JPS61261006A - Continuously kneading machine - Google Patents

Continuously kneading machine

Info

Publication number
JPS61261006A
JPS61261006A JP60104261A JP10426185A JPS61261006A JP S61261006 A JPS61261006 A JP S61261006A JP 60104261 A JP60104261 A JP 60104261A JP 10426185 A JP10426185 A JP 10426185A JP S61261006 A JPS61261006 A JP S61261006A
Authority
JP
Japan
Prior art keywords
rotor
chamber
bearing
kneading machine
section
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP60104261A
Other languages
Japanese (ja)
Inventor
Shinji Hashizume
慎治 橋爪
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 JP60104261A priority Critical patent/JPS61261006A/en
Publication of JPS61261006A publication Critical patent/JPS61261006A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • B29C48/365Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pumps, e.g. piston pumps
    • B29C48/37Gear pumps

Landscapes

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

Abstract

PURPOSE:To obtain the two axes continuing mixer having two layer floor type and the height of said floor remarkably lower than that of a usual machine by causing kneaded material to be water-exhausting type being able to discharge along the axial direction of a chamber and a rotor. CONSTITUTION:Material is continuously thrown in through a material-throwing inlet 3, while rotating a rotor 1, and the material is transferred into a kneading part 18 from a material sending part 17, and then is crashed to pieces, sheared and kneaded in molten state. The kneaded material is sent out to the side of a material-discharging part 19 by the thrust of a screw shaft. The material with pressure is successively exhausted under concentrically pushing from an exhausting mouth 14 through a passing space 15 provided at the side of a bear ing hausing 4 by way of the junction path 14a at chamber side. Accordingly, by connecting a die or a gear pump to this exhausting mouth 14 in series, a continuous mixer plus a die or the system of horizontal connecting in series of the gear pump may be easily obtained, whereby both initial and running costs may be remarkably reduced, and the control and maintenance management are also easily achieved.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、ロータ軸の両端がそれぞれベアリングによっ
て支持される両持構造の2軸ロータを持つ連続混練機の
改良に係る。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to an improvement of a continuous kneading machine having a two-shaft rotor with a dual-support structure in which both ends of the rotor shaft are supported by bearings.

〈従来技術〉 高分子物質の混練(同一物質のホモジナイジング化ある
いは異物質の混合または反J5)’を目的とした機械は
、大別して各種1軸押出機、同2軸押出機および混練押
出機の3つに別れる押出機系とオープンロール、パッチ
式混練機および連続混練機の6つに別れる混練機系との
2系統6種類に分類することができる。始めの6つに別
れる押出機系においても混練作用はあるが、その主目的
は押出作用を行なうことであり、混線作用は副次的な目
的に止まるのであり、こ几に対し後の6つに別れるロー
ル、混練機ではその主目的が混練作用に置かれることは
いうまでもない。またこれら機種における混練作用は、
既知のようic2壁間の相互作用(1壁固定で他の1壁
が運動する、あるいは2壁が別の運動をする)によって
生じる剪断作用によって、内部に充滴する材料に剪断力
を与え、目的の混線を行なわせようとするものである。
<Prior art> Machines for the purpose of kneading polymeric substances (homogenizing the same substance, mixing different substances, or anti-J5) are broadly classified into various types of single-screw extruders, co-twin-screw extruders, and kneading extruders. It can be classified into two systems and six types: an extruder system which is divided into three types, and a kneader system which is divided into six types: an open roll kneader, a patch type kneader, and a continuous kneader. Although the extruder system, which is divided into the first six types, also has a kneading effect, its main purpose is to perform the extrusion effect, and the cross-mixing effect is only a secondary purpose. It goes without saying that the main purpose of the rolls and kneading machines, which are divided into two types, is kneading. In addition, the kneading action in these models is
As is known, the shearing force generated by the interaction between two IC walls (one wall is fixed and the other wall moves, or two walls move in different ways) applies a shearing force to the material filling the inside, This is an attempt to cause the intended crosstalk.

