JP6719347B2 - Twin screw extruder - Google Patents
Twin screw extruder Download PDFInfo
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- JP6719347B2 JP6719347B2 JP2016179984A JP2016179984A JP6719347B2 JP 6719347 B2 JP6719347 B2 JP 6719347B2 JP 2016179984 A JP2016179984 A JP 2016179984A JP 2016179984 A JP2016179984 A JP 2016179984A JP 6719347 B2 JP6719347 B2 JP 6719347B2
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- gate
- screw
- kneading
- twin
- screw extruder
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- 238000004898 kneading Methods 0.000 claims description 57
- 239000000463 material Substances 0.000 claims description 17
- 238000004140 cleaning Methods 0.000 claims description 6
- 230000002093 peripheral effect Effects 0.000 claims description 5
- 229920005989 resin Polymers 0.000 description 9
- 239000011347 resin Substances 0.000 description 9
- 238000011144 upstream manufacturing Methods 0.000 description 4
- 238000011109 contamination Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 229920005992 thermoplastic resin Polymers 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/48—Mixing; 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
- B29B7/482—Mixing; 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 provided with screw parts in addition to other mixing parts, e.g. paddles, gears, discs
- B29B7/483—Mixing; 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 provided with screw parts in addition to other mixing parts, e.g. paddles, gears, discs the other mixing parts being discs perpendicular to the screw axis
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/268—Throttling of the flow, e.g. for cooperating with plasticising elements or for degassing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means 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
- B29C48/40—Means 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
- B29C48/402—Means 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 the screws having intermeshing parts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
- B29C2948/926—Flow or feed rate
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
本発明は、スクリュに対向するゲートを設けてそのゲートの開閉により混練物が送られる流路の広狭を制御して混練度を調整する二軸押出機に関する。 The present invention relates to a twin-screw extruder in which a gate facing a screw is provided and the degree of kneading is adjusted by controlling the width and width of a flow path through which the kneaded material is fed by opening and closing the gate.
押出機の混練の対象となる熱可塑性樹脂は種々様々であり、またその溶融粘度は高粘度のものから低粘度のものに亘る。そして、これらの熱可塑性樹脂には種々の添加物が添加される。かかる対象物を分散性良く混練するためには、適切な混練条件やスクリュエレメントの選定が必要であるがそれのみでは十分でないことから、混練物が送られる流路を絞って混練物の充填率や滞留時間を制御して混練度を調整する方法が種々提案されている。 There are various kinds of thermoplastic resins to be kneaded in the extruder, and the melt viscosity thereof ranges from high viscosity to low viscosity. Then, various additives are added to these thermoplastic resins. In order to knead such an object with good dispersibility, it is necessary to select appropriate kneading conditions and screw elements, but this alone is not sufficient. Therefore, the flow rate of the kneaded material is reduced and the filling rate of the kneaded material is reduced. Various methods have been proposed for adjusting the kneading degree by controlling the residence time and the residence time.
例えば、特許文献1に、シリンダの貫通内孔に2本のスクリュが回転できるように挿入され、その長手方向に供給部と、第1輸送部と、第1混練部と、ゲート部と、第2輸送部と第2混練部兼吐出部とが形成され、前記ゲート部において混練度調整が行われるとともに、最も上流に位置する前記第1混練部において、前記シリンダの貫通内孔の壁面に移動自在に設けられた壁面体をスクリュの軸直角方向へ移動させることにより、前記シリンダの貫通内孔の壁面とスクリュの外周との間隔を変化させて可塑化調整を行うスクリュ式二軸混練押出機の混練度調整装置が提案されている。この混練度調整装置は、従来困難であった溶融粘度が高い樹脂から低い樹脂まで良好に混練することができるとされる。 For example, in Patent Document 1, two screws are rotatably inserted in a through hole of a cylinder, and a supply unit, a first transport unit, a first kneading unit, a gate unit, and a first screw unit are provided in a longitudinal direction of the screw. A second transporting part and a second kneading part/discharging part are formed, and the kneading degree is adjusted in the gate part, and the first kneading part located at the most upstream is moved to the wall surface of the through-hole of the cylinder. A screw-type twin-screw kneading extruder that adjusts plasticization by changing the distance between the wall surface of the through-hole of the cylinder and the outer circumference of the screw by moving a freely provided wall body in the direction perpendicular to the screw axis. A kneading degree adjusting device has been proposed. It is said that this kneading degree adjusting device can satisfactorily knead a resin having a high melt viscosity to a resin having a low melt viscosity, which has been difficult in the past.
