JPH0533481B2 - - Google Patents
Info
- Publication number
- JPH0533481B2 JPH0533481B2 JP62280178A JP28017887A JPH0533481B2 JP H0533481 B2 JPH0533481 B2 JP H0533481B2 JP 62280178 A JP62280178 A JP 62280178A JP 28017887 A JP28017887 A JP 28017887A JP H0533481 B2 JPH0533481 B2 JP H0533481B2
- Authority
- JP
- Japan
- Prior art keywords
- foaming
- outer diameter
- heating furnace
- degree
- core
- 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
- 238000005187 foaming Methods 0.000 claims description 40
- 238000000034 method Methods 0.000 claims description 17
- 238000010438 heat treatment Methods 0.000 claims description 15
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 238000007765 extrusion coating Methods 0.000 claims description 3
- 230000005865 ionizing radiation Effects 0.000 claims description 3
- 238000000354 decomposition reaction Methods 0.000 claims description 2
- 238000005259 measurement Methods 0.000 claims description 2
- 229920000098 polyolefin Polymers 0.000 claims description 2
- 239000004604 Blowing Agent Substances 0.000 claims 2
- 229920005992 thermoplastic resin Polymers 0.000 claims 2
- 239000012212 insulator Substances 0.000 description 5
- 239000006260 foam Substances 0.000 description 4
- 239000004088 foaming agent Substances 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 3
- 239000004020 conductor Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000002666 chemical blowing agent Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010894 electron beam technology Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Classifications
-
- 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
- B29C48/15—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor incorporating preformed parts or layers, e.g. extrusion moulding around inserts
- B29C48/154—Coating solid articles, i.e. non-hollow articles
-
- 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
- B29C48/92—Measuring, controlling or regulating
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92114—Dimensions
- B29C2948/92123—Diameter or circumference
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92438—Conveying, transporting or storage of articles
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92609—Dimensions
- B29C2948/92619—Diameter or circumference
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92933—Conveying, transporting or storage of articles
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Molding Of Porous Articles (AREA)
- Processes Specially Adapted For Manufacturing Cables (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、高発泡絶縁電線の発泡度を長手方向
において均一化せしめることができる改良された
製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an improved manufacturing method capable of making the degree of foaming of a highly foamed insulated wire uniform in the longitudinal direction.
[従来の技術と問題点]
コンピユータを頂点に、情報関連機器の高性能
化は日進月歩の趨勢にあり、高速化、高密度実装
化、あるいは雑音低減化など要求性能はますます
酷しくなりつつある。そして、これらに使われる
電線・ケーブル類にも高度の性能が要求されるよ
うになつた。[Conventional technology and problems] The performance of information-related equipment, with computers at its peak, is increasing rapidly, and performance requirements such as higher speeds, higher density packaging, and noise reduction are becoming increasingly severe. . Moreover, the electric wires and cables used in these applications are now required to have a high level of performance.
高発泡絶縁電線は、絶縁体の誘導率を低減せし
め、とくに高周波における伝送障害を解決するも
のとして、上記の情勢に適合すべく開発されたも
のであるが、このような所期目的に応えるために
は、発泡度を70〜80%と高くし、しかも全長に亘
り均等な発泡度を維持して長手方向に性能のバラ
ツキが生じないことが必要であり、上記要求特性
の高度化に伴い、この発泡のコントロールが主要
な課題となりつつある。 Highly foamed insulated wire was developed to meet the above situation by reducing the inductivity of the insulator and solving transmission problems, especially at high frequencies. In order to achieve this, it is necessary to increase the degree of foaming to 70-80%, and maintain a uniform degree of foaming over the entire length so that there is no variation in performance in the longitudinal direction.As the above-mentioned required characteristics become more sophisticated, Controlling this foaming is becoming a major issue.
