JPH10305477A - Method for control of barrel temperature of double-screw extruding machine - Google Patents

Method for control of barrel temperature of double-screw extruding machine

Info

Publication number
JPH10305477A
JPH10305477A JP9132807A JP13280797A JPH10305477A JP H10305477 A JPH10305477 A JP H10305477A JP 9132807 A JP9132807 A JP 9132807A JP 13280797 A JP13280797 A JP 13280797A JP H10305477 A JPH10305477 A JP H10305477A
Authority
JP
Japan
Prior art keywords
temperature
barrel
controlled
area
temperature control
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
Application number
JP9132807A
Other languages
Japanese (ja)
Inventor
Norishige Maeda
徳重 前田
Koji Watanabe
高次 渡辺
Kuniaki Endo
邦昭 遠藤
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.)
Shibaura Machine Co Ltd
Original Assignee
Toshiba Machine Co 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 Toshiba Machine Co Ltd filed Critical Toshiba Machine Co Ltd
Priority to JP9132807A priority Critical patent/JPH10305477A/en
Publication of JPH10305477A publication Critical patent/JPH10305477A/en
Pending 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
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/918Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling
    • B29C48/9185Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling in the direction of the stream of the material
    • 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
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92895Barrel or housing

Abstract

PROBLEM TO BE SOLVED: To prevent a raw material from being thermally decomposed even though its operation is continued for a long time by a method wherein a temperature detection device is provided respectively to an upper side and a lower side of a barrel in each temperature control area, and an upper half and a lower half of the barrel are separately controlled in temperature. SOLUTION: A barrel 20 is divided into a plurality of temperature control areas C1 , C2 , C3 , C4 from a raw material supply opening 22 to a discharge opening 23. Then, heaters 24 to 27 is respectively provided to a barrel upper side of each area, and heaters 28 to 31 is respectively provided to a barrel lower side of each area. Further, thermo-couples 32 to 35 for detecting upper half temperature, and thermo-couples 36 to 39 for detecting lower half temperature are provided. Then, for example, only the C1 wherein a temperature difference between up and down becomes maximum is controlled in temperature separately for up and down, and the other area C2 to C4 are controlled in temperature by control of the upper side equipped with a heater capable of being controlled by cooling in which water passes through a cooling pipe. Consequently, though operated for a long time, thermal decomposition does not occur, and deteriorated matter is not generated.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は異方向回転の二軸押出機
のバレルの上半分および下半分を別々に温度制御する温
度制御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a temperature control method for separately controlling the upper half and the lower half of a barrel of a twin screw extruder having different rotations.

【0002】[0002]

【従来技術】異方向回転の二軸押出機はPVC等の熱分
解し易い原料の混練、溶融に用いられ、図4に示すよう
にスクリュ1の挿入された原料供給口2及びベント口3
を有するバレル4を複数個の温度制御区域C1 、C2
3 、C4 に分割し、各区域に各バレル4の外側面にヒ
ータ5、6、7および8を設けるとともに、上側、或い
は下側に熱伝対9、10、11、12等の温度検出装置
を設け、バレル4内に供給される原料が熱分解しない程
度の温度に設定し、成形を行ってきた。
2. Description of the Related Art A twin-screw extruder of different rotation is used for kneading and melting raw materials which are easily thermally decomposed, such as PVC, and as shown in FIG.
Barrel 4 having a plurality of temperature control zones C 1 , C 2 ,
C 3, is divided into C 4, provided with a heater 5, 6, 7 and 8 on the outer surface of each barrel 4 in each zone, the upper, or the temperature of the thermocouple 9, 10, 11, 12, etc. on the lower side A detecting device is provided, and the temperature is set to such a degree that the raw material supplied into the barrel 4 is not thermally decomposed, and molding has been performed.