また、特許文献2に、バレル内に回転自在に挿通され且つ混練部を備えた混練スクリュで混練される材料を上流側から下流側に向けて送りながら連続的に混練する処理装置に設けられる混練度調整機構であって、前記混練スクリュの混練部の下流側に設けられて、材料を上流側に押し戻すことで前記混練部での滞留を促す押戻し部と、前記押戻し部の外周面に対向する対向面を有すると共に押戻し部に対して前記対向面が近接離反することで前記材料の混練度を調整する混練度調整部材とを有する混練度調整機構が提案されている。この混練度調整機構は、混練度調整部材の滞留作用と押戻し部の上流側への押し戻し作用とが相互に作用するので、混練度調整部材を開閉しても混練度が急激に変化せず線形的に変化するとされる。また、混練度調整機構は、混練度調整部材が全閉時にバレルの内周面から突出しないので混練スクリュに作用するスラスト力を低くすることができるとされる。 Further, in Patent Document 2, a kneading device provided in a processing device for continuously kneading a material to be kneaded by a kneading screw having a kneading portion rotatably inserted in a barrel and feeding the material from upstream to downstream. A degree adjusting mechanism, which is provided on the downstream side of the kneading section of the kneading screw and which pushes back the material to the upstream side to promote retention in the kneading section, and an outer peripheral surface of the pushing back section. A kneading degree adjusting mechanism has been proposed that has a facing surface facing each other and has a kneading degree adjusting member that adjusts the kneading degree of the material by moving the facing surface closer to and away from the push-back portion. In this kneading degree adjusting mechanism, since the staying action of the kneading degree adjusting member and the pushing-back action of the push-back portion to the upstream side interact, the kneading degree does not change rapidly even when the kneading degree adjusting member is opened and closed. It is said to change linearly. Further, it is said that the kneading degree adjusting mechanism can reduce the thrust force acting on the kneading screw because the kneading degree adjusting member does not project from the inner peripheral surface of the barrel when fully closed.
特許文献1に記載の二軸混練押出機の混練度調整装置は、従来困難であった溶融粘度が高い樹脂から低粘度の樹脂まで良好に混練することができるが、このためには、第1混練部に設けられる壁面体の内面がシリンダの貫通内孔の壁面に一致した状態(可塑化位置M)から壁面体の内面がシリンダの貫通内孔の壁面から上下に大きく離れた状態(非可塑化位置N)まで移動することにより合成樹脂原料の可塑化調整が行われる混練度調整装置と、ゲート部に設けられるフライトが形成されていない円柱状のスクリュとこのスクリュの外周に沿うように離隔可能に設けられたロータリースロットバーからなるロータリースロットバー式混練度調整装置と、2つの混練度調整装置を設けなければならないという問題がある。 The kneading degree adjusting device of the twin-screw kneading extruder described in Patent Document 1 can satisfactorily knead a resin having a high melt viscosity to a resin having a low viscosity, which has been difficult in the past. From the state where the inner surface of the wall surface body provided in the kneading part coincides with the wall surface of the through hole of the cylinder (plasticization position M), the inner surface of the wall surface body is largely separated from the wall surface of the through hole of the cylinder vertically (non-plasticizing). The kneading degree adjusting device that adjusts the plasticization of the synthetic resin raw material by moving to the liquefying position N), the cylindrical screw with no flight formed in the gate part, and the separating part along the outer periphery of this screw. There is a problem that it is necessary to provide a rotary slot bar type kneading degree adjusting device composed of a rotary slot bar that is possible and two kneading degree adjusting devices.
特許文献2に記載の混練度調整機構は、従来困難であった溶融粘度が低い樹脂の混練度調整が困難であるという問題がある。また、特許文献1に記載の混練度調整装置又は特許文献2に記載の混練度調整機構はいずれもシリンダ又はバレル内壁に凹みを有する形態で使用されるので、この凹みに混流物が固着又は離脱して所望の混練が困難になり、さらに製品にコンタミを生じるという不具合がある。また、特許文献1に記載のゲート部に設けられる円柱状のスクリュにおいても同様に混流物が固着又は離脱して製品にコンタミを生じるという不具合がある。 The kneading degree adjusting mechanism described in Patent Document 2 has a problem that it is difficult to adjust the kneading degree of a resin having a low melt viscosity, which has been difficult in the past. In addition, since the kneading degree adjusting device described in Patent Document 1 or the kneading degree adjusting mechanism described in Patent Document 2 is used in a form in which the inner wall of the cylinder or barrel has a recess, the mixed flow adheres to or separates from the recess. As a result, the desired kneading becomes difficult, and further, the product is contaminated. Further, in the cylindrical screw provided in the gate portion described in Patent Document 1, similarly, there is a problem that the mixed flow material is fixed or released to cause contamination of the product.