前記した押出機系と、混練機系との領域における機構的
な相違としては、押出機系においてはその回軸(一般に
はスクリュ軸〕が軸受ベアリングによって軸一端を支持
される片持構造とされるに対し、混練機系ではその回転
軸(一般にはロールま+hロータ)が軸受ベアリングに
よって軸部+4#’i支持される両持構造とされる点で
ある。この理由は、混練機系の各機種においては、何れ
も大きな剪断作用を必要とするため、ロールあるいはロ
ータに発生する相互反力(ロール聞あるいはロータ間を
開くように働らく力)、あるいは外壁に対する曲げが大
きくなり、このため回転軸上両持構造とすることが必要
であり、かつこれによって回転軸の寿命を長くする効果
をもたらすのである。本発明は前記混練機系における特
に連続混練機を対象とするものであるが、連続混練ia
について仮りに定義付けをすれば、押出作用の有無は問
わず、1本以上の回転体から成る混練機であって、材料
を混練する回転体部分の軸方向両側に軸受ベアリング支
持構造を持つものと概括されるが、このような連続混練
機としては既知のように各種の機種が存在するが、その
最も一般的な連続混練機の1つを第1図に説示する。同
図に示されたものは米国7ア一レル社製のrFCMJと
通称される機種であって、水平かつ平行に対置される2
本のロータ131(図では1本のみで図示ロータの向う
側にもう1本のロータが存在する〕の1木はロング、他
の1木はショートとされ、ロングロータ(311は減速
機、電動機(図示省略)によって駆動され、図示のよう
にコネクチングギヤ金が付設され、このギヤから他方の
ショートロータ1B!+側に伝動され、これらロータc
111は図示のように駆動部7レーム側においてその一
端側が球面コロ軸受時關お工びスラスト軸受−によって
支持され、駆動部フレーム側にダストストップG51’
t−へてホッパ部側チャンバ内面が連続状かつ分離自在
にロータclIl!3Ilt−包囲して設けられ、ホッ
パ部間と対応するロータ6111311には材料送り用
のスクリュ軸部(31a)が形成さル、またチャンバ部
間と対応するロータ脂11311には前方翼、後方翼、
排出翼等の混練翼(31b)が形成され、ホッパ部曽か
ら連続的に供給される材料がスクリュ軸部(31a)を
介してチャンバ部靭内に連続的に供給され、このチャン
バ内で材料はロータチップ部とチャンバ内面との隙間を
通過する時にぜん断を受けて粉砕された後、溶融し、ね
じれ方向の異なる混練翼による前後方向の移動と20一
タ間の材料授受によって分散され、混練済み材料は図示
の回度可変なオリフィス關から連続的に排出されるので
あり、ロータet+!3幻の他方の軸端はスリーブ4Q
’を介して、球面コロ軸受lにより支持されるのであり
、(6)はダストストップ、(43はチャンバ部−の移
動用シリンダ、国はオリフィス關における開度可変装置
を示し、前記シリンダf43 Vcよってチャンバ部β
ηホッパ部例をダストストップ(6)位置から軸方向に
移動させ、チャンバ内面とロータ表面の清掃を行なうの
である。また−圓はロータallチャンバ部のηの冷却
をも行なう冷却装置を示し、特にこの型式ではチャンバ
の冷却機!’tドリルドサイド方式として冷却能力の向
上を企図しており、この冷却能力は材料の排出温度T 
dieおよび比エネルギーレベルEsルミ自由に変更で
きる機能を持っており、ホッパ部間には図示省略しであ
るが連続フィーダを接続して材料が連続的に供給さn、
エネルギーレベルを自由に変更できるようにロータ回転
数と処理量とは独立した変数どなっており、連続混練機
では前記フィーダから°供給される材料の量をそのまま
吐出するのであり、またロータ!311則の回転数は可
変であって材料の混線条件によって最適のジャーレート
の採用が可能であり、供給される材料の量と回転数は任
意+CC投打可能され、チャンバ部3η端において直角
方向に関口される吐出口であるオリフィス關のクリアラ
ンスθは可変であるが、θの値を変更しても吐出量は不
変で、オリフィス通過材料の速度が変化するに止まり、
開度可変のオリフィス關の機能は材料に与えるエネルギ
ーレベルを変更し得る点にある。
The mechanical difference between the extruder system and the kneader system described above is that in an extruder system, the rotating shaft (generally a screw shaft) has a cantilevered structure with one end of the shaft supported by a bearing. In contrast, in a kneader system, the rotating shaft (generally a roll or rotor) is supported by a bearing.The reason for this is that the kneader system Each model requires a large shearing action, which increases the mutual reaction force generated on the rolls or rotors (the force that acts to open the rolls or between the rotors), or the bending against the outer wall. It is necessary to have a double-support structure on the rotating shaft, and this has the effect of lengthening the life of the rotating shaft.The present invention is particularly directed to continuous kneading machines in the above-mentioned kneading machine system. , continuous kneading ia
If we were to define it, it would be a kneading machine that consists of one or more rotating bodies, regardless of whether or not it has an extrusion function, and that has bearing support structures on both axial sides of the rotating body that kneads materials. Although there are various known types of continuous kneading machines, one of the most common continuous kneading machines is shown in FIG. The model shown in the figure is a model commonly known as rFCMJ made by 7Arel Corporation in the United States, and two
One rotor 131 (in the figure, there is only one rotor, and there is another rotor on the other side of the illustrated rotor) is long, and the other one is short. (not shown), and a connecting gear is attached as shown in the figure, and the power is transmitted from this gear to the other short rotor 1B!+ side, and these rotors c
As shown in the figure, one end of 111 is supported by a spherical roller bearing on the frame side of the drive unit 7, and a thrust bearing made in conjunction with a spherical roller bearing, and a dust stop G51' is provided on the drive unit frame side.
t-The inner surface of the chamber on the hopper side is continuous and separable from the rotor clIl! 3Ilt-A screw shaft portion (31a) for feeding the material is formed on the rotor 6111311 which is surrounded and corresponds to between the hopper portions, and a front wing and a rear wing are formed on the rotor fat 11311 which corresponds to between the chamber portions. ,
A kneading blade (31b) such as a discharge blade is formed, and the material continuously supplied from the hopper part is continuously supplied into the chamber part through the screw shaft part (31a). When passing through the gap between the rotor tip and the inner surface of the chamber, the material is sheared and pulverized, and then melted and dispersed by moving back and forth by kneading blades with different twist directions and by transferring and receiving material between the 20 and 20 meters. The kneaded material is continuously discharged from the rotor et+! 3. The other shaft end of phantom is sleeve 4Q
(6) is a dust stop, (43 is a cylinder for moving the chamber part, and Japan is a variable opening device in relation to the orifice, and the cylinder f43 is supported by a spherical roller bearing l. Therefore, the chamber part β
The η hopper section is moved in the axial direction from the dust stop (6) position to clean the inner surface of the chamber and the surface of the rotor. Also, -en indicates a cooling device that also cools the rotor all chamber parts, especially in this model, a chamber cooling device! 't drilled side method is planned to improve the cooling capacity, and this cooling capacity is at the material discharge temperature T.
It has the function of freely changing the die and specific energy level, and a continuous feeder (not shown) is connected between the hopper sections to continuously supply materials.
The rotor rotation speed and throughput are independent variables so that the energy level can be changed freely, and in a continuous kneading machine, the amount of material fed from the feeder is directly discharged, and the rotor! The rotation speed according to the 311 rule is variable, and the optimum jar rate can be adopted depending on the material cross-circuit conditions. The clearance θ between the orifice, which is the discharge port to be closed, is variable, but even if the value of θ is changed, the discharge amount remains unchanged, and the only change is the speed of the material passing through the orifice.
The function of a variable orifice link is that the energy level imparted to the material can be varied.

