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JPH0338089B2 - - Google Patents
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JPH0338089B2 - - Google Patents

Info

Publication number
JPH0338089B2
JPH0338089B2 JP61172096A JP17209686A JPH0338089B2 JP H0338089 B2 JPH0338089 B2 JP H0338089B2 JP 61172096 A JP61172096 A JP 61172096A JP 17209686 A JP17209686 A JP 17209686A JP H0338089 B2 JPH0338089 B2 JP H0338089B2
Authority
JP
Japan
Prior art keywords
mixing chamber
rotors
supply port
gear pump
discharge 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.)
Expired - Lifetime
Application number
JP61172096A
Other languages
Japanese (ja)
Other versions
JPS6328609A (en
Inventor
Yasuji Orimo
Futashi Fukui
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

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】 (産業上の利用分野) 本発明は、二軸混練機に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a twin-screw kneader.

(従来の技術) プラスチツク、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練材料の供
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ユ
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イード用スクリユ羽根によつ
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ユ羽根によつて混練され
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つて後方か
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
手段によつて行なうのである。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
通する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練材料の供給口
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内にはスクリユ羽根を有するロー
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
続混練装置においては、単に被混練材料を混練し
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によつて連
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・プラスチツクス・イン
タナシヨナル誌、1985年6月号登載……フアーレ
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90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、これによつて
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 polymeric 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 a mixing chamber in which a supply port for materials to be kneaded and a discharge port for kneaded materials are provided at both ends of the mixing chamber. The main outer shell surrounding the mixing chamber is equipped with heat treatment means for heating or cooling, such as a heater. The materials are transferred to the mixing chamber, are kneaded by the stirring and kneading screw blades in the same rotor, and are discharged in a molten state from the discharge port. The mixing chamber is pushed forward from the rear by the materials continuously introduced from the mixing chamber, 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 and laterally, two mixing chambers 2 having a cylindrical cross section that are parallel to each other and communicate at the central portion are formed.
At one longitudinal end of the mixing chamber 2, a supply port 5 for the material to be kneaded is provided with an upward opening, and at the other end, a discharge port 3 for the kneaded material is provided with a downward opening. A pair of rotors 4, 4 having screw blades are installed parallel and rotatably,
A gear pump 26 as a discharge control means is directly connected to the material discharge port 3. In addition, in such a continuous kneading device, the kneading is not completed by simply kneading the materials to be kneaded, but the kneaded materials that have been brought into a molten and fluidized state are processed using a pelletizer (granulation device) or other device, as shown in Fig. 9, for example. The 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 kneading machine including the gear pump 26 A molding machine 28 whose side is installed on the second floor 30 of a two-story building and includes a transfer pipe 29
It is also known that the sides are forced to be installed separately on the ground floor 31. In order to eliminate the disadvantages of the two-story structure in the conventional technology, a new continuous kneading device as shown in Figure 10 has been developed (published in Modern Plastics International, June 1985 issue... ...Fuarel Inc.). That is, as shown in the figure, the main outer shell 1 and the mixing chamber 2
and a kneading machine consisting of rotors 4, 4,
The material supply port 5 is opened upward, while the kneaded material discharge port 3 is opened horizontally, and the material supply port 5 is opened horizontally. A gear pump 26 is directly connected to the discharge port 3, and a 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つてし
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、従つ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、この種混練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から被混練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
ととなつて、混合室および2軸ロータ間における
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 Figs. 8 and 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, troublesome operational management, difficulty in maintaining the gear pump, which is installed directly below the kneading machine, and furthermore, the length of the transfer pipe 29, which is the communication passage between the molding machine 28 side and the gear pump 26, and therefore There are problems such as an increase in the 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 recognized, the continuous kneading machine By changing the direction of the rotors by 90 degrees to make them oriented vertically, the pair of rotating rotors 4, 4, which are parallel to each other in the horizontal direction, is the most efficient and frequently used method in this type of kneading machine. , vertically in parallel vertically, which means that when the material to be kneaded is supplied from the material supply port 5, the material is supplied only to the upper rotor 4 side, and the mixing chamber and the This creates an imbalance in the filling degree of the material between the rotors and the shaft, and this also results in uneven material temperature, which poses a problem in that it is difficult to obtain a homogeneous kneading content.

