JPH028562B2 - - Google Patents
Info
- Publication number
- JPH028562B2 JPH028562B2 JP58063009A JP6300983A JPH028562B2 JP H028562 B2 JPH028562 B2 JP H028562B2 JP 58063009 A JP58063009 A JP 58063009A JP 6300983 A JP6300983 A JP 6300983A JP H028562 B2 JPH028562 B2 JP H028562B2
- Authority
- JP
- Japan
- Prior art keywords
- screw
- resin
- zone
- filler
- screw groove
- 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
Links
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
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
- B29B7/428—Parts or accessories, e.g. casings, feeding or discharging means
- B29B7/429—Screws
-
- 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
- B29C48/53—Screws having a varying channel depth, e.g. varying the diameter of the longitudinal screw trunk
-
- 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
- B29C48/56—Screws having grooves or cavities other than the thread or the channel
-
- 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
- B29C48/565—Screws having projections other than the thread, e.g. pins
-
- 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
- B29C48/65—Screws with two or more threads neighbouring threads or channels having different configurations, e.g. one thread being lower than its neighbouring thread
-
- 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
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
本発明は樹脂成形機等における樹脂の可塑化混
練装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a plasticizing and kneading device for resin in a resin molding machine or the like.
抽出成形機や射出成形機等の成形機において、
各種のフイラーを樹脂とともに可塑化混練装置内
に直接投入して成形する直接複合成形には各種の
難しい問題がある。即ち、フイラーの完全分散が
極めて困難で、2次凝集が発生したり、或は、フ
イラーの切断、破損の問題等多くの難しい問題が
ある。特に、樹脂がペレツトの場合は難しく、ビ
ーズ状或はパウダー状の場合は粒径が小さいため
比較的簡単なので、ここでは、主にペレツト状の
樹脂を対象にして説明する。 In molding machines such as extraction molding machines and injection molding machines,
Direct composite molding, in which various fillers and resins are directly introduced into a plasticizing and kneading device and molded, has various difficult problems. That is, it is extremely difficult to completely disperse the filler, and there are many difficult problems such as secondary agglomeration, cutting, and breakage of the filler. In particular, it is difficult to do this when the resin is in the form of pellets, whereas it is relatively easy to do so when the resin is in the form of beads or powder because the particle size is small, so here we will mainly explain the resin in the form of pellets.
本発明はこれらの問題を解決するためのもの
で、主に成形機のスクリユに関するものである。 The present invention is intended to solve these problems and mainly relates to a screw for a molding machine.
一般に、通常の成形機では、第1図に示すよう
に、スクリユ1は材料供給孔2側から供給ゾーン
3、及び、圧縮ゾーン4と計量ゾーン5とでなる
可塑化混練ゾーン6で構成される。圧縮ゾーン4
は、スクリユ溝深さが漸次浅くなり、通過断面積
が減少する。したがつて、供給孔2から供給され
た樹脂とフイラーからなる材料は供給ゾーン3を
通過する段階で予熱され、供給ゾーン3からは推
進圧によつて漸次圧縮されながら圧縮ゾーン4へ
輸送される。圧縮ゾーン4では、スクリユ溝の通
過面積が漸次減少するため、材料はますます加圧
され、その溶融形態は第2図に示すような溶融モ
デルに代表されるような形態をとる。 Generally, in a normal molding machine, as shown in FIG. 1, the screw 1 is composed of a supply zone 3 from the material supply hole 2 side, and a plasticization kneading zone 6 consisting of a compression zone 4 and a metering zone 5. . compression zone 4
In this case, the screw groove depth gradually becomes shallower, and the passage cross-sectional area decreases. Therefore, the material consisting of resin and filler supplied from the supply hole 2 is preheated when passing through the supply zone 3, and is transported from the supply zone 3 to the compression zone 4 while being gradually compressed by the propulsion pressure. . In the compression zone 4, the passing area of the screw groove gradually decreases, so that the material is increasingly pressurized, and its melting form takes on a form represented by the melting model shown in FIG. 2.