本発明は、このような従来の問題点に鑑み、混練度を調整するゲートに起因するコンタミを防止することができ、従来困難であった溶融粘度が高い樹脂から低粘度の樹脂まで良好に混練度を調整することができる二軸押出機を提供することを目的とする。 In view of such conventional problems, the present invention can prevent contamination due to a gate for adjusting the degree of kneading, and kneads well from a resin having a high melt viscosity to a resin having a low viscosity, which has been difficult in the past. An object of the present invention is to provide a twin-screw extruder whose degree can be adjusted.
本発明に係る二軸押出機は、二軸押出機のシリンダ横断面にスクリュを挟んで開閉し、混練物の下流への移送流路を絞って混練度調整を行うゲートが設けられた二軸押出機であって、前記スクリュのゲートに対向する部分のゲートスクリュエレメントは、1ピッチ以上の長さを有してセルフクリーニングするように相互にかみ合い、前記ゲートは、前記シリンダの内周面から前記ゲートスクリュエレメントの山径にほぼ等しい位置まで突出して前記移送流路を絞ることができる突出量調整手段を有してなる。 The twin-screw extruder according to the present invention is a twin-screw extruder provided with a gate for adjusting the degree of kneading by opening and closing a screw in the cylinder cross section of the twin-screw extruder, and squeezing the transfer passage to the downstream of the kneaded material. In the extruder, a gate screw element of a portion facing the gate of the screw has a length of 1 pitch or more and is engaged with each other so as to be self-cleaning, and the gate is formed from an inner peripheral surface of the cylinder. The gate screw element is provided with a protrusion amount adjusting means capable of protruding to a position substantially equal to the mountain diameter of the gate screw element to narrow the transfer passage.
上記発明において、ゲートスクリュエレメントは、搬送部又は混練部に設けられるスクリュエレメントの山径より5%〜20%小さい山径を有するものであるのがよい。また、ゲートスクリュエレメントは、逆フライト又は逆ずらしニーディングディスクにすることができる。 In the above invention, the gate screw element preferably has a mountain diameter that is 5% to 20% smaller than the mountain diameter of the screw element provided in the conveying section or the kneading section. Also, the gate screw element can be a reverse flight or reverse offset kneading disc.
また、上記発明において、ゲートは、混練部の下流に設けられるのがよい。 Further, in the above invention, the gate is preferably provided downstream of the kneading section.
本発明に係る二軸押出機は、混練度を調整するゲートに起因するコンタミを防止することができ、従来困難であった溶融粘度が高い樹脂から低粘度の樹脂まで良好に混練度を調整することができる。 The twin-screw extruder according to the present invention can prevent contamination due to a gate that adjusts the kneading degree, and adjusts the kneading degree satisfactorily from a resin having a high melt viscosity to a resin having a low viscosity, which was conventionally difficult. be able to.