従来、発泡絶縁電線を製造する一般的方法は、
絶縁材料中に熱分解型の化学発泡剤を混練した
り、揮発性発泡用液体を含浸させたり、あるいは
直接気泡形成用ガスを圧入したりして、これを高
圧の押出機より常圧の大気中に押出し被覆し、そ
の際の減圧効果に依存して発泡せしめるものであ
つた。しかし、このような方法では、大きな発泡
度を期待することができない上、その発泡度にバ
ラツキが生じ易く、全長に亘り均一な発泡度を維
持することは困難であつた。 Conventionally, the general method for manufacturing foam insulated wire is
A pyrolytic chemical blowing agent is kneaded into the insulating material, a volatile foaming liquid is impregnated into the insulation material, or a gas for forming bubbles is directly injected into the insulation material. The material was extruded and coated inside, and foaming was caused by the effect of reduced pressure at that time. However, with such a method, a large degree of foaming cannot be expected, and the degree of foaming tends to vary, making it difficult to maintain a uniform degree of foaming over the entire length.
そこで、発泡を押出機内と大気との上記圧力差
に依存せず、発泡剤として熱分解型の発泡剤を使
用し、これを押出被覆する際の押出温度を前記発
泡剤の分解温度以下にとどめておいて被覆し、そ
の後加熱炉内を通過させることにより発泡させる
方法がとられるようになり、これによつて発泡度
の格段の向上と均一化を図り得るようになつた。 Therefore, foaming does not depend on the above-mentioned pressure difference between the inside of the extruder and the atmosphere, and instead a pyrolyzable foaming agent is used as the foaming agent, and the extrusion temperature during extrusion coating is kept below the decomposition temperature of the foaming agent. A method of foaming by coating the foam in a heating furnace and then passing it through a heating furnace has become available, which has made it possible to significantly improve the degree of foaming and make it more uniform.
図は、そのような方法により高発泡絶縁電線を
製造している様子を示す説明図であり、1は発泡
前のコア、10は発泡後のコアである。図におい
て、未発泡の絶縁体が押出被覆された未発泡コア
1は加熱炉3内を通過せしめられることにより発
泡し、発泡コア10を得て引取機5により連続的
に引取られる。 The figure is an explanatory diagram showing how a highly foamed insulated wire is manufactured by such a method, and 1 is a core before foaming, and 10 is a core after foaming. In the figure, an unfoamed core 1 coated with an unfoamed insulator by extrusion is passed through a heating furnace 3 and foamed to obtain a foamed core 10, which is continuously taken off by a take-off machine 5.
この際、発泡度のバラツキをなくす手段とし
て、従来は加熱炉の温度と引取機5の引取り速度
を一定とし、可能な限り外径変動の少ない未発泡
コア1を供給する方法がとられてきた。しかし、
押出における条件の設定を各ロツト毎にすべて同
一条件に保持することは非常に困難であり、同一
ロツトにおいても変動が起り外径が変化すること
は、この種製造方法における宿命であつて、上記
外径のコントロールのみで発泡度のバラツキをコ
ントロールすることは不可能に近いことであつ
た。 At this time, as a means to eliminate variations in the degree of foaming, conventional methods have been used to keep the temperature of the heating furnace and the take-up speed of the take-off machine 5 constant, and to supply unfoamed cores 1 with as little variation in outer diameter as possible. Ta. but,
It is very difficult to maintain the same extrusion conditions for each lot, and it is the fate of this type of manufacturing method that variations occur even in the same lot, resulting in changes in the outer diameter. It was nearly impossible to control the variation in foaming degree only by controlling the outer diameter.
[発明の目的]
本発明は、上記したような実情にかんがみてな
されたものであり、加熱前の未発泡コア径に変動
があつても、発泡度については全長に亘り均一な
発泡を行なわせ得る高発泡絶縁電線の製造方法を
提供しようとするものである。[Object of the Invention] The present invention has been made in view of the above-mentioned circumstances, and it is an object of the present invention to achieve uniform foaming over the entire length even if the diameter of the unfoamed core before heating varies. The purpose of the present invention is to provide a method for producing highly foamed insulated wires.
