JPS6328609A - Inclined type continuous kneading device - Google Patents

Inclined type continuous kneading device

Info

Publication number
JPS6328609A
JPS6328609A JP61172096A JP17209686A JPS6328609A JP S6328609 A JPS6328609 A JP S6328609A JP 61172096 A JP61172096 A JP 61172096A JP 17209686 A JP17209686 A JP 17209686A JP S6328609 A JPS6328609 A JP S6328609A
Authority
JP
Japan
Prior art keywords
mixing chamber
gear pump
rotors
discharge port
supply port
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP61172096A
Other languages
Japanese (ja)
Other versions
JPH0338089B2 (en
Inventor
Yasuji Orimo
折茂 泰而
Futashi Fukui
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 JP61172096A priority Critical patent/JPS6328609A/en
Publication of JPS6328609A publication Critical patent/JPS6328609A/en
Publication of JPH0338089B2 publication Critical patent/JPH0338089B2/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
    • 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
    • B29C48/27Cleaning; Purging; Avoiding contamination

Abstract

PURPOSE:To dissolve the trouble of difficult maintenance of a gear pump by a method wherein a mixing chamber, in which flighted screw rotors are contained, is titled together with an outer shell main drum. CONSTITUTION:Plastic material, which is continuously supplied from a vertically upward open material supplying port 8, is filled over two rotors 7, which are disposed in an array in oblique direction, so as to be advanced in a mixing chamber 6 by the pivoting of the rotors 7 and feeder screw flights 10. The plastic material is kneaded at the gap made between the screw flight 10 and the inner surface of the mixing chamber 6 so as to be melted and plasticized in order to be flowed through a discharge port 9 and metered and pressure-fed with a gear pump 4. Next, the plastic material is extruded from a forming die and cut through the rotation of a high speed cutter so as to be granulated into the form of pellets. Because the mixing chamber 6 is tilted, the uniform supplying distribution of material to the two rotors 7 is made possible.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、排出制御用ギヤポンプを五線済み材料の排出
口に直結するタイプの連続混練装置の改善に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an improvement in a continuous kneading device of the type in which a gear pump for controlling discharge is directly connected to a discharge port for stuffed material.

