JPH069815B2 - Twin screw different diameter kneading extruder - Google Patents

Twin screw different diameter kneading extruder

Info

Publication number
JPH069815B2
JPH069815B2 JP63273277A JP27327788A JPH069815B2 JP H069815 B2 JPH069815 B2 JP H069815B2 JP 63273277 A JP63273277 A JP 63273277A JP 27327788 A JP27327788 A JP 27327788A JP H069815 B2 JPH069815 B2 JP H069815B2
Authority
JP
Japan
Prior art keywords
cylinder
screw
wall
portions
kneading extruder
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
JP63273277A
Other languages
Japanese (ja)
Other versions
JPH02120006A (en
Inventor
稔 吉田
英樹 水口
邦弘 堀江
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works 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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP63273277A priority Critical patent/JPH069815B2/en
Publication of JPH02120006A publication Critical patent/JPH02120006A/en
Publication of JPH069815B2 publication Critical patent/JPH069815B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • B29C48/63Screws having sections without mixing elements or threads, i.e. having cylinder shaped sections
    • 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
    • B29C48/41Intermeshing counter-rotating 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
    • B29C48/36Means 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
    • B29C48/45Axially movable 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
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/52Screws with an outer diameter varying along the longitudinal axis, e.g. for obtaining different thread clearance
    • B29C48/525Conical 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
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/535Screws with thread pitch varying along the longitudinal axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating

Landscapes

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

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、二軸異径の混練押出機に関し、特に、シリン
ダの移動に伴う混練度合(絞り度合)の調節を巾広く行
うことができるようにすると共に、連続運転中における
シリンダの軸方向移動の操作を容易化するめの新規な改
良に関する。
TECHNICAL FIELD The present invention relates to a kneading extruder having a twin-screw different diameter, and in particular, it is possible to widely adjust the kneading degree (drawing degree) accompanying the movement of the cylinder. And a new improvement for facilitating the operation of the axial movement of the cylinder during continuous operation.

[従来の技術] 従来、用いられていたこの種の二軸異径の混練押出機と
しては、第4図にて示す、例えば、特公昭47-42583号公
報及び特公昭58-87013号公報に開示された構成を挙げる
ことができる。
[Prior Art] This type of twin-screw different diameter kneading extruder that has been conventionally used is shown in FIG. 4, for example, in Japanese Patent Publication No. 47-42583 and Japanese Patent Publication No. 58-87013. The disclosed configurations may be mentioned.

すなわち、図において、符号1で示されるものは、本体
2に設けられた油圧シリンダ3によって軸方向に移動可
能に設けられたシリンダであり、このシリンダ1内に
は、2個の大径の軸穴からなる第1軸穴1a及び壁1f
によって仕切られた2個の小径の軸穴からなる一対の2
軸穴1b及び1cが連続して形成されている。
That is, in the figure, what is denoted by reference numeral 1 is a cylinder provided so as to be movable in the axial direction by a hydraulic cylinder 3 provided in the main body 2, and in this cylinder 1, two large diameter shafts are provided. First shaft hole 1a and wall 1f consisting of holes
A pair of 2 consisting of two small-diameter shaft holes partitioned by
The shaft holes 1b and 1c are continuously formed.

前記シリンダ1の後端1dは、前記本体2に形成された
ストッパ部2aと当接可能に構成され、このシリンダ1
の軸方向における移動距離は、前記後端1dに当接して
配設されたダイヤルゲージ4によって測定される。
A rear end 1d of the cylinder 1 is configured to be able to contact a stopper portion 2a formed on the main body 2.
The moving distance in the axial direction of is measured by a dial gauge 4 arranged in contact with the rear end 1d.

前記各軸穴1a〜1c内には、互いに外径が異なる第1
スクリュ部5及び第2スクリュ部6を一体に有する一対
の第1スクリュ軸7及び第2スクリュ軸8が互いに噛合
した状態で回転自在に配設されており、各スクリュ軸7
及び8は、減速機構9と連結軸10を介して接続されて
おり、軸方向には固定された状態で設けられている。
In each of the shaft holes 1a to 1c, a first outer diameter different from each other is provided.
A pair of a first screw shaft 7 and a second screw shaft 8 integrally having a screw portion 5 and a second screw portion 6 are rotatably arranged in a meshed state with each other, and each screw shaft 7
And 8 are connected to the reduction mechanism 9 via a connecting shaft 10, and are provided in a state of being fixed in the axial direction.