〈発明が解決しようとする問題点〉 上記した代表例において見られる2軸連続混練機におけ
る問題点は次の点にある。即ち従来技術では、ロール乃
至ロータによる回転体(R)の両軸端t−第2図で示す
ようにベアリングCB) (B) V′cjつて固定し
、従ってベアリング(B) (B)間の回転体(R)の
所要位置で回転体@)上に材料を図示のように供給した
時には、材料の排出もまたベアリング(B)(B)間で
行なわねばならないことが必須とされる。このよりな必
要条件は、ベアリング彰)の内面側が回転体(R)に密
着する必要があり、かつベアリング(BJの外面がハウ
ジング内面に密着する構造から不可避的に生じるのであ
る。またこれら連続混練機においては、従来は何れも単
独に使用され、材料の流れ方向から見て上流側の材料フ
ィード部および下流側の材料ディスチャージ部は共に離
れて設けられ、その間において前者では固定材料、後者
では溶融材料が自由落下によって授受される型式となっ
ているが、最近では混練機+押出機という処理形態から
、混練機+ギヤポンプといり処理形態が開発され、押出
機に比べてギヤポンプは機械単品としてのイニシアルコ
ストおよびこれを用いた同一規模のプラントにおけるラ
ンニングコストにおいて、共に安価であるという大きな
利点を持っている。
<Problems to be Solved by the Invention> The problems with the two-screw continuous kneading machine seen in the above-mentioned representative examples are as follows. That is, in the prior art, both shaft ends t of the rotating body (R) by the roll or rotor are fixed at the bearing CB) (B) V'cj as shown in FIG. When the material is fed as shown onto the rotating body (R) at the desired position on the rotating body (R), it is essential that the material also be discharged between the bearings (B). This additional requirement arises unavoidably from the structure in which the inner surface of the bearing (BJ) needs to be in close contact with the rotating body (R), and the outer surface of the bearing (BJ) is in close contact with the inner surface of the housing. Conventionally, in a machine, both are used independently, and the upstream material feed section and the downstream material discharge section are provided separately when viewed from the material flow direction, and between them, the former is used to store fixed material, while the latter is used to store melted material. This is a type of system in which materials are delivered and received by free fall, but recently a processing system of kneading machine + gear pump has been developed from a processing system of kneading machine + extruder, and compared to extruder, gear pump is more efficient as a single machine. It has the great advantage of being inexpensive both in terms of initial cost and running cost in a plant of the same scale using it.

