JPS5944093B2 - Continuous kneading machine - Google Patents

Continuous kneading machine

Info

Publication number
JPS5944093B2
JPS5944093B2 JP56084588A JP8458881A JPS5944093B2 JP S5944093 B2 JPS5944093 B2 JP S5944093B2 JP 56084588 A JP56084588 A JP 56084588A JP 8458881 A JP8458881 A JP 8458881A JP S5944093 B2 JPS5944093 B2 JP S5944093B2
Authority
JP
Japan
Prior art keywords
rotor
rotors
kneading
kneading machine
continuous kneading
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP56084588A
Other languages
Japanese (ja)
Other versions
JPS5817825A (en
Inventor
茂三 川上
公雄 井上
紘 尾村
勝美 小川
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 JP56084588A priority Critical patent/JPS5944093B2/en
Publication of JPS5817825A publication Critical patent/JPS5817825A/en
Publication of JPS5944093B2 publication Critical patent/JPS5944093B2/en
Expired 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
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/57Screws provided with kneading disc-like elements, e.g. with oval-shaped elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/70Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms
    • B01F27/701Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms comprising two or more shafts, e.g. in consecutive mixing chambers
    • B01F27/702Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms comprising two or more shafts, e.g. in consecutive mixing chambers with intermeshing paddles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • B29C48/405Intermeshing co-rotating screws

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Description

【発明の詳細な説明】 この発明は連続式混練機の改良に関するものである。[Detailed description of the invention] This invention relates to an improvement of a continuous kneader.

従来、ゴムやプラスチック材料等の混練を行なうための
各種の連続式混練機が用いられているが、従来の混練機
はロータと混練室の壁との間に形成される空間の形状が
ロータの回転によつて変化することを利用して混練を行
なうようにしている。
Conventionally, various continuous kneading machines have been used to knead rubber and plastic materials, etc., but in conventional kneading machines, the shape of the space formed between the rotor and the wall of the kneading chamber is similar to that of the rotor. Kneading is performed by taking advantage of the changes caused by rotation.

このような混練室の形状の変化を利用して行なう混練は
材料の混合、分散に適し、ゴム、プラスチック、食品等
の粘性物質の混練にはよいが、カーボンと微量のテフロ
ンとの混練のばあいのように粉体と極小量の添加物の混
練においては流動性が大きく、充分な混練は期待できな
い。この発明はこのような従来の欠点の解決のためにな
されたものであり、ロータの形状を改良することによつ
て圧縮せん断効果を高め、これによつて粉体と微量添加
物との混合が良好に行なわれるようにしたものである。
Kneading that takes advantage of changes in the shape of the kneading chamber is suitable for mixing and dispersing materials, and is good for kneading viscous substances such as rubber, plastics, and foods, but it is not suitable for kneading carbon and a small amount of Teflon. When kneading a powder and a very small amount of additives, such as Ai, the fluidity is large and sufficient kneading cannot be expected. This invention was made to solve these conventional drawbacks, and improves the compression shearing effect by improving the shape of the rotor, thereby improving the mixing of powder and trace additives. This is to ensure that it is carried out well.

すなわち、この発明は、二軸連続混練機に於ける混練ロ
ータの混練部において、ロータ軸心間距離をロータの最
大半径の二倍より小さく設定するとともに、両ロータの
回転速度を同一に設定し、少なくとも一方のロータを横
断面形状で回転方向前方側が回転方向後方側よりも中心
線から大きく膨出するように形成したものである。
That is, in the kneading section of the kneading rotor in a two-shaft continuous kneading machine, the distance between the rotor axes is set to be smaller than twice the maximum radius of the rotor, and the rotational speed of both rotors is set to be the same. , at least one of the rotors is formed in a cross-sectional shape such that the front side in the rotational direction protrudes more from the centerline than the rear side in the rotational direction.

このようにロータをいわゆる噛合い型に形成するととも
に、両ロータが干渉しないように回転速度を同一にして
いる。以下、この発明の実施例を図面によつて説明する
In this way, the rotors are formed into a so-called meshing type, and the rotational speeds of both rotors are made the same so as not to interfere with each other. Embodiments of the present invention will be described below with reference to the drawings.

