JPH0363944B2 - - Google Patents

Info

Publication number
JPH0363944B2
JPH0363944B2 JP20131485A JP20131485A JPH0363944B2 JP H0363944 B2 JPH0363944 B2 JP H0363944B2 JP 20131485 A JP20131485 A JP 20131485A JP 20131485 A JP20131485 A JP 20131485A JP H0363944 B2 JPH0363944 B2 JP H0363944B2
Authority
JP
Japan
Prior art keywords
tube
resin
vacuum chamber
pipe
cooling
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
JP20131485A
Other languages
Japanese (ja)
Other versions
JPS6260632A (en
Inventor
Keizo Abe
Yoshinori Kishi
Michio Satomoto
Yasuo Sugimoto
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.)
Hitachi Cable Ltd
Original Assignee
Hitachi Cable 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 Hitachi Cable Ltd filed Critical Hitachi Cable Ltd
Priority to JP60201314A priority Critical patent/JPS6260632A/en
Publication of JPS6260632A publication Critical patent/JPS6260632A/en
Publication of JPH0363944B2 publication Critical patent/JPH0363944B2/ja
Granted legal-status Critical Current

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  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Description

【発明の詳細な説明】 [発明の背景と目的] 本発明は、一般に熱収縮チユーブと呼ばれる樹
脂管を製造の際に半径方向拡張構造を改良した熱
収縮樹脂管連続製造装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Background and Objects of the Invention] The present invention relates to a continuous manufacturing apparatus for heat-shrinkable resin tubes, which has an improved radial expansion structure when manufacturing resin pipes, generally called heat-shrinkable tubes.

熱収縮樹脂管を連続製造するブロウイングライ
ンは、原樹脂管(樹脂管の材料)を軸方向に伸ば
さず半径方向にのみ拡大成形することを目的とす
るものである。成形部において原樹脂管を拡大成
形するにはその樹脂管温度をその軟化点以上で溶
融点以下に、材質等により異なるが一般に100℃
〜140℃の成形適正温度に加熱して成形している。
この成形適正温度では原樹脂管は、ゼリー状態に
やわらかくなつており、軸方向の伸びを零にして
成形部まで送り込むことは困難である。本出願人
は上記ブロウイングラインにおいてゼリー状原樹
脂管を極低張力として伸びを零近くにして成形部
に送り込む方法を既に出願中である。これは有効
なものであり、ある公差内に製造できるが、軸方
向の伸びを零にすることはできない。即ち、成形
部で原樹脂管を半径方向に拡大成形するとき、ゴ
ム風船をふくらませると同様に原樹脂管の伸び
は、半径方向及び軸方向の全方向に伸びる。この
成形法は従来より各種の案が提示されているが、
いずれも上記した風船状態の拡張となるため、成
形部までの伸びが零であつても軸方向の伸びを零
にすることは不可能である。これは、勿論のこ
と、成形部入口まで適正成形一定温度でゼリー状
原樹脂管を伸びが零近くの極低張力で送り込んだ
場合のことである。従つて、従来の方法では、ブ
ロウ成形時に原樹脂管の軸方向伸びを零とするこ
とは困難な問題となつていた。
A blowing line that continuously manufactures heat-shrinkable resin pipes is intended to expand and mold raw resin pipes (resin pipe material) only in the radial direction without stretching them in the axial direction. To expand and mold a raw resin tube in the molding section, the temperature of the resin tube must be above its softening point and below its melting point, although it varies depending on the material etc., but generally 100℃.
It is heated and molded to the appropriate molding temperature of ~140℃.
At this proper molding temperature, the raw resin tube is soft to a jelly state, and it is difficult to feed it to the molding section with zero elongation in the axial direction. The present applicant has already applied for a method in which the jelly-like raw resin tube is fed into the molding section in the above-mentioned blowing line with extremely low tension and elongation close to zero. Although this is effective and can be manufactured within certain tolerances, it does not allow for zero axial elongation. That is, when the raw resin tube is expanded and molded in the radial direction in the molding section, the raw resin tube expands in all directions, radial and axial, similar to when a rubber balloon is inflated. Various proposals have been proposed for this molding method, but
In both cases, the balloon state is expanded, so even if the elongation up to the molded part is zero, it is impossible to make the elongation in the axial direction zero. This, of course, is the case when the jelly-like raw resin tube is fed to the entrance of the molding section at an appropriate molding temperature at a constant temperature and under extremely low tension with almost no elongation. Therefore, in the conventional method, it has been difficult to reduce the axial elongation of the raw resin tube to zero during blow molding.

