JPH0439022A - Series two-stage extruding machine - Google Patents
Series two-stage extruding machineInfo
- Publication number
- JPH0439022A JPH0439022A JP2146728A JP14672890A JPH0439022A JP H0439022 A JPH0439022 A JP H0439022A JP 2146728 A JP2146728 A JP 2146728A JP 14672890 A JP14672890 A JP 14672890A JP H0439022 A JPH0439022 A JP H0439022A
- Authority
- JP
- Japan
- Prior art keywords
- screw
- stage
- raw materials
- extruding machine
- 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.)
- Pending
Links
- 239000002994 raw material Substances 0.000 claims abstract description 27
- 230000010006 flight Effects 0.000 abstract description 10
- 239000011347 resin Substances 0.000 abstract description 8
- 229920005989 resin Polymers 0.000 abstract description 8
- 238000002844 melting Methods 0.000 abstract description 4
- 230000008018 melting Effects 0.000 abstract description 4
- 238000002156 mixing Methods 0.000 abstract description 3
- 238000010008 shearing Methods 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract description 2
- 239000006185 dispersion Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 238000001125 extrusion Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 4
- 239000000155 melt Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 235000012438 extruded product Nutrition 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
Classifications
-
- 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
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/67—Screws having incorporated mixing devices not provided for in groups B29C48/52 - B29C48/66
-
- 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
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/64—Screws with two or more threads
- B29C48/645—Screws with two or more threads neighbouring threads and channels having identical configurations
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明はプラスチックの可塑化溶融を行う押出機、ゴム
用押出機等に適用可能な直列二段押出機に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an in-line two-stage extruder applicable to an extruder for plasticizing and melting plastics, an extruder for rubber, and the like.
(従来の技術)
従来もプラスチックを可塑化溶融させる押出機において
、第8図に示すような直列二段押出機が提案されている
。この押出機は、最近ポリプロピレンやポリスチレン等
の二軸延伸フィルムを製造する場合に、特に多く使用さ
れる様になって来ている。(Prior Art) Conventionally, as an extruder for plasticizing and melting plastic, a two-stage series extruder as shown in FIG. 8 has been proposed. This extruder has recently come into widespread use, especially when producing biaxially stretched films of polypropylene, polystyrene, and the like.
通常第1段押出機のスクリュ1′とシリンダ2′は、小
口径で高速にして、可塑化、溶融機能を受は持たせ、第
2段押出機のスクリュ8とシリンダ9は大口径、低速に
して、冷却、均質化機能並びにポンピング機能を受は持
たせている。Usually, the screw 1' and cylinder 2' of the first stage extruder have a small diameter and high speed to have plasticizing and melting functions, and the screw 8 and cylinder 9 of the second stage extruder have a large diameter and low speed. The receiver has cooling, homogenizing, and pumping functions.
なお、第1段押出機において3は減速駆動装置、4は駆
動電動機、5は加熱用ヒータ、6はホッパ、また第2段
押出機において10は減速駆動装置、11は駆動電動機
、12は加熱用ヒータ、13はシリンダ冷却ユニット、
14はダイ、15は押出品である。この様に機能を2つ
の押出機に分担させると、小型押出機で大容量の製品を
品質良く押し出すことが可能になる。In addition, in the first stage extruder, 3 is a deceleration drive device, 4 is a drive electric motor, 5 is a heating heater, and 6 is a hopper, and in the second stage extruder, 10 is a deceleration drive device, 11 is a drive electric motor, and 12 is a heating device. 13 is a cylinder cooling unit,
14 is a die, and 15 is an extruded product. By sharing the functions between two extruders in this way, it becomes possible to extrude a large volume of products with good quality using a small extruder.
(発明が解決しようとする課題)
従来の直列二段押出機では、樹脂は第8図に示す如く第
1段押出機のスクリュ1′の先端部を経た後、接続管7
′を通って第2段押出機に送られる。しかしながら押出
量を従来能力以上に増加させるべく、第1段押出機のス
クリュ回転を更に高速化させると、第1段押出機先端で
の樹脂は温度的なバラツキが大きくなり、未溶融物も混
入する等極めて不均質な状態となる。このため第2段押
出機で、これを均質化させるためには、口径を大きくし
たり、L/Dを長くしたりする等の仕様を変更する必要
があった。(Problems to be Solved by the Invention) In the conventional two-stage series extruder, the resin passes through the tip of the screw 1' of the first stage extruder, and then passes through the connecting pipe 7.