(従来の技術) プラスチック、ゴム等の各種高分子材料や可塑性材料の
混練を行なう連続混練機乃至装置は、いうまでもなくよ
く知られている処であり、一般的にその構成は、長手方
向の両端に被混線材料の供給口と混練済み材料の排出口
とが設けられる混合室内に、材料の移動および混練を行
なうスクリュ羽根を軸長方向周面に形成した回転ロータ
の一対が平行に並設され、混合室を囲む外殻主胴にヒー
タ等の加熱あるいは冷却の熱処理手段が付設されたもの
であり、供給口から投入された材料は回転ロータにおけ
るフィード用スクリュ羽根によって前方に移動されて混
練部に入り、同ロータにおける撹拌混練用スクリュ羽根
によって混練されて、溶融状態下に排出口から排出され
、このさい既知のように混合室内における材料の移動は
、投入口から連続的に投入される材料によって後方から
押されて前方に逐次移動されるもので、混合室内部圧力
の制御は排出口側に設けられる排出制御手段によって行
なうのである。かかる排出制御手段の1つとして材料排
出口にギヤポンプを直結する型式も既知であり、例えば
特公昭56−3091号公報に開示されたものがそれで
ある。以下第8図および第9図について、本発明と対応
する要部のみを説示する。即ち水平横向きに置かれた連
続混練機の外殻主胴1には、平行されかつ中央部分で連
通ずる2個の円筒状断面の混合室2が形成され、混合室
2の長手方向一端には被混線材料の供給口5が上向き開
口状に設けられるとともに、他端には混練済み材料の排
出口3が下向き開口状に設けられ、混合室2内にはスク
リュ羽根を有するロータ4,4の一対が平行状かつ可回
動に装設され、前記材料排出口3には排出制御手段とし
てのギヤポンプ26が直結されるのである。またかかる
連続混′t7L装置においては、単に被混線材料を混練
して完結するものでなく、溶融流動状態とされた混練済
み材料は、例えば第9図に示すように、ペレタイザー(
造粒装置)その他の成形機28とギヤポンプ26の吐出
口とを移送管路29によって連結し、混練済み材料を目
的の成形製品化するのであり、このさい各機械高さの関
係上、ギヤポンプ26を含む混練機側を2階建て建屋の
2階フロア30上に設置し、移送管路29を含む成形機
28側は1階フロア31上に分離状に設置することを余
儀なくされることも既知である。かかる従来技術におけ
る2階建て構成の不利を解消するために、第10図に示
すような新しい連続混練装置も開発されている(モダン
・プラスチックス・インタナショナル誌、1985年6
月号登載・・・・・・ファーレル社)。即ち図示のよう
に外殻主胴1と混合室2およびロータ4,4とから成る
混練機を、第8.9図に示した水平横向きの姿勢から9
0度変向して垂直縦向きの姿勢として設置し、材料供給
口5は上向き開口させるに反し、混練済みの材料排出口
3は横向きに開口させ、同排出口3にギヤポンプ26を
直結するとともに、このギヤポンプ26に成形機28を
直結する方式であり、これによって必要な一連の設備を
1階フロア31上に設置可能としたものである。
(Prior Art) Continuous kneading machines and devices for kneading various polymer materials and plastic materials such as plastics and rubber are, needless to say, well-known, and are generally configured in the longitudinal direction. A pair of rotating rotors having screw blades formed on the circumferential surface in the axial direction for moving and kneading the materials are arranged in parallel in the mixing chamber, which has a supply port for the materials to be mixed and a discharge port for the mixed materials at both ends. A heating or cooling heat treatment means such as a heater is attached to the main outer shell surrounding the mixing chamber, and the material input from the supply port is moved forward by the feed screw blade in the rotating rotor. The material enters the kneading section, is kneaded by the stirring and kneading screw blades in the same rotor, and is discharged from the discharge port in a molten state.At this time, as is known, the movement of the material in the mixing chamber is carried out continuously through the input port. The mixing chamber is pushed from the rear by the material and sequentially moved forward, and the internal pressure of the mixing chamber is controlled by a discharge control means provided on the discharge port side. As one such discharge control means, a type in which a gear pump is directly connected to the material discharge port is also known, such as the one disclosed in Japanese Patent Publication No. 56-3091. 8 and 9, only the main parts corresponding to the present invention will be explained below. That is, in the main outer shell 1 of the continuous kneading machine placed horizontally, there are formed two mixing chambers 2 with cylindrical cross sections that are parallel to each other and communicate with each other at the center. A supply port 5 for the material to be mixed is provided with an upward opening, and at the other end, a discharge port 3 for the mixed material is provided with a downward opening. A pair of pumps are installed in a parallel and rotatable manner, and a gear pump 26 as a discharge control means is directly connected to the material discharge port 3. In addition, in such a continuous mixing device, the material to be mixed is not simply kneaded, but the mixed material in a melted and fluidized state is transferred to a pelletizer (for example, as shown in FIG. 9).
(Pelletizer) The other molding machine 28 and the discharge port of the gear pump 26 are connected by a transfer pipe 29 to turn the kneaded material into the desired molded product.Due to the height of each machine, the gear pump 26 It is also known that the kneading machine side including the kneading machine must be installed on the second floor 30 of a two-story building, and the molding machine 28 side including the transfer pipe 29 must be installed separately on the first floor 31. It is. In order to overcome the disadvantages of the two-story structure in the prior art, a new continuous kneading device as shown in Figure 10 has been developed (Modern Plastics International, June 1985).
Published in the monthly issue (Farrell Publishing). That is, as shown in the figure, the kneading machine consisting of the outer shell main body 1, the mixing chamber 2, and the rotors 4, 4 is moved from the horizontal position shown in Fig. 8.9 to 9.
The material supply port 5 is opened upward, while the kneaded material discharge port 3 is opened horizontally, and a gear pump 26 is directly connected to the discharge port 3. The molding machine 28 is directly connected to the gear pump 26, thereby making it possible to install a series of necessary equipment on the first floor 31.

