and down at the same time,
Screws 11a are formed to move in opposite directions up and down only at the locations corresponding to the upper and lower movable bodies 6a and 6b, and smooth adjustment bolts 11 are inserted into both sides by passing through the upper and lower movable bodies 6a and 6b and the barrel 2. Pulleys 12, 12 are fixed to the upper ends of these adjustment bolts 11, 11, respectively, and a transmission band 13, such as a chain or belt, is stretched between these pulleys.

14は調節ボルト11の一方に固着したハンド
ルであり、手動にて該ハンドルを回転させること
により調節ボルト11を回転して可動体6a,6
bの位置関係を調整する。
14 is a handle fixed to one side of the adjustment bolt 11, and by manually rotating the handle, the adjustment bolt 11 is rotated, and the movable bodies 6a, 6 are rotated.
Adjust the positional relationship of b.

15はバレル2の側部に取付けた目盛りであ
り、上方の可動体6a側端に取付けた指針16が
対応する位置関係に設けている。
15 is a scale attached to the side of the barrel 2, and is provided in a positional relationship corresponding to the pointer 16 attached to the end of the upper movable body 6a.

第6図の実施例は、第4図の実施例にある構成
に第5図にある目盛り15と指針16を付設した
構成であり、また第7図の実施例は、可動体6
a,6bを単独又は同時に調整できる如く、バレ
ル2の上下に油圧シリンダ17a,17bを夫々
設け、該シリンダのピストンロツド18a,18
bの先端に可動体6a,6bを夫々螺着してなる
構成である。
The embodiment shown in FIG. 6 has a structure in which the scale 15 and pointer 16 shown in FIG. 5 are added to the structure shown in the embodiment shown in FIG. 4, and the embodiment shown in FIG.
Hydraulic cylinders 17a and 17b are provided on the upper and lower sides of the barrel 2, respectively, so that the piston rods 18a and 18 of the cylinders can be adjusted individually or simultaneously.
It has a structure in which movable bodies 6a and 6b are screwed onto the tips of b, respectively.

副オリフイス機構の構成は前示の通りである
が、本発明の混練機では混練ロータ1の排出部1
d箇所を第8図ABにある通り、排出する混練材
の発熱を極力避ける意味で、αだけの高さを有す
る突起部1eをバレル2内壁面と所定のチツプク
リアランスを有する状態にして設けたものであ
り、同図Bは180゜位相差を設けた位置に突起物
1eを2個設けた構成とする。
The configuration of the sub-orifice mechanism is as described above, but in the kneading machine of the present invention, the discharge part 1 of the kneading rotor 1
As shown in Fig. 8 AB, at point d, a protrusion 1e having a height of α is provided with a predetermined tip clearance with the inner wall surface of the barrel 2, in order to avoid heat generation of the kneaded material to be discharged as much as possible. Figure B shows a configuration in which two protrusions 1e are provided at positions with a 180° phase difference.

なお、ロータ1の有翼部分の断面形状として
は、第9図に示す如き2方向の翼1b、または第
10図に示す如き3方向の翼1b′を有する構造が
望ましく、材料を吐出側に推進する方向に捩れた
翼と押し戻す方向に捩れた翼または捩れない翼の
組合わせで有翼部分が構成される。
Note that the cross-sectional shape of the winged portion of the rotor 1 is preferably a structure having wings 1b in two directions as shown in FIG. 9, or wings 1b' in three directions as shown in FIG. The winged part is made up of a combination of wings twisted in the direction of propulsion and wings twisted in the direction of pushing back or wings that do not twist.

しかして、前記ホツパー3を通して連続定量的
に供給された材料は、バレル2内において、バレ
ル2内面とロータ1,1との間を通過する間にロ
ータ1,1の回転により溶融混練され、然る後、
吐出口5の吐出オリフイス4から連続的に排出さ
れるが、この場合、一般的にバレル2内の材料の
滞溜時間を長くするほどよく混練される。
Thus, the material continuously and quantitatively supplied through the hopper 3 is melted and kneaded by the rotation of the rotors 1, 1 while passing between the inner surface of the barrel 2 and the rotors 1, 1 in the barrel 2. After
The material is continuously discharged from the discharge orifice 4 of the discharge port 5, and in this case, generally, the longer the residence time of the material in the barrel 2, the better the kneading.