' and sent to the second stage extruder. However, when the screw rotation speed of the first-stage extruder is further increased in order to increase the extrusion amount beyond the conventional capacity, the temperature of the resin at the tip of the first-stage extruder increases, and unmelted substances are mixed in. This results in an extremely heterogeneous state. Therefore, in order to homogenize the second stage extruder, it was necessary to change the specifications such as increasing the diameter or lengthening the L/D.
このように第8図の直列二段押出機では、押出量を従来
能力以上に増加させるべく、第1段押出機のスクリュ回
転を更に高速化させると、第1段押出機先端での原料は
温度のバラツキが大きくなり、未溶融物も混入する等極
めて不均質な状態となる。このため従来以上に押出能力
を上げることは、従来構造のままでは極めて困難であっ
た。In this way, in the series two-stage extruder shown in Fig. 8, when the screw rotation speed of the first-stage extruder is further increased in order to increase the extrusion amount beyond the conventional capacity, the raw material at the tip of the first-stage extruder is The temperature variation becomes large and unmelted substances are mixed in, resulting in an extremely non-uniform state. For this reason, it has been extremely difficult to increase the extrusion capacity beyond the conventional structure with the conventional structure.
また接続管7′に異物濾過用のフィルタを設ける場合が
あるが、この場合には原料は完全溶融していることが必
要で、もしメルト中に未溶融物が混入する場合には、フ
ィルタに詰って第1段押出機先端に圧力変動を住しさせ
る原因となる。In addition, a filter for filtering out foreign matter may be installed in the connecting pipe 7', but in this case, the raw material must be completely melted, and if unmelted matter gets mixed into the melt, the filter This causes blockage and pressure fluctuations at the tip of the first stage extruder.
本発明は第1段押出機を出た原料を、できるだけ均質化
させることにより、押出能力を向上させようとするもの
である。The present invention aims to improve the extrusion capacity by homogenizing the raw material exiting the first stage extruder as much as possible.
(課題を解決するための手段)
このため本発明は、第1段押出機と第2段押出機を直列
に接続した直列二段押出機において、第1段押出機のス
クリュ先端側に、同スクリュの途中の位置から側方へ原
料を排出する第2段押出機に通じる出口を設けると共に
、同出口に位1する部分の第1段押出機のスクリュを2
条以上の多条フライト形状、又はこれに類イ以する形状
としてなるもので、これを課題解決のための手段とする
ものである。(Means for Solving the Problems) For this reason, the present invention provides a two-stage extruder in which a first-stage extruder and a second-stage extruder are connected in series. In addition to providing an outlet leading to the second stage extruder that discharges the raw material to the side from a position midway through the screw, the screw of the first stage extruder at the part located at the same exit is
It is a multi-flight shape with more than one strip, or a similar shape, and is used as a means to solve the problem.
(作用)
原料はスクリュが回転するに伴いフライトによって第1
段押出機出口部で切断され、薄層化されながら進む。従
ってスクリュの回転に伴って異なった溝にある原料が次
々と薄層化されて積層するので、境界面が常に更新され
て混合が効率的に促進される。これにより樹脂の可塑化
度合のバラツキや温度バラツキが均一化し、均質な原料
が得られる。また切断時、樹脂に与えられる剪断エネル
ギーも溶融の均質化に効果がある。(Function) As the screw rotates, the raw material is transported to the first place by flight.
It is cut at the exit of the stage extruder and advances while being made into a thin layer. Therefore, as the screw rotates, the raw materials in different grooves are successively thinned and stacked, so that the boundary surfaces are constantly updated and mixing is promoted efficiently. As a result, variations in the degree of plasticization of the resin and variations in temperature are made uniform, and a homogeneous raw material can be obtained. Furthermore, the shearing energy given to the resin during cutting is also effective in homogenizing the melt.
(実施例)
以下本発明を図面の実施例について説明すると、第1図
〜第7図は本発明の実施例を示し、3は減速駆動装置、
4は駆動電動機、5は加熱用ヒータ、6はホッパ、8は
第2段押出機スクリュ、9はシリンダ、10は減速駆動
装置、11は駆動電動機、12は加熱用ヒータ、13は
シリンダ冷却ユニット、14はダイ、15は押出品であ
り、これらは第8図の従来と同じである。(Embodiment) The present invention will be described below with reference to the embodiments of the drawings. Figs. 1 to 7 show embodiments of the present invention, 3 is a deceleration drive device,
4 is a drive motor, 5 is a heating heater, 6 is a hopper, 8 is a second stage extruder screw, 9 is a cylinder, 10 is a reduction drive device, 11 is a drive motor, 12 is a heating heater, 13 is a cylinder cooling unit , 14 is a die, and 15 is an extruded product, which are the same as the conventional one shown in FIG.