前記第1スクリュ部5は、リードの小さいフライトで構
成された原料供給部7a及び8aと、リードの大きいフ
ライトで形成された混練部7b及び8bとから構成され
ると共に、前記各スクリュ軸7及び8における各スクリ
ュ部5及び6間には、外径が変化する位置の異径部を構
成するテーパ部7c及び8cが形成されている。
The first screw part 5 is composed of raw material supply parts 7a and 8a formed by flights with small leads and kneading parts 7b and 8b formed by flights with large leads, and the screw shafts 7 and Between the screw portions 5 and 6 in 8, there are formed taper portions 7c and 8c forming different diameter portions at positions where the outer diameter changes.

前記シリンダ1における前記テーパ部7c及び8cに対
応する各軸穴1b及び1cの内壁位置に内壁テーパ部1
eが形成され、これらの各テーパ部7c及び8cと前記
内壁テーパ部1eとの間には、間隙t1が形成されてい
る。
The inner wall taper portion 1 is provided at the inner wall positions of the shaft holes 1b and 1c corresponding to the taper portions 7c and 8c in the cylinder 1.
e is formed, and a gap t 1 is formed between each of the tapered portions 7c and 8c and the inner wall tapered portion 1e.

従って、前述の構成においては、連続運転中にシリンダ
を軸方向に可変移動させて間隙t1を変化させることに
よって、各スクリュ部5及び6の混練部7b及び8b内
の充満率を変化させると共に滞留時間をも変化させ、原
料の混練度合を調節していた。
Therefore, in the above-described configuration, the cylinder is variably moved in the axial direction during the continuous operation to change the gap t 1, thereby changing the filling rate in the kneading parts 7b and 8b of the screw parts 5 and 6, and The residence time was also changed to adjust the kneading degree of the raw materials.

[発明が解決しようとする課題] 従来の二軸異径の混練押出機は以上のように構成されて
いたため、次のような課題を有していた。
[Problems to be Solved by the Invention] Since the conventional twin-screw different diameter kneading extruder is configured as described above, it has the following problems.

すなわち、前述の隙間t1のみを調節することによっ
て、原料(樹脂)の流れ抵抗(圧力損失)をつけるよう
にしているが、この場合、第5図に示されるように、テ
ーパ部7cを流れる原料(樹脂)の圧力損失の計算式
は、簡略的に例えて平行板内を流れるものと考えると、 但し、ΔP=抵抗値 μ=樹脂粘度 Q=樹脂の通過量 W=通過する幅 L=通過する長さ t1=樹脂が通過する隙間 前述の(1)式から求めることができるが、隙間t1は3乗
で変化するため、シリンダ1と各スクリュ軸7及び8の
関係位置を正確且つ微細に調節する必要があり、このテ
ーパ部7c及び8cのテーパ角度を小さくし、シリンダ
1の大きい移動量でも隙間t1の変化が極力小となるよ
うに構成されているが、この隙間t1とテーパ部7c及
び8cの角度θの関係は、第6図で示すように、 t1=sinθ×χ(シリンダ移動量)・・・(2) で表されるため、限られた二軸間距離では通常15°以
上が限度であった。
That is, the flow resistance (pressure loss) of the raw material (resin) is provided by adjusting only the above-mentioned gap t 1 , but in this case, as shown in FIG. 5, the taper portion 7c flows. The pressure loss calculation formula for the raw material (resin) can be simplified as follows: However, ΔP = resistance value μ = resin viscosity Q = resin passing amount W = passing width L = passing length t 1 = resin passing gap, which can be obtained from the above equation (1), but the gap t Since 1 changes with the third power, it is necessary to precisely and finely adjust the relational position between the cylinder 1 and the screw shafts 7 and 8, and the taper angle of the taper portions 7c and 8c should be reduced to make a large movement of the cylinder 1. Although the amount of change in the clearance t 1 is minimized, the relationship between the clearance t 1 and the angle θ of the tapered portions 7c and 8c is t 1 = sin θ ×, as shown in FIG. Since χ (cylinder movement amount) is expressed by (2), the limit between the two axes is usually 15 ° or more in the limited distance between the two axes.