第2図において、スクリユ溝7で形成されたソ
リツドベツド(未溶融体)8は、スクリユ溝7中
の圧力により加熱筒9の内壁へ押圧される際に、
加熱筒9からの熱と、スクリユ回転に伴うスクリ
ユ1と加熱筒等9内壁の相対ずれによる剪断作用
により、ソリツドベツド8の加熱筒9内壁接触面
から溶融してメルトフイルム10を形成し、これ
をスクリユフライト11でかきとつて溶融体12
をスクリユフライト11の推進側にプールする。
しかしながら、この溶融形態では、スクリユ溝7
の中で、材料はスクリユ溝7内の推進圧によつて
ソリツドベツド8が形成される為、ソリツドベツ
ド8内部は相対移動がない。したがつて、ソリツ
ドベツド8自体の昇温はソリツドベツド8周囲か
らの熱伝導に依存して昇温するしかなく、可塑化
混練ゾーン6の圧縮ゾーン4では、ソリツドベツ
ド8内部のフイラー及び樹脂は充分予熱されない
まま加圧され、ますますフイラー同士がかためら
れ、仮にフイラー付近の樹脂が軟化溶融しても、
フイラー間へ樹脂が含浸することがなく、未分散
塊や、2次凝集の原因となる欠点を有する。又、
充分予熱のないまま加圧されたソリツドベツド8
は、スクリユ溝7内に発生した推進圧により加熱
筒9に強く押しつけられ、メルトフイルム10の
ところで強い剪断力をスクリユ回転により受け、
フイラーの切断、破損の原因となる欠点を有す
る。 In FIG. 2, when the solid bed (unmelted material) 8 formed in the screw groove 7 is pressed against the inner wall of the heating cylinder 9 by the pressure in the screw groove 7,
Due to the heat from the heating tube 9 and the shearing action caused by the relative displacement between the screw 1 and the inner wall of the heating tube 9 as the screw rotates, the solid bed 8 is melted from the contact surface of the inner wall of the heating tube 9 to form a melt film 10. Molten material 12 scraped with screw flight 11
is pooled on the propulsion side of Skrill Flight 11.
However, in this melted form, the screw groove 7
Since the solid bed 8 is formed by the propelling pressure in the screw groove 7, there is no relative movement inside the solid bed 8. Therefore, the temperature of the solid bed 8 itself can only be raised depending on heat conduction from the surroundings of the solid bed 8, and the filler and resin inside the solid bed 8 are not sufficiently preheated in the compression zone 4 of the plasticization and kneading zone 6. As the pressure is applied, the fillers become more and more hardened, and even if the resin near the filler softens and melts,
This has the drawback that the resin does not impregnate between the fillers, causing undispersed lumps and secondary agglomeration. or,
Solid bed 8 pressurized without sufficient preheating
is strongly pressed against the heating cylinder 9 by the propulsion pressure generated in the screw groove 7, and receives a strong shearing force at the melt film 10 due to the rotation of the screw.
It has the disadvantage of causing cutting and damage to the filler.
本発明は、これらの欠点を解消すべく、スクリ
ユフライトの推進側から反推進側へ連通したスク
リユ溝底よりさらに深い凹部を設けることによ
り、スクリユ溝内の推進圧力を減少させること
と、スクリユ溝内の材料に複雑な相対移動を起
し、熱的均質性と昇温速度を高めることにより、
無理のない溶融を行い、フイラーの2次凝集や切
断破損を防ぎうるようにしたものである。 In order to eliminate these drawbacks, the present invention reduces the propulsion pressure in the screw groove by providing a recess deeper than the bottom of the screw groove that communicates from the propulsion side to the anti-propulsion side of the screw flight. By causing complex relative movement of the material in the groove and increasing thermal homogeneity and heating rate,
This allows for easy melting and prevents secondary agglomeration and breakage of the filler.
つぎに、図面に示した実施例によつて、本発明
を説明する。 Next, the present invention will be explained with reference to embodiments shown in the drawings.
第3図に本発明の1実施例を示す。第4図はそ
の拡大図である。 FIG. 3 shows one embodiment of the present invention. FIG. 4 is an enlarged view.