(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傾斜させるよ
うにしたものであり、具体的には、長手方向の両
端に被混練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
を行なうスクリユ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
ユ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 has the following features:
The entire mixing chamber including the rotating rotor, which is the main part of such a continuous kneading device, is tilted with respect to the horizontal direction, and specifically, there is a supply port for the material to be kneaded and a supply port for the kneaded material at both ends in the longitudinal direction. In a continuous kneading device, a screw blade rotor for moving and kneading materials is rotatably installed in a mixing chamber provided with a discharge port, and a gear pump for discharge control is directly connected to the material discharge port. The mixing chamber including the rotor is installed in a horizontal position inclined with respect to the horizontal direction, the material supply port is opened in the vertical direction, and the material discharge port is opened in the horizontal direction, and a gear pump is directly connected to the discharge port. be.

(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図に亘つて示すように、連続混練機3の
主体部分である処の、一対のスクリユ羽根ロータ
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45゜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練材料
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
傾斜に伴つ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つて横向きに形成し、
この水平方向に向かう一端にギヤポンプ4を直結
することによつて、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(排出制御装置)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図に示さ
れるように、45゜角の傾斜配設によつて、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階床面である床面1
2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から被混練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は上面に向つて共に露呈され、第1
0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、投入材料は自
重によつて下側に落下し易いので45゜角の傾斜に
よつて、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, as shown in FIGS. When installing the horizontally elongated outer shell main body 11 having the mixing chamber 6 installed therein in a parallel and rotatable manner on a target floor surface 12 as shown in FIG. The mixing chamber 6 including the rotor 7 is on the floor 12
In the illustrated example, the mixing chamber 6 is installed together with the main outer shell 11 in an inclined horizontal position at an angle of inclination of 45 degrees with respect to the horizontal direction parallel to the mixing chamber 6. The supply port 8 for the material to be kneaded, which is provided in a continuous manner, is a supply port that opens upward in the vertical direction as shown in the fourth figure, and the supply port 8, which is provided in a continuous manner at the other end in the longitudinal direction of the mixing chamber 6, is a supply port for discharging the mixed materials. As shown in FIG. 6, the outlet 9 is opened obliquely downward as the mixing chamber 6 is inclined at an angle of 45 degrees, and is further turned by an angle of 45 degrees to form a sideways opening in the horizontal direction.
By directly connecting the gear pump 4 to one end facing in the horizontal direction, the following effects can be obtained. That is, FIG. 1 shows a gear pump (discharge control device) directly connected to a kneaded material discharge port 9 oriented horizontally in a continuous kneader 3 according to the present invention, which is installed on a floor surface 12 at an angle of 45 degrees. 4, the target molding machine 1
As an example, a pelletizer (granulating device) 5 is shown connected, but as shown in FIGS. 1 and 6, the 8th,
In the case of the horizontal horizontal type shown in Figure 9, there is no need to separate the equipment on both the upper and lower floors, such as the continuous kneading machine on the second floor and the molding machine 28 on the first floor, and it is possible to use the continuous kneading machine on the second floor and the molding machine 28 on the first floor.
By tilting the mixing chamber 6 and orienting the discharge port 9 horizontally, the gear pumps 4 can be arranged side by side on the same plane. This is easily possible by reducing the overall height. 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 kneaded is introduced and supplied from the supply port 8, the pair of rotors 7, 7 are parallel to each other on the slope line. Then, both rotors 7, 7 are exposed together toward the top surface, and the first
The rotors shown in FIG. Although the receiving area on the rotor 7 side is slightly larger, the input material tends to fall downward due to its own weight, so the 45° angle inclination allows the same amount to be fed to both rotors 7 and 7 sides. Since this is moved and kneaded while filling the mixing chamber 6, a homogeneous melt-kneading result can be maintained without the risk of non-uniform filling or uneven temperature of the materials.