(発明が解決しようとする問題点) 上記した従来技術においては次の点においてそれぞれ問
題点が存在する。ギヤポンプを具備した連続混練装置と
して基準的な第8.9図に示された従来技術においては
、いうまでもなく機械高さが高くなること、これによる
2階建て建屋の必要によるイニシアルコストの増大、機
械全体の保守、操業管理の面倒、特に混練機直下に入っ
てしまうギヤポンプのメンテナンスの困難、更には成形
機28側とギヤポンプ26との連絡通路である移動管路
29の長大化、従ってその排出圧力の増大、無用な発熱
トラブルの発生等において問題点があり、また第10図
に示した改善された従来技術においては、機械高さの減
少はこれを認め得るとしても、連続混練機を90度変向
させて垂直縦向きとすることは、この種?gYi機にお
いて最も効率的として多用されている処の、水平方向に
平行して並列している1対の回転ロータ4,4が、垂直
方向の上下に並列する姿勢となり、このことは材料供給
口5から被混線材料を投入供給するに当り、材料は上位
のロータ4側にのみ供給されることとなって、混合室お
よび2軸ロ一タ間における材料の充満度に不均衡を生じ
るとともに、このことは材料温度のムラをも生じる結果
となり、均質な混練内容を得ることが難しい点において
問題点がある。
(Problems to be Solved by the Invention) The above-mentioned conventional techniques each have the following problems. In the conventional technology shown in Fig. 8.9, which is a standard continuous kneading device equipped with a gear pump, it goes without saying that the height of the machine increases and the initial cost increases due to the need for a two-story building. , maintenance of the entire machine and operation management are troublesome, and in particular, maintenance of the gear pump that is installed directly below the kneading machine is difficult.Furthermore, the transfer pipe 29, which is a communication passage between the molding machine 28 side and the gear pump 26, is becoming longer, and therefore, the There are problems such as an increase in discharge pressure and the occurrence of unnecessary heat generation troubles.Also, in the improved conventional technology shown in Fig. 10, although the reduction in machine height can be acknowledged, it is difficult to use a continuous kneading machine. Is this kind of thing possible to turn it 90 degrees and make it vertical? The pair of rotating rotors 4, 4, which are most efficiently used in the gYi machine and are parallel to each other in the horizontal direction, are placed in parallel vertically, and this means that the material supply port When the material to be mixed is supplied from the mixing chamber 5, the material is supplied only to the upper rotor 4 side, causing an imbalance in the filling degree of the material between the mixing chamber and the two-shaft rotor. This also results in unevenness in the temperature of the material, which poses a problem in that it is difficult to obtain homogeneous kneading contents.

(問題点を解決するための手段) 本発明は、これらの問題点を解決するために、かかる連
続混練装置の主体部分である回転ロータを含む混合室全
体を水平方向に対し1頃斜させるようにしたものであり
、具体的には、長手方向の両端に被混線材料の供給口と
混練済み材料の排出口とが設けられる混合室内に材料の
移動および混練を行なうスクリュ羽根ロータを可回動に
装設するとともに、前記材料排出口に排出制御用ギヤポ
ンプを直結する連続混練装置において、前記スクリュ羽
根ロータを含む混合室が水平方向に対し傾斜した横向き
姿勢に設置され、前記材料供給口は鉛直方向に開設され
るとともに材料排出口は水平方向に開設され、該排出口
にギヤポンプを直結することにある。
(Means for Solving the Problems) In order to solve these problems, the present invention provides a method in which the entire mixing chamber including the rotating rotor, which is the main part of the continuous kneading device, is tilted about 1° with respect to the horizontal direction. Specifically, the screw blade rotor that moves and kneads the materials into the mixing chamber, which has a supply port for the materials to be mixed and a discharge port for the mixed materials at both longitudinal ends, is rotatable. In a continuous kneading device in which a gear pump for discharge control is directly connected to the material discharge port, the mixing chamber including the screw blade rotor is installed in a horizontal position inclined with respect to the horizontal direction, and the material supply port is arranged in a vertical direction. The material outlet is opened in the horizontal direction, and the material outlet is opened in the horizontal direction, and a gear pump is directly connected to the outlet.