[発明の概要]
すなわち、本発明の要旨とするところは、加熱
炉通過方式の発泡方法において、未発泡コアの外
径と発泡コアの外径をそれぞれ測定する測定機を
配置し、その外径測定結果を引取機の引取スピー
ドにフイードバツクし、当該引取スピードをコア
径の変動によりコントロール可能ならしめたこと
にあり、それにより発泡度のコントロールを可能
にして、つねに所望の均一な発泡度を有する発泡
絶縁電線を安定して製造可能ならしめたものであ
る。[Summary of the Invention] That is, the gist of the present invention is that in a heating furnace passage method foaming method, measuring machines are arranged to measure the outer diameter of an unfoamed core and the outer diameter of a foamed core, and the outer diameter of the foamed core is measured. The measurement results are fed back to the take-up speed of the take-up machine, and the take-up speed can be controlled by changing the core diameter. This makes it possible to control the foaming degree and always maintain the desired uniform foaming degree. This makes it possible to stably manufacture foam insulated wires.
[実施例]
以下に、本発明について実施例に基いて説明す
る。[Examples] The present invention will be described below based on Examples.
一定炉長で一定温度の加熱炉内に未発泡コアを
通過させ、所定の発泡度を得ようとすれば、外径
の大きいコアはゆつくりと通過させ外径の小さい
コアは速く通過させる必要があることは、理の通
りである。 If you want to pass an unfoamed core through a heating furnace at a constant temperature and a constant furnace length to obtain the desired degree of foaming, it is necessary to pass the core with a large outer diameter slowly and the core with a small outer diameter quickly. It is logical that there is.
従つて、外径を全長均一なものとなし得れば、
同一スピードで通過させることにより全長同一発
泡度の製品を得ることができる。これが前記従来
の知見に立つ発泡度コントロール法である。しか
し、この方法では、もしもなんらかの原因で未発
泡コアに外径変動が生じたとすれば、その変動に
応じて発泡度が変動してしまう結果となり、外径
のコントロールが前記した通り困難であることを
考慮すれば、つねに不安定要素を内包したコント
ロール法といわねばならず、今日の機器の発達か
ら電線特性への要求がますます酷しさを増しつつ
あるとき、問題は大きい。 Therefore, if the outer diameter can be made uniform over the entire length,
By passing at the same speed, a product with the same foaming degree over the entire length can be obtained. This is a foaming degree control method based on the above-mentioned conventional knowledge. However, with this method, if the outer diameter of the unfoamed core fluctuates for some reason, the degree of foaming will change accordingly, making it difficult to control the outer diameter as described above. Considering this, it must be said that the control method always includes unstable elements, and as the demands on wire characteristics become more and more severe due to the development of today's equipment, this becomes a serious problem.
いま、発泡前の絶縁体の断面積をAとし、導体
の径をd、そのときの未発泡コアの外径をD1と
すると、
A=π/4(D1 2−d2) ……(1)
となる。 Now, if the cross-sectional area of the insulator before foaming is A, the diameter of the conductor is d, and the outer diameter of the unfoamed core at that time is D1 , then A = π/4 (D 1 2 - d 2 )... (1) becomes.
つぎに、上記断面積Aなる絶縁体が発泡し、コ
アの外径が増大した発泡後のコアの外径をD2と
し、そのときの発泡度がx%であるとすると、簡
便法によりD2は(2)式によつて表わすことができ
る。 Next, if the insulator with the above cross-sectional area A is foamed and the outer diameter of the core after foaming is D2 , and the degree of foaming at that time is x%, D can be calculated by a simple method. 2 can be expressed by equation (2).