今従来の混練機+押出機システムと、混練機+ギヤポン
プシステムを′考えて見ると、第6図(幻(b) K示
すように、前者は(a)で示すように押出機(ET)は
1階707(I)[、混練機(M)C)は2階−yo7
(n)に、ま友原料フィーダ(FD)は3階フロア側の
ように、6層の設置フロアが最低必要であるに対し、後
者では同図(b)に示すように、孜@70アは2層で済
む力ζその高さHU前者の高さbtc比し大きく取るこ
とが必要とされ、更に混練機(MX)のための設置架台
(〜*t−必要とされ、建屋を含めたイニシアルコスト
の点で後者が前者に比し安価ではあるが、この(b)の
形me更に合理化することが可能ではないかと考えられ
る。
If we consider the conventional kneading machine + extruder system and the kneading machine + gear pump system, as shown in Figure 6 (phantom (b)), the former is an extruder (ET) as shown in (a). is on the 1st floor 707 (I) [, kneading machine (M)C) is on the 2nd floor -yo7
In (n), the Mayu raw material feeder (FD) requires a minimum of 6 installation floors, such as the 3rd floor, whereas in the latter case, as shown in the same figure (b), The force required for two layers ζ Its height HU needs to be larger than the height btc of the former, and the installation frame (~*t- is required, including the building) for the kneading machine (MX) Although the latter is cheaper than the former in terms of initial cost, it is thought that form (b) can be further rationalized.

く問題点を解決するための手段〉 本発明は従来技術における上記問題点を解決するために
なされ念ものであって、このため本発明においては、従
来の連続混練機においては、何五もその混練済み材料が
後続する材料によって押し出されるオリフィス+81部
分がチャンバ、ロータの軸方向に対し直角VC設けるこ
とを余儀なくされている事実に着目し、混練済み材料を
かかる垂直排出型からチャンバ、ロータの軸方向に沿っ
て排出できる水平排出型とすることにより、第4図に模
式的に示すよりに、混練機(MX)と例えばギヤボン7
’(GP)t−図示の通り水平方向に同一フロア上で直
結可能とし、こfLICよってフィーダ(FD)を含め
て2層フロア(IJ((1)形態とし、かつフロア高さ
ht−従来よりも著しく低いものとできるようにしたも
ので、具体的には、平行に対置された2本のロータ軸の
各軸上に材料送り部、材料混線部および材料排出部を設
けて成る2軸達続混練機において、前記材料排出部より
下流に両ロータ軸の各軸受ベアリングをロータ軸とのシ
ール構造を介して保持するとともに、両ロータ軸を包囲
するチャンバ内面と前記ベアリング外周との間において
ベアリング外@を迂回する混線済み材料の通過空間を備
えたハウジングをチャンバと一体に取付け、前記チャン
バにおける前記ロータ軸の軸受部よQ軸方向の前方位置
に、前記混練済み材料通過空間よりの材料の合流排出口
t′投けることにある。
Means for Solving the Problems> The present invention has been devised to solve the above problems in the prior art. Focusing on the fact that the orifice +81 part where the mixed material is pushed out by the following material is forced to be provided with a VC perpendicular to the axial direction of the chamber and rotor, By using a horizontal discharge type that can discharge along the direction, it is possible to mix the kneader (MX) and gear bone 7, for example, as shown schematically in Fig. 4.
'(GP) t - As shown in the figure, it is possible to connect directly on the same floor in the horizontal direction. Specifically, it is a two-shaft rotor shaft consisting of two parallel rotor shafts with a material feeding section, a material mixing section, and a material discharging section on each axis. In the continuous kneading machine, each bearing of both rotor shafts is held downstream from the material discharge section through a seal structure with the rotor shaft, and a bearing is held between the inner surface of the chamber surrounding both rotor shafts and the outer periphery of the bearing. A housing provided with a passage space for the mixed material to bypass the outside @ is installed integrally with the chamber, and a housing for the material from the mixed material passage space is installed at a position in front of the bearing part of the rotor shaft in the chamber in the Q-axis direction. The merging outlet t' is to be thrown.

