JPS5837628Y2 - extruder - Google Patents

extruder

Info

Publication number
JPS5837628Y2
JPS5837628Y2 JP1980076913U JP7691380U JPS5837628Y2 JP S5837628 Y2 JPS5837628 Y2 JP S5837628Y2 JP 1980076913 U JP1980076913 U JP 1980076913U JP 7691380 U JP7691380 U JP 7691380U JP S5837628 Y2 JPS5837628 Y2 JP S5837628Y2
Authority
JP
Japan
Prior art keywords
dalmage
screw
resin
extruder
cylinder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP1980076913U
Other languages
Japanese (ja)
Other versions
JPS571635U (en
Inventor
謙作 中村
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP1980076913U priority Critical patent/JPS5837628Y2/en
Publication of JPS571635U publication Critical patent/JPS571635U/ja
Application granted granted Critical
Publication of JPS5837628Y2 publication Critical patent/JPS5837628Y2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/68Barrels or cylinders
    • B29C48/685Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads
    • B29C48/686Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads having grooves or cavities
    • 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
    • B29C48/53Screws having a varying channel depth, e.g. varying the diameter of the longitudinal screw trunk
    • 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
    • B29C48/575Screws provided with elements of a generally circular cross-section for shearing the melt, i.e. shear-ring elements
    • 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
    • B29C48/67Screws having incorporated mixing devices not provided for in groups B29C48/52 - B29C48/66

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Description

【考案の詳細な説明】 本考案は混線機能を備えた押出機に関するものである。[Detailed explanation of the idea] The present invention relates to an extruder with crosstalk function.

一般にこの種の押出機は混線部にダルメージタイプスク
リュを用いているが、この形式のものは混線部における
スクリューとシリンダとの間の開口面積が一定であるか
ら、使用する樹脂が粘度の低い溶隔樹脂の場合は混練部
での通過速度が速くなって混線性が悪くなり、逆に粘度
の高い溶隔樹脂の場合は混練部での抵抗が大きくなり通
過速度がおそくなり、処理速度が低下する欠点があった
Generally, this type of extruder uses a dalmage type screw in the cross-conducting section, but this type has a constant opening area between the screw and cylinder in the cross-conducting section, so the resin used has a low viscosity. In the case of melt resin, the passing speed in the kneading section increases, resulting in poor wire crosstalk.On the other hand, in the case of high viscosity melt resin, the resistance in the kneading part increases, slowing the passing speed, and the processing speed decreases. There was a drawback that it decreased.

そこで本考案は上記混線部での樹脂通過速度を調節し得
るように構成することにより上記欠点を一挙に解決する
ばかりでなく新たな利点を有した押出機を提供しようと
するものである。
Therefore, the present invention aims to provide an extruder which not only solves the above-mentioned drawbacks at once but also has new advantages by configuring the extruder to be able to adjust the speed of resin passing through the cross-conducting section.

以下本考案の一実施例を図面に基づいて詳述する。An embodiment of the present invention will be described below in detail with reference to the drawings.

第1図〜第5図に示す押出機1において、2は主スクリ
ユであり、途中の大径軸3外周に螺旋状のダルメージ4
,4・・・・・・を適当間隔おきに形成してダルメージ
スクリュ5を形成している。
In the extruder 1 shown in FIGS. 1 to 5, 2 is a main screw, and a spiral dalmage 4 is attached to the outer periphery of a large diameter shaft 3 in the middle.
, 4, . . . are formed at appropriate intervals to form the dalmage screw 5.

そしてダルメージスクリュ5の中央部外周には各ダルメ
ージ4の途中を仕切る環状塩6を設けて、各ダルメージ
4を非連続状態としている。
An annular salt 6 is provided on the outer periphery of the central portion of the dalmage screw 5 to partition the middle of each dalmage 4, so that each dalmage 4 is in a discontinuous state.