ここに、導体の径dは一定とみてよいから、所
望の発泡度x%は、(2)式よりしてD1とD2により
定まることがわかる。 Here, since the diameter d of the conductor can be considered constant, it can be seen from equation (2) that the desired degree of foaming x% is determined by D 1 and D 2 .
本発明においては、図に示すように加熱炉3通
過前に外径測定機2を設置しておいて、前記未発
泡コア1の外径D1を測定する。ついで、外径測
定機2よりコアの移動経路上の正確な長さLとな
るところであつて、かつ加熱炉3を通過した位置
に発泡コア10の外径D2を測定する外径測定機
4を設置しておく。 In the present invention, as shown in the figure, an outer diameter measuring device 2 is installed before passing through the heating furnace 3, and the outer diameter D1 of the unfoamed core 1 is measured. Next, an outer diameter measuring device 4 is used to measure the outer diameter D 2 of the foamed core 10 at a position on the movement path of the core that is the exact length L from the outer diameter measuring device 2 and has passed through the heating furnace 3. Set it up.
このように設置し、両測定機2および4のコア
移動経路上における離間長さLを予め定めておけ
ば、コアの同一位置における前記外径D1および
D2が自動的に測定され、それによつて前記(2)式
における所望の発泡度xが得られているか否かが
直ちにわかるから、もしそのような発泡度に直接
変動を与えるそれぞれの外径D1およびD2に変動
が生じたら、これをフイードバツクさせ、引取機
5の引取スピードをそれに見合つてコントロール
せしめるようにすれば、つねに一定の発泡度を保
持せしめることができ、全長に亘り均一な発泡度
を有する高発泡絶縁電線を入手することができ
る。 If installed in this way and the separation length L of both measuring instruments 2 and 4 on the core moving path is determined in advance, the outer diameter D 1 and
Since D 2 is automatically measured and it is immediately known whether the desired degree of foaming x in equation (2) above has been obtained, if the respective outer diameters that directly vary the degree of foaming If fluctuations occur in D 1 and D 2 , this can be fed back and the take-up speed of the take-up machine 5 can be controlled accordingly, making it possible to always maintain a constant degree of foaming and ensure uniform foaming over the entire length. Highly foamed insulated wires having a degree of foaming are available.
上記高発泡絶縁電線の絶縁体としては、ポリオ
レフインとりわけ誘電率が小さく発泡剤との配合
や押出加工が容易なポリエチレンが広く使用され
ているが、強度や耐熱性能に難があるところから
これを架橋する例が多い。この架橋手段には種々
あるが、一般に細物サイズであるこの種電線にと
つては、電子線の如き電離性放射線を照射する方
法を用いるのが好ましい。すなわち、未発泡のコ
アの押出し後、電離性放射線照射装置を通過させ
て架橋し、そのまま加熱炉に通過させて発泡させ
ることにより、一つの工程において高発泡架橋絶
縁電線を容易に入手することができるのである。 As the insulator for the above-mentioned highly foamed insulated wire, polyolefin, especially polyethylene, which has a low dielectric constant and is easy to mix with foaming agents and extrude, is widely used, but it is difficult to crosslink because of its strength and heat resistance. There are many examples of this. Although there are various crosslinking methods, it is preferable to use a method of irradiating ionizing radiation such as an electron beam for this kind of electric wire, which is generally thin in size. That is, after extruding an unfoamed core, it is passed through an ionizing radiation irradiation device to be crosslinked, and then passed through a heating furnace to be foamed, thereby making it possible to easily obtain a highly foamed crosslinked insulated wire in one step. It can be done.
なお、発泡度の連続測定法として、キヤパシタ
ンスを連続して測定する方法も考えられるが、1
ロツトが10Kmにも及ぶ長尺体となるこの種電線の
場合、電線のアースがとれたにしても、測定機か
らの距離に変化が生ずるから、正確な値を得るこ
とができず、その意味で本発明に係る方法はまこ
とにすぐれた方法ということができる。 In addition, as a method for continuously measuring the degree of foaming, a method of continuously measuring capacitance can also be considered, but 1.