第3,4図において、加熱筒9内にスクリユ1
が回転自在もしくは回転自在で軸線方向に摺動自
在に内設され、材料供給孔2にはフイーダ20が
設けられて、材料の供給量をコントロールでき
る。スクリユ1は材料供給孔2側から供給ゾーン
3、圧縮ゾーン4と計量ゾーン5で構成される。
圧縮ゾーン4と計量ゾーン5を総称して可塑化混
練ゾーン6と呼ぶことにする。供給ゾーン3から
可塑化混練ゾーン6にかけてのゾーン13におい
て、スクリユ1には、スクリユフライト11を横
切り、かつ、スクリユ溝底14よりさらに深い凹
部15で、スクリユフライト11の推進側16と
反推進側17とを連通させる。フイーダ20によ
り、材料をスクリユ溝7に満杯にならぬようスク
リユ1へ飢餓供給して、材料がスクリユ溝7の中
で自由移動できる自由空間18を確保しながら、
材料を供給ゾーン3で移動させる。 In Figures 3 and 4, a screw 1 is placed inside the heating cylinder 9.
is rotatably or freely rotatable and slidably disposed in the axial direction, and the material supply hole 2 is provided with a feeder 20 to control the amount of material supplied. The screw 1 is composed of a supply zone 3, a compression zone 4, and a metering zone 5 from the material supply hole 2 side.
The compression zone 4 and the metering zone 5 will be collectively referred to as the plasticizing and kneading zone 6. In the zone 13 extending from the supply zone 3 to the plasticizing and kneading zone 6, the screw 1 has a concave portion 15 that crosses the screw flight 11 and is deeper than the screw groove bottom 14, and is opposite to the propelling side 16 of the screw flight 11. It communicates with the propulsion side 17. The feeder 20 feeds the material to the screw 1 so that the screw groove 7 does not become full, while ensuring a free space 18 in which the material can freely move within the screw groove 7.
The material is moved in feed zone 3.
本発明によるスクリユは上記のような構成を有
するが、次にその作動を説明する。 The screw according to the present invention has the above-mentioned configuration, and its operation will be explained next.
前述の如く、フイーダ20により、供給孔2を
経て、スクリユ1部へ材料を供給するが、スクリ
ユ溝7で材料が完全充満しないようにフイーダ2
0の供給量を適切にコントロールする。ここで
は、スクリユ溝7の中で材料が自由に移動できる
よう自由空間18を確保することが肝要で、材料
の充満率は30〜70%が望ましい。材料は供給ゾー
ン3を加熱筒9からの受熱で予熱されながらスク
リユ回転により前方へ輸送され、ゾーン13にお
いて第5図、第6図に示すような態様を示す。 As mentioned above, the feeder 20 supplies the material to the screw 1 part through the supply hole 2, but the feeder 20 is careful not to completely fill the screw groove 7 with the material.
Appropriately control the supply amount of 0. Here, it is important to secure a free space 18 so that the material can move freely in the screw groove 7, and the filling rate of the material is preferably 30 to 70%. The material is transported forward through the supply zone 3 by the rotation of the screw while being preheated by heat received from the heating cylinder 9, and in the zone 13 exhibits the mode shown in FIGS. 5 and 6.
第5図1〜4は材料が固体状態で予熱を受けて
昇温し、軟化溶融するまでの作用順序と樹脂の態
様を示す。すなわち、前述の如くスクリユ溝7の
中で自由空間18を有するためスクリユ11の回
転により、材料は、第5図1,3に矢印で示すよ
うな動きを行いタンブラの中の材料のように材料
同士が相対移動を行う。スクリユ溝底14及びフ
ライト11に設けた凹部15においては、第5図
2,4に矢印で示すような動きを示す。即ち、材
料は推進側16から反推進側17へ凹部15を経
て移動する。又、凹部15は、凹部15に入つた
材料をスクリユ1の回転によりすくい上げて、反
対側で排出する動作も行う。したがつて、スクリ
ユ溝7の中で材料が極めて複雑な動きを行うた
め、スクリユ溝7の材料のすべてが加熱筒9の内
壁やスクリユフライト11の側壁やスクリユ溝底
14に接して受熱して、フイラーも樹脂も全対的
に均一に昇温する。かくして、予熱を受けて樹脂
が軟化し、ペレツトの表面が溶融し、ないしは粘
着性が生ずると、フイラーとの接着が始まる。こ
の状態が常圧下で実施されるため、フイラー同士
の固着は起らず、フイラーがペレツト表層の溶融
樹脂と粘着した上でペレツトから剥離される。し
たがつて、常に新しい粘着樹脂と新しいフイラー
が接触し、両者の混合が進行する。このことは、
加圧作用に起因して、フイラー同士の固着がな
く、フイラーの2次凝集が起らないことを意味
し、フイラー間への樹脂の含浸が容易に行わるこ
とを意味する。又、スクリユ溝7内で材料が自由
に動くことができる自由空間18を経て溶融樹脂
の揮発分や吸湿分が後方へ容易に排出される。か
くして、漸次、フイラーと樹脂の混合が行われ、
可塑化混練ゾーン6へ移行する段階ではフイラー
とペレツトはそれぞれ樹脂が溶融する直前の軟化