く作  用〉 本発明の技術的手段によれば、!!!!5図および第6
図に示すように、2本のロータ(1)(11(図例では
1本のみ全示し、このロータ+11の向う側に他の1木
が平行して水平に対置されている)を既知のようにチャ
ンバ(2)内に配設し、チャンバ(2)の一端間側に設
けた材料投入口;3)ヲ上流側とし、これ工り図向って
右側を下流側とする。材料投入口(3)の上流側から各
ロータ(1)filの軸周には、第5図示のようにスク
リュ軸による材料送り部覇、捩れ翼による混練翼を既知
のように設けた材料混線部端を形成し、この材料混練部
端に続いて材料送り部σ力と同様、スクリュ軸VCよる
材料排出部叫勿連続状に形成し、このよ5なロータfi
lの前端側を軸受ベアリングによって可回*VC@叉す
るに当り、本発明においては、ロータ11+の前端部で
あるテーバエンド部tto)2テーパリング(9)ヲ介
してベアリング、1例ではラジアルベアリング[51K
よって支持する際、第5.6図示のよりに、チャンバ(
2)を横断して、チャンバ(2)と一体に組込まれるベ
アリングハクリング+411Cベアリング(51ヲ包囲
状に支持させ、チャンバ(21の内面とベアリング(6
1の外周との間において、ハクリング(4)に材料排出
部吐材料混練部端と連通する混練済み材料の通過空間σ
5)の複数個を、同ハウジング+41に形成するリプα
et介して、前記両ロータIINIIの各ベアリング+
51161を囲むように形成し、ITr記ハウジング(
4)のロータ(1)+11に向う面には、溶融材料がベ
アリング[51側に侵入するのを防シールリング(7)
を弾支バネ(8)とともに設けてシールし、更にチャン
バ12)の延長としてハクリング14)の前方(下流側
)Kアダプタoat設け、このアダプタ賭とハクリング
(4)の前面に付設し之ヘッドリング醤とI’(よって
、@記複数の混線済み材料の通過空間す5)を通過して
未た材料の合流路(14a)k持つ排出ロu4t−軸中
心位11に投けるのであり、こflCよって次の作用が
生じるのである。即ち第5凶において、ロータ+11 
fil ’i回転させるとともに、材料投入口+31か
ら連続的に材料を投入し、材料送り部σηより材料は混
練部(1報内へ移動され、既知のように混練翼を介して
材料の粉砕、剪断、溶融混練が従来の連続混練機と同様
に送られ、混線済み材料は連続的に供給される材料の材
料送り部σηにおけるスクリュ軸部の推力による排出能
力によって材料排出部端側に送り出さ几、ここから更に
liQ記ペアリングハウジング(4)側に友けた通過空
l11u51”へてチャンバ側の合流路f14a)i介
し排出口部から圧力に持って集中的に逐次押出し排出さ
れることになる。従ってこの排出口Hにダイ筐たはギヤ
ポンプを図示省略しであるが直結状に接続配置すること
によって、容易な圧力下で押出さ九る場合はダイによっ
て直ちに押出しが得ら九、また容易な圧力で押出されな
い場合は、ギヤポンプを経由しτ増圧し、ギヤポンプ下
流に付設したダイを介して押出すことが可能である。こ
のさい本発明混練機における排出口(I41VCおける
排出圧力は、ギヤポンプの吸引側に必要なサクション圧
力として好適に使われることになる。従って本発明混練
機によれば、先に第4図で示しな混練機+ギヤポンプの
レイアウトはきわめて容易に実施可能となるのである0 〈実施例〉 木発F!A混練機の適切な実施例を第5.6因について
説示する。I5図において示した実施例は要部のみを示
したに止まるが、ロータfil filの凶向って左方
には先に第1図で例示した連続混練機におけるドライブ
エンド部分の構造が用いら九ることは同様であり、チャ
ンバ(2)はドライブエンド部分の架構に対し同様に進
退移動自在に接続されて、駆動および清掃が可能である
ようにされる。即ち従来の連続混練機に比べ、本発明で
は材料混線部賭に続く材料排出部(1111以下の構造
、が相濫するものである。ハクリング(4)の全体形状
は第6図に例示さ几る通り、取付けるべきチャンバ(2
)の横断面形状と適合し、図示のようにチャン−・<m
の内面形状と対応し、かつベアリング(6)の外周を囲
むように、1例では6個の混練済み材料の通過空間06
4がリブQ句による仕切りを介し工事費に列設される。
According to the technical means of the present invention,! ! ! ! Figures 5 and 6
As shown in the figure, two rotors (1) (11 (in the figure, only one is fully shown, and on the other side of this rotor +11, another tree is placed horizontally in parallel) are arranged in a known manner. A material inlet 3) is disposed in the chamber (2) and provided between one end of the chamber (2); the material input port 3) is defined as the upstream side, and the right side as viewed from the drawing is defined as the downstream side. From the upstream side of the material input port (3) to the axial periphery of each rotor (1), as shown in Figure 5, there is a material feed section provided with a screw shaft, and a material mixing blade provided with a kneading blade using a twisted blade. Following the end of the material kneading section, a material discharging section by the screw shaft VC is formed in a continuous manner, similar to the material feeding section σ force, and a rotor fi of this type is formed.
In order to rotate the front end side of the rotor 11+ by a bearing, in the present invention, the front end of the rotor 11+, which is the tapered end part tto)2, is connected to the bearing via the tapered ring (9), in one example, a radial bearing. [51K
Therefore, when supporting the chamber (
2), the bearing Hakling+411C bearing (51) which is integrated with the chamber (2) is supported in an encircling manner, and the inner surface of the chamber (21) and the bearing (6
1, there is a passage space σ for the kneaded material that communicates with the end of the material discharge part and the material kneading part in the hack ring (4).
Reply α in which multiple pieces of 5) are formed in the same housing +41
Each bearing of both rotors IINII +
51161, and the ITr housing (
On the surface facing the rotor (1) +11 of 4), there is a seal ring (7) to prevent molten material from entering the bearing [51 side].
A K adapter oat is provided in front (downstream side) of the hack ring 14) as an extension of the chamber 12), and this adapter is attached to the front of the hack ring (4). It passes through the sauce and I' (therefore, the passage space 5 for multiple mixed materials) and is thrown into the discharge bowl U4t-axis center 11, which has a confluence path (14a) for unused materials. The following effects occur due to flC. That is, in the fifth evil, rotor +11
fil 'i is rotated, and the material is continuously inputted from the material input port +31, and the material is moved from the material feeding section ση into the kneading section (1 section), and as is known, the material is pulverized through the kneading blades. Shearing and melting and kneading are carried out in the same way as in a conventional continuous kneading machine, and the mixed material is sent out to the end of the material discharge section by the discharge capacity of the screw shaft in the material feed section ση of the continuously supplied material. From here, it is intensively pushed out and discharged under pressure from the discharge port section through the confluence path f14a)i on the chamber side to the passage space l11u51'' which is further connected to the pairing housing (4) side of liQ. .Therefore, by directly connecting and arranging a die casing or a gear pump (not shown) to this discharge port H, when extrusion is to be performed under easy pressure, extrusion can be immediately obtained by the die, and it is also easy to extrude. If it is not extruded at a certain pressure, it is possible to increase the pressure by τ via a gear pump and extrude it through a die attached downstream of the gear pump. Therefore, according to the kneading machine of the present invention, the kneading machine + gear pump layout shown in FIG. 4 can be implemented very easily. 0 <Example> An appropriate example of the Kihatsu F!A kneading machine will be explained regarding factor 5.6.The example shown in Fig. I5 only shows the main part, but the rotor fil. On the left side, the structure of the drive end part of the continuous kneading machine illustrated in FIG. In other words, compared to conventional continuous kneading machines, the present invention has a material discharging section (structure 1111 and below) that follows the material mixing section (structure 1111 and below) that conflict with each other. The overall shape of the hack ring (4) is as shown in Fig.
) is compatible with the cross-sectional shape of the chang-<m
In one example, six kneaded material passage spaces 06 correspond to the inner surface shape of the bearing (6) and surround the outer periphery of the bearing (6).
4 are arranged in the construction cost through the partition by the rib Q phrase.