従って、第3図で示されるように、シリンダ移動量χの
小さい部分で見ると、隙間t1の3乗で効くため、抵抗
値ΔPとシリンダ移動量χとの関係は、変化度合が極め
て顕著であり、例えば、シリンダ1を加熱から冷却に切
替えた際に発生するシリンダ1の熱膨張変化等の微妙な
影響によっても変化するため、シリンダ1移動の適切な
調節が極めて難しく、又、その調節範囲も限られてい
た。
Therefore, as shown in FIG. 3, when viewed in a portion where the cylinder movement amount χ is small, the third power of the clearance t 1 is effective, so that the relationship between the resistance value ΔP and the cylinder movement amount χ has a very remarkable change degree. However, for example, since it also changes due to a subtle influence such as a thermal expansion change of the cylinder 1 that occurs when the cylinder 1 is switched from heating to cooling, it is extremely difficult to appropriately adjust the movement of the cylinder 1, and The range was also limited.

さらに、混練度の高いものを求める場合、極力隙間t1
を狭くする必要があるが、テーパ部7c及び8cとシリ
ンダ1とが接触することになり、最少限の隙間t1を保
つための機械的ストッパーを設けなくてはならなかっ
た。
Furthermore, when a high kneading degree is desired, the gap t 1 is as much as possible.
However, since the tapered portions 7c and 8c come into contact with the cylinder 1, it is necessary to provide a mechanical stopper for keeping the minimum clearance t 1 .

従って、高い混練を必要とする場合には、特別に製作さ
れた高混練スクリュに交換しなければならないと云う課
題も有していた。
Therefore, when high kneading is required, there is also a problem that the specially manufactured high kneading screw must be replaced.

本発明は、以上のような課題を解決するためになされた
もので、特に、シリンダの移動に伴う混練度合(絞り度
合)の調節を巾広く容易に行うことができるようにする
と共に、連続運転中におけるシリンダの軸方向移動の操
作を容易化するようにした二軸異径の混練押出機を提供
することを目的とする。
The present invention has been made to solve the above problems, and in particular, enables wide and easy adjustment of the kneading degree (drawing degree) accompanying the movement of the cylinder, and continuous operation. It is an object of the present invention to provide a kneading extruder having different biaxial diameters, which facilitates the operation of axial movement of the cylinder inside.

[課題を解決するための手段] 本発明による二軸異径の混練押出機は、軸方向に移動可
能に設けられたシリンダ内に回転自在に設けられた一対
のスクリュ軸と、前記各スクリュ軸にテーパ部を介して
形成され互いに外径の異なる第1スクリュ部及び第2ス
クリュ部と、前記テーパ部に対応する前記シリンダの内
壁に形成された内壁テーパ部とよりなるものにおいて、
前記テーパ部に隣接して形成された円柱状部と、前記内
壁テーパ部に隣接して形成された内壁筒部とを備えた構
成である。
[Means for Solving the Problem] A twin-screw different-diameter kneading extruder according to the present invention includes a pair of screw shafts rotatably provided in a cylinder movably provided in an axial direction, and the screw shafts. A first screw part and a second screw part which are formed via a tapered part and have different outer diameters from each other, and an inner wall tapered part formed on the inner wall of the cylinder corresponding to the tapered part,
This is a configuration including a columnar portion formed adjacent to the tapered portion and an inner wall tubular portion formed adjacent to the inner wall tapered portion.

