JPH0581430B2 - - Google Patents

Info

Publication number
JPH0581430B2
JPH0581430B2 JP1295559A JP29555989A JPH0581430B2 JP H0581430 B2 JPH0581430 B2 JP H0581430B2 JP 1295559 A JP1295559 A JP 1295559A JP 29555989 A JP29555989 A JP 29555989A JP H0581430 B2 JPH0581430 B2 JP H0581430B2
Authority
JP
Japan
Prior art keywords
outer diameter
resin
mandrel
extruder
molten resin
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
Application number
JP1295559A
Other languages
Japanese (ja)
Other versions
JPH03155918A (en
Inventor
Ken Niwa
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.)
Sumitomo Riko Co Ltd
Original Assignee
Tokai Rubber Industries 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 Tokai Rubber Industries Ltd filed Critical Tokai Rubber Industries Ltd
Priority to JP1295559A priority Critical patent/JPH03155918A/en
Publication of JPH03155918A publication Critical patent/JPH03155918A/en
Publication of JPH0581430B2 publication Critical patent/JPH0581430B2/ja
Granted 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
    • B29C48/92Measuring, 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
    • B29C2948/92009Measured parameter
    • B29C2948/92114Dimensions
    • B29C2948/92123Diameter or circumference
    • 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
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92361Extrusion unit
    • B29C2948/92409Die; Nozzle zone
    • 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
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92438Conveying, transporting or storage of articles
    • 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
    • B29C2948/92609Dimensions
    • B29C2948/92619Diameter or circumference
    • 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
    • B29C2948/92904Die; Nozzle zone
    • 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
    • B29C2948/92933Conveying, transporting or storage of articles

Landscapes

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

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ホース製造に用いる可撓性の樹脂マ
ンドレル、特に高精度な外径寸法を有する樹脂マ
ンドレルを製造する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a flexible resin mandrel used for manufacturing hoses, and particularly to an apparatus for manufacturing a resin mandrel having a highly accurate outer diameter.

〔従来の技術〕[Conventional technology]

従来、樹脂マンドレルの製造には第2図に示す
ような装置を使用し、原料樹脂ペレツトを押出機
1のホツパードライヤー2に投入し、押出機1で
加熱溶融させながらスクリユーの回転により溶融
樹脂4を押出ヘツド3から連続的に押出し、所定
内径のサイジングダイ5を通して断面円形に成形
した後、冷却水槽6で冷却し、冷却的に得られる
樹脂マンドレル8を回転するキヤタピラを備えた
引取機7で引き取る方法が用いられている。引取
機7を出た樹脂マンドレル8は、巻取機9により
巻取皿等に巻き取られる。
Conventionally, a device as shown in Fig. 2 has been used to manufacture resin mandrels. Raw resin pellets are fed into a hopper dryer 2 of an extruder 1, and while being heated and melted by the extruder 1, the molten resin is produced by rotating a screw. 4 is continuously extruded from an extrusion head 3, passed through a sizing die 5 of a predetermined inner diameter, and formed into a circular cross-section, and then cooled in a cooling water tank 6. The method used is to pick it up. The resin mandrel 8 that has come out of the take-up machine 7 is wound onto a winding plate or the like by a wind-up machine 9.

このようにして製造される樹脂マンドレル8の
外径φは、一義的にはサイジングダイ5の内径と
引取機7による樹脂マンドレル8の引取速度の関
係によつて決定される。従つて、従来はサイジン
グダイ5の内径に応じて経験的に求められた引取
速度で引取りながら、巻取つた樹脂マンドレル8
の外径φをノギス等で実際に測定し、得られた外
径測定値に応じて逐次引取速度を微調整すること
によつて外径寸法を制御していた。
The outer diameter φ of the resin mandrel 8 manufactured in this manner is primarily determined by the relationship between the inner diameter of the sizing die 5 and the drawing speed of the resin mandrel 8 by the drawing machine 7. Therefore, in the past, the resin mandrel 8 was wound while being taken off at a taking-off speed determined empirically according to the inner diameter of the sizing die 5.
The outer diameter dimension was controlled by actually measuring the outer diameter φ with a caliper or the like, and finely adjusting the take-up speed sequentially according to the obtained outer diameter measurement value.