本発明は上記の状況に鑑みてなされたものであ
り、半径方向にのみ収縮し軸方向には収縮するこ
とのない高精度な熱収縮樹脂管を製造できる熱収
縮樹脂管連続製造装置を提供することを目的とし
たものである。
The present invention has been made in view of the above-mentioned circumstances, and provides a continuous heat-shrinkable resin pipe manufacturing device that can manufacture highly accurate heat-shrinkable resin pipes that contract only in the radial direction but not in the axial direction. It is intended for this purpose.

[発明の概要] 本発明の熱収縮樹脂管連続製造装置は、加熱槽
で加熱された原樹脂管が送り込まれ内側から圧縮
気体で加圧され外側を真空引きし完成樹脂管に拡
張成形される真空室と、上記成形された上記完成
樹脂管が導入し冷却される本冷却洗浄水槽と、該
本冷却洗浄水槽から引き出された該完成樹脂管を
引き取るモータに駆動される引取機とを設けてな
り、上記本冷却洗浄水槽側の上記真空室壁に密嵌
されると共に該真空室内位置の管壁に多数の小穴
が開口され内側で上記圧縮気体が上記原樹脂管内
に導入されて上記完成樹脂管が形成される成形管
と、上記真空室内で上記原樹脂管が軸方向の伸び
をほぼ零とし半径方向に拡大成形される伸びの分
だけ上記引取機の上記原樹脂管引取速度よりも早
い速度でモータに駆動され上記真空室に該原樹脂
を送り込む送込ロールと、該成形管の上記真空室
外部側の端部位置が該真空室及び上記本冷却洗浄
水槽間に位置されると共に上記完成樹脂管が上記
成形管の内周に遊嵌された状態の該成形管端部及
び該完成樹脂管外周を冷却シール潤滑水がシー
ル、かつ、該完成樹脂管外周及び該成形管内周の
ギヤツプ間から上記真空室内へ噴出する該冷却シ
ール潤滑水を供給する冷却水ノズルとを設けたも
のである。即ち、引取速度に対する送込ロール速
度を、成形管内にて原樹脂管が拡張されるとき半
径方向に伸びる分だけ早くなるように引取機と同
調させ、また、成形後の伸びを少なくとするため
成形管の出口端の完成樹脂管の外周を冷却水でシ
ールすると共に成形管内周と完成樹脂管外周との
間に冷却水を真空室内部側に流し冷却、潤滑、真
空封止作用を行わせるものである。
[Summary of the Invention] The continuous manufacturing apparatus for heat-shrinkable resin tubes of the present invention is configured such that a raw resin tube heated in a heating tank is fed, pressurized with compressed gas from the inside, evacuated the outside, and expanded into a finished resin tube. A vacuum chamber, a main cooling washing water tank into which the molded finished resin pipe is introduced and cooled, and a taking machine driven by a motor to take over the finished resin pipe pulled out from the main cooling washing water tank are provided. The finished resin is tightly fitted into the wall of the vacuum chamber on the side of the main cooling washing water tank, and a number of small holes are opened in the tube wall located in the vacuum chamber, and the compressed gas is introduced into the raw resin tube inside. The molded tube in which the tube is formed and the raw resin tube in the vacuum chamber have almost zero elongation in the axial direction and are expanded in the radial direction. A feed roll driven by a motor at high speed to feed the raw resin into the vacuum chamber, and an end position of the forming tube on the outside of the vacuum chamber are located between the vacuum chamber and the main cooling washing water tank, and the above-mentioned The finished resin pipe is loosely fitted to the inner periphery of the molded tube, and the end portion of the molded pipe and the outer periphery of the completed resin pipe are cooled and sealed with lubricating water, and the gap between the outer periphery of the finished resin pipe and the inner periphery of the molded pipe is sealed. A cooling water nozzle for supplying the cooling seal lubricating water jetted into the vacuum chamber from between the cooling water nozzles and the vacuum chamber is provided. That is, in order to synchronize the feed roll speed with respect to the take-up speed with the take-off machine so that it becomes faster by the amount of radial elongation when the raw resin pipe is expanded in the forming pipe, and to reduce elongation after forming. The outer periphery of the completed resin tube at the outlet end of the molded tube is sealed with cooling water, and the cooling water is flowed inside the vacuum chamber between the inner periphery of the molded tube and the outer periphery of the completed resin tube to perform cooling, lubrication, and vacuum sealing effects. It is something.