(作  用) 本発明の前記した技術的手段によれば、第1図乃至第7
図に亘って示すように、連続混練機3の主体部分である
処の、一対のスクリュ羽根ロータ7.7を平行にかつ可
回動に装設した混合室6を内部に有する横長の外殻主胴
11を、第6図に示すような目的の床面12上に固定的
に設置するに当り、前記両ロータ7を含む混合室6が床
面12と平行する水平方向に対して、図例では456の
傾斜角のもとに、傾斜した横向き姿勢下に外殻主胴11
とともに設置されるのであり、更に前記混合室6の長手
方向一端に連通状に設ける被混線材料の供給口8は第4
図示のように鉛直方向の上向きに開口する供給口とされ
るとともに、混合室6の長手方向他端に連通状に設ける
混練済み材料の排出口9は、第6図示のように混合室6
の45°角の傾斜に伴って斜め下方に開口されるのを、
更に45″角変向させて水平方向に向って横向きに形成
し、この水平方向に向かう一端にギヤポンプ4を直結す
ることによって、次の作用が得られる。即ち第1図は本
発明に係る45°角傾斜して床面12上に設置した連続
混練機3における水平方向の横向きとされた混練済みの
材料排出口9に直結したギヤポンプ4に、目的の成形機
の1例としてペレタイザー(造粒装置)5を連結したも
のを示しているが、第1図および第6閣に示されるよう
に、45°角の傾斜配設によって、第8.9図に示した
水平横向き型式の場合、2階に連続式混練機、1階に成
形機28のように装置を上下両階に分設する必要なく、
1隋床面である床面12上に全体を平面的に連結配設で
きることになり、これは混合室6を傾斜させるとともに
排出口9を水平方向に向わせることにより、ギヤポンプ
4を同一平面上に並設可能として、機構全高をより低く
することにより、容易に可能となるのである。更に本発
明では、傾斜させた混合室6における材料供給口8を鉛
直方向に開口することにより、同供給口8から被混線材
料を投入供給した場合、一対のロータ7.7は傾斜線上
に並列して両ロータ7.7は上面に向って共に路呈され
、第10図に示したロータが鉛直方向において上下に並
び、上位のロータのみが露呈することなく、投入された
材料は斜め上下方向に並列する両ロータ7.7に直接連
帯的に供給され、斜め上位のロータ7側の受入面積は若
干大きいが、役人材料は自重によって下側に落下し易い
ので、45°角の傾斜によって、両ロータ7.7側に同
一量が給与されることになり、これが混合室6内に充満
しつつ、移動、混練作用を受けるため、充満度の不均一
や材料の温度ムラ等の欠陥の生じるおそれなく、均質な
溶融混練結果を維持できるのである。
(Function) According to the above-mentioned technical means of the present invention, FIGS.
As shown in the figures, the main part of the continuous kneading machine 3 is an oblong outer shell having a mixing chamber 6 inside which is equipped with a pair of screw blade rotors 7.7 in parallel and rotatable manner. When the main body 11 is fixedly installed on the target floor surface 12 as shown in FIG. In the example, under an inclination angle of 456, the outer main body 11 is placed in a tilted horizontal position.
Furthermore, a fourth supply port 8 for the material to be mixed is provided in communication with one longitudinal end of the mixing chamber 6.
As shown in the figure, the supply port opens upward in the vertical direction, and the discharge port 9 for the kneaded materials provided in communication with the other longitudinal end of the mixing chamber 6 is connected to the mixing chamber 6 as shown in the sixth figure.
The opening is diagonally downward due to the 45° angle of inclination.
The following effect can be obtained by further turning the gear pump 45'' by 45'' angle and forming it horizontally, and by directly connecting the gear pump 4 to one end facing the horizontal direction. A pelletizer (granulation machine) is connected to a gear pump 4 directly connected to a kneaded material discharge port 9 that is oriented horizontally in a continuous kneading machine 3 that is installed on a floor surface 12 with an angle of 90°. 5 is connected, but as shown in Figure 1 and Figure 6, by installing the device at an angle of 45 degrees, in the case of the horizontal sideways type shown in Figure 8.9, 2 There is no need to separate equipment on both the upper and lower floors, such as a continuous kneading machine on the first floor and a molding machine 28 on the first floor.
This means that the entire gear pump 4 can be connected and arranged in a flat plane on the floor surface 12, which is a floor surface. This can be easily achieved by lowering the overall height of the mechanism by allowing it to be installed in parallel on the top. Furthermore, in the present invention, by opening the material supply port 8 in the inclined mixing chamber 6 in the vertical direction, when the material to be mixed is supplied from the supply port 8, the pair of rotors 7, 7 are arranged in parallel on the slope line. Then, both rotors 7.7 are exposed together toward the upper surface, and the rotors shown in FIG. The receiving area on the diagonally upper rotor 7 side is slightly larger, but since the material for officials tends to fall downward due to its own weight, the 45° angle inclination allows The same amount is supplied to both rotors 7 and 7, and this fills the mixing chamber 6 while being moved and kneaded, resulting in defects such as uneven filling and uneven temperature of the material. A homogeneous melt-kneading result can be maintained without fear.