そして、本発明の混練機では、混練開始時には
出口箇所5のオリフイス機構4を油圧シリンダ7
で作動して全閉する。これは、ホツパ3より定量
供給された材料が未溶融の粉末状(powder)で
あるがため該オリフイス4を開放したまゝでは充
分な滞溜時間が混練機内で確保することができな
いので、未溶融の状態で排出される可能性が高
く、これを防止する理由からである。
In the kneading machine of the present invention, the orifice mechanism 4 at the outlet location 5 is connected to the hydraulic cylinder 7 at the start of kneading.
It operates and closes completely. This is because the material supplied quantitatively from the hopper 3 is in the form of unmelted powder, so if the orifice 4 is left open, sufficient residence time cannot be secured in the kneading machine. This is because there is a high possibility that it will be discharged in a molten state, and this is to be prevented.

混練開始時に混練機内に供給された材料が充分
に混練されたとみなされる時間の経過後に到れ
ば、前示の排出箇所5のオリフイス4を開放する
と共に、混練翼1cと排出部1dとの間に設けた
絞り部1cに設けた副オリフイスの可動体6を手
動にして調整し、該可動体6とロータ1の絞り部
1cとの間隙を調整して当該位置での材料通過空
間断面積を変化させる。
When the time has elapsed when it is considered that the materials supplied into the kneading machine at the start of kneading have been sufficiently kneaded, the orifice 4 of the above-mentioned discharge location 5 is opened, and the gap between the kneading blade 1c and the discharge portion 1d is opened. Manually adjust the movable body 6 of the auxiliary orifice provided in the constriction part 1c provided at change.

この場合、本発明の副オリフイス機構はロータ
1の絞り部1cが略断面円形としている関係上、
混練物材料が当該絞り部1cの円周上の回転体に
より調整するので、材料の溶融材料の性状からみ
て軸方向へ未混練のまま通過する度合が少なく、
充分な滞溜時間が採れ、もつて、混練機にあるシ
ヨートパスの現象が阻止でき、均一な混練物が得
られる。
In this case, since the auxiliary orifice mechanism of the present invention has a constricted portion 1c of the rotor 1 having a substantially circular cross section,
Since the kneaded material is adjusted by the rotating body on the circumference of the constricted part 1c, there is little chance of the material passing unkneaded in the axial direction, considering the properties of the molten material.
By providing sufficient residence time, the phenomenon of shot passes in the kneader can be prevented and a uniform kneaded product can be obtained.

<実施例> バレル内径 50mmφ 高圧ポリエチレン (MI=2)/カーボンブラ
ツク=74/26 生 産 量 60Kg/hr ロータ回転数 750RPM 主オリフイス 全開(27mm) の状態で、連続混練機に於いて、副オリフイス機
構を作動させた場合の混練物の温度並びにカーボ
ン分散度指数と同オリフイスの開度との関係を測
定したところ、第11図のグラフに示す通りの結
果を得た。
<Example> Barrel inner diameter 50mmφ High pressure polyethylene (MI=2)/carbon black=74/26 Production volume 60Kg/hr Rotor rotation speed 750RPM Main orifice fully open (27mm), sub orifice in continuous kneading machine When the temperature of the kneaded material and the relationship between the carbon dispersity index and the opening degree of the orifice were measured when the mechanism was operated, results as shown in the graph of FIG. 11 were obtained.

第11図のグラフによれば、主オリフイス機構
の開度を全開し、副オリフイスの開度を絞れば混
練物の温度は上昇し、カーボンの分散は向上して
いることが判る。
According to the graph in FIG. 11, it can be seen that by fully opening the main orifice mechanism and narrowing the opening of the auxiliary orifice, the temperature of the kneaded material increases and the dispersion of carbon improves.