かかる従来の外径寸法制御により実際に得られ
る樹脂マンドレルの外径φは厳密に一定ではあり
えず、例えば外径φの基準値が7.1mmの場合には
±0.10mm程度の大きなバラツキを生じていた。
The outer diameter φ of the resin mandrel actually obtained by such conventional outer diameter size control cannot be strictly constant; for example, when the standard value of the outer diameter φ is 7.1 mm, there is a large variation of about ±0.10 mm. Ta.

然るに、最近では自動車の高性能化に伴なつ
て、高圧燃料噴射用ホース等でホース内径寸法を
重視する傾向にあり、このためホース製造用の樹
脂マンドレルの外径寸法精度の向上が要求される
ようになつた。
However, as the performance of automobiles has improved recently, there has been a tendency to place more emphasis on the inner diameter of hoses used in high-pressure fuel injection hoses, etc., and for this reason, there is a need to improve the accuracy of the outer diameter dimensions of resin mandrels used for manufacturing hoses. It became like that.

要望される高精度な内径のホースを製造する為
に、従来の方法により製造した樹脂マンドレルで
は外径が所定の公差を超える部分は使用出来ない
ので、マンドレルの製造歩留が極端に低下する問
題があつた。
In order to manufacture hoses with the desired high-precision inner diameter, resin mandrels manufactured using conventional methods cannot be used in areas where the outer diameter exceeds a specified tolerance, resulting in an extremely low mandrel manufacturing yield. It was hot.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明はかかる従来の事情に鑑み、高精度な外
径寸法を有する樹脂マンドレルを容易に製造する
ことの出来る装置を提供することを目的とする。
SUMMARY OF THE INVENTION In view of the conventional circumstances, it is an object of the present invention to provide an apparatus that can easily manufacture a resin mandrel having a highly accurate outer diameter.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的を達成するため、本発明では、押出機
から連続押出した溶融樹脂をサイジングダイを通
して断面円形に成形し、冷却して得られる樹脂マ
ンドレルを引取機で連続的に引取る樹脂マンドレ
ルの製造装置において、冷却後の樹脂マンドレル
の外径を測定する第1外径測定器と、樹脂マンド
レルの外径測定値を予め定めた基準値と比較し、
基準値からの増加又は減少に応じて引取速度を増
加又は減少させる第1制御装置と、押出機の押出
ヘツドとサイジングダイとの間で溶融樹脂の外径
を測定する第2外径測定器と、溶融樹脂の外径測
定値を予め定めた基準値と比較し、基準値からの
増加又は減少に応じて押出機の溶融樹脂吐出量を
減少又は増加させる第2制御装置とを備えたこと
を特徴とする。
In order to achieve the above object, the present invention provides a resin mandrel manufacturing apparatus in which a molten resin continuously extruded from an extruder is molded into a circular cross section through a sizing die, and the resin mandrel obtained by cooling is continuously taken off by a take-off machine. A first outer diameter measuring device that measures the outer diameter of the resin mandrel after cooling is used, and the measured outer diameter of the resin mandrel is compared with a predetermined reference value,
a first controller that increases or decreases the take-up speed in accordance with an increase or decrease from a reference value; a second outer diameter measuring device that measures the outer diameter of the molten resin between the extrusion head and the sizing die of the extruder; , a second control device that compares the measured outer diameter of the molten resin with a predetermined reference value and reduces or increases the amount of molten resin discharged from the extruder in accordance with the increase or decrease from the reference value. Features.