(実施例) 本発明装置の適切な実施例を、第1図乃至第7図に亘っ
て説示する。第1図において示した本発明における連V
f、?R練機3における横長の外殻主胴11は基本的に
は第2図および第6図に示すように、一対のスクリュ羽
根ロータ7.7の中心を連ねる線を上下を境界として主
胴片11a、 llbの両者に分割されてフランジ結合
されるとともに、下部側の主胴片11b側には床面12
に固設するためのスタンド脚11cが適所に設けられる
。混練する材料の供給口8を起点とし、混練された材料
の排出口9を終点とし、両者の間において主胴ll内に
形成される混合室6は、従来と同様に2個の円筒形空間
が中央部において連通された双円筒断面形状のものであ
り、混合室6内に平行に貫挿される一対のスクリュ羽根
ロータ7.7は従来と同様、その軸周面に、材料供給口
8側から第4図に示すように材料フィード用のネジ形状
のスクリュ羽根10を形成するとともに、前方の混練部
においては図示省略しであるが、混練用のスクリュ羽根
を従来と同様に具備したものであり、材料供給口8より
後方に延びるロータ軸は、第2図および第3図に示すよ
うに外殻主胴ll内において適宜軸受部により軸支され
るとともに、両ロータ軸は連動ギヤ13.13によって
相反方向に可回動に連結され、この内、一方のロータ軸
は第1図示のように、モータ1、減速機2に連結されて
可回動とされる。これらは従来と同様である。また材料
供給口8は第1図および第3.4図に示すように、実施
例ではロータ7.7を囲みかつ鉛直方向において上向開
口状に形成されたボックス状のものとされ、かっ接結フ
ランジ14.14を前後方向に備え、これを外殻主胴1
1側に設けた接結フランジ15.15と接結することに
よって一体化されている。このようなロータ7.7を含
む混合室6を、第2図乃至第7図に亘って示されるよう
に、床面12と平行な水平方向に対し、実施例では45
″角の傾斜姿勢として配設するのであり、従って一方の
ロータ7は傾斜方向の上位に、他方のロータ7は下位に
並列することになり、材料供給口8は混合室6の傾斜姿
勢において鉛直方向の上向きに開口するように設計され
ていることにより、同供給口8においてその底に並列す
る一対のロータ7.7は路呈面が大小に異なっても、と
もに供給口8からの役人材料に対して露呈することにな
る。
(Example) A suitable example of the apparatus of the present invention will be described with reference to FIGS. 1 to 7. Series V in the present invention shown in FIG.
f,? As shown in FIGS. 2 and 6, the horizontally long outer shell main body 11 of the R kneading machine 3 is basically divided into main body pieces with the upper and lower boundaries being a line connecting the centers of a pair of screw blade rotors 7.7. 11a and llb and are joined by flanges, and a floor surface 12 is provided on the lower main body piece 11b side.
Stand legs 11c are provided at appropriate locations for fixing to the stand. The mixing chamber 6, which starts from the supply port 8 for the materials to be kneaded and ends at the discharge port 9 for the kneaded materials, and is formed in the main body 11 between the two, has two cylindrical spaces as in the past. A pair of screw blade rotors 7.7, which are inserted in parallel into the mixing chamber 6, have a bicylindrical cross-sectional shape in which they are communicated at the center, and a pair of screw blade rotors 7.7, which are inserted in parallel into the mixing chamber 6, have a shaft circumferential surface on the material supply port 8 side, as in the conventional case. As shown in FIG. 4, a thread-shaped screw blade 10 for feeding the material is formed, and the front kneading section is also provided with a screw blade for kneading, although not shown in the figure. As shown in FIGS. 2 and 3, the rotor shaft extending rearward from the material supply port 8 is supported by appropriate bearings within the main outer shell 11, and both rotor shafts are supported by interlocking gears 13. 13 so as to be rotatable in opposite directions, and one of the rotor shafts is rotatably connected to a motor 1 and a speed reducer 2, as shown in the first figure. These are the same as before. In addition, as shown in FIGS. 1 and 3.4, the material supply port 8 is box-shaped in the embodiment, surrounding the rotor 7.7 and opening upward in the vertical direction. A connecting flange 14.14 is provided in the front and rear direction, and this is attached to the outer shell main body 1.
It is integrated by connecting with a connecting flange 15.15 provided on one side. As shown in FIGS. 2 to 7, the mixing chamber 6 including such a rotor 7.7 is placed at an angle of 45 mm in the horizontal direction parallel to the floor surface 12.
Therefore, one rotor 7 is arranged in the upper part in the inclined direction, and the other rotor 7 is arranged in the lower part, and the material supply port 8 is arranged vertically in the inclined position of the mixing chamber 6. By being designed to open upward in the direction, the pair of rotors 7.7 that are parallel to each other at the bottom of the supply port 8 are able to handle the material from the supply port 8 even if the road surface is different in size. will be exposed to.