これは、副オリフイスの開度調整により混練物
の練りの調節ができ、かつカーボン分散が向上
し、結局、この種混練機の問題点であるシヨート
パスが防止できる。
This allows adjustment of the kneading of the kneaded material by adjusting the opening degree of the sub-orifice, improves carbon dispersion, and ultimately prevents shot passes, which is a problem with this type of kneader.

叙上の如く、本発明の連続式混練機は、排出部
のオリフイスとは別個に、ロータの混練翼部と排
出部との間に断面円形の絞り部とこれに対応する
可動体とで構成する副オリフイスを設けた構成に
したので、混練材料が排出部直前に於いて混練物
の充満度が増加し、ロータチツプ部に喰い込まれ
る機会が増大すると共に混練物中に未分散粒子が
混入することが防止でき、結局、混練物の品質が
良好とできる。
As described above, the continuous kneading machine of the present invention includes a constriction part with a circular cross section and a corresponding movable body between the kneading blade part of the rotor and the discharge part, separately from the orifice of the discharge part. Since the structure is equipped with an auxiliary orifice, the degree of filling of the kneaded material increases immediately before the discharge section, increasing the chance that the kneaded material will be bitten into the rotor tip, and undispersed particles will be mixed into the kneaded material. As a result, the quality of the kneaded product can be improved.

更に、排出部のオリフイス機構だけでは充分で
なかつた混練物の温度を広範囲に調節することが
できるので、より一層の混練物の品質が改善でき
る。
Furthermore, since the temperature of the kneaded material can be adjusted over a wide range, which was not sufficient with the orifice mechanism of the discharge section alone, the quality of the kneaded material can be further improved.

また、ロータの排出部に突起物を設けてあるの
で、混練物の発熱を抑止することが可能なので混
練物の品質向上に一助となる。
Further, since the protrusions are provided on the discharge portion of the rotor, it is possible to suppress heat generation of the kneaded material, which helps improve the quality of the kneaded material.

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

第1図は混練機の混練時間と剪断速度との関係
を示すグラフ、第2図は連続混練機の吐出オリフ
イスの開度と材料滞溜時間との関係を示すグラ
フ、第3図乃至第10図は本発明連続式混練機の
実施例を示すもので、第3図は連続混練機全体を
示す縦断面図、第4図は第3図のA−A線に沿う
断面図、第5図乃至第7図は副オリフイス機構の
実施例を示す断面図、第8図は混練ロータの排出
部断面を示す拡大断面図、第9図及び第10図は
混練翼部分を示す断面図、第11図は、副オリフ
イス開度と混練押出物温度及びカーボン分散度指
数との関係を示すグラフである。 1……混練ロータ、2……混練機バレル、3…
…ホツパ、4……吐出オリフイス、5……吐出
口、6……絞り部材、7……油圧シリンダ、1
0,11……調整ボルト、12……プーリー、1
3……伝動帯、14……ハンドル。
Figure 1 is a graph showing the relationship between the kneading time and shear rate of the kneading machine, Figure 2 is a graph showing the relationship between the opening degree of the discharge orifice of the continuous kneader and material residence time, and Figures 3 to 10 The figures show an embodiment of the continuous kneading machine of the present invention, in which Fig. 3 is a longitudinal sectional view showing the entire continuous kneading machine, Fig. 4 is a sectional view taken along line A-A in Fig. 3, and Fig. 5 7 to 7 are cross-sectional views showing an embodiment of the sub-orifice mechanism, FIG. 8 is an enlarged cross-sectional view showing a cross section of the discharge part of the kneading rotor, FIGS. 9 and 10 are cross-sectional views showing the kneading blade portion, and FIG. The figure is a graph showing the relationship between the opening degree of the sub-orifice, the temperature of the kneaded extrudate, and the carbon dispersion index. 1...Kneading rotor, 2...Kneading machine barrel, 3...
...Hopper, 4...Discharge orifice, 5...Discharge port, 6...Aperture member, 7...Hydraulic cylinder, 1
0, 11...Adjustment bolt, 12...Pulley, 1
3...Transmission band, 14...Handle.