以下、本発明を実施するための形態について図面を基に説明する。図1は、本発明に係る二軸押出機にゲートが設けられた部分の断面を示す。本二軸押出機10は、図1(a)に示すように、シリンダ11の横断面にスクリュ12を挟んで開閉するゲート15、すなわち上下動するゲート扉150Aとゲート扉150Bを備えたゲート15を有し、スクリュ12はゲート15に対向する部分にゲートスクリュエレメント125を有している。そして、ゲートスクリュエレメント125は1ピッチ以上の長さを有しており、図1(b)に示すように、セルフクリーニングするように相互にかみ合うようになっている。ゲート15は、シリンダ11の内周面からゲートスクリュエレメント125の山径にほぼ等しい位置まで突出して(閉じて)移送流路を絞ることができる突出量調整手段(図示せず)を有している。
Hereinafter, embodiments for carrying out the present invention will be described with reference to the drawings. FIG. 1 shows a cross section of a portion where a gate is provided in a twin-screw extruder according to the present invention. As shown in FIG. 1A, the twin-
ゲート15は、上述のように、突出量調整手段によりその突出量が調整されるようになっている。図1(b)に示すように、ゲート扉15A、ゲート扉15Bは突出量調整手段により上下動し、最大突出量になるとき(全閉時)はゲートスクリュエレメント125にほとんど接してその山径にほぼ等しい位置まで突出する。ゲート扉150A、ゲート扉150Bの突出量が最小のとき(全開時)は、ゲート扉150A、150Bがシリンダ内面Cとほぼ面一状態になっている。ゲート扉150A、ゲート扉150Bの突出量の調整、すなわちゲート15を開閉することにより混練物の移送流路を絞ることができ、混練部における混練物の充満率や混練物の滞留時間を調整し、混練度調整を行うことができる。本二軸押出機においては、ゲート15(150A、150B)が常にシリンダ内面Cから突出する状態で使用されるから、図1(b)に示すメンテナンス状態のようなシリンダ内面に凹みが形成されることがない。このため、シリンダ内面の凹みに混練物が固着又は離脱することによる不具合を防止することができる。なお、ゲート15は、メンテナンス時には図1(b)に示すように、ゲート扉150A、ゲート扉150Bをシリンダ内面Cよりも引っ込ませることができるようになっており、メンテナンスのときにゲート扉150A、ゲート扉150Bを上下動させ、ゲート回りの清掃、メンテナンスを行うことができる。
As described above, the projection amount of the
ゲート15に対向してゲートスクリュエレメント125が設けられている。ゲートスクリュエレメント125は、1ピッチ以上の長さを有し、相互にかみ合いセルフクリーニングできるようになっている。このため、ゲートスクリュエレメント125は、新鮮な表面を維持することができる。
A
また、ゲートスクリュエレメント125は、搬送部や混乱部に設けられる通常のスクリュエレメントよりは小さくなっている。ゲートスクリュエレメント125の山径は、図2(a)に示すように、図2(b)に示す通常のスクリュエレメント120の山径Dの(0.95〜0.80)*D、すなわち、5〜20%小さくするのがよい。これにより、移送流路を絞って所要の混練度調整を行うことができるとともに、混練物及びゲート部分に所要の圧力変動を与えることができ、シリンダ内面Cから突出したゲート15に混練物が固着するのを防止することができる。なお、図2において、A寸法はスクリュ中心間距離である。
Further, the
ゲートスクリュエレメント125は、その形状を逆フライト又は逆ずらしニーディングディスクを使用することができる。これにより、混練部における混練物の充満率や滞留時間の調整範囲をさらに拡大することができる。なお、逆ずらしニーディングディスクは、
セルフクリーニングを有し、搬送能力は低いが高い混練圧力を生じさせることができるスクリュエレメントである。
The
It is a screw element which has self-cleaning and can generate a high kneading pressure with a low carrying capacity.
10 二軸押出機
11 シリンダ
12 スクリュ
120 通常のスクリュエレメント
125 ゲートスクリュエレメント
15 ゲート
150A、150B ゲート扉
125 ゲートスクリュエレメント
10 twin screw extruder
11 cylinders
12 screws
120 Normal screw element
125 gate screw element
15 gates
150A, 150B gate door
125 gate screw element
Claims (4)
前記スクリュのゲートに対向する部分のゲートスクリュエレメントは、1ピッチ以上の長さを有してセルフクリーニングするように相互にかみ合い、
前記ゲートは、前記シリンダの内周面から前記ゲートスクリュエレメントの山径にほぼ等しい位置まで突出して前記移送流路を絞ることができる突出量調整手段を有してなる二軸押出機。 A twin-screw extruder provided with a gate for adjusting the degree of kneading by opening and closing a screw in the cylinder cross section of the twin-screw extruder, and squeezing the transfer passage to the downstream of the kneaded material,
The gate screw element of the portion facing the gate of the screw has a length of 1 pitch or more and is engaged with each other so as to be self-cleaning,
The gate is a twin-screw extruder having projection amount adjusting means that can project from the inner peripheral surface of the cylinder to a position approximately equal to the mountain diameter of the gate screw element to narrow the transfer passage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2016179984A JP6719347B2 (en) | 2016-09-14 | 2016-09-14 | Twin screw extruder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2016179984A JP6719347B2 (en) | 2016-09-14 | 2016-09-14 | Twin screw extruder |
Publications (2)
Publication Number | Publication Date |
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JP2018043419A JP2018043419A (en) | 2018-03-22 |
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