混合室6の他端に設けられる混合済み材料の排出口9は
、第6図に示されるように混合室6が45@角の傾斜姿
勢下において水平方向に向かうようにされるため、混合
室6と連通ずる部分においてガイド屈曲部16を一側に
曲成し、更に45″角変向させることにより、排出口9
の主たる流動部分を、図示のように水平方向に向かわせ
ることができ、かつ最短の長さでこれを得ることができ
る。この水平方向の開口端をギヤポンプ4の入口側に接
結することによって、ギヤポンプ4を同一平面内で混練
機3の一側に並列設置可能とするのである。
The discharge port 9 for mixed materials provided at the other end of the mixing chamber 6 is oriented horizontally when the mixing chamber 6 is tilted at an angle of 45° as shown in FIG. By bending the guide bending part 16 to one side at the part where it communicates with the outlet 9 and further turning it by 45'' angle, the outlet 9
The main flow part of can be directed horizontally as shown and can be obtained with the shortest possible length. By connecting this horizontal open end to the inlet side of the gear pump 4, the gear pump 4 can be installed in parallel on one side of the kneading machine 3 within the same plane.

第7図は混合室6の他端を閉塞しかつロータ7.7の他
端を密封軸支するための既知のエンド部17を示してい
る。
FIG. 7 shows a known end 17 for closing off the other end of the mixing chamber 6 and for sealingly supporting the other end of the rotor 7.7.

この実施例によれば、例えばプラスチック材料をペレタ
イザー5によって造粒成形するに当っての1例を述べる
と、モータ1、減速機2によって連続混練機3における
一対のスクリュ羽根ロータ7.7を回動させるとともに
、垂直方向に上向き開口した材料供給口8から、ポリエ
チレン、ポリプロピレン等のプラスチック材料を、図示
しないが計量フィーダ等を介して連続的に供給するので
あり、供給された材料は斜め方向に並設された両ロータ
7上に亘って充満し、ロータ7の回動、フィーダ用スク
リュ羽+110によって混合室6内を前進して混練部分
における剪断撹拌用の既知のスクリュ羽根(図示省略)
と混合室6の内面との間において混練されて溶融可塑化
され、後続する材料によって押出され状に材料排出口9
を流動して、その水平横向きの排出口9端よりギヤポン
プ4側に送られる。ギヤポンプ4によって溶融流動状の
材料は昇圧されてペレタイザー5側に圧送され、成形グ
イよりの押出し、高速力フタの回転切断によりペレット
状に造粒された製品が得られることになる。このさい溶
融材料の温度コントロールおよび連続混練機における動
力コントロールは、既知のように排出口9における圧力
をギヤポンプ4の回転数によって制御することによりな
されることはいうまでもな(、従来技術と同様であり、
また第1図において、ギヤポンプ4 (その駆動モータ
18、減速機19を含む)およびペレタイザー5を、図
向って下方へ後退させて後、連続混′!fA機3におけ
る混合室6側を図向って左方に移動させ、清掃その他の
メンテナンスを行なうことも、従来のこの種のものと同
様である。
According to this embodiment, for example, when plastic material is granulated and molded by the pelletizer 5, a pair of screw blade rotors 7 and 7 in the continuous kneader 3 are rotated by the motor 1 and the reducer 2. At the same time, a plastic material such as polyethylene or polypropylene is continuously supplied from a material supply port 8 that opens upward in the vertical direction via a measuring feeder (not shown), and the supplied material is fed in an oblique direction. The mixture is filled over both rotors 7 arranged in parallel, and is advanced in the mixing chamber 6 by the rotation of the rotor 7 and feeder screw blades + 110, and known screw blades (not shown) for shearing and stirring in the kneading part.
The material is kneaded and melted and plasticized between the material and the inner surface of the mixing chamber 6, and is extruded by the subsequent material into the material discharge port 9.
is sent to the gear pump 4 side from the horizontally oriented discharge port 9 end. The molten fluid material is pressurized by the gear pump 4 and is forced to the pelletizer 5 side, and a product granulated into pellets is obtained by extrusion from a forming guide and rotary cutting by a high-speed force lid. At this time, it goes without saying that the temperature control of the molten material and the power control in the continuous kneader are performed by controlling the pressure at the discharge port 9 by the rotation speed of the gear pump 4 as is known (similar to the prior art). and
Further, in FIG. 1, after the gear pump 4 (including its drive motor 18 and reduction gear 19) and the pelletizer 5 are retreated downward in the figure, continuous mixing is performed! Moving the mixing chamber 6 side of the fA machine 3 to the left in the figure to perform cleaning and other maintenance is also the same as in conventional machines of this type.