(実施例) 本発明装置の適切な実施例を、第1図乃至第7
図に亘つて説示する。第1図において示した本発
明における連続混練機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、一対のスクリユ羽根ロータ7,7の中心を連
ねる線を上下を境界として主胴片11a,11b
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11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ユ羽根ロータ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イード用のネジ形状
のスクリユ羽根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てあるが、混練用の
スクリユ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11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によつて相反方
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ツ
クス状のものとされ、かつ接結フランジ14,1
4を前後方向に備え、これを外殻主胴11側に設
けた接結フランジ15,15と接結することによ
つ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図に亘つて示
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、従つて一方のロータ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つ
ても、ともに供給口8からの投入材料に対して露
呈することになる。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
す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つて、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。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。
(Example) Appropriate examples of the device of the present invention are shown in Figs. 1 to 7.
This will be explained with reference to the figures. Basically, the horizontally long outer shell main body 11 of the continuous kneader 3 of the present invention shown in FIG. 1 connects the centers of a pair of screw blade rotors 7, 7, as shown in FIGS. 2 and 6. Main body pieces 11a, 11b with the upper and lower lines as boundaries
The main body piece 11b on the lower side is provided with a stand leg 11c at an appropriate position to be fixed to the floor 12. The mixing chamber 6, which is formed in the main body 11 between the two starting from the supply port 8 for the material to be kneaded and ending at the discharge port 9 for the kneaded material, has two cylindrical spaces as in the past. A pair of screw blade rotors 7, 7 are inserted in parallel into the mixing chamber 6, and have a bicylindrical cross-sectional shape in which the rotors are communicated at the center.
As in the conventional case, screw-shaped screw blades 10 for feeding the material are formed on the peripheral surface of the shaft from the material supply port 8 side as shown in FIG. 4, and the front kneading section is not shown. However, it is equipped with screw blades for kneading as in the past, and the rotor shaft extending rearward from the material supply port 8 is
As shown in FIGS. 2 and 3, the main body 11 is supported by appropriate bearings, and
Both rotor shafts are rotatably connected in opposite directions by interlocking gears 13, 13, and one of the rotor shafts is rotatably connected to a motor 1 and a speed reducer 2, as shown in the first diagram. It is said that These are the same as before. In addition, as shown in FIG. 1 and FIGS. 3 and 4, the material supply port 8 is in the form of a box that surrounds the rotors 7 and 7 and is opened upward in the vertical direction. Connection flange 14,1
4 in the front-rear direction, and are integrated by connecting with connecting flanges 15, 15 provided on the outer shell main body 11 side. Such a rotor 7,7
As shown in FIGS. 2 to 7, the mixing chamber 6 including the Therefore, one rotor 7 is arranged in parallel at the upper side in the inclined direction, and the other rotor 7 is arranged at the lower side, and the material supply port 8 is designed to open upward in the vertical direction when the mixing chamber 6 is in the inclined position. As a result, the pair of rotors 7, 7 that are parallel to each other at the bottom of the supply port 8 are both exposed to the material input from the supply port 8, even if the road surfaces are different in size. The mixed material outlet 9 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 degrees, as shown in FIG. By bending the guide bending part 16 to one side at the part communicating with the outlet 9 and further changing the direction by an angle of 45 degrees, 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. FIG. 7 shows a known end 17 for closing 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、例えばプラスチツク材料
をペレタイザー5によつて造粒成形するに当つて
の1例を述べると、モータ1、減速機2によつて
連続混練機3における一対のスクリユ羽根ロータ
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ツク材料を、図示しない
が計量フイ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上に亘つて充満し、ロータ7の回動、フ
イーダ用スクリユ羽根10によつて混合室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
クリユ羽根(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
料によつ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によつて溶融流動
状の材料は昇圧されてペレタイザー5側に圧送さ
れ、成形ダイよりの押出し、高速カツタの回転切
断によりペレツ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の回転数によつて制御することによりなさ
れることはいうまでもなく、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、図向つて下方へ後退させて後、連続
混練機3における混合室6側を図向つて左方に移
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 in the continuous kneading machine 3 are controlled by the motor 1 and the reducer 2. , 7, and 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 weighing feeder (not shown), and the supplied material The mixture is filled over both rotors 7 arranged in parallel in a diagonal direction, and is advanced in the mixing chamber 6 by the rotation of the rotor 7 and the screw blades 10 for the feeder to form a known screw for shear stirring in the kneading section. The material is kneaded and melted and plasticized between the vane (not shown) and the inner surface of the mixing chamber 6, and is extruded by the following material and flows through the material outlet 9 in a shape, and the end of the horizontal outlet 9 is extruded by the following material. It is sent to the gear pump 4 side. The molten fluid material is pressurized by the gear pump 4 and is forced into the pelletizer 5, where it is extruded from a molding die and cut by rotation with a high-speed cutter to obtain a product granulated into pellets. At this time, it goes without saying that the temperature control of the molten material and the power control in the continuous kneading machine are performed by controlling the pressure at the discharge port 9 by the rotation speed of the gear pump 4, as is known, and as is well known in the art. Similarly, in FIG. 1, after the gear pump 4 (including its drive motor 18 and reduction gear 19) and pelletizer 5 are retreated downward in the figure, the mixing chamber 6 side of the continuous kneader 3 is shown in the figure. Moving it to the left and performing cleaning and other maintenance is also the same as with conventional devices of this type.