[実施例] 以下本発明の熱収縮樹脂管連続製造装置を実施
例を用い図面により説明する。図は断面説明図で
ある。図において、1は加熱室、2は加熱槽、3
はポリエチレングリコールからなる加熱媒体、4
は送込ロール、5は送込駆動モータ用アンプ、6
は送込駆動モータである。7は送込駆動モータ用
タコジエネレータ、8は成形用冷却管、9は成形
管である。10は真空室、11は冷却水ノズル、
12は冷却シール潤滑水、13は本冷却洗浄水
槽、14はエアワイパー、15は引取機、16は
引取駆動モータ用アンプ、17は引取駆動モー
タ、18は引取駆動モータ用タコジエネレータ、
19は同調速度設定器、20は基準引取速度設定
器である。また、21は原樹脂管、22は完成樹
脂管、23は低定温水槽、24は循環ポンプ、2
5は真空圧力計、26は真空調整バルブ、27は
ミストセパレータ、28は真空ポンプ、29は低
圧力制御バルブ、30は内部加圧力計である。
[Example] The continuous manufacturing apparatus for heat-shrinkable resin pipes of the present invention will be explained below using examples and drawings. The figure is an explanatory cross-sectional view. In the figure, 1 is a heating chamber, 2 is a heating tank, and 3
is a heating medium made of polyethylene glycol, 4
is the feed roll, 5 is the feed drive motor amplifier, 6
is the feed drive motor. 7 is a tachometer generator for the feed drive motor, 8 is a cooling pipe for forming, and 9 is a forming pipe. 10 is a vacuum chamber, 11 is a cooling water nozzle,
12 is cooling seal lubricating water, 13 is a main cooling cleaning water tank, 14 is an air wiper, 15 is a take-up machine, 16 is an amplifier for take-up drive motor, 17 is take-up drive motor, 18 is a tachometer generator for take-up drive motor,
19 is a synchronized speed setter, and 20 is a reference take-up speed setter. In addition, 21 is an original resin pipe, 22 is a finished resin pipe, 23 is a low constant temperature water tank, 24 is a circulation pump, 2
5 is a vacuum pressure gauge, 26 is a vacuum adjustment valve, 27 is a mist separator, 28 is a vacuum pump, 29 is a low pressure control valve, and 30 is an internal pressure gauge.

そして、加熱室1内の加熱槽2により出た原樹
脂管21は、成形管9の入口部に組み込まれた送
込ロール4により真空室10内に送り込まれ内部
にある成形管9の部分で半径方向に拡大伸ばされ
つつ完成樹脂管22となつて冷却シール潤滑水1
2、本冷却洗浄水槽13、エアワイパー14を経
由して引取機15に引きとられるようになつてい
る。加熱槽2内においては、加熱媒体3によつて
原樹脂管21は成形適正一定温度に加熱される。
加熱された原樹脂管21は送込ロール4によりス
リツプしないように挟み込まれて送り込まれ、真
空室10内の成形管9部で引取機15後方の完成
樹脂管22の端末より原樹脂管21内に導入され
た加熱エア(圧縮空気)と真空圧との和の圧力で
一気に膨張されると同時に成形用冷却管8、冷却
シール潤滑水12により冷却されながら成形され
る。冷却水ノズル11よりの冷却水は、完成樹脂
管22の外周の成形管9の端部をシールし成形管
9の開口端より真空室10の方向へ成形管9内壁
と完成樹脂管22の外周面との間の微少なギヤツ
プを通して吸い込まれるため、そのギヤツプ間で
の潤滑剤として、また、冷却効果を増加すること
及び真空室10内と外気のシール作用を行なうこ
とで成形作用に重要な役割を果している。
Then, the raw resin tube 21 discharged from the heating tank 2 in the heating chamber 1 is fed into the vacuum chamber 10 by the feed roll 4 built into the inlet of the forming tube 9, and the part of the forming tube 9 inside is fed into the vacuum chamber 10. While being expanded and stretched in the radial direction, it becomes a completed resin pipe 22 and the cooling seal lubricating water 1
2. It is designed to be taken up by a take-up machine 15 via a main cooling washing water tank 13 and an air wiper 14. In the heating tank 2, the raw resin pipe 21 is heated by the heating medium 3 to a constant temperature suitable for molding.
The heated raw resin tube 21 is sandwiched between feed rolls 4 so as not to slip, and is fed into the raw resin tube 21 from the end of the finished resin tube 22 behind the take-up machine 15 at the formed tube 9 section in the vacuum chamber 10. The molded material is expanded at once by the sum of the heated air (compressed air) introduced into the molded air and the vacuum pressure, and at the same time is molded while being cooled by the molding cooling pipe 8 and the cooling seal lubricating water 12. The cooling water from the cooling water nozzle 11 seals the end of the molded tube 9 on the outer periphery of the completed resin tube 22 and flows from the open end of the molded tube 9 toward the vacuum chamber 10 onto the inner wall of the molded tube 9 and the outer periphery of the completed resin tube 22. Since it is sucked in through the minute gap between the surface and the surface, it plays an important role in the forming operation by acting as a lubricant between the gaps, increasing the cooling effect, and performing a sealing action between the inside of the vacuum chamber 10 and the outside air. is fulfilled.