状態の温度付近に達している。 FIGS. 5 1 to 4 show the order of action and the state of the resin, in which the material is preheated in a solid state, the temperature is raised, and the material is softened and melted. That is, as mentioned above, since there is a free space 18 in the screw groove 7, the rotation of the screw 11 causes the material to move as shown by the arrows in FIGS. 1 and 3, and the material moves like the material in the tumbler. They move relative to each other. The screw groove bottom 14 and the recess 15 provided in the flight 11 exhibit movements as shown by arrows in FIGS. 2 and 4. That is, the material moves from the propelling side 16 to the counter-propelling side 17 through the recess 15. The recess 15 also performs the operation of scooping up the material that has entered the recess 15 by rotating the screw 1 and discharging it on the opposite side. Therefore, since the material moves in an extremely complicated manner in the screw groove 7, all of the material in the screw groove 7 comes into contact with the inner wall of the heating tube 9, the side wall of the screw flight 11, and the screw groove bottom 14, and receives heat. As a result, the temperature of both the filler and the resin increases uniformly. Thus, as the resin softens under preheating and the surface of the pellet melts or becomes sticky, it begins to adhere to the filler. Since this condition is carried out under normal pressure, the fillers do not stick to each other, and the fillers are peeled off from the pellets after adhering to the molten resin on the surface layer of the pellets. Therefore, new adhesive resin and new filler always come into contact with each other, and mixing of the two progresses. This means that
This means that the fillers do not stick to each other due to the pressurizing action, meaning that secondary aggregation of the fillers does not occur, and it means that the resin can be easily impregnated between the fillers. In addition, the volatile matter and moisture content of the molten resin are easily discharged to the rear through the free space 18 in which the material can move freely within the screw groove 7. In this way, filler and resin are gradually mixed,
At the stage of transition to the plasticizing kneading zone 6, the filler and pellets have reached temperatures near the softened state just before the resin melts.
スクリユ溝7の通過断面積が減じている圧縮ゾ
ーン4ではスクリユ溝7が材料で充満され、いわ
ば軟化ソリツドベツド19を形成し、第6図1〜
4に示すような作用順序と溶融態様を示す。 In the compression zone 4, where the passage cross-sectional area of the screw groove 7 is reduced, the screw groove 7 is filled with material, forming a so-called softened solid bed 19, as shown in FIGS.
4 shows the action order and melting mode.
第6図1,3は、スクリユ回転により軟化ソリ
ツドベツド19が加熱筒9の内壁との剪断作用に
より、小さい剪断力で容易に変形し、溶融して、
フイラーの混入した溶融体12がスクリユフライ
ト11によりかきとられ、前方へ推進される場合
を示す。第6図2,4において、樹脂は軟化はし
ているが、樹脂同士の粘着が充分でない軟化ソリ
ツドベツド19の場合は、凹部15に落ち込み、
ソリツドベツド8が崩壊し、その崩壊面に溶融樹
脂12が接触し、より一層の全対的溶融と混合を
促進する。ここで特徴的なことは、スクリユフラ
イト11の推進側16と反推進側17とが凹部1
5で連通しているため、スクリユ溝7内の圧力維
持は、第1図に示したような通常のスクリユ1に
比べてはるかに小さく、したがつて、大きな剪断
力が生じることなく、又、必要としない点にあ
る。即ち、通常のスクリユのように、未だ充分加
熱昇温されていないフイラーと樹脂の混合未溶融
体のソリツドベツド8を高圧下で加熱筒9内壁に
押しつけ、その押圧接触面に強い剪断作用をスク
リユ回転により加えて、一気に融点を越し、溶融
を完了させる態様でない為、フイラーの切断、破
損がなく、又、フイラーが高圧下でかためられた
上で一気に溶融した樹脂にくるまれて発生する未
分散塊や2次凝集を発生させることがない。 FIGS. 6 1 and 3 show that the softened solid bed 19 is easily deformed and melted by a small shearing force due to the shearing action with the inner wall of the heating cylinder 9 due to the rotation of the screw.