その数は固より自由である。前記リプ川が通過空間(1
57と交互に存在していることにより、ハクリング(4
)に発生する力を充分受けられる構造強度が得られる。
The number is more flexible than fixed. The Lipu River passes through space (1
By existing alternately with 57, Hackling (4
) can provide sufficient structural strength to withstand the forces generated.

またシールリング(7)はロータ[11の材料排出部1
191の流れ方向前端にバネ(81ヲ介し弾接すること
によって、溶融状惑の混練済み材料がベアリング(51
内に侵入するのを防止しているが、この防止構造はハク
リング(4)の広い面を利用して容易にかつ自由に設計
可能である。合流路(14a)を有する排出口部を形成
する一fcめの外側のアダプタ賎はチャンバ(2)の延
長構造として形成され、ポルH2O1等でハクリング(
4)とともにチャンバ(2)側に一体に組立てられ、ま
虎このアダプタ(131と対応するヘッドリング(12
+はハクリング(4)に付属する部材としてかつベアリ
ング(51テーバリング(9)テーパエンド+101側
七叉持しかつ混練済み材料の侵入防止を兼ねるものとし
て、ハクリング(4)に例えばネジ込み等によって固定
され、ヘッドリング(14の外面、アダプタ031の内
面を適宜加工して合流路(14a)が形成さ几るように
する。またハクリング+4HCはベアリング(5)への
潤滑油注入口1B)が図示のようVC設けらnるととも
に長時間運転TiC際して予想さ九る若干の材料漏れ排
出口(11)が設けられ、これらは何れも前記リプae
+’を利用して形成する。尚チャンバ(2)は先に述べ
友ように軸方向の移動が可能であるため、テーバリンク
taトロータ111のテーパエンド10間のクリアラン
スがmtm可能で、こ九によりシールリング(7]のシ
ール面圧の調整が可能となっている。
Further, the seal ring (7) is attached to the material discharge portion 1 of the rotor [11].
By coming into elastic contact with the front end of the bearing (51) in the flow direction through the spring (81), the kneaded material in the molten state is brought into contact with the front end of the bearing (51).
This preventive structure can be easily and freely designed by utilizing the wide surface of the hack ring (4). The first fc outer adapter cap, which forms the discharge port having the confluence channel (14a), is formed as an extension of the chamber (2), and is hacked with Pol H2O1 or the like.
4) on the chamber (2) side, and the adapter (131) and the corresponding head ring (12
+ is fixed to the hack ring (4) by screwing, for example, as a member attached to the hack ring (4) and also as a bearing (51 taper ring (9) taper end + 101 side seven-pronged support and also to prevent the intrusion of the mixed material). , the outer surface of the head ring (14) and the inner surface of the adapter 031 are processed appropriately to form a merging path (14a). Also, for the Hakling +4HC, the lubricating oil inlet 1B to the bearing (5) is In addition to providing a VC, there are also some material leakage outlets (11) that are expected to occur during long-term operation of the TiC, both of which are connected to the above-mentioned lip ae.
Form using +'. In addition, since the chamber (2) is movable in the axial direction as mentioned earlier, the clearance between the tapered ends 10 of the taper link ta rotor 111 can be mtm, and this allows the sealing surface pressure of the seal ring (7) to be reduced by mtm. Adjustment is possible.