ここで第8図と相違する点について説明すると、1は第
1段押出機スクリュで、先端部1aは2条以上の多条フ
ライト形状に構成されている。Here, the differences from FIG. 8 will be explained. Reference numeral 1 denotes a first stage extruder screw, and the tip end 1a is configured in a multi-flight shape with two or more threads.
2は第1段押出機スクリュシリンダで、前記スクリュl
の先端部1aの途中の位置から原料を第2段押出機に通
じる接続管7へ排出する出口16を有する。2 is a screw cylinder of the first stage extruder, and the screw l
It has an outlet 16 for discharging the raw material from a midway position of the tip 1a to the connecting pipe 7 leading to the second stage extruder.
次に作用を説明すると、第1段押出機で可塑化熔融され
た原料は、第1図の出口16を通り、接続管7を経由し
て第2段押出機へ送られる。Next, to explain the operation, the raw material plasticized and melted in the first stage extruder passes through the outlet 16 in FIG. 1 and is sent to the second stage extruder via the connecting pipe 7.
原料がシリンダ2から出口16へ押し出される時、スク
リュ1の回転によって出口16の原料は、スクリュ1の
先端部1aの2条以上多条のフライトによって切断され
る。第2図の場合はスクリュ1回転で原料は2度切断さ
れ、第4図(先端部21には放射状のフライト21aが
形成されている)の場合は4度切断される。When the raw material is pushed out from the cylinder 2 to the outlet 16, the raw material at the outlet 16 is cut by two or more flights at the tip 1a of the screw 1 as the screw 1 rotates. In the case of FIG. 2, the raw material is cut twice in one rotation of the screw, and in the case of FIG. 4 (radial flights 21a are formed at the tip 21), the raw material is cut four times.
また原料の出口16における管内押出速度は、高速で回
転する多条フライトの速度に比べて非常に遅いので、原
料は第2図、第4図の出口16に図示した如く、薄層2
2.23が重なった状態で送られる。原料が切断され、
薄層化される状態は、第3図、第5図で一層理解される
。In addition, since the extrusion speed of the raw material in the tube at the outlet 16 is very slow compared to the speed of the multi-filament flight rotating at high speed, the raw material is transferred into a thin layer 2 as shown at the outlet 16 in FIGS. 2 and 4.
2.23 will be sent overlapping. The raw material is cut,
The state of thinning is better understood in FIGS. 3 and 5.
なお、第2図〜第5図に記載した実施例は、原料を通常
のスクリュフライトで切断する構造としているが、フラ
イト形状はどの様なものでもよく、要するに切断できさ
えすればよい。例えば第3図の先端部1aを第7図の先
端部24に、第5図の先端部21を第6図の先端部25
のように変形させてもよい。また以上の実施例において
第2段押出機に代え、ギヤポンプの様なメルトポンプを
採用することもできる。Although the embodiments shown in FIGS. 2 to 5 have a structure in which the raw material is cut with ordinary screw flights, the shape of the flights may be any shape, as long as the material can be cut. For example, the tip 1a in FIG. 3 is replaced with the tip 24 in FIG. 7, and the tip 21 in FIG. 5 is replaced with the tip 25 in FIG.
It may be modified as follows. Furthermore, in the above embodiments, a melt pump such as a gear pump may be used instead of the second stage extruder.
(発明の効果)
以上詳細に説明した如く本発明は構成されているので、
原料はスクリュが回転するに伴い、フライトによって第
1段押出機出口で切断されて、薄層化されながら進む。(Effects of the Invention) Since the present invention is configured as explained in detail above,
As the screw rotates, the raw material is cut by flights at the exit of the first-stage extruder and advances while being made into a thin layer.