〔作用〕[Effect]

前記の如く、樹脂マンドレルの外径φは一義的
にはサイジングダイの内径と樹脂マンドレルの引
取速度の関係によつて決定されるが、押出される
溶融樹脂は柔軟であるから、押出ヘツドからの溶
融樹脂は外径が漸減しながらサイジングダイに引
込まれるうえ、両者間の所定位置での外径Dも押
出機の吐出量の微妙な変化により変動し、この溶
融樹脂の外径Dの変動によつて樹脂マンドレルの
外径φが影響されることが判つた。
As mentioned above, the outer diameter φ of the resin mandrel is primarily determined by the relationship between the inner diameter of the sizing die and the take-up speed of the resin mandrel, but since the molten resin to be extruded is flexible, the The molten resin is drawn into the sizing die while its outer diameter gradually decreases, and the outer diameter D at a predetermined position between the two also fluctuates due to subtle changes in the discharge rate of the extruder. It was found that the outer diameter φ of the resin mandrel was influenced by

そこで本発明においては、通常行なわれている
樹脂マンドレルの引取速度の制御に加えて、押出
ヘツドとサイジングダイの間での溶融樹脂の外径
Dを測定し、この値が常に一定の基準値となるよ
うに溶融樹脂吐出量を制御することとし、外径測
定器とPID制御装置等を用いて装置化することに
よつて、樹脂マンドレルの引取速度及び溶融樹脂
の外径Dを自動的に且つ迅速に制御管理でき、こ
れにより従来に比べて外径精度が極めて高い樹脂
マンドレルを人手を要さず簡単に製造できるよう
になつたものである。
Therefore, in the present invention, in addition to the usual control of the take-up speed of the resin mandrel, the outer diameter D of the molten resin between the extrusion head and the sizing die is measured, and this value is always kept at a constant reference value. By controlling the amount of molten resin discharged so that This allows quick control and management, and as a result, it has become possible to easily manufacture resin mandrels with extremely high outside diameter accuracy, without requiring human labor, compared to conventional methods.

尚、外径測定器としては、半導体レーザー等の
平行走査された光ビームが樹脂マンドレル又は溶
融樹脂に当つた影を受光部で検出する光走査式寸
法測定装置等を使用できる。又、制御装置として
は、市販のコンピユータ制御装置を使用できる
が、特にPI又はPID制御動作を行なう制御装置が
好ましい。
As the outer diameter measuring device, an optical scanning dimension measuring device or the like can be used, which uses a light receiving section to detect the shadow of a parallel-scanned light beam of a semiconductor laser or the like hitting the resin mandrel or molten resin. Further, as the control device, a commercially available computer control device can be used, but a control device that performs a PI or PID control operation is particularly preferred.

〔実施例〕〔Example〕

本発明の一具体例を第1図により説明する。 A specific example of the present invention will be explained with reference to FIG.

この樹脂マンドレル製造装置の本体部分は従来
と同様であり、原料樹脂ペレツトを投入するホツ
パードライヤー2やスクリユーの回転により溶融
樹脂4を連続的に押出す押出ヘツド3を備えた樹
脂用の押出機1、押出機1から押出された溶融樹
脂4を断面円形に成形する所定内径のサイジング
ダイ5、サイジングダイ5に連続して設けた冷却
水槽6、冷却して得られる樹脂マンドレル8を連
続的に引取る引取機7、及び引取機7の後方に設
置した樹脂マンドレル8の巻取機9からなる。
The main body of this resin mandrel manufacturing apparatus is the same as the conventional one, and is a resin extruder equipped with a hopper dryer 2 into which raw resin pellets are input, and an extrusion head 3 which continuously extrudes molten resin 4 by rotating a screw. 1. A sizing die 5 with a predetermined inner diameter that molds the molten resin 4 extruded from the extruder 1 into a circular cross section, a cooling water tank 6 provided continuously to the sizing die 5, and a resin mandrel 8 obtained by cooling the resin mandrel 8 continuously. It consists of a take-up machine 7 for take-up, and a winder 9 for a resin mandrel 8 installed behind the take-off machine 7.