第1図において、1はモータ、2は歯車減速機、3は送
りスクリュー、4は混練部のロータ、5はトラフである
。ロータ4は、第2図に示すように、回転軸6に取付け
た二翼で構成され、かつ各翼は中心線40に対して回転
方向前方の縁7が回転方向後方の縁8より大きく膨出す
るように形成されている。また他方の回転軸6には円環
状のスペーサ9を取付けている。回転方向前方の縁7は
一定の曲率を有し、この接線とそれに対向する位置のト
ラフ5の接線とのなす角が材料の喰込角となる。
In FIG. 1, 1 is a motor, 2 is a gear reducer, 3 is a feed screw, 4 is a rotor of the kneading section, and 5 is a trough. As shown in FIG. 2, the rotor 4 is composed of two blades attached to a rotating shaft 6, and each blade has an edge 7 at the front in the rotational direction with respect to the center line 40 that expands more than an edge 8 at the rear in the rotational direction. It is designed to come out. Further, an annular spacer 9 is attached to the other rotating shaft 6. The front edge 7 in the rotational direction has a constant curvature, and the angle between this tangent and the tangent of the trough 5 at the opposite position is the penetration angle of the material.

すなわち、第3図に示すように縁7上の点Dとトラフ5
上の点Cと接線のなす角θが喰込角θとなり、となる。
That is, as shown in FIG. 3, point D on edge 7 and trough 5
The angle θ formed between the upper point C and the tangent line is the penetration angle θ, and is expressed as follows.

また縁7は中心線40より大きく膨出しているために喰
込角は小さくなつている。従来は第7図に示すようにロ
ータ41は中心線40からの膨出量が小さく、従つて喰
込角は大きかつた。従来の形状のロータでは一対のロー
タ41,41とトラフ5との間に形成される混練室が口
ータ41の回転によつて変化することにより混練を行な
つていたために、混合、分散は良好に行なわれるが、圧
縮せん断作用はほとんどなかつた。これに対して上記第
2図のロータ4では喰込角が一定で小さいために圧縮せ
ん断作用が主に行なわれる。そしてこの圧縮せん断作用
が行なわれることによつてはじめて粉体と微量の添加物
との良好な混練がなされる。圧縮せん断作用は喰込角が
小さくなる程増大するが、喰込角を小さくするには縁7
を大きく膨出させなければならず、膨出量が大きくなる
と混練室の容積が小さくなつて材料の滞留時間が短かく
なつて混練が不充分となるおそれがある。そこで回転方
向後方の縁8の膨出量はできるだけ小さくしている。カ
ーボンにごく少量のテフロンを添加した材料の混練を行
なつたところ、喰込角θと混練度すなわち製品の品質と
の関係は第4図に示すようになつた。すなわち、第7図
に示す従来装置では品質限界線30よりはるかに下の点
20であつたが、上記第2図に示すロータで喰込角θが
17たのものを用いると点10に示すように良好な製品
が得られた。同図より喰込角θを25良以下にすれば良
好な混練が行なわれることがわかる。第2図の構成では
スペーサ9側の混練室には原料が滞留することになり、
これによつて原料の素通りを防止する堰の作用を果すこ
とになる。
Furthermore, since the edge 7 is bulged out more than the center line 40, the penetration angle is smaller. Conventionally, as shown in FIG. 7, the amount of protrusion of the rotor 41 from the center line 40 was small, and therefore the angle of bite was large. In the conventional rotor configuration, mixing and dispersion are difficult because the kneading chamber formed between the pair of rotors 41, 41 and the trough 5 changes as the rotor 41 rotates. Although it performed well, there was little compression shear action. On the other hand, in the rotor 4 shown in FIG. 2, the penetration angle is constant and small, so that the compressive shearing action is mainly performed. It is only when this compression-shearing action is performed that the powder and a small amount of additives are properly kneaded. The compressive shear action increases as the penetration angle becomes smaller, but in order to reduce the penetration angle, the edge 7
If the amount of swelling becomes large, the volume of the kneading chamber will become smaller and the residence time of the material will become shorter, which may result in insufficient kneading. Therefore, the amount of bulge of the rear edge 8 in the rotational direction is made as small as possible. When a material containing carbon with a very small amount of Teflon added was kneaded, the relationship between the penetration angle θ and the degree of kneading, that is, the quality of the product, was as shown in FIG. That is, in the conventional device shown in FIG. 7, the point 20 was far below the quality limit line 30, but when using the rotor shown in FIG. A good product was obtained. From the same figure, it can be seen that good kneading can be achieved if the penetration angle θ is set to 25 mm or less. In the configuration shown in FIG. 2, the raw materials will remain in the kneading chamber on the side of the spacer 9,
This acts as a weir to prevent raw materials from passing through.