成形管9の開口端が直接本冷却洗浄水槽13へ
接続しない理由は、スタート時成形管9内へ多量
の水が吸い込まれないように(成形前は原樹脂管
21は細い)少量の水でシールするためである。
尚、運転中もこの冷却シール潤滑水12は極く少
量で十分であり完成樹脂管22を冷却し冷却中も
充分な潤滑を与えることにより、冷却後の軸方向
の伸びを少なくできる。一方、本質的な問題とし
て原樹脂管21を成形管9内でふくらますと、風
船状に半径、軸方向のあらゆる方向に拡大成形さ
れる。しかし、このとき、軸方向の伸びを零とす
ることは、送込ロール4の速度を引取機15の速
度より軸方向に伸びる割合だけ早くするように、
それぞれの引取駆動モータ17、送込駆動モータ
6の同調速度を制御することにより達成できる。
本実施例では、引取速度が5m/min、送込速度
5.5m/minのとき完成樹脂管22の軸方向伸び
は零となつた。勿論、無制限に引取速度に対して
送込ロール速度を早くすることはできない。材
質、温度、速度、サイズ、圧力等にもよるが、本
実施例では半径方向の伸びは200%が限度であつ
た。このとき、軸方向の伸びは、伸び方向に対し
て「負」、即ち、縮む現象となる。
The reason why the open end of the molding tube 9 is not directly connected to the main cooling wash water tank 13 is to prevent a large amount of water from being sucked into the molding tube 9 at the start (the base resin tube 21 is thin before molding). This is for sealing.
Incidentally, even during operation, a very small amount of this cooling seal lubricating water 12 is sufficient, and by cooling the completed resin pipe 22 and providing sufficient lubrication even during cooling, axial elongation after cooling can be reduced. On the other hand, the essential problem is that when the raw resin tube 21 is inflated within the molding tube 9, it is expanded and molded in all directions, radially and axially, like a balloon. However, at this time, setting the elongation in the axial direction to zero means making the speed of the feed roll 4 faster than the speed of the take-up machine 15 by the proportion of elongation in the axial direction.
This can be achieved by controlling the synchronized speeds of the take-up drive motor 17 and feed drive motor 6, respectively.
In this example, the take-up speed is 5 m/min, and the feeding speed is 5 m/min.
At 5.5 m/min, the axial elongation of the completed resin pipe 22 became zero. Of course, the feed roll speed cannot be made faster than the take-up speed without limit. Although it depends on the material, temperature, speed, size, pressure, etc., in this example, the radial elongation was limited to 200%. At this time, the elongation in the axial direction is "negative" with respect to the elongation direction, that is, it becomes a shrinking phenomenon.