またスクリュが多条フライト形状に類似する形状の場合
には、1つのフライトで切断されて次のフライトで切断
される迄は、この両フライトの間の溝にある原料が積層
される。従ってスクリュの回転に伴って異なった溝にあ
る原料が次々と薄層化されて積層するので、境界面が常
に更新され、混合が効率的に促進される。これにより樹
脂の可塑化度合のバラツキや温度バラツキが均一化し、
均質な原料が得られる。また切断時、樹脂に与えられる
剪断エネルギーも溶融の均質化に効果がある。以上のこ
とから直列二段押出機の押出能力を従来より格段に向上
させることができる。Further, when the screw has a shape similar to a multi-flight shape, the raw material in the groove between the two flights is stacked until it is cut in one flight and cut in the next flight. Therefore, as the screw rotates, the raw materials in different grooves are successively thinned and stacked, so that the boundary surfaces are constantly updated and mixing is promoted efficiently. This equalizes variations in the degree of plasticization and temperature variations in the resin,
A homogeneous raw material is obtained. Furthermore, the shearing energy given to the resin during cutting is also effective in homogenizing the melt. From the above, the extrusion capacity of the two-stage in-line extruder can be significantly improved compared to conventional extruders.
第1図は本発明の第1実施例に係る直列二段押出機の側
断面図、第2図は第1図におけるA部の拡大断面図、第
3図は第2図のB−B断面図、第4図は本発明の第2実
施例の第2図に対、応して示す拡大断面図、第5図は第
4図のC〜り
C断面図、第6図は第3実施例で、第1図と構造を異に
するスクリュの断面図、第7図は第4実施例で第1図と
構造を異にするスクリュの断面図、第8図は従来の直列
二段押出機を示す側断面図である。
図の主要部分の説明
1−第1段押出機スクリュ
1a・・−スクリュ先端部
2−第1段押出機シリンダ
8−第2段押出機スクリュ
16−出口
第3図
1A5r:!U
第2図
JP)4図Fig. 1 is a side sectional view of a two-stage in-line extruder according to the first embodiment of the present invention, Fig. 2 is an enlarged sectional view of section A in Fig. 1, and Fig. 3 is a sectional view taken along line B-B in Fig. 2. 4 is an enlarged sectional view corresponding to FIG. 2 of the second embodiment of the present invention, FIG. 5 is a sectional view from C to C of FIG. 4, and FIG. 6 is a sectional view of the third embodiment. For example, Fig. 7 is a cross-sectional view of a screw with a structure different from Fig. 1, Fig. 7 is a sectional view of a screw of the fourth embodiment and a structure different from Fig. 1, and Fig. 8 is a conventional in-line two-stage extrusion. It is a side sectional view showing the machine. Explanation of main parts of the figure 1 - 1st stage extruder screw 1a... - Screw tip 2 - 1st stage extruder cylinder 8 - 2nd stage extruder screw 16 - Exit Figure 3 1A5r:! U Figure 2 JP) Figure 4
Claims (1)
押出機において、第1段押出機のスクリュ先端側に、同
スクリュの途中の位置から側方へ原料を排出する第2段
押出機に通じる出口を設けると共に、同出口に位置する
部分の第1段押出機のスクリュを2条以上の多条フライ
ト形状、又はこれに類似する形状としたことを特徴とす
る直列二段押出機。In a series two-stage extruder in which a first-stage extruder and a second-stage extruder are connected in series, a second stage extruder that discharges raw materials from a midway position of the screw to the side of the screw tip of the first-stage extruder Two stages in series, characterized by having an outlet leading to the stage extruder, and having the screw of the first stage extruder located at the exit in a multi-flight shape with two or more threads, or a shape similar to this. Extruder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2146728A JPH0439022A (en) | 1990-06-05 | 1990-06-05 | Series two-stage extruding machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2146728A JPH0439022A (en) | 1990-06-05 | 1990-06-05 | Series two-stage extruding machine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0439022A true JPH0439022A (en) | 1992-02-10 |
Family
ID=15414234
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2146728A Pending JPH0439022A (en) | 1990-06-05 | 1990-06-05 | Series two-stage extruding machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0439022A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06250645A (en) * | 1993-02-23 | 1994-09-09 | Katsumi Hagitani | Tuning unit |
WO1999047337A1 (en) * | 1998-03-18 | 1999-09-23 | Loughborough University Innovations Limited | Method and apparatus for mixing |
KR100843609B1 (en) * | 2006-03-09 | 2008-07-03 | 주식회사 엘지화학 | Incompatible high molecule resin extruding machine |
-
1990
- 1990-06-05 JP JP2146728A patent/JPH0439022A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06250645A (en) * | 1993-02-23 | 1994-09-09 | Katsumi Hagitani | Tuning unit |
WO1999047337A1 (en) * | 1998-03-18 | 1999-09-23 | Loughborough University Innovations Limited | Method and apparatus for mixing |
KR100843609B1 (en) * | 2006-03-09 | 2008-07-03 | 주식회사 엘지화학 | Incompatible high molecule resin extruding machine |
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