更に本装置においては、冷却水槽6と引取機7
の間に樹脂マンドレル8の外径φを測定する第1
外径測定器10を備え、得られた外径測定値を市
販のPID制御装置からなる第1制御装置11にお
いて予め定めた基準値と比較し、基準値からの増
加又は減少に応じた制御信号で引取機7のモータ
ー回転数を変化させることにより、引取速度を増
加又は減少させる。引取速度の制御は逐次行なつ
ても良いが、本装置では最初に適切な引取速度に
設定すれば以後そのまま一定に保持してよく、下
記する溶融樹脂4の外径制御によつて外径精度が
充分に高い樹脂マンドレル8が得られる。
Furthermore, in this device, a cooling water tank 6 and a take-up machine 7 are provided.
During the first step, the outer diameter φ of the resin mandrel 8 is measured.
A first controller 11 comprising an outer diameter measuring device 10 compares the obtained outer diameter measurement value with a predetermined reference value in a first control device 11 consisting of a commercially available PID control device, and generates a control signal according to an increase or decrease from the reference value. By changing the rotation speed of the motor of the take-up machine 7, the take-up speed is increased or decreased. The withdrawal speed may be controlled sequentially, but in this device, if the withdrawal speed is set to an appropriate value first, it can be kept constant from then on, and the outer diameter accuracy can be maintained by controlling the outer diameter of the molten resin 4 as described below. A resin mandrel 8 having a sufficiently high value can be obtained.

又、押出機1の押出ヘツド3とサイジングダイ
5との間の所定位置には第2外径測定器12が設
けてあり、溶融樹脂4の外径Dを測定する。第2
外径測定器12で測定した溶融樹脂4の外径測定
値を、市販のPID制御装置である第2制御装置1
3において予め定めた基準値と比較し、基準値か
らの増加又は減少に応じた制御信号により押出機
1のスクリユー回転数を変化させて、押出機1か
らの溶融樹脂吐出量を減少又は増加させるように
なつている。
Further, a second outer diameter measuring device 12 is provided at a predetermined position between the extrusion head 3 and the sizing die 5 of the extruder 1, and measures the outer diameter D of the molten resin 4. Second
The outer diameter measurement value of the molten resin 4 measured by the outer diameter measuring device 12 is transferred to the second control device 1 which is a commercially available PID control device.
3, the screw rotation speed of the extruder 1 is changed by a control signal according to the increase or decrease from the reference value, and the amount of molten resin discharged from the extruder 1 is decreased or increased. It's becoming like that.

かかる本発明装置によれば、溶融樹脂4の外径
Dを基準値に対して±0.2mm程度の精度で制御で
き、従つて樹脂マンドレルの外径φを基準値に対
して±0.035mm程度の従来より!?かに高い精度で
管理できる。しかも、押出機1の押出ヘツド3と
サイジングダイ5との距離を30〜90mmに設定する
ことによつて、この間で溶融樹脂吐出量の微細な
変化を吸収でき、制御タイミングのズレを無くし
て、溶融樹脂4の外径Dひいては樹脂マンドレル
の外径φを更に高い精度に管理出来る。
According to the apparatus of the present invention, the outer diameter D of the molten resin 4 can be controlled with an accuracy of about ±0.2 mm with respect to the reference value, and therefore the outer diameter φ of the resin mandrel can be controlled with an accuracy of about ±0.035 mm with respect to the reference value. It can be managed with much higher precision than before! Moreover, by setting the distance between the extrusion head 3 of the extruder 1 and the sizing die 5 to 30 to 90 mm, minute changes in the amount of molten resin discharged can be absorbed during this time, eliminating deviations in control timing. The outer diameter D of the molten resin 4 and, in turn, the outer diameter φ of the resin mandrel can be controlled with even higher precision.