7はシリンダであり、内周面8の上記環状塩6に対向す
る位置には環状塩6外周面9に適当な間隔を隔てて環状
溝10を形成している。
Reference numeral 7 denotes a cylinder, and an annular groove 10 is formed on the outer peripheral surface 9 of the annular salt 6 at a position on the inner peripheral surface 8 facing the annular salt 6 at an appropriate interval.

そしてこの環状溝10の両側壁面11.11はナーパー
面に形成している。
Both side wall surfaces 11.11 of this annular groove 10 are formed into a narrowed surface.

12は主スクリユ2を軸方向に任意の位置に移動するた
めの調節手段であって、主スクリユ2の基端13にキー
14を介して摺動可能に嵌合したスリーブ15をシリン
ダ7に対して定位置で回転すべく設け、該スリーブ15
の外周にはモーター16により回転される駆動ギヤ17
を取付け、スリーブ15の一端にロックナツト18付き
押しネジ19を螺着し、該押しネジ19を主スクリユ2
に接当させたものである。
12 is an adjusting means for moving the main screw 2 to an arbitrary position in the axial direction, and a sleeve 15 slidably fitted to the base end 13 of the main screw 2 via a key 14 is moved relative to the cylinder 7. The sleeve 15 is provided to rotate in a fixed position.
A drive gear 17 rotated by a motor 16 is mounted on the outer periphery of the
Attach the push screw 19 with the lock nut 18 to one end of the sleeve 15, and screw the push screw 19 into the main screw 2.
It is placed in contact with the

上記のように構成した押出機1の作用について述べる。The operation of the extruder 1 configured as described above will be described.

樹脂を入口20よりシリンダ7内に供給した場合、該樹
脂は主スクリユ2により出口21側へ移送され、その移
送途中のダルメージスクリュ5のダルメージ4を通過す
る間に混線作用が与えられる。
When resin is supplied into the cylinder 7 from the inlet 20, the resin is transferred to the outlet 21 side by the main screw 2, and crosstalk is applied while passing through the dalmage 4 of the dalmage screw 5 during the transfer.

このダルメージ4を通過する際に、樹脂の粘度が高いと
、樹脂の流れが悪くなるが、調節手段12により環状塩
6を第4図のように環状溝10の中央に位置させて環状
塩6と環状溝10との間の隙間を大きく開口しておけば
樹脂の通過速度が低下することはなく、従って適度な混
練作用が与えられるとともにシリンダ7内の圧力か゛異
常に高まることもない。
When passing through this dalmage 4, if the resin has a high viscosity, the flow of the resin will be poor. If the gap between the cylinder 7 and the annular groove 10 is left wide open, the resin passage speed will not be reduced, so that an appropriate kneading effect will be provided and the pressure inside the cylinder 7 will not increase abnormally.

また樹脂の粘度が低いと、樹脂の流れが良くなり混線性
が低下するが、環状塩6を第5図のように環状溝10の
片側にずらせて環状塩6と環状溝10との間の隙間を小
さくしておけば樹脂の通過速度が増大することはなく、
従って混線性が低下したりシリンダ7内の圧力が異常に
低下することはない。
In addition, when the viscosity of the resin is low, the flow of the resin is improved and crosstalk is reduced. However, by shifting the annular salt 6 to one side of the annular groove 10 as shown in FIG. If the gap is kept small, the resin passage speed will not increase.
Therefore, there is no possibility that the wire crosstalk is reduced or the pressure inside the cylinder 7 is abnormally reduced.

このように取扱う樹脂の粘度に合せて環状塩6と環状溝
10との間の隙間の開口量を調節することにより混線部
における樹脂の流れを所望の速度に調節でき、混線性の
低下や、シリンダ7内の圧力の異常な増減現象を防止で
きる。
By adjusting the opening amount of the gap between the annular salt 6 and the annular groove 10 in accordance with the viscosity of the resin to be handled in this way, the flow of the resin in the crosstalk section can be adjusted to a desired speed, reducing crosstalk, Abnormal increases and decreases in the pressure within the cylinder 7 can be prevented.