[作用] 本発明による二軸異径の混練押出機においては、スクリ
ュ軸のテーパ部に隣接して円柱状部を設け、テーパ部の
原料抵抗(樹脂抵抗)に円柱状部の原料抵抗(樹脂抵
抗)を加算することにより、従来よりも高い混練効果と
幅広い調節ができると共に、シリンダ移動量と抵抗値の
関係が従来ほど敏感でないように構成されており、比較
的精度の低い調節で混練度の調節を容易に行うことがで
きる。
[Operation] In the twin-screw different diameter kneading extruder according to the present invention, a columnar portion is provided adjacent to the taper portion of the screw shaft, and the raw material resistance (resin resistance) of the cylindrical portion is added to the raw material resistance (resin resistance) of the taper portion. By adding (resistance), a higher kneading effect and wider adjustment than before can be performed, and the relationship between the cylinder movement amount and the resistance value is configured to be less sensitive than before, and the kneading degree can be adjusted with relatively low accuracy. Can be easily adjusted.

すなわち、前述した(1)式によって隙間t1は3乗で効く
が、そこを流れる長さLは1乗で比例しているため、シ
リンダとスクリュ軸の相対位置を変えることにより、円
柱状部と内壁筒部が重合する有効長Dがその抵抗値とな
り、これが1乗の変化であるため、第3図で示すA及び
Bでしえすように、シリンダ移動量χに対する抵抗値Δ
Pの変化特性が従来よりも大幅にゆるい勾配となる。
That is, according to the above-mentioned formula (1), the clearance t 1 is effective as a cube, but the length L flowing there is proportional to a cube, so that the cylindrical portion is changed by changing the relative position of the cylinder and the screw shaft. Since the effective length D at which the inner wall cylinder overlaps becomes the resistance value, which is a change of the first power, as shown in A and B shown in FIG. 3, the resistance value Δ with respect to the cylinder movement amount χ.
The change characteristic of P has a much gentler gradient than before.

従って、第1図の状態で、シリンダを右方向に移動させ
ると、テーパ部すなわち隙間t1は開く方向で抵抗が下
り、又、同時に円柱状部の有効長Dも縮む方向となり抵
抗も下るため、円柱状部とテーパ部を隣接させて連続的
に形成することにより抵抗値を加算することができ、シ
リンダ移動量χに対する抵抗値ΔPの変化曲線を大幅に
ゆるやかにすることができるものである。
Therefore, when the cylinder is moved to the right in the state shown in FIG. 1, the taper portion, that is, the clearance t 1 decreases in resistance in the opening direction, and at the same time, the effective length D of the columnar portion decreases and the resistance also decreases. By continuously forming the columnar portion and the tapered portion adjacent to each other, the resistance value can be added, and the change curve of the resistance value ΔP with respect to the cylinder movement amount χ can be remarkably gentle. .

[実施例] 以下、図面と共に本発明による二軸異径の混練押出機の
好適な実施例について詳細に説明する。
[Embodiment] A preferred embodiment of a kneading extruder having a different biaxial diameter according to the present invention will be described in detail below with reference to the drawings.

尚、従来例と同一又は同等部分については同一符号を用
いて説明する。
The same or equivalent parts as those of the conventional example will be described using the same reference numerals.

第1図から第3図迄は、本発明による二軸異径の混練押
出機を示すためのものであり、第1図は全体構成を示す
断面図、第2図は第1図の要部を示す拡大断面図、第3
図は抵抗値の特性図である。
FIGS. 1 to 3 are for showing a kneading extruder having a twin-screw different diameter according to the present invention. FIG. 1 is a sectional view showing the entire structure, and FIG. 2 is a main part of FIG. 3 is an enlarged sectional view showing
The figure is a characteristic diagram of the resistance value.

図において、符号1で示されるものは、本体2に設けら
れた油圧シリンダ3によって軸方向に移動可能に設けら
れたシリンダであり、このシリンダ1内には、2個の軸
穴からなる大径の第1軸穴1a及び壁1fによって仕切
られた2個の小径の軸穴からなる一対の第2軸穴1b及
び1cが連続して形成されている。
In the figure, reference numeral 1 denotes a cylinder provided axially movable by a hydraulic cylinder 3 provided in a main body 2, and a large diameter cylinder formed of two axial holes is provided in the cylinder 1. A pair of second shaft holes 1b and 1c composed of two small-diameter shaft holes partitioned by the first shaft hole 1a and the wall 1f are continuously formed.