A case is shown in which the molten material 12 containing filler is scraped off by the screw flight 11 and propelled forward. In FIGS. 6 2 and 4, in the case of a softened solid bed 19 where the resin is softened but the adhesion between the resins is not sufficient, the bed falls into the recess 15.
The solid bed 8 collapses, and the molten resin 12 comes into contact with the collapsed surface, promoting further total melting and mixing. What is characteristic here is that the propulsion side 16 and anti-propulsion side 17 of the screw flight 11 are in the recess 1.
5, the pressure maintained within the screw groove 7 is much smaller than that of a normal screw 1 as shown in FIG. The point is that you don't need it. That is, like a normal screw, the solid bed 8, which is a mixed, unmelted mixture of filler and resin whose temperature has not yet been sufficiently heated, is pressed against the inner wall of the heating cylinder 9 under high pressure, and a strong shearing action is applied to the pressed contact surface by the rotation of the screw. In addition, since the melting point is not reached all at once and melting is not completed, there is no cutting or damage to the filler, and there is no dispersion that occurs when the filler is hardened under high pressure and then wrapped in the melted resin all at once. No lumps or secondary aggregation occurs.
このように、本発明によれば、フイラーと樹脂
が大気圧下で混合しながら昇温し、フイラーと樹
脂が常に同一付近の温度であるため、フイラー間
に樹脂が含浸しやすく、又、スクリユ溝内のフイ
ラーと樹脂がいたるところで均一温度であるた
め、一斉的な溶融と、フイラーと樹脂の混合が行
われるため、前述の如く、フイラーの分散がよ
く、かつ、切断破損の少ないという複合成形にお
いては極めて大きな効果が得られる。 As described above, according to the present invention, the filler and resin are heated while being mixed under atmospheric pressure, and the filler and resin are always at about the same temperature. Since the filler and resin in the groove are at a uniform temperature everywhere, simultaneous melting and mixing of the filler and resin occur, resulting in composite molding with good filler dispersion and less breakage as described above. An extremely large effect can be obtained.
前述の説明は、主としてフイラーと樹脂を直接
成形する場合についてであるがフイラーのない通
常の樹脂のみの可塑化の場合は、可塑化能力の向
上、均質な可塑化による品質の向上、及び、ハイ
サイクル成形という大きな効果がある。即ち、複
合成形でない通常の成形の場合はフイーダ20が
ない為、供給ゾーン3のスクリユ溝7は未溶融樹
脂で充満される。なお、本発明によらない場合、
第2図の溶融形態になることは前述の通りであ
る。 The above explanation mainly concerns the case where filler and resin are directly molded, but in the case of plasticizing only ordinary resin without filler, there are improvements in plasticizing ability, quality through homogeneous plasticization, and high quality. Cycle molding has a great effect. That is, in the case of normal molding other than composite molding, since there is no feeder 20, the screw groove 7 in the supply zone 3 is filled with unmelted resin. In addition, when not according to the present invention,
As described above, the melted state shown in FIG. 2 is obtained.