上記実施例では環状塩6部において隣接したダルメージ
4を分離状態に形成したが、第6図に示すように溝22
によって互に連通状態に形成してもよい。
In the above embodiment, adjacent dalmages 4 were formed in a separated state in the annular salt 6 portion, but as shown in FIG.
They may be formed in communication with each other.

以上実施例に示すように本考案押出機によればダルメー
ジスクリュとシリンダとの間の開口面積を増減できるか
らいかなる粘度の樹脂でも通過速度を加減できて確実に
混線できるとともにシリンダ内の圧力の異常な上昇又は
低下をも防止できて樹脂温度を所望の値に保持すること
ができる。
As shown in the examples above, according to the extruder of the present invention, the opening area between the dalmage screw and the cylinder can be increased or decreased, so the passage speed of resin of any viscosity can be adjusted, and crosstalk can be reliably achieved, and the pressure inside the cylinder can be reduced. Abnormal rise or fall can also be prevented, and the resin temperature can be maintained at a desired value.

しかも樹脂の押出圧力も調節できる等すぐれた利点を有
している。
Furthermore, it has excellent advantages such as being able to adjust the extrusion pressure of the resin.

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

第1図〜第5図は本考案の一実施例を示し、第1図は縦
断面図、第2図は第1図の要部拡大図、第3図は第2図
のA−A断面図、第4図、第5図はそれぞれ作動状態を
示す断面図、第6図は別の実施例を示す断面図である。 2・・・・・・主スクリユ、3・・・・・・ダルメージ
スクリュ、4・・・・・・ダルメージ、6・・・・・・
環状塩、7・・・・・・シリンダ、10・・・・・・環
状溝、12・・・・・・調節手段。
Figures 1 to 5 show an embodiment of the present invention, with Figure 1 being a longitudinal sectional view, Figure 2 being an enlarged view of the main parts of Figure 1, and Figure 3 being a cross section taken along line AA in Figure 2. 4 and 5 are sectional views showing the operating state, respectively, and FIG. 6 is a sectional view showing another embodiment. 2... Main screw, 3... Dalmage screw, 4... Dalmage, 6...
Annular salt, 7... cylinder, 10... annular groove, 12... adjustment means.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 主スクリユの一部にダルメージスクリュを形成した押出
機において、ダルメージスクリュの一部外周にはダルメ
ージの途中を仕切る環状塩を設け、シリンダの内周面の
環状塩に対向する位置には環状基外周面に適当な間隔を
隔てて環状溝を形成し、ダルメージスクリュを軸方向任
意の位置に移動するための調節手段を構成したことを特
徴とする押出機。
In an extruder in which a Dalmage screw is formed in a part of the main screw, a ring salt is provided on a part of the outer periphery of the Dalmage screw to partition the middle of the Dalmage, and a ring salt is provided on the inner peripheral surface of the cylinder at a position opposite to the ring salt. An extruder characterized in that annular grooves are formed on the base outer peripheral surface at appropriate intervals, and adjustment means for moving the dalmage screw to any position in the axial direction is configured.
JP1980076913U 1980-06-02 1980-06-02 extruder Expired JPS5837628Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1980076913U JPS5837628Y2 (en) 1980-06-02 1980-06-02 extruder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1980076913U JPS5837628Y2 (en) 1980-06-02 1980-06-02 extruder

Publications (2)

Publication Number Publication Date
JPS571635U JPS571635U (en) 1982-01-06
JPS5837628Y2 true JPS5837628Y2 (en) 1983-08-25

Family

ID=29439519

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1980076913U Expired JPS5837628Y2 (en) 1980-06-02 1980-06-02 extruder

Country Status (1)

Country Link
JP (1) JPS5837628Y2 (en)

Also Published As

Publication number Publication date
JPS571635U (en) 1982-01-06

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