本発明の混練機に2いて、ギヤポンプ七排出口圓側に配
置する場合、ギヤポンプのサクション圧力は一般VC+
o*/iを越えることはないので、混練機における材料
送り部(171VCおける推力を、排出口(I41VC
おける材料圧が最高10Kg/cIIとなるようにI4
置けば、ギヤポンプのサクション圧力を補充するものと
して、好適である。またこの排出口部の直前に、材料に
付加するエネルギーレベルヲ変える目的で、流路断面を
可変とする構造を設けることができる。第5図に示した
排出口部の近傍に、例えば流路と垂直にネジを設け、そ
のネジを締め込むことによって流路を狭くするような、
流FjI!r全自動的にかつ連続してそり面積1に変更
できる構造乃至装@t−投ければ、これに工って混練機
内部の材料の充満度全変更し、材料に加えられるエネル
ギーレベルを自在に変化でき、混練度のコントロールが
可能となるのである。
When the kneading machine of the present invention is installed on the side of the gear pump 7 discharge port, the suction pressure of the gear pump is generally VC +
o*/i, the thrust at the material feed section (171VC) of the kneader is transferred to the discharge port (I41VC
I4 so that the material pressure at the
If installed, it is suitable for replenishing the suction pressure of the gear pump. Immediately in front of this discharge port, a structure can be provided that allows the cross section of the flow path to be varied in order to change the energy level added to the material. For example, a screw is installed perpendicular to the flow path near the outlet shown in FIG. 5, and the flow path is narrowed by tightening the screw.
Style FjI! rA structure or device that can fully automatically and continuously change the warping area to 1. If you use this, you can change the fullness of the material inside the kneading machine and freely control the energy level applied to the material. This allows the degree of kneading to be controlled.

〈発明の効果〉 本発F!Aによれば、従来の連続混練機において不可避
とされていた混練品軸方向と直角方向に混練済み材料を
落下排出させる垂直吐出しに対し、本発明では混練済み
材料全混練部軸方向にそのままかつ加圧下に押出す水平
吐出しか容易に可能であり、この几め従来の連続混練機
+押出機あるいは連続混練機十ギヤポンプにおける建屋
を含めての設置空間の高いこと、多層フロア構成による
据付設置の面倒をなくし、連続混練機+ダイあるいはギ
ヤポンプの水平直結方式が容易に可能となり、イニシア
ル、ランニングコストの何れをも著しく低減でき、力・
つ機械制御、保守管理もきわめて容易化されることにな
り、実用的に多用されている連続混練機の問題点全解決
し、更にその利用価値を高めるものとして優れたもので
ある。
<Effect of the invention> Original F! According to A, in contrast to the vertical discharge in which the kneaded material is dropped and discharged in a direction perpendicular to the axial direction of the kneaded product, which was considered unavoidable in conventional continuous kneading machines, in the present invention, the kneaded material is discharged as it is in the axial direction of the entire kneading part. In addition, only horizontal discharge of extrusion under pressure is easily possible, and this method requires a high installation space including the building for conventional continuous kneading machines + extruders or continuous kneading machines with 10 gear pumps, and installation due to the multi-layer floor structure. This eliminates the trouble of horizontally connecting a continuous kneading machine + die or gear pump, significantly reducing both initial and running costs, and reducing force and
Machine control and maintenance management are also made extremely easy, and this is an excellent product that solves all of the problems of continuous kneading machines that are widely used in practice, and further increases its utility value.