本発明においては、前記したように、供給ゾー
ン3のスクリユ溝7を充満した樹脂は、スクリユ
の推進圧力でスクリユ溝7の中で圧縮され、ソリ
ツドベツド8を形成する。形成されたソリツドベ
ツド8の中心部はソリツドベツド8周囲からの伝
熱に依存するしかないため、ソリツドベツド8の
外周部と中心部とでは温度分布が異る。ソリツド
ベツド8は加熱筒9内壁に押圧され、この押圧面
から順次溶融されてスクリユフライト11の推進
側に溶融体12としてプールされる。本発明によ
るスクリユ形状の領域にソリツドベツド8が達
し、この領域を通過する状態は第6図3,4の溶
融形態を取る。即ち、ソリツドベツド8は凹部1
5部に落ち込み、崩壊し、その崩壊面に溶融樹脂
が剪断接触し、ソリツドベツド8は昇温が促進さ
れ、溶融樹脂は一層の昇温を防止される。このよ
うに溶融の効率が上り、可塑化能力の向上が大き
い。スクリユフライト11の推進側16と反推進
側17とが凹部15で連通されていてスクリユ溝
7内の圧力維持が小さく、加熱筒9内壁への押圧
が小さくなり、スクリユ回転による剪断力が小さ
い。したがつて、溶融点を一気に通りこして高温
の溶融樹脂を作るという局部過熱の可塑化を行う
ことが防止されるのは勿論であり、低温樹脂でも
均一な溶融樹脂が得られ、局部的未溶融、もしく
は高粘度部を擁する不均溶融による流動性の低下
がなく、低温高流動によるハイサイクル成形が可
能であるという大きな利点がある。 In the present invention, as described above, the resin filling the screw groove 7 of the supply zone 3 is compressed within the screw groove 7 by the propelling pressure of the screw to form the solid bed 8. Since the center of the formed solid bed 8 is dependent on heat transfer from the surroundings of the solid bed 8, the temperature distribution is different between the outer periphery and the center of the solid bed 8. The solid bed 8 is pressed against the inner wall of the heating cylinder 9, and is sequentially melted from this pressed surface and pooled as a melt 12 on the propelling side of the screw flight 11. When the solid bed 8 reaches the screw-shaped region according to the invention and passes through this region, it assumes the melting state shown in FIGS. 3 and 4. That is, the solid bed 8 is in the recess 1.
The solid bed 8 falls into 5 parts and collapses, and the molten resin comes into shear contact with the collapsed surface, promoting the temperature rise of the solid bed 8 and preventing the molten resin from further temperature rise. In this way, the melting efficiency is increased and the plasticizing ability is greatly improved. The propulsion side 16 and anti-propulsion side 17 of the screw flight 11 are communicated through the recess 15, so that the pressure maintained in the screw groove 7 is small, the pressure on the inner wall of the heating cylinder 9 is small, and the shearing force due to screw rotation is small. . Therefore, it goes without saying that plasticization caused by local overheating, which involves passing through the melting point all at once to create a high-temperature molten resin, is prevented, and a uniform molten resin can be obtained even with low-temperature resin, and localized plasticization is prevented. It has the great advantage that there is no reduction in fluidity due to melting or non-uniform melting with high viscosity parts, and high cycle molding is possible due to low temperature and high fluidity.
なお、第7図は第3,4図に示した本発明の1
実施例のスクリユ1の展開図であり、凹部15を
軸線方向に沿つて設けたものであるが、第8図及
び第9図は円周方向に比較的に短い凹部15また
は長い凹部15を設けたそれぞれ他の実施例を示
すスクリユ1の展開図である。第10図はスクリ
ユフライト11と逆ねじの方向に凹部15を設け
たさらに他の実施例を示すスクリユ1の展開図で
ある。 Note that FIG. 7 shows one example of the present invention shown in FIGS. 3 and 4.
This is a developed view of the screw 1 according to the embodiment, in which a recess 15 is provided along the axial direction, whereas FIGS. 8 and 9 show a case in which a relatively short recess 15 or a long recess 15 is provided in the circumferential direction. FIG. 6 is a developed view of the screw 1 showing other embodiments. FIG. 10 is a developed view of the screw 1 showing yet another embodiment in which a screw flight 11 and a recess 15 are provided in the direction of the reverse thread.
第8〜10図のものにおいても、第3〜7図に
示したものと同様に、良好な可塑化混練を得るこ
とができる。 Good plasticization and kneading can be obtained in the cases shown in FIGS. 8 to 10 as well as in the cases shown in FIGS. 3 to 7.
このように、本発明によれば、スクリユフライ
トを横切つたスクリユ溝深さよりも深い凹部で、
スクリユフライトの推進側と反推進側を連通させ
たので、スクリユ溝内の推進圧力を減少させると
ともに、スクリユ溝内の材料に複雑な相対移動を
行わせ、熱的均質性と昇温速度を高めることによ
り、無理のない溶融を行い、フイラーの2次凝集
や切断破損を防ぐことができる。したがつて、良
好な可塑化混練を行うことができ、良品質の樹脂
成形品を確実容易に得ることができるようにな
る。 As described above, according to the present invention, in a recess that is deeper than the depth of the screw groove that traverses the screw flight,
By communicating the propulsion side and anti-propulsion side of the screw flight, the propulsion pressure in the screw groove is reduced, and the material in the screw groove undergoes complex relative movement, improving thermal homogeneity and temperature rise rate. By increasing the melting point, melting can be carried out without strain, and secondary agglomeration and breakage of the filler can be prevented. Therefore, good plasticization and kneading can be performed, and a resin molded product of good quality can be reliably and easily obtained.