成形管9のの真空室10内にある部分は細い穴
が多数あり真空室10内と連通されている。ま
た、成形管9には成形用冷却管8が巻回され、低
定温水槽23より潤滑ポンプ24を経由して冷却
水が循環されるようになつている。また、循環ポ
ンプ24からは冷却水ノズル11へも給水されて
いる。本冷却洗浄水槽13は完成樹脂管22を完
全冷却すると共に完成樹脂管22の表面上に付着
した加熱媒体のポリエチレングリコールを洗浄す
る。原樹脂管21の内部加圧用エアは、定圧力制
御バルブ29を経由して完成樹脂管22へ接続さ
れている。真空圧力計25、内部加圧力計30は
それぞれの圧力を指示する。引取機15は引取駆
動モータ17、引取駆動モータ用タコジエネレー
タ18及び引取駆動モータ用アンプ16によつて
構成される速度制御系駆動部にて駆動されるよう
になつている。送込ロール4は、送込駆動モータ
6、送込駆動モータ用タコジエネレータ7及び送
込駆動モータ用アンプ5による駆動部にて駆動さ
れ、同調速度設定器19を経由して引取機15と
同調運転できるようになつている。引取機15が
速度基準であり引取機15の速度は設定器20に
よつて与えられるようになつている。
A portion of the molded tube 9 located within the vacuum chamber 10 has many thin holes and communicates with the inside of the vacuum chamber 10. Further, a molding cooling pipe 8 is wound around the molding tube 9, and cooling water is circulated from a low constant temperature water tank 23 via a lubricating pump 24. Water is also supplied from the circulation pump 24 to the cooling water nozzle 11 . The main cooling and cleaning water tank 13 completely cools the finished resin pipe 22 and cleans polyethylene glycol of the heating medium adhering to the surface of the finished resin pipe 22. Air for internal pressurization of the original resin pipe 21 is connected to the finished resin pipe 22 via a constant pressure control valve 29 . The vacuum pressure gauge 25 and the internal pressurization pressure gauge 30 indicate their respective pressures. The take-up machine 15 is driven by a speed control system drive unit composed of a take-up drive motor 17, a take-up drive motor tachometer generator 18, and a take-up drive motor amplifier 16. The feed roll 4 is driven by a drive unit including a feed drive motor 6, a tachometer generator 7 for the feed drive motor, and an amplifier 5 for the feed drive motor, and is operated in synchronization with the take-up machine 15 via a synchronized speed setting device 19. I'm starting to be able to do it. The take-off machine 15 is a speed reference, and the speed of the take-off machine 15 is given by a setting device 20.

一方、送込ロール4の表面は原樹脂管21に外
傷を与えない範囲でスリツプ防止のためにロール
レツト加工状の粗さに形成されている。送込ロー
ル4は原樹脂管21のサイズが数多くあるため、
各サイズに適合するように上下ロールとも成形管
9中心に対し同距離に無段階可変にセツトできる
構造であり、その可変状態のまま駆動モートルに
接続しなければならない。このため、送込ロール
4と送込駆動モータ6との間の接続は、クランク
接点等では不可能(スプリングカツプリングは角
度不均一のため不可)であり、シユミツトカツプ
リングの特殊接手(図示せず)を取り付けてあ
る。成形管9内での成形は引取機15後方より拡
大された樹脂管内へ一定の内部加圧(本実施例で
はエア)と成形部での外部真空圧により拡大成形
されるが送込ロール以前では真空圧がないため拡
大されない。成形状件としては、送込ロール速
度、引取速度、樹脂管温度、冷却水温度及び真空
圧を、それぞれのサイズ、材質の樹脂管に対し一
定に最適条件としてセツトする必要がある。
On the other hand, the surface of the feeding roll 4 is roughened to the extent that it does not cause any damage to the raw resin tube 21 in order to prevent slipping. Since the feed roll 4 has many sizes of raw resin pipes 21,
In order to suit each size, both the upper and lower rolls can be set at the same distance from the center of the forming tube 9 in a steplessly variable manner, and must be connected to a drive motor in this variable state. For this reason, the connection between the feed roll 4 and the feed drive motor 6 cannot be made using a crank contact, etc. (spring couplings are not possible due to uneven angles), and a special coupling of Schmitt couplings ( (not shown) is attached. The molding inside the molding tube 9 is expanded by constant internal pressure (air in this example) into the expanded resin tube from the rear of the take-up machine 15 and external vacuum pressure at the molding section, but before the feeding roll. It is not expanded because there is no vacuum pressure. As for the forming conditions, it is necessary to set the feeding roll speed, take-up speed, resin tube temperature, cooling water temperature, and vacuum pressure as constant optimum conditions for each size and material of the resin tube.