【0003】[0003]

【発明が解決しょうとする課題】しかしながら、原料の
熱分解が起きない程度の温度設定にもかかわらず、長時
間の運転を続けると熱分解による劣化物質が発生し、成
形品に混入して品質の低下を招いた。
However, even if the temperature is set so as not to cause thermal decomposition of the raw material, if the operation is continued for a long period of time, degraded substances are generated by the thermal decomposition and mixed into the molded product to obtain quality. Led to a decline.

【0004】発明者等は種々テストをした結果、図5の
ようにバレルの上側と下側では温度が異なり、原料供給
口2下の温度制御区域C1 では運転開始後75MIN で下
側温度は上側温度より31Cも高くなった。このため
長時間の運転を続けるとバレルの設定温度より高温の部
分に接している原料が熱分解により劣化し、成形品に混
入することが判明した。
As a result of various tests conducted by the inventors, as shown in FIG. 5, the temperature is different between the upper side and the lower side of the barrel. In the temperature control section C 1 below the raw material supply port 2, the lower side temperature becomes 75 MIN after the start of operation. 31 above the upper temperature . C also got higher. For this reason, it has been found that if the operation is continued for a long time, the raw material in contact with the portion having a temperature higher than the set temperature of the barrel is deteriorated by thermal decomposition and mixed into the molded product.

【0005】本発明野目的は前述のような事柄に鑑み成
されたもので、異方向回転の二軸押出機のバレルの複数
の温度制御区域の上半分および下半分を別々に温度制御
し、長時間の運転を続けても原料が熱分解しない温度制
御方法を提供することにある。
The present invention has been made in view of the above-mentioned circumstances, and separately controls the upper and lower halves of a plurality of temperature control zones of a barrel of a counter-rotating twin-screw extruder, It is an object of the present invention to provide a temperature control method in which a raw material is not thermally decomposed even if the operation is continued for a long time.

【0006】[0006]

【課題を解決するための手段】前述の目的を達成するた
め本発明はバレルの外周面に設けた加熱装置により温度
制御する異方向回転の二軸押出機のバレル温度制御方法
において、前記バレルを複数の温度制御区域に分割する
とともに、各温度制御区域にバレルの上側、下側の夫々
に温度検出装置を設け、バレルの上半分および下半分を
別々に温度制御することを特徴とする二軸押出機のバレ
ル温度制御方法とした。
According to the present invention, there is provided a method of controlling the temperature of a barrel of a twin screw extruder having a different direction, wherein the temperature is controlled by a heating device provided on the outer peripheral surface of the barrel. Biaxial, wherein the temperature control section is divided into a plurality of temperature control sections, and a temperature detecting device is provided on each of the upper and lower sides of the barrel in each temperature control section, and the upper half and the lower half of the barrel are separately temperature-controlled. An extruder barrel temperature control method was used.

【0007】またバレルの上半分および下半分を別々に
温度制御する温度制御区域は原料供給口下部付近の制御
区域のみであることを特徴とする二軸押出機のバレル温
度制御方法とした。
[0007] Further, there is provided a barrel temperature control method for a twin-screw extruder, wherein the temperature control section for separately controlling the upper half and the lower half of the barrel is only the control section near the lower part of the raw material supply port.

【0008】[0008]

【発明の実施の形態】異方向回転の二軸押出機のバレル
を複数の温度制御区域に分割するとともに、各温度制御
区域にバレルの上側、下側の夫々に温度検出装置を設
け、バレルの上半分および下半分を別々に温度制御す
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The barrel of a twin-screw extruder having a different direction of rotation is divided into a plurality of temperature control sections, and a temperature detection device is provided in each of the temperature control sections on the upper and lower sides of the barrel, respectively. The upper and lower halves are separately temperature controlled.