(発明の効果) 本発明の連続混練装置によれば、そのスクリュ羽根ロー
タ7.7を含む混合室6を外殻主胴11とともに、水平
方向に対して実施例のように45″角(この角度数(直
は自由に設定可能である)内外の傾斜角度下に傾斜させ
た姿勢とすることによって、従来量も多用されている水
平横向き配置姿勢のものに比し、2階建て建屋の必要や
ギヤポンプのメンテナンス困難等の不利を解消し、成形
機械を併設するに当り、同−床面上にコンパクトに設置
し、かつギヤポンプ4のメンテナンスもきわめて容易化
される。また第10図に示した水平横向きを90゜角変
更した改善手段に対しては、斜め横向き姿勢によって、
その材料供給口8において一対のスクリュ羽根ロータ7
.7を共に供給口入口に向って路呈させるとともに、傾
斜によって両ロータ7に対する均等な材料供給分布が可
能となり、改善手段における鉛直方向上位のロータフの
みに材料が供給されることによる混合室内における材料
充満度の不均一や材料発熱温度のムラを生じる欠陥をな
くし、水平横向きのものと同等の均質な混練内容を51
保できる点において優れるのであり、材料排出口にギヤ
ポンプを直結する型式の連続混練手段として利点大であ
る。
(Effects of the Invention) According to the continuous kneading device of the present invention, the mixing chamber 6 including the screw blade rotor 7.7, together with the outer shell main body 11, is arranged at an angle of 45″ (this angle) with respect to the horizontal direction as in the embodiment. The number of angles (direction can be set freely) and the angle of inclination inside and outside are tilted downwards, which reduces the need for two-story buildings compared to the horizontally lateral arrangement that is often used in the past. This eliminates disadvantages such as difficulties in maintenance of the gear pump 4 and the gear pump 4, and when a molding machine is attached to the molding machine, it can be installed compactly on the floor, and the maintenance of the gear pump 4 is extremely easy. For improvement measures that changed the horizontal sideways orientation by 90 degrees, by changing the horizontal sideways posture,
A pair of screw blade rotors 7 are provided at the material supply port 8.
.. 7 toward the inlet of the supply port, and the inclination makes it possible to distribute the material evenly to both rotors 7, and the material is supplied only to the upper rotor in the vertical direction in the improvement means, thereby reducing the material in the mixing chamber. Eliminates defects that cause unevenness in filling degree and uneven material heat generation temperature, and achieves homogeneous kneading content equivalent to horizontal kneading.
It is excellent in that it can maintain the temperature of the material, and is a great advantage as a continuous kneading means of the type in which a gear pump is directly connected to the material discharge port.