前記シリンダ1の後端1dは、前記本体2に形成された
ストッパ部2aと当接可能に構成され、このシリンダ1
の軸方向における移動距離は、前記後端1dに当接して
配設されたダイヤルゲージ4によって測定される。
A rear end 1d of the cylinder 1 is configured to be able to contact a stopper portion 2a formed on the main body 2.
The moving distance in the axial direction of is measured by a dial gauge 4 arranged in contact with the rear end 1d.

前記軸穴1a〜1c内には、互いに外径が異なる第1ス
クリュ部5及び第2スクリュ部6を一体に有する一対の
第1スクリュ軸7及び第2スクリュ軸8が互いに噛合し
た状態で回転自在に配設されており、各スクリュ軸7及
び8は、減速機構9と連結軸10を介して接続されてお
り、軸方向には固定された状態で設けられている。
Inside the shaft holes 1a to 1c, a pair of first screw shaft 7 and second screw shaft 8 integrally having a first screw part 5 and a second screw part 6 having different outer diameters rotate in a state of being meshed with each other. The screw shafts 7 and 8 are freely arranged, are connected to the reduction mechanism 9 via a connecting shaft 10, and are fixed in the axial direction.

前記各第1スクリュ部5は、リードの小さいフライトで
形成された原料供給部7a及び8aと、リードの大きい
フライトで形成された混練部7b及び8bとから構成さ
れると共に、前記各スクリュ軸7及び8における各スク
リュ部5及び6間には、外径が変化する位置の異径部を
構成するテーパ部7c及び8c並びに円柱状部7e及び
8eが互いに隣接し且つ連続して形成されている。
Each of the first screw parts 5 is composed of raw material supply parts 7a and 8a formed by a flight with a small lead, and kneading parts 7b and 8b formed by a flight with a large lead. Between the screw portions 5 and 6 of the screw rods 8 and 8, tapered portions 7c and 8c and cylindrical portions 7e and 8e, which form different diameter portions at positions where the outer diameter changes, are formed adjacent to and continuous with each other. .

前記シリンダ1における前記テーパ部7c及び8cに対
応する各軸穴1a及び1cの内壁位置には内壁テーパ部
1eが形成され、これらの各テーパ部7c及び8cと前
記内壁テーパ部1eとの間には間隙t1が形成されてい
る。
An inner wall taper portion 1e is formed at an inner wall position of each of the shaft holes 1a and 1c corresponding to the taper portions 7c and 8c of the cylinder 1, and between the respective taper portions 7c and 8c and the inner wall taper portion 1e. Has a gap t 1 .

さらに、前記各円柱状部7e及び8eに対応する各軸穴
1b及び1cの内壁には、内壁筒部1ba及び1caが
形成されており、前記各円柱状部7e及び8eと各内壁
筒部1ba及び1ca間には、隙間t2が形成されると
共に、第2図で示すように、互いに重合する有効長Dが
形成されている。
Further, inner wall cylinders 1ba and 1ca are formed on the inner walls of the shaft holes 1b and 1c corresponding to the cylinder parts 7e and 8e, respectively, and the cylinder parts 7e and 8e and the inner wall cylinders 1ba are formed. Between 1 and 1ca, a gap t 2 is formed and, as shown in FIG. 2, an effective length D that overlaps each other is formed.

本発明による二軸異径の混練押出機は、前述したように
構成されており、以下に、その動作について説明する。
The twin-screw different-diameter kneading extruder according to the present invention is configured as described above, and its operation will be described below.

まず、減速機構9の駆動により、各スクリュ軸7及び8
が互いに噛合した状態で、所定の回転数に基づいて回転
する状況下において、シリンダ1内の原料供給部7a及
び8aに樹脂原料が供給されると、混練部7b及び8b
よって混練され、隙間t1及びt2を経て各第2スクリュ
部6及び各軸穴1b及び1cによって構成される昇圧部
11(押出部)を経て外部に押出される。
First, by driving the reduction mechanism 9, the screw shafts 7 and 8 are driven.
When the resin raw material is supplied to the raw material supply portions 7a and 8a in the cylinder 1 under the condition that they rotate with each other in a meshed state with each other, the kneading portions 7b and 8b.
Thus kneaded is extruded to the outside through the gap t 1 and t 2 booster 11 which is composed of the second screw part 6 and Kakujikuana 1b and 1c via (extrusion section).