【0009】[0009]

【実施例】図1および図2により本発明の1実施例を説
明すると、20は二軸押出機のバレルで、内径面に2本
のスクリュ21が図示してない駆動部により基部(図中
右方向)を機体本体に片持ち状態で支承され、互いに異
方向に回転自在に挿入されている。バレル20は原料供
給口22から吐出口23側へ向かって複数の温度制御区
域(本実施例はC1 、C2 、C3 、C4 の4区域)に分
けてあり、各区域にはバレル上側にはヒータ24ないし
27を、バレル下側にはヒータ28ないし31を設ける
とともに、上半分の温度を検出する熱伝対32ないし3
5および下半分の温度を検出する熱伝対36ないし39
が設けてある。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to FIGS. 1 and 2. Reference numeral 20 denotes a barrel of a twin-screw extruder. (Right direction) is supported by the fuselage body in a cantilever state, and is inserted rotatably in different directions from each other. The barrel 20 is divided into a plurality of temperature control sections (four sections of C 1 , C 2 , C 3 and C 4 in this embodiment) from the raw material supply port 22 to the discharge port 23 side, and each section has a barrel. Heaters 24 to 27 are provided on the upper side, heaters 28 to 31 are provided on the lower side of the barrel, and thermocouples 32 to 3 for detecting the temperature of the upper half are provided.
Thermocouples 36 to 39 for detecting temperature of 5 and lower half
Is provided.

【0010】以上説明したような構成となっており、異
方向回転二軸押出機(東芝機械製斜軸押出機)TEC−
67により本発明の上下別々に温度制御するテストを行
った。 テストは図3で示す表のように上下の温度差が
一番大きくなったC1 のみ上下別々に温度制御し、他の
区域C2 ないしC4 は冷却パイプに水が通る冷却制御が
可能なヒータを取付けた上側の制御で行った。その結果
長時間運転でも熱分解がなく、従って劣化物もでなかっ
た。
[0010] The above-explained structure is such that a different direction twin screw extruder (oblique screw extruder manufactured by Toshiba Machine Co.) TEC-
67, a test for separately controlling the upper and lower temperatures of the present invention was performed. Test temperature controlled only C 1 the temperature difference becomes largest in the vertical up and down separately as shown in the table shown in FIG. 3, is C 4 to other areas C 2 no possible cooling control the cooling pipe through which water The control was performed by the upper control with the heater attached. As a result, there was no thermal decomposition even after a long operation, and there was no deterioration.

【0011】図3の表から理解されるように、C2 、C
4 は運転中ヒータはOFF状態で、冷却パイプに水が通
る冷却制御が作動し、バレルの下側は上側より7〜10
C低く制御された。またC3 のベント部はスクリュ溝
部における充満度が低く、半可塑化した高温の原料がバ
レルの下側を流れるため、下側の温度が高くなったと推
測される。
As can be understood from the table of FIG. 3, C 2 , C
4 is a state in which the heater is in an OFF state during operation, a cooling control in which water passes through the cooling pipe is operated, and the lower side of the barrel is 7 to 10 from the upper side.
. C was controlled low. The vent of C 3 has a low degree of filling in the screw groove, the high-temperature and semi-plasticized material is to flow the underside of the barrel is estimated that the temperature of the lower side is increased.

【0012】[0012]

【発明の効果】以上説明したように異方向回転の二軸押
出機のバレル上側および下側の温度制御を別々に行うこ
とにより、長時間運転でも熱分解がなく、劣化物も発生
しない温度制御方法となった。
As described above, by separately controlling the upper temperature and lower temperature of the barrel of a twin-screw extruder of different rotation, temperature control that does not cause thermal decomposition even during long-time operation and does not cause deterioration. Became the way.

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

【図1】本発明の1実施例を示す図で、バレルの軸方向
の断面図。
FIG. 1 is a view showing one embodiment of the present invention, and is an axial sectional view of a barrel.

【図2】本発明の1実施例の示す図1のA−A断面図。FIG. 2 is a sectional view taken along line AA of FIG. 1 showing one embodiment of the present invention.

【図3】本発明の1実施例のテスト結果を示す表。FIG. 3 is a table showing test results of one example of the present invention.