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

第1図は従来の連続混練機1例の縦断正面図、I!12
図は両持構造の説明図、第5図は従来の混練機据付プラ
ントの模式図、第4図は本発明混練機据付プラントの模
式図、第5図は同混練機実流側の要部縦断正面図、第6
図は第5図A−A線断面図である。 +11・・・ロータ、(2]・・・チャンバ、(3)・
・・材料投入口、(4)・・・ベアリングハクリング、
(51・・・ベアリング、(71・・・シールリング、
(9)・・・テーパリング、 1101・・・テーパエ
ンド、 U2I・・・ヘッドリング、賭・・・アダプタ
、(14I・・・材料排出口、051・・・材料通過空
間、殉・・・リプ、■・・・材料送り部、081・・・
材料混練部、す9)・・・材料排出部。
Figure 1 is a longitudinal sectional front view of an example of a conventional continuous kneading machine, I! 12
The figure is an explanatory diagram of the dual support structure, Figure 5 is a schematic diagram of a conventional kneader installation plant, Figure 4 is a schematic diagram of a kneader installation plant of the present invention, and Figure 5 is a main part of the actual flow side of the kneader. Vertical front view, No. 6
The figure is a sectional view taken along the line A-A in FIG. +11...Rotor, (2)...Chamber, (3)・
...Material input port, (4)...Bearing hack ring,
(51...Bearing, (71...Seal ring,
(9)...Taper ring, 1101...Taper end, U2I...Head ring, Brace...Adapter, (14I...Material discharge port, 051...Material passage space, Martyr...Rep ,■...Material feed section, 081...
Material kneading section, 9)...Material discharge section.

Claims (1)

【特許請求の範囲】 1、平行に対置された2本のロータ軸の各軸上に材料送
り部、材料混練部および材料排出部を設けて成る2軸連
続混練機において、前記材料排出部より下流に両ロータ
軸の各軸受ベアリングをロータ軸とのシール構造を介し
て保持するとともに、両ロータ軸を包囲するチャンバ内
面と前記ベアリング外周との間においてベアリング部を
迂回する混練済み材料の通過空間を備えたハウジングを
チャンバと一体に取付け、前記チャンバにおける前記ロ
ータ軸の軸受部より軸方向の前方位置に、前記混練済み
材料通過空間よりの材料の合流排出口を設けることを特
徴とする連続混練機。 2、前記材料排出部において材料に与えられる推力が前
記合流排出口において最高10kg/cm^2の材料圧
を持つことを特徴とする特許請求の範囲第1項記載の連
続混練機。 3、前記合流排出口直前に材料流路の連続断面積可変装
置を設けることにより、混練機内部の材料に加えられる
エネルギーレベルの設定自在とされることを特徴とする
特許請求の範囲第1項記載の連続混練機。 4、前記合流排出口を同一フロア上で直接ギヤポンプに
連結することにより、高分子材料を混練、押出すことを
特徴とする特許請求の範囲第1項記載の連続混練機。
[Claims] 1. In a two-shaft continuous kneading machine comprising a material feeding section, a material kneading section, and a material discharging section provided on each of two rotor shafts arranged in parallel to each other, from the material discharging section. A passage space for the mixed material that holds each bearing of both rotor shafts downstream through a seal structure with the rotor shaft, and that bypasses the bearing section between the inner surface of the chamber that surrounds both rotor shafts and the outer periphery of the bearing. The continuous kneading method is characterized in that a housing is integrally attached to a chamber, and a confluence/discharge port for the material from the kneaded material passage space is provided in the chamber at a position axially forward of the bearing portion of the rotor shaft. Machine. 2. The continuous kneading machine according to claim 1, wherein the thrust force applied to the material at the material discharge section has a maximum material pressure of 10 kg/cm^2 at the combined discharge port. 3. The energy level applied to the material inside the kneading machine can be set freely by providing a device for continuously varying the cross-sectional area of the material flow path immediately before the confluence/discharge port. Continuous kneading machine as described. 4. The continuous kneading machine according to claim 1, wherein the polymer material is kneaded and extruded by directly connecting the combined discharge port to a gear pump on the same floor.
JP60104261A 1985-05-15 1985-05-15 Continuously kneading machine Pending JPS61261006A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60104261A JPS61261006A (en) 1985-05-15 1985-05-15 Continuously kneading machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60104261A JPS61261006A (en) 1985-05-15 1985-05-15 Continuously kneading machine

Publications (1)

Publication Number Publication Date
JPS61261006A true JPS61261006A (en) 1986-11-19

Family

ID=14375985

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60104261A Pending JPS61261006A (en) 1985-05-15 1985-05-15 Continuously kneading machine

Country Status (1)

Country Link
JP (1) JPS61261006A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7350960B2 (en) * 2004-07-07 2008-04-01 Tech. Process & Engineering, Inc. Dual flight rotors for continuous mixer assembly

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7350960B2 (en) * 2004-07-07 2008-04-01 Tech. Process & Engineering, Inc. Dual flight rotors for continuous mixer assembly

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