上記装置を使用して、押出径約14mmの押出ヘツ
ド3と内径7.5mmのサイジングダイ5との距離を
45mmに設定し、外径基準値7.1mmのポリエステル
の樹脂マンドレルを製造した。最初に、第1外径
測定器10で樹脂マンドレル8の外径φを測定し
ながら第1制御装置11により引取速度を自動的
に増減し、外径7.1mmの樹脂マンドレル8が得ら
れた時点で引取速度を固定した。この段階で得ら
れる樹脂マンドレル8の外径寸法精度は約7.1±
0.10mmであつた。次に、固定した引取速度のまま
押出ヘツド3から20mmの位置に設けた第2外径測
定器12により溶融樹脂4の外径Dを測定し、第
2制御装置13により押出機1のスクリユー回転
数を自動的に変化させて溶融樹脂吐出量を制御し
た。溶融樹脂4の外径Dは制御開始前は12〜14mm
の範囲でバラツキがあつたが、上記制御により
13.2±0.2mmの範囲に収められ、得られた樹脂マ
ンドレル8の外径φは7.1mm+0.04 -0.03mmとなり、極め
て高精度であつた。
Using the above device, measure the distance between the extrusion head 3 with an extrusion diameter of approximately 14 mm and the sizing die 5 with an inner diameter of 7.5 mm.
45 mm, and a polyester resin mandrel with an outer diameter standard value of 7.1 mm was manufactured. First, while measuring the outer diameter φ of the resin mandrel 8 with the first outer diameter measuring device 10, the first controller 11 automatically increases or decreases the take-up speed, and when the resin mandrel 8 with an outer diameter of 7.1 mm is obtained. The withdrawal speed was fixed. The outer diameter dimensional accuracy of the resin mandrel 8 obtained at this stage is approximately 7.1±
It was 0.10mm. Next, the outer diameter D of the molten resin 4 is measured by the second outer diameter measuring device 12 installed at a position 20 mm from the extrusion head 3 while keeping the take-up speed fixed, and the screw rotation of the extruder 1 is controlled by the second controller 13. The amount of molten resin discharged was controlled by automatically changing the number. The outer diameter D of the molten resin 4 is 12 to 14 mm before starting control.
Although there was some variation within the range of
The outside diameter of the resin mandrel 8 obtained was 7.1 mm +0.04 -0.03 mm, which was extremely high precision.

〔発明の効果〕〔Effect of the invention〕

本発明装置によれば、樹脂マンドレルの引取速
度と共に、押出機からの溶融樹脂の外径を自動的
に管理して、極めて高精度な外径寸法を有する樹
脂マンドレルを簡単に製造することが出来る。
According to the apparatus of the present invention, it is possible to automatically manage the outside diameter of the molten resin from the extruder as well as the take-up speed of the resin mandrel, and easily manufacture a resin mandrel having an extremely highly accurate outside diameter. .

しかも、製造する樹脂マンドレルの種類に応じ
て外径を変更する場合にも、引取速度の設定及び
溶融樹脂の吐出量並びに外径の管理が自動的に、
迅速且つ正確に行なわれるので、短時間で容易に
外径精度の高い他品種の樹脂マンドレルの製造に
切り替えることができる。
Moreover, even when changing the outer diameter depending on the type of resin mandrel being manufactured, the setting of the take-up speed, the discharge amount of molten resin, and the management of the outer diameter can be done automatically.
Since the process is carried out quickly and accurately, it is possible to easily switch to manufacturing other types of resin mandrels with high outer diameter accuracy in a short time.