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

第1図は本発明装置実施例の成形機を含む全体平面図、
第2図はロータ連動部を示す第1図C−C線断面図、第
3図は材料供給口連結部を示す第1図C−C線断面図、
第4図は材料供給口要部を示す第1図C−C線断面図、
第5図は混合室断面形状を示す第1図C−C線断面図、
第6図は材料排出口要部を示す第1図C−C線断面図、
第7図は混合室エンド部を示す第1図C−C線断面図、
第8.9図はギヤポンプ付き水平横向き連続混練機の各
要部説明図、第1O図は同90度変向式連続混練機の要
部説明図である。 1・・・駆動モータ、2・・・減速機、3・・・連続混
練機、4・・・ギヤポンプ、5・・・ペレタイザー、6
・・・混合室、7・・・スクリュ羽根ロータ、8・・・
材料供給口、9・・・材料排出口。 特 許 出 願 人  株式会社神戸製鋼所−一・ニニ
二J 月 図
FIG. 1 is an overall plan view including a molding machine according to an embodiment of the present invention;
FIG. 2 is a cross-sectional view taken along the line C-C in FIG. 1 showing the rotor interlocking part, FIG. 3 is a cross-sectional view taken along the line C-C in FIG. 1 showing the material supply port connection part,
Fig. 4 is a sectional view taken along the line C-C in Fig. 1 showing the main part of the material supply port;
FIG. 5 is a sectional view taken along the line C-C in FIG. 1 showing the cross-sectional shape of the mixing chamber;
FIG. 6 is a sectional view taken along the line C-C in FIG. 1 showing the main part of the material discharge port;
FIG. 7 is a sectional view taken along line C-C in FIG. 1 showing the end portion of the mixing chamber;
Fig. 8.9 is an explanatory diagram of each main part of a horizontal horizontal continuous kneading machine with a gear pump, and Fig. 1O is an explanatory diagram of main parts of the same 90-degree direction change type continuous kneading machine. 1... Drive motor, 2... Reducer, 3... Continuous kneader, 4... Gear pump, 5... Pelletizer, 6
...Mixing chamber, 7...Screw blade rotor, 8...
Material supply port, 9...material discharge port. Patent applicant: Kobe Steel, Ltd.

Claims (1)

【特許請求の範囲】[Claims] (1)長手方向の両端に被混線材料の供給口と混練済み
材料の排出口とが設けられる混合室内に材料の移動およ
び混練を行なうスクリュ羽根ロータを可回動に装設する
とともに、前記材料排出口に排出制御用ギヤポンプを直
結する連続混練装置において、前記スクリュ羽根ロータ
を含む混合室が水平方向に対し傾斜した横向き姿勢に設
置され、前記材料供給口は鉛直方向に開設されるととも
に材料排出口は水平方向に開設され、該排出口にギヤポ
ンプを直結することを特徴とする傾斜形連続混練装置。
(1) A screw blade rotor for moving and kneading the materials is rotatably installed in a mixing chamber in which a supply port for materials to be mixed and a discharge port for mixed materials are provided at both ends in the longitudinal direction. In a continuous kneading device in which a gear pump for discharge control is directly connected to the discharge port, the mixing chamber including the screw blade rotor is installed in a horizontal position inclined with respect to the horizontal direction, and the material supply port is opened in the vertical direction, and the material discharge port is opened in the vertical direction. An inclined continuous kneading device characterized in that an outlet is opened in the horizontal direction and a gear pump is directly connected to the outlet.
JP61172096A 1986-07-22 1986-07-22 Inclined type continuous kneading device Granted JPS6328609A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61172096A JPS6328609A (en) 1986-07-22 1986-07-22 Inclined type continuous kneading device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61172096A JPS6328609A (en) 1986-07-22 1986-07-22 Inclined type continuous kneading device

Publications (2)

Publication Number Publication Date
JPS6328609A true JPS6328609A (en) 1988-02-06
JPH0338089B2 JPH0338089B2 (en) 1991-06-07

Family

ID=15935465

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61172096A Granted JPS6328609A (en) 1986-07-22 1986-07-22 Inclined type continuous kneading device

Country Status (1)

Country Link
JP (1) JPS6328609A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02122650U (en) * 1989-03-20 1990-10-08
CN102357936A (en) * 2011-06-27 2012-02-22 蚌埠市振中橡塑制品有限公司 Open-type rubber mixing mill

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02122650U (en) * 1989-03-20 1990-10-08
CN102357936A (en) * 2011-06-27 2012-02-22 蚌埠市振中橡塑制品有限公司 Open-type rubber mixing mill

Also Published As

Publication number Publication date
JPH0338089B2 (en) 1991-06-07

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