Claims (1)

【特許請求の範囲】 1 一端に材料供給口を他端に材料吐出口を有
し、断面が連通する2つの円であるバレルと1
と、材料供給口よりの材料を前方に送るスクリユ
ウ部1aと、送り翼戻し翼からなる混練部1b
と、材料吐出口に向かつて混練材料を送る排出部
1dを順次形成したロータからなり、該ロータは
バレル内に異方向回転状に2本配置されてなる2
軸連続式混練機において、バレルの材料吐出口は
ロータ軸方向に直角に開口し、この吐出口に開度
調整可能な第1の絞り部を設け、各ロータの混練
部と排出部の間にロータ外形に等しいか、または
小径の円形断面の材料通過部1cを設け、この材
料通過部を同心円状に囲む進退可能な2分割され
た可動体をバレルに取り付け、この材料通過部と
可動体で第2の絞り部を形成したことを特徴とす
る2軸連続式混練機。 2 ロータの排出部は、略円形断面の外周に設け
られた1以上の突起物により吐出口へ材料を送る
ようになつていることを特徴とする特許請求の範
囲第1項記載の2軸連続式混練機。
[Claims] 1. A barrel that has a material supply port at one end and a material discharge port at the other end, and whose cross section is two circles communicating with each other.
, a screw section 1a for forwarding the material from the material supply port, and a kneading section 1b consisting of sending and returning blades.
and a rotor in which a discharge portion 1d for feeding the kneaded material toward the material discharge port is sequentially formed, and two rotors are arranged inside the barrel to rotate in different directions.
In a shaft-continuous kneading machine, the material discharge port of the barrel opens at right angles to the rotor axis direction, and this discharge port is provided with a first constriction part whose opening degree can be adjusted, and a first throttle part is provided between the kneading part and the discharge part of each rotor. A material passage section 1c with a circular cross section equal to or smaller than the rotor outer diameter is provided, and a movable body divided into two parts concentrically surrounding this material passage section and movable back and forth is attached to the barrel, and this material passage section and the movable body A two-screw continuous kneading machine characterized by forming a second constricted part. 2. The two-axis continuous system according to claim 1, wherein the discharge part of the rotor is configured to send material to the discharge port by one or more protrusions provided on the outer periphery of a substantially circular cross section. Type kneading machine.
JP56073294A 1981-05-14 1981-05-14 Two-shaft continuous mixer Granted JPS57187022A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56073294A JPS57187022A (en) 1981-05-14 1981-05-14 Two-shaft continuous mixer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56073294A JPS57187022A (en) 1981-05-14 1981-05-14 Two-shaft continuous mixer

Publications (2)

Publication Number Publication Date
JPS57187022A JPS57187022A (en) 1982-11-17
JPS6246208B2 true JPS6246208B2 (en) 1987-10-01

Family

ID=13513989

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56073294A Granted JPS57187022A (en) 1981-05-14 1981-05-14 Two-shaft continuous mixer

Country Status (1)

Country Link
JP (1) JPS57187022A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3755513B1 (en) 2018-02-20 2023-07-05 COLMEC S.p.A. Method for operating a twin-screw mixer-extruder, including a presser body for defining a controlled volume of a compounding chamber

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0641135B2 (en) * 1989-04-04 1994-06-01 株式会社神戸製鋼所 Kneading control device for continuous kneader
US7674492B2 (en) * 2006-10-23 2010-03-09 Wenger Manufacturing, Inc. Preconditioner having independently driven high-speed mixer shafts
CN102173004B (en) * 2011-01-25 2013-02-20 青岛科技大学 Dual-rotor structure for continuous plastication of block-shaped rubbers and plastication device adopting rotors
JP6465091B2 (en) * 2016-09-30 2019-02-06 トヨタ自動車株式会社 Biaxial extrusion kneader and method for producing electrode paste using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3755513B1 (en) 2018-02-20 2023-07-05 COLMEC S.p.A. Method for operating a twin-screw mixer-extruder, including a presser body for defining a controlled volume of a compounding chamber

Also Published As

Publication number Publication date
JPS57187022A (en) 1982-11-17

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