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

第1図は本発明の一具体例による高精度樹脂マ
ンドレル製造装置を示す概略構成図であり、第2
図は従来の樹脂マンドレル製造装置の概略構成図
である。 1……押出機、2……ホツパードライヤー、3
……押出ヘツド、4……溶融樹脂、5……サイジ
ングダイ、6……冷却水槽、7……引取機、8…
…樹脂マンドレル、9……巻取機、10……第1
外径測定器、11……第1制御装置、12……第
2外径測定器、13……第2制御装置。
FIG. 1 is a schematic configuration diagram showing a high-precision resin mandrel manufacturing apparatus according to a specific example of the present invention, and FIG.
The figure is a schematic diagram of a conventional resin mandrel manufacturing apparatus. 1...Extruder, 2...Hopper dryer, 3
... Extrusion head, 4 ... Molten resin, 5 ... Sizing die, 6 ... Cooling water tank, 7 ... Taking machine, 8 ...
... Resin mandrel, 9 ... Winding machine, 10 ... 1st
Outer diameter measuring device, 11...first control device, 12...second outer diameter measuring device, 13...second control device.

Claims (1)

【特許請求の範囲】 1 押出機から連続押出した溶融樹脂をサイジン
グダイを通して断面円形に成形し、冷却して得ら
れる樹脂マンドレルを引取機で連続的に引取る樹
脂マンドレルの製造装置において、冷却後の樹脂
マンドレルの外径を測定する第1外径測定器と、
樹脂マンドレルの外径測定値を予め定めた基準値
と比較し、基準値からの増加又は減少に応じて引
取速度を増加又は減少させる第1制御装置と、押
出機の押出ヘツドとサイジングダイとの間で溶融
樹脂の外径を測定する第2外径測定器と、溶融樹
脂の外径測定値を予め定めた基準値と比較し、基
準値からの増加又は減少に応じて押出機の溶融樹
脂吐出量を減少又は増加させる第2制御装置とを
備えたことを特徴とする高精度樹脂マンドレルの
製造装置。 2 押出機の押出ヘツドとサイジングダイとの距
離が30〜90mmであることを特徴とする、請求項1
記載の高精度樹脂マンドレルの製造装置。
[Scope of Claims] 1. In a resin mandrel manufacturing apparatus in which a molten resin continuously extruded from an extruder is molded into a circular cross-section through a sizing die, and the resin mandrel obtained by cooling is continuously taken up by a take-up machine, a first outer diameter measuring device for measuring the outer diameter of the resin mandrel;
A first control device that compares the measured outer diameter of the resin mandrel with a predetermined reference value and increases or decreases the take-up speed according to the increase or decrease from the reference value, and an extrusion head and a sizing die of the extruder. A second outer diameter measuring device is used to measure the outer diameter of the molten resin, and the outer diameter measurement value of the molten resin is compared with a predetermined reference value, and the molten resin of the extruder is adjusted depending on the increase or decrease from the reference value. 1. A high-precision resin mandrel manufacturing apparatus, comprising: a second control device that reduces or increases the discharge amount. 2. Claim 1, characterized in that the distance between the extrusion head of the extruder and the sizing die is 30 to 90 mm.
The described high-precision resin mandrel manufacturing equipment.
JP1295559A 1989-11-14 1989-11-14 Apparatus for preparing highly accurate resin mandrel Granted JPH03155918A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1295559A JPH03155918A (en) 1989-11-14 1989-11-14 Apparatus for preparing highly accurate resin mandrel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1295559A JPH03155918A (en) 1989-11-14 1989-11-14 Apparatus for preparing highly accurate resin mandrel

Publications (2)

Publication Number Publication Date
JPH03155918A JPH03155918A (en) 1991-07-03
JPH0581430B2 true JPH0581430B2 (en) 1993-11-12

Family

ID=17822211

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1295559A Granted JPH03155918A (en) 1989-11-14 1989-11-14 Apparatus for preparing highly accurate resin mandrel

Country Status (1)

Country Link
JP (1) JPH03155918A (en)

Also Published As

Publication number Publication date
JPH03155918A (en) 1991-07-03

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