このように本実施例の熱収縮樹脂管連続製造装
置は、引取速度より半径方向に伸びる分だけ早く
送られるように形成された送込ロールを設けたの
で、原樹脂管をふくらませる際に軸方向伸びをほ
ぼ零とし半径方向にのみ拡大成形され、また、成
形管の端部とこの成形管の内側に遊嵌された完成
樹脂管外周との間を冷却シール潤滑水でシールす
る冷却ノズルが配設されたので、冷却水が成形管
内周と完成樹脂管外周との間を真空室内に吸引さ
れシールすると共に潤滑液の機能を果たし完成樹
脂管の冷却を促進する。従つて、半径方向にのみ
収縮し軸方向には収縮することがない高精度の熱
収縮樹脂管を製造できる。
In this way, the continuous heat-shrinkable resin tube manufacturing apparatus of this embodiment is equipped with a feed roll that is formed to be fed faster than the take-up speed by the amount that it extends in the radial direction, so that when inflating the raw resin tube, it is possible to It is expanded only in the radial direction with almost zero elongation, and is equipped with a cooling nozzle that uses cooling seal lubricating water to seal between the end of the formed tube and the outer periphery of the finished resin tube that is loosely fitted inside the formed tube. As a result, the cooling water is sucked into the vacuum chamber between the inner periphery of the molded tube and the outer periphery of the completed resin tube to create a seal, and also functions as a lubricating fluid to promote cooling of the completed resin tube. Therefore, it is possible to manufacture a highly accurate heat-shrinkable resin tube that contracts only in the radial direction and does not contract in the axial direction.

上記実施例では、送込ロールは1組であるが、
複数組もしくは上下、水平の両方向にセツトする
ようにしてもよい。また、送込ロールは成形管入
口部でその内面まで出るようにセツトされている
が、送込ロールの直後へ成形管を配置する構造で
もよい。そして、送込ロールは実施例ではフラツ
トな面で、かつ、表面がローレツト状のものであ
るがセンタリングの目的にて樹脂管の通過する中
心部のみ樹脂管を適当に挟みこめるように溝部を
設けてもよい。
In the above embodiment, there is one set of feed rolls, but
They may be set in multiple sets or in both vertical and horizontal directions. Further, although the feed roll is set so as to extend to the inner surface of the forming tube at the inlet portion thereof, a structure in which the forming tube is disposed immediately after the feed roll may also be used. In the embodiment, the feed roll has a flat surface and a knurled surface, but for the purpose of centering, grooves are provided only in the center where the resin pipe passes, so that the resin pipe can be properly caught. It's okay.

[発明の効果] 以上記述した如く本発明の熱収縮樹脂管連続製
造装置は、半径方向にのみ収縮し軸方向には収縮
することがない高精度な熱収縮樹脂管を製造でき
る効果を有するものである。
[Effects of the Invention] As described above, the continuous manufacturing apparatus for heat-shrinkable resin pipes of the present invention has the effect of manufacturing highly accurate heat-shrinkable resin pipes that contract only in the radial direction and do not contract in the axial direction. It is.