第1図は本発明に類した従来の装置の1例を示
す正面図、第2図は第1図の装置における樹脂の
溶融形態を示す説明図、第3図は本発明の1実施
例を示す正面図、第4図は第3図の1部拡大図、
第5図1〜4および第6図1〜4はそれぞれ本発
明の装置におけ樹脂の溶融形態を示す説明図、第
7図は第4図に示すスクリユの展開図、第8〜1
0図はそれぞ本発明の他の実施例を示すスクリユ
部の展開図ある。
1……スクリユ、2……樹脂供給孔、3……供
給ゾーン、6……可塑化混練ゾーン、7……スク
リユ溝、8……ソリツドベツド、9……加熱筒、
11……スクリユフライト、12……溶融体、1
4……スクリユ溝底、15……凹部、16……推
進側、17……反推進側、18……自由空間、1
9……軟化ソリツドベツド、20……フイーダ。
FIG. 1 is a front view showing an example of a conventional device similar to the present invention, FIG. 2 is an explanatory diagram showing the melting form of resin in the device of FIG. 1, and FIG. 3 is an illustration of an example of the present invention. The front view shown in Fig. 4 is an enlarged view of a part of Fig. 3.
5. 1 to 4 and 6. 1 to 4 are explanatory diagrams showing the melted form of the resin in the apparatus of the present invention, respectively. FIG. 7 is a developed view of the screw shown in FIG. 4, and 8 to 1.
Figure 0 is a developed view of the screw portion showing other embodiments of the present invention. 1... Screw, 2... Resin supply hole, 3... Supply zone, 6... Plasticization kneading zone, 7... Screw groove, 8... Solid bed, 9... Heating cylinder,
11...Skrillophrite, 12...Melted body, 1
4... Screw groove bottom, 15... Concavity, 16... Propulsion side, 17... Anti-propulsion side, 18... Free space, 1
9...Softened solid bed, 20...Feeder.
Claims (1)
方向に摺動自在のスクリユを設け、該スクリユ部
には材料供給孔側から供給ゾーン、可塑化混練ゾ
ーンを設け、供給ゾーンと可塑化混練ゾーンの両
方或はそのいずれか一方に、スクリユフライトを
横切つたスクリユ溝深さより深い凹部で、スクリ
ユフライトの推進側と反推進側を連通させたこと
を特徴とする樹脂の可塑化混練装置。1. A rotatable or freely rotatable screw that is slidable in the axial direction is provided in the heating cylinder, and a supply zone and a plasticization kneading zone are provided from the material supply hole side in the screw part, and the supply zone and the plasticization kneading zone are connected to each other. A plasticizing and kneading device for resin, characterized in that the propulsion side and the counter-propulsion side of the screw flight are connected to each other by a recess deeper than the depth of the screw groove that crosses the screw flight in either or both of them.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58063009A JPS59188419A (en) | 1983-04-12 | 1983-04-12 | Resin plasticization and kneading equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58063009A JPS59188419A (en) | 1983-04-12 | 1983-04-12 | Resin plasticization and kneading equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59188419A JPS59188419A (en) | 1984-10-25 |
| JPH028562B2 true JPH028562B2 (en) | 1990-02-26 |
Family
ID=13216886
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58063009A Granted JPS59188419A (en) | 1983-04-12 | 1983-04-12 | Resin plasticization and kneading equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59188419A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01156005U (en) * | 1988-04-07 | 1989-10-26 | ||
| JP2574480Y2 (en) * | 1990-07-31 | 1998-06-11 | 三浦工業株式会社 | Fluidized bed heat exchanger |
-
1983
- 1983-04-12 JP JP58063009A patent/JPS59188419A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59188419A (en) | 1984-10-25 |
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