【図4】従来の二軸押出機のバレル部の軸方向の断面を
示す図。
FIG. 4 is a diagram showing an axial cross section of a barrel portion of a conventional twin-screw extruder.

【図5】従来の二軸押出機の設定温度と検出温度の時間
的変化を示すグラフ。
FIG. 5 is a graph showing a temporal change in a set temperature and a detected temperature of a conventional twin-screw extruder.

【符号の説明】[Explanation of symbols]

20 バレル 21 スクリュ 22 材料供給口 23 吐出口 24、25、26、27 ヒータ(バレル上側用) 28、29、30、31 ヒータ(バレル下側用) 32、33、34、35 熱伝対(バレル上側用) 36、37、38、39 熱伝対(バレル下側用) Reference Signs List 20 barrel 21 screw 22 material supply port 23 discharge port 24, 25, 26, 27 heater (for upper barrel) 28, 29, 30, 31 heater (for lower barrel) 32, 33, 34, 35 thermocouple (barrel) 36, 37, 38, 39 Thermocouple (for lower barrel)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 バレルの外周面に設けた加熱装置により
温度制御する異方向回転の二軸押出機のバレル温度制御
方法において、前記バレルを複数の温度制御区域に分割
するとともに、各温度制御区域にバレルの上側、下側の
夫々に温度検出装置を設け、バレルの上半分および下半
分を別々に温度制御することを特徴とする二軸押出機の
バレル温度制御方法。
1. A method for controlling the temperature of a barrel of a twin-screw extruder having a different direction in which a temperature is controlled by a heating device provided on an outer peripheral surface of a barrel, wherein the barrel is divided into a plurality of temperature control sections, Wherein a temperature detecting device is provided on each of the upper and lower sides of the barrel, and the upper and lower halves of the barrel are separately temperature-controlled.
【請求項2】 前記バレルの上半分および下半分を別々
に温度制御する温度制御区域は原料供給口下部付近の制
御区域のみであることを特徴とする前記請求項1記載の
二軸押出機のバレル温度制御方法。
2. The twin-screw extruder according to claim 1, wherein a temperature control zone for separately controlling the upper half and the lower half of the barrel is only a control zone near a lower portion of a raw material supply port. Barrel temperature control method.
JP9132807A 1997-05-07 1997-05-07 Method for control of barrel temperature of double-screw extruding machine Pending JPH10305477A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9132807A JPH10305477A (en) 1997-05-07 1997-05-07 Method for control of barrel temperature of double-screw extruding machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9132807A JPH10305477A (en) 1997-05-07 1997-05-07 Method for control of barrel temperature of double-screw extruding machine

Publications (1)

Publication Number Publication Date
JPH10305477A true JPH10305477A (en) 1998-11-17

Family

ID=15090048

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9132807A Pending JPH10305477A (en) 1997-05-07 1997-05-07 Method for control of barrel temperature of double-screw extruding machine

Country Status (1)

Country Link
JP (1) JPH10305477A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005193670A (en) * 2004-01-02 2005-07-21 Everfocus Worldwide Co Ltd The formation method which enables the control of fine open cell core in fluid polymer material, and its apparatus
JP2006341478A (en) * 2005-06-09 2006-12-21 Mitsubishi Heavy Ind Ltd Continuous kneader and kneading system equipped with kneader

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005193670A (en) * 2004-01-02 2005-07-21 Everfocus Worldwide Co Ltd The formation method which enables the control of fine open cell core in fluid polymer material, and its apparatus
JP4559846B2 (en) * 2004-01-02 2010-10-13 エバーフォーカス ワールドワイド カンパニー リミテッド Generation method and apparatus capable of controlling microbubble nuclei in fluid polymer material
JP2006341478A (en) * 2005-06-09 2006-12-21 Mitsubishi Heavy Ind Ltd Continuous kneader and kneading system equipped with kneader

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