第5図は1翼型ロータ44を両方に適用した例を示し、
各ロータ44は回転方向前方の縁7は小さな喰込角とな
るように構成している。この構成ではロータ44の移動
空間が大きいために材料が流れやすく、撹拌効果も大き
くなるという利点がある。第6図は2翼型ロータ45,
46を一対用いた例を示し、各ロータの形状は基本的に
は上記各ロータと同じである。
FIG. 5 shows an example in which a single-blade rotor 44 is applied to both,
Each rotor 44 is configured such that the front edge 7 in the rotational direction has a small biting angle. This configuration has the advantage that since the moving space of the rotor 44 is large, the material flows easily and the stirring effect is also increased. FIG. 6 shows a two-blade rotor 45,
An example is shown in which a pair of rotors 46 are used, and the shape of each rotor is basically the same as each rotor described above.

このロータのばあい、ロータ相互のクリーニング作用が
果されるように一方のロータ46の外径を多少小さく設
定し、ロータが干渉しないようにしている。外径が小さ
い方のロータ46とトラフ5との間のクリーニング作用
はないが、このクリーニング作用を生じさせるためにト
ラフ5の内径を小さくしてもよい。上記第2図、第5図
、第6図のロータのうちいずれを採用してもよいが、こ
れらを組合わせて採用することもできる。
In the case of this rotor, the outer diameter of one rotor 46 is set to be somewhat small so that the rotors can perform a mutual cleaning action, and the rotors do not interfere with each other. Although there is no cleaning action between the rotor 46 and the trough 5, which have a smaller outer diameter, the inner diameter of the trough 5 may be made smaller in order to produce this cleaning action. Any of the rotors shown in FIGS. 2, 5, and 6 may be used, but a combination of these may also be used.

例えば第1図において混練部に入口側から、第2図のロ
ータ4、第5図のロータ44および第6図のロータ45
,46を順次配置するなどして材料に応じて最も適切な
配置とすればよい。以上説明したように、この発明は圧
縮せん断効果が充分に発揮されるようにロータを構成し
たものであり、粉体に微量の添加物を混入させた材料の
混練にすぐれた効果を発揮するものである。
For example, in FIG. 1, the rotor 4 in FIG. 2, the rotor 44 in FIG. 5, and the rotor 45 in FIG.
, 46 may be arranged in sequence to find the most appropriate arrangement depending on the material. As explained above, the rotor of this invention is configured so that the compression-shearing effect is sufficiently exerted, and it exhibits an excellent effect in kneading materials in which small amounts of additives are mixed into powder. It is.

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

第1図はこの発明の実施例を示す装置の縦断面図、第2
図はその−線断面図、第3図はロータ喰込角の説明図、
第4図は喰込角と製品品質との関係図、第5,6図はそ
れぞれ他の実施例を示す第2図相当図、第7図は従来の
ロータの第2図相当図である。 4,44,45,46・・・・・・ロータ、5・・・・
・・トラフ、7・・・・・・回転方向前方の縁、θ・・
・・・・喰込角。
Fig. 1 is a vertical sectional view of a device showing an embodiment of the present invention;
The figure is a cross-sectional view taken along the - line, and Figure 3 is an explanatory diagram of the rotor penetration angle.
FIG. 4 is a diagram of the relationship between the penetration angle and product quality, FIGS. 5 and 6 are diagrams corresponding to FIG. 2 showing other embodiments, and FIG. 7 is a diagram corresponding to FIG. 2 of a conventional rotor. 4, 44, 45, 46... Rotor, 5...
...Trough, 7... Front edge in the direction of rotation, θ...
...Engraving angle.