(発明の効果) 本発明の連続混練装置によれば、そのスクリユ
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(この角度数値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つ
て、従来最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、同一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
向き姿勢によつて、その材料供給口8において一
対のスクリユ羽根ロータ7,7を共に供給口入口
に向つて路呈させるとともに、傾斜によつて両ロ
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7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
質な混練内容を確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 rotors 7, 7 is connected to the outer shell main body 11.
In addition, by tilting the camera at an angle of 45 degrees (this angle value can be freely set) to the horizontal direction as shown in the example below, it is possible to achieve the most commonly used posture in the past. Compared to the horizontal horizontal arrangement, it eliminates the disadvantages such as the need for a two-story building and the difficulty of maintaining the gear pump, and when installing a molding machine, it can be installed compactly on the same floor, and the gear pump 4 can be installed compactly on the same floor. Maintenance is also greatly facilitated. In addition, with respect to the improvement means in which the horizontal sideways orientation shown in FIG. In addition, the inclination makes it possible to distribute the material evenly to both rotors 7, and the degree of material filling in the mixing chamber is uneven due to the material being supplied only to the vertically upper rotor 7 in the improvement means. It is superior in that it eliminates defects that cause unevenness in material heat generation temperature and ensures homogeneous kneading content equivalent to that of the horizontal type, 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 the drawing]

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A−
A線断面図、第3図は材料供給口連結部を示す第
1図B−B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D−D線断面図、第6図は材料
排出口要部を示す第1図E−E線断面図、第7図
は混合室エンド部を示す第1図F−F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10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…排出制御装置(ギヤポンプ)、5…ペレ
タイザー、6…混合室、7…スクリユ羽根ロー
タ、8…材料供給口、9…材料排出口。
Fig. 1 is an overall plan view including a molding machine according to an embodiment of the present invention, and Fig. 2 is a diagram showing a rotor interlocking part.
3 is a sectional view taken along the line B-B in FIG. 1 showing the material supply port connecting 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, and FIG. 1 is a sectional view taken along the line D-D in FIG. 1 showing the cross-sectional shape of the mixing chamber, FIG. 6 is a sectional view taken along the line E-E in FIG. 1 showing the main part of the material discharge port, and FIG. Figure F-F line sectional view,
8 and 9 are explanatory diagrams of the main parts of the horizontal lateral continuous kneading machine equipped with a gear pump, and FIG. 10 is an explanatory diagram of the main parts of the same 90 degree continuous kneading machine. 1... Drive motor, 2... Reducer, 3... Continuous kneading machine, 4... Discharge control device (gear pump), 5... Pelletizer, 6... Mixing chamber, 7... Screw blade rotor, 8... Material supply port, 9... Material discharge Exit.

Claims (1)

【特許請求の範囲】 1 材料搬送方向両端側に被混練材料の供給口8
と混練済み材料の排出口9が設けられた混合室6
内に、材料の搬送及び混練を行なう一対のロータ
7,7が互いに平行にかつ回動自在に挿通され、
前記排出口9に排出制御装置4が直結される二軸
混練機において、 前記ロータ7,7を含む混合室6は、その横手
方向において水平に対して傾斜した横向き姿勢に
配置され、前記排出口9は混合室6の水平横手方
向に開設され、かつ供給口8は一対のロータ7,
7が共に当該供給口8内に露呈するように混合室
6の鉛直方向に開設されていることを特徴とする
二軸混練機。
[Claims] 1. Supply ports 8 for the material to be kneaded on both ends in the material conveyance direction.
and a mixing chamber 6 provided with a discharge port 9 for the mixed materials.
A pair of rotors 7, 7 for conveying and kneading the materials are inserted into the inside so as to be rotatable and parallel to each other.
In a two-shaft kneading machine in which a discharge control device 4 is directly connected to the discharge port 9, the mixing chamber 6 including the rotors 7, 7 is arranged in a horizontal position inclined with respect to the horizontal in its lateral direction, and the discharge port 9 is opened in the horizontal and lateral direction of the mixing chamber 6, and the supply port 8 is connected to a pair of rotors 7,
7 are opened in the vertical direction of the mixing chamber 6 so as to be exposed in the supply port 8.
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 JPS6328609A (en) 1988-02-06
JPH0338089B2 true 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)

Families Citing this family (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
JPS6328609A (en) 1988-02-06

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