前述の状態において、混練部7b及び8bにおける樹脂
原料の混練度を調節する場合、油圧シリンダ3によって
シリンダ1を軸方向に移動し、隙間t1の大きさ並びに
円柱状部7e及び8eと内壁筒部1ba及び1ca間の
有効長Dを変化させることによって任意に行うことがで
きる。
In the above-mentioned state, when adjusting the degree of kneading of the resin raw material in the kneading parts 7b and 8b, the cylinder 1 is moved in the axial direction by the hydraulic cylinder 3, and the size of the gap t 1 and the cylindrical parts 7e and 8e and the inner wall cylinder are adjusted. This can be arbitrarily performed by changing the effective length D between the portions 1ba and 1ca.

すなわち、本発明においては、テーパ部7c及び8cの
樹脂抵抗に円柱状部7e及び8eの樹脂抵抗を加算する
ことにより、従来よりも高い混練効果と幅広い調節がで
きると共に、シリンダ移動量χと抵抗値ΔPの関係が従
来ほど敏感な変化度合でなくなり、比較的精度の低い調
節で混練度の調節を行うことができる。
That is, in the present invention, by adding the resin resistance of the cylindrical portions 7e and 8e to the resin resistance of the taper portions 7c and 8c, a higher kneading effect and a wider adjustment than before can be achieved, and the cylinder movement amount χ and the resistance can be increased. The relationship of the value ΔP is not as sensitive as the conventional one, and the kneading degree can be adjusted with relatively low accuracy.

つまり、前述の(1)式によって隙間t1は3乗で効くが、
そこを流れる長さLは1乗で比例しているため、シリン
ダ1と各スクリュ軸7及び8の相対位置を変えることに
より、円柱状部7e及び8eと内壁筒部1ba及び1c
aが互いに重合する有効長Dがその抵抗値となり、これ
が1乗の変化であるため、第3図で示すA及びB曲線で
示すように、シリンダ移動量χに対する抵抗値ΔPの変
化特性が従来特性よりも大幅にゆるい勾配となることが
明らかである。
That is, although the gap t 1 is raised to the third power according to the equation (1),
Since the length L flowing there is proportional to the first power, by changing the relative positions of the cylinder 1 and the screw shafts 7 and 8, the cylindrical portions 7e and 8e and the inner wall tubular portions 1ba and 1c are changed.
Since the effective length D in which a overlaps with each other becomes the resistance value, and this is the change of the first power, the change characteristic of the resistance value ΔP with respect to the cylinder movement amount χ is conventionally as shown by the curves A and B shown in FIG. It is clear that the slope is much gentler than the characteristic.

従って、第1図の状態で、シリンダ1を右方向に移動さ
せると、テーパ部7c及び8cすなわち隙間t1は開く
方向に移動するため抵抗が下り、又、同時に、内壁筒部
1ba及び1caに対する円柱状部7e及び8eの有効
長Dも縮少する方向となり、抵抗も下るため、この円柱
状部7e及び8eとテーパ部7c及び8cを隣接させて
連続的に形成することにより抵抗値を加算することがで
き、シリンダ移動量χに対する抵抗値ΔPの変化曲線を
大巾にゆるやかにすることができる。
Therefore, when the cylinder 1 is moved to the right in the state shown in FIG. 1, the taper portions 7c and 8c, that is, the gap t 1 moves in the opening direction, so that the resistance is lowered, and at the same time, the inner wall tube portions 1ba and 1ca are removed. Since the effective length D of the cylindrical portions 7e and 8e is also reduced and the resistance is reduced, the resistance value is added by continuously forming the cylindrical portions 7e and 8e and the tapered portions 7c and 8c adjacent to each other. Therefore, the change curve of the resistance value ΔP with respect to the cylinder movement amount χ can be widened gently.