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

図は本発明の熱収縮樹脂管連続製造装置の実施
例の断面説明図である。 2……加熱槽、4……送込ロール、6……送込
モータ、9……成形管、10……真空室、11…
…冷却水ノズル、12……冷却シール潤滑水、1
3……本冷却洗浄水槽、15……引取機、17…
…引取駆動モータ、21……原樹脂管、22……
完成樹脂管。
The figure is an explanatory cross-sectional view of an embodiment of the continuous manufacturing apparatus for heat-shrinkable resin pipes of the present invention. 2... Heating tank, 4... Feeding roll, 6... Feeding motor, 9... Forming tube, 10... Vacuum chamber, 11...
...Cooling water nozzle, 12...Cooling seal lubricating water, 1
3... Main cooling washing water tank, 15... Taking machine, 17...
...Take-up drive motor, 21... Raw resin pipe, 22...
Completed resin pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 加熱槽で加熱された原樹脂管が送り込まれ内
側から圧縮気体で加圧され外側を真空引きし完成
樹脂管に拡張成形される真空室と、上記成形され
た該完成樹脂管が導入し冷却される本冷却洗浄水
槽と、該本冷却洗浄水槽から引き出された該完成
樹脂管を引き取るモータに駆動される引取機とを
設けたものにおいて、上記本冷却洗浄水槽側の上
記真空室壁に密嵌されると共に該真空室内位置の
管壁に多数の小穴が開口され内側で上記圧縮気体
が上記原樹脂内に導入されて上記完成樹脂管が形
成される成形管と、上記真空室内で上記原樹脂管
が軸方向の伸びをほぼ零とし半径方向に拡大成形
される伸びの分だけ上記引取機の上記原樹脂管引
取速度よりも早い速度でモータに駆動され上記真
空室に該原樹脂を送り込む送込ロールと、該成形
管の上記真空室外部側の端部位置が該真空室及び
上記本冷却洗浄水槽間に位置されると共に上記完
成樹脂管が上記成形管の内周に遊嵌された状態の
該成形管端部及び該完成樹脂管外周を冷却シール
潤滑水がシールし、かつ、該完成樹脂管外周及び
該成形管内周のギヤツプ間から上記真空室内へ噴
出する該冷却シール潤滑水を供給する冷却水ノズ
ルとを設けたことを特徴とする熱収縮樹脂管連続
製造装置。
1. A vacuum chamber where the raw resin tube heated in the heating tank is fed, pressurized from the inside with compressed gas, evacuated the outside, and expanded into a finished resin tube, and the finished resin tube formed above is introduced and cooled. A main cooling washing water tank is provided, and a taking machine driven by a motor that takes over the finished resin pipe pulled out from the main cooling washing water tank is provided. A molded tube that is fitted into the tube and has a large number of small holes opened in the tube wall located in the vacuum chamber, and the compressed gas is introduced into the raw resin inside to form the finished resin tube, and The resin tube is driven by a motor at a speed higher than the raw resin pipe take-up speed of the take-up machine to feed the raw resin into the vacuum chamber by the amount of elongation that causes the resin tube to expand in the radial direction with almost zero elongation in the axial direction. The feed roll and the end position of the formed tube on the outside of the vacuum chamber are located between the vacuum chamber and the main cooling washing water tank, and the completed resin tube is loosely fitted to the inner periphery of the formed tube. Cooling seal lubricating water seals the end of the molded pipe and the outer periphery of the completed resin pipe in the state, and the cooling seal lubricating water is jetted into the vacuum chamber from between the gaps on the outer periphery of the finished resin pipe and the inner periphery of the molded pipe. A continuous manufacturing device for heat-shrinkable resin pipes, characterized in that it is equipped with a cooling water nozzle for supplying cooling water.
JP60201314A 1985-09-11 1985-09-11 Continuous manufacturing device for heat-shrink resin tube Granted JPS6260632A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60201314A JPS6260632A (en) 1985-09-11 1985-09-11 Continuous manufacturing device for heat-shrink resin tube

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60201314A JPS6260632A (en) 1985-09-11 1985-09-11 Continuous manufacturing device for heat-shrink resin tube

Publications (2)

Publication Number Publication Date
JPS6260632A JPS6260632A (en) 1987-03-17
JPH0363944B2 true JPH0363944B2 (en) 1991-10-03

Family

ID=16438955

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60201314A Granted JPS6260632A (en) 1985-09-11 1985-09-11 Continuous manufacturing device for heat-shrink resin tube

Country Status (1)

Country Link
JP (1) JPS6260632A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4134341A1 (en) * 1990-11-16 1992-05-21 Theysohn Friedrich Fa DEVICE FOR PRODUCING A PROFILE BODY
CN103722643A (en) * 2014-01-15 2014-04-16 长园电子(集团)有限公司 Expanding mould of heat shrinking pipe
JP5778831B1 (en) 2014-03-31 2015-09-16 月島機械株式会社 Method of drying workpiece and horizontal rotary dryer
JP5847350B1 (en) 2015-09-15 2016-01-20 月島機械株式会社 Method of drying terephthalic acid and horizontal rotary dryer

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0587059A (en) * 1991-09-27 1993-04-06 Kyocera Corp Uniaxis eccentric screw pump
JP2005248756A (en) * 2004-03-02 2005-09-15 Kobe Steel Ltd Gear rotor for gear pump, and gear pump
JP2005299494A (en) * 2004-04-12 2005-10-27 Heishin Engineering & Equipment Co Ltd Stator for uniaxial eccentric screw pump

Also Published As

Publication number Publication date
JPS6260632A (en) 1987-03-17

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