Claims (1)

【特許請求の範囲】 1 二軸連続混練機に於ける混練ロータの混練部におい
て、ロータ軸心間距離をロータの最大半径の二倍より小
さく設定するとともに、両ロータの回転速度を同一に設
定し、少なくとも一方のロータを横断面形状で回転方向
前方側が回転方向後方側よりも中心線から大きく膨出す
るように形成したことを特徴とする連続式混練機。 2 特許請求の範囲第1項において、他方のロータを回
転軸から周方向に均等に突出するスペーサで構成したこ
とを特徴とする連続式混練機。 3 特許請求の範囲第1項において、他方のロータを上
記一方のロータと同様の形状にしたことを特徴とする連
続式混練機。
[Claims] 1. In the kneading section of the kneading rotors in the two-shaft continuous kneading machine, the distance between rotor axes is set to be smaller than twice the maximum radius of the rotors, and the rotational speeds of both rotors are set to be the same. A continuous kneading machine characterized in that at least one of the rotors is formed in a cross-sectional shape such that the front side in the rotation direction protrudes more from the center line than the rear side in the rotation direction. 2. A continuous kneading machine according to claim 1, characterized in that the other rotor is constituted by a spacer that projects evenly in the circumferential direction from the rotating shaft. 3. A continuous kneading machine according to claim 1, characterized in that the other rotor has the same shape as the one rotor.
JP56084588A 1981-06-01 1981-06-01 Continuous kneading machine Expired JPS5944093B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56084588A JPS5944093B2 (en) 1981-06-01 1981-06-01 Continuous kneading machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56084588A JPS5944093B2 (en) 1981-06-01 1981-06-01 Continuous kneading machine

Publications (2)

Publication Number Publication Date
JPS5817825A JPS5817825A (en) 1983-02-02
JPS5944093B2 true JPS5944093B2 (en) 1984-10-26

Family

ID=13834823

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56084588A Expired JPS5944093B2 (en) 1981-06-01 1981-06-01 Continuous kneading machine

Country Status (1)

Country Link
JP (1) JPS5944093B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60189324U (en) * 1984-05-28 1985-12-14 三菱重工業株式会社 Vertical stirring mixing device
JPS61243182A (en) * 1985-04-19 1986-10-29 Nitsukan Kogyo Kk Potassium titanate fibers plated with metal and its production
DE102009059072A1 (en) * 2009-12-18 2011-06-22 Bayer Technology Services GmbH, 51373 Screw elements for extruding viscoelastic masses
JP2013010083A (en) * 2011-06-30 2013-01-17 Shin Nichinan:Kk Kneader

Also Published As

Publication number Publication date
JPS5817825A (en) 1983-02-02

Similar Documents

Publication Publication Date Title
US3471131A (en) Continuous mixing apparatus
US3652062A (en) Mixing apparatus
US4300840A (en) Kneader for compounded resin
US3749375A (en) Process for mixing, kneading and granulating thermosetting plastic material in continuous operation
US3900187A (en) Continuous mixing and/or kneading machine with co-wiping single lead screws
JPH01317534A (en) Self-wiping type continuous mixer having enlarged inner diameter hole part
JPS5944093B2 (en) Continuous kneading machine
JPS6347107A (en) Device for kneading rubber-like material
US3656718A (en) Helical blade mixer
US1936248A (en) Mixing machine
EP1033217A2 (en) Rotor for a mixer and mixer having the same
US3147514A (en) Processing plastic and other multiphase materials
JPS63165105A (en) Mixer
JPS60154030A (en) Cone-type extruder
EP0947301B1 (en) Continuous kneading machine
CN112549494B (en) Foamed plastic extruding machine
JP2889758B2 (en) Horizontal twin-screw kneader
JPH04171033A (en) Continuous kneader
JPS63130128A (en) Kneading extrusion apparatus
JPS5832917Y2 (en) Structure of screw of extrusion molding machine
CN214131132U (en) Groove-shaped mixing machine for pharmacy
JPS58189026A (en) Degassing apparatus for continuous dual shaft kneader
JP2518789B2 (en) Open type kneader
JPS5627338A (en) Extrusion molding machine
SU939268A1 (en) Disc extruder for processing polymeric materials