そのため、シリンダ1の移動操作は、従来のように極め
てきつい精度を要求されるものではなく、ラフな機構に
よりシリンダ1を移動させることにより、任意の混練度
を容易に得ることができる。
Therefore, the moving operation of the cylinder 1 does not require extremely tight precision as in the conventional case, and an arbitrary kneading degree can be easily obtained by moving the cylinder 1 by a rough mechanism.

又、前述の第3図で示す曲線A及びAaにおける隙間t
2は、曲線B及びBaにおける隙間t2よりも小さく設定
した場合を示している。
Further, the gap t on the curves A and Aa shown in FIG.
2 shows the case where it is set smaller than the gap t 2 in the curves B and Ba.

尚、前述の状態では、シリンダ1を右方向に移動して、
隙間t1を開くと共に、円柱状部7e及び8eの有効長
Dを縮少する状態について述べたが、前述と逆に、シリ
ンダ1を左方向に移動することにより、隙間t1を閉め
ると共に、円柱状部7e及び8eの有効長Dを長くする
ことができるものである。
In the above state, the cylinder 1 is moved to the right,
Although the state in which the clearance t 1 is opened and the effective length D of the cylindrical portions 7e and 8e is reduced has been described, contrary to the above, by moving the cylinder 1 to the left, the clearance t 1 is closed and The effective length D of the cylindrical portions 7e and 8e can be increased.

[発明の効果] 本発明による二軸異径の混練押出機は、以上のように構
成されているため、次のような効果を得ることができ
る。
[Advantages of the Invention] Since the kneading extruder having different biaxial diameters according to the present invention is configured as described above, the following effects can be obtained.

すなわち、従来のテーパ部を用いた隙間の構成に加え
て、シリンダに形成された内壁筒部に対応する円柱状部
を連続的に形成したため、シリンダ移動量に対する原料
抵抗(樹脂抵抗)の変化度合を大幅にゆるやかにするこ
とができ、高い混練調節(絞り効果)と幅の広い混練範
囲を極めて容易に得ることができる。
That is, in addition to the conventional configuration of the gap using the taper portion, the cylindrical portion corresponding to the inner wall cylinder portion formed in the cylinder is continuously formed, so that the degree of change of the raw material resistance (resin resistance) with respect to the cylinder movement amount. It is possible to significantly loosen, and it is possible to obtain a high kneading control (squeezing effect) and a wide kneading range extremely easily.

又、シリンダ移動量に対する原料抵抗(樹脂抵抗)の変
化度合がゆるやかであるため、シリンダを移動させる精
度も極めてラフな構成及び調節動作で良くなり、連続運
転中における混練度の調節が大幅に容易となる。
In addition, since the degree of change in the material resistance (resin resistance) with respect to the cylinder movement amount is gentle, the accuracy of moving the cylinder can be improved by an extremely rough configuration and adjustment operation, and the kneading degree can be adjusted easily during continuous operation. Becomes