In the case of this type of electric wire, which is a long piece with a length of 10 km, even if the wire is grounded, the distance from the measuring device changes, making it impossible to obtain accurate values. Therefore, the method according to the present invention can be said to be a truly excellent method.
[発明の効果]
以上の通り、本発明に係る方法によれば、発泡
度の変動が2%以下、静電容量において
±1.5pF/m以下といつた、外観のきれいな均
一発泡特性を有する高発泡絶縁電線を入手可能な
らしめるものであり、その工業的価値は非常に大
きなものがある。[Effects of the Invention] As described above, according to the method according to the present invention, a highly uniform foaming product with a beautiful appearance and uniform foaming characteristics, such as a fluctuation in foaming degree of 2% or less and a capacitance of ±1.5 pF/m or less, can be obtained. This makes it possible to obtain foam insulated wires, and its industrial value is extremely large.
図は本発明に係る製造方法の実施状況を示す説
明図である。
1……未発泡コア、2,4……コア外径測定
機、3……加熱炉、5……引取機、10……発泡
したコア。
The figure is an explanatory diagram showing the implementation status of the manufacturing method according to the present invention. 1... Unfoamed core, 2, 4... Core outer diameter measuring device, 3... Heating furnace, 5... Taking machine, 10... Foamed core.
Claims (1)
泡性組成物を、前記発泡剤の分解温度よりも低い
温度で押出被覆し、当該被覆線を加熱炉に通過せ
しめることにより発泡せしめる発泡絶縁電線の製
造方法において、前記加熱炉通過の前と後にそれ
ぞれ発泡前と発泡後のコアの外径を測定し得る外
径測定機を配置し、外径測定結果をフイードバツ
クして加熱炉通過の際のスピードをコントロール
し、発泡度を均一化せしめる高発泡絶縁電線の製
造方法。 2 発泡性組成物を押出被覆後、加熱炉通過前に
電離性放射線を照射して架橋せしめる特許請求の
範囲第1項記載の製造方法。 3 熱可塑性樹脂がポリオレフインである特許請
求の範囲第1または2項記載の製造方法。[Scope of Claims] 1. Extrusion coating of a foamable composition comprising a thermoplastic resin and a pyrolyzable blowing agent at a temperature lower than the decomposition temperature of the blowing agent, and passing the coated wire through a heating furnace. In the method for manufacturing a foamed insulated wire that is foamed by foaming, an outer diameter measuring machine capable of measuring the outer diameter of the core before and after foaming is placed before and after passing through the heating furnace, respectively, and the outer diameter measurement results are fed back. A method for producing highly foamed insulated wire that controls the speed of passage through a heating furnace and uniformizes the degree of foaming. 2. The manufacturing method according to claim 1, wherein the foamable composition is crosslinked by irradiation with ionizing radiation after extrusion coating and before passing through a heating furnace. 3. The manufacturing method according to claim 1 or 2, wherein the thermoplastic resin is polyolefin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62280178A JPH01122523A (en) | 1987-11-05 | 1987-11-05 | Manufacture of low density insulated electric wire |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62280178A JPH01122523A (en) | 1987-11-05 | 1987-11-05 | Manufacture of low density insulated electric wire |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01122523A JPH01122523A (en) | 1989-05-15 |
| JPH0533481B2 true JPH0533481B2 (en) | 1993-05-19 |
Family
ID=17621383
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62280178A Granted JPH01122523A (en) | 1987-11-05 | 1987-11-05 | Manufacture of low density insulated electric wire |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01122523A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2605248B2 (en) * | 1992-04-30 | 1997-04-30 | 豊田合成株式会社 | Extrusion control device of extruder |
-
1987
- 1987-11-05 JP JP62280178A patent/JPH01122523A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01122523A (en) | 1989-05-15 |
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