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

第1図から第3図迄は本発明による二軸異径の混練押出
機を示すためのもので、第1図は全体構成を示す断面
図、第2図は第1図の要部を示す拡大断面図、第3図は
シリンダ移動量に対する抵抗値変化について従来構成と
本発明構成における変化度合を示す特性図、第4図から
第6図は従来の二軸異径の混練押出機を示すためのもの
で、第4図は全体構成を示す断面図、第5図及び第6図
は第4図に要部の動作原理を示す動作説明図である。 1はシリンダ、1eは内壁テーパ部、1ba,1caは
内壁筒部、5は第1スクリュ部、6は第2スクリュ部、
7は第1スクリュ軸、8は第2スクリュ軸、7c,8c
はテーパ部、7e,8e円柱状部、t1は隙間、Dは有
効長である。
FIGS. 1 to 3 are for showing a kneading extruder having a twin-screw different diameter according to the present invention. FIG. 1 is a sectional view showing the entire structure, and FIG. 2 is a main part of FIG. FIG. 3 is an enlarged sectional view, FIG. 3 is a characteristic diagram showing the degree of change in resistance value with respect to the cylinder movement amount in the conventional configuration and the configuration of the present invention, and FIGS. 4 to 6 show a conventional biaxial different diameter kneading extruder. FIG. 4 is a cross-sectional view showing the entire structure, and FIGS. 5 and 6 are operation explanatory views showing the operation principle of the main part in FIG. 1 is a cylinder, 1e is an inner wall taper portion, 1ba and 1ca are inner wall cylinder portions, 5 is a first screw portion, 6 is a second screw portion,
7 is a first screw shaft, 8 is a second screw shaft, 7c, 8c
Is a tapered portion, 7e, 8e columnar portions, t 1 is a gap, and D is an effective length.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】軸方向に移動可能に設けられたシリンダ
(1)内に回転自在に設けられた一対のスクリュ軸(7,8)
と、前記各スクリュ軸(7,8)にテーパ部(7c,8c)を介して
形成され互いに外径の異なる第1スクリュ部(5)及び第
2スクリュ部(6)と、前記テーパ部(7c,8c)に対応する前
記シリンダ(1)の内壁に形成された内壁テーパ部(1e)と
よりなる二軸異径の混練押出機において、前記テーパ部
(7c,8c)に隣接して形成された円柱状部(7e,8e)と、前記
内壁テーパ部(1e)に隣接して形成された内壁筒部(1ba,1
ca)とを備え、前記シリンダ(1)の軸方向移動に伴い、前
記テーパ部(7c,8c)と内壁テーパ部(1e)による隙間(t1)
を可変とすると共に、前記円柱状部(7e,8e)と内壁筒部
(1ba,1ca)によって重合形成される有効長(D)を可変とす
るように構成したことを特徴とする二軸異径の混練押出
機。
1. A cylinder provided so as to be movable in the axial direction.
A pair of screw shafts (7,8) rotatably installed in (1)
A first screw portion (5) and a second screw portion (6) formed on the screw shafts (7, 8) via taper portions (7c, 8c) and having different outer diameters, and the taper portion ( 7c, 8c) corresponding to the inner wall of the cylinder (1) corresponding to the inner wall tapered portion (1e) formed on the inner wall of the twin-screw different diameter kneading extruder, the taper portion
(7c, 8c) cylindrical portion (7e, 8e) formed adjacent to, and the inner wall tapered portion (1e) formed adjacent to the inner wall tubular portion (1ba, 1
ca), and the gap (t 1 ) between the tapered portions (7c, 8c) and the inner wall tapered portion (1e) along with the axial movement of the cylinder ( 1 ).
And the cylindrical part (7e, 8e) and the inner wall cylinder part
A twin-screw different diameter kneading extruder, characterized in that the effective length (D) polymerized and formed by (1ba, 1ca) is variable.
JP63273277A 1988-10-31 1988-10-31 Twin screw different diameter kneading extruder Expired - Lifetime JPH069815B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63273277A JPH069815B2 (en) 1988-10-31 1988-10-31 Twin screw different diameter kneading extruder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63273277A JPH069815B2 (en) 1988-10-31 1988-10-31 Twin screw different diameter kneading extruder

Publications (2)

Publication Number Publication Date
JPH02120006A JPH02120006A (en) 1990-05-08
JPH069815B2 true JPH069815B2 (en) 1994-02-09

Family

ID=17525602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63273277A Expired - Lifetime JPH069815B2 (en) 1988-10-31 1988-10-31 Twin screw different diameter kneading extruder

Country Status (1)

Country Link
JP (1) JPH069815B2 (en)

Families Citing this family (6)

* 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
WO2007006327A1 (en) * 2005-07-12 2007-01-18 Borealis Technology Oy Counter-rotating twin screw extruder
US20080267003A1 (en) * 2007-04-24 2008-10-30 Shashank Gulabchand Kasliwal Extrusion method and apparatus
JP5508571B1 (en) * 2013-05-15 2014-06-04 東芝機械株式会社 Twin screw extruder
JP6639800B2 (en) * 2014-05-08 2020-02-05 東芝機械株式会社 Screw for extruder, extruder and extrusion method
JP6446234B2 (en) * 2014-10-27 2018-12-26 東芝機械株式会社 Screw for extruder, screw element, extruder and extrusion method

Also Published As

Publication number Publication date
JPH02120006A (en) 1990-05-08

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