JP2547764B2 - Optical fiber manufacturing method - Google Patents
Optical fiber manufacturing methodInfo
- Publication number
- JP2547764B2 JP2547764B2 JP62083065A JP8306587A JP2547764B2 JP 2547764 B2 JP2547764 B2 JP 2547764B2 JP 62083065 A JP62083065 A JP 62083065A JP 8306587 A JP8306587 A JP 8306587A JP 2547764 B2 JP2547764 B2 JP 2547764B2
- Authority
- JP
- Japan
- Prior art keywords
- fiber
- liquid
- optical fiber
- tubular cooling
- gas
- 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 - Fee Related
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/02—Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor
- C03B37/025—Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor from reheated softened tubes, rods, fibres or filaments, e.g. drawing fibres from preforms
- C03B37/027—Fibres composed of different sorts of glass, e.g. glass optical fibres
- C03B37/02718—Thermal treatment of the fibre during the drawing process, e.g. cooling
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2205/00—Fibre drawing or extruding details
- C03B2205/50—Cooling the drawn fibre using liquid coolant prior to coating, e.g. indirect cooling via cooling jacket
- C03B2205/51—Cooling the drawn fibre using liquid coolant prior to coating, e.g. indirect cooling via cooling jacket using liquified or cryogenic gas
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2205/00—Fibre drawing or extruding details
- C03B2205/50—Cooling the drawn fibre using liquid coolant prior to coating, e.g. indirect cooling via cooling jacket
- C03B2205/52—Cooling the drawn fibre using liquid coolant prior to coating, e.g. indirect cooling via cooling jacket by direct contact with liquid coolant, e.g. as spray, mist
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Surface Treatment Of Glass Fibres Or Filaments (AREA)
- Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 この発明は光フアイバの製造方法に関し、更に詳述す
れば光フアイバ用母材(以下、単に「母材」という)を
加熱溶融して、母材先端から一定の張力で線引きして得
られたフアイバ(以下、「線引きフアイバ」という)の
表面に樹脂被覆して光フアイバに仕上げる光フアイバの
製造方法の改良に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a method for producing an optical fiber, more specifically, by heating and melting an optical fiber base material (hereinafter simply referred to as “base material”), The present invention relates to an improvement in a method for producing an optical fiber by coating the surface of a fiber (hereinafter, referred to as "drawn fiber") obtained by drawing from the tip of a base material with a constant tension to form an optical fiber by coating with a resin.
通常、光フアイバの製造は次のようにして行つてい
る。すなわち、第2図に示すように予め別途作製の母材
1を、加熱炉2内の炉心管3内に送り出し、加熱溶融し
た母材1先端から一定の張力で線引きし、得られた線引
きフアイバ4を、線引き過程中の自然放熱で冷却させな
がら、樹脂液を入れたコーテイングダイス5中を通過さ
せ、線引きフアイバ4の表面に樹脂液を被覆させた後、
炉15で焼き固め、得られた光フアイバ7をドラム8に巻
き取るようにしていた。Usually, the optical fiber is manufactured as follows. That is, as shown in FIG. 2, a separately prepared base material 1 is sent into a furnace core tube 3 in a heating furnace 2 and drawn from the tip of the heated and melted base material 1 with a constant tension to obtain a drawn fiber. 4 is passed through a coating die 5 containing a resin solution while being cooled by natural heat dissipation during the drawing process to coat the surface of the drawing fiber 4 with the resin solution.
The optical fiber 7 obtained by baking in a furnace 15 was wound around a drum 8.
このように、光フアイバ7を製造するときに、線引き
フアイバ4の表面に樹脂被覆する理由は、次の通りであ
る。The reason why the surface of the wire drawing fiber 4 is coated with the resin when the optical fiber 7 is manufactured is as follows.
すなわち、線引きフアイバ4の径は100〜150μm程度
のガラス繊維であるから極めて弱く、100g前後の引張荷
重で容易に破断する。That is, since the diameter of the drawn fiber 4 is glass fiber having a diameter of about 100 to 150 μm, it is extremely weak and easily broken by a tensile load of about 100 g.
また、材質がガラスであるから金属とは異なりぜい性
破壊をおこし、フアイバ表面についた小さな傷でも成長
し破壊の原因となる。Further, since the material is glass, unlike metal, it causes brittle fracture, and even small scratches on the fiber surface grow and cause fracture.
それ故に、線引きフアイバ表面を樹脂被覆して、引張
り強度や曲げ強度を向上させる方法が採用されている。Therefore, a method of coating the surface of the drawing fiber with a resin to improve the tensile strength and the bending strength is adopted.
一方、光フアイバ製造の生産性を高めるためには、フ
アイバの線引き速度を早くする必要がある。ところが、
線引きフアイバの表面に紫外線硬化性樹脂等の合成樹脂
を被覆するときは、その線引きフアイバは加熱溶融した
母材から線引きしたものであるから、線引き過程におい
て、熱放散して冷却されるといつても、未だ十分冷却さ
れない場合があり、そのような状態でコーテイングダイ
ス5中を通すと、コーテイング層は線引きフアイバの熱
的影響を受け、線引きフアイバ周囲の樹脂粘度が低下し
すぎてコーテイング層の寸法が安定しない問題が生じ
る。On the other hand, in order to increase the productivity of optical fiber manufacturing, it is necessary to increase the fiber drawing speed. However,
When coating the surface of the drawing fiber with a synthetic resin such as an ultraviolet curable resin, the drawing fiber is drawn from the heated and melted base material, so when the drawing fiber dissipates heat and cools down. However, when it is passed through the coating die 5 in such a state, the coating layer is thermally affected by the drawing fiber, and the resin viscosity around the drawing fiber is excessively reduced, and the dimension of the coating layer is decreased. Will be unstable.
このような不具合を解消するため、従来は特公昭54−
39496号公報に示されるように加熱溶融した母材から線
引きした直後のフアイバ表面にガスを吹き付け、フアイ
バを冷却するようにしていた。これを第3図に示すが、
同図中の6は冷却用ガスをあらわし、その他の第2図と
共通する符号は第2図と同じを意味する。In order to eliminate such a problem, the conventional Japanese Patent Publication Sho 54-
As described in Japanese Patent No. 39496, a gas is blown onto the fiber surface immediately after drawing from the heated and melted base material to cool the fiber. This is shown in FIG.
Reference numeral 6 in the figure represents a cooling gas, and the other reference numerals common to those in FIG. 2 mean the same as those in FIG.
ところで、生産性向上のためにフアイバの線引き速度
を大にすればする程、同じ装置では、同距離でより短時
間により大きな熱量を奪つて冷却せねばならない。上記
公報に提案されるガス吹きつけによる冷却では、ガス流
量をより大にする又はガスの温度をより低くすることが
考えられるが、ガス温度を低くするといつても限度があ
り、またフアイバを冷却すればガス温度はだんだん上つ
ていくので線引速度増大に追随した冷却を行なうにはガ
ス流量を大きくする方法しかない。しかしながらガス流
量を大きくするとフアイバの線ブレの問題が起こつてく
る。By the way, as the fiber drawing speed is increased in order to improve the productivity, the same apparatus has to take a larger amount of heat in the same distance in a shorter time and cool it. In the cooling by spraying gas proposed in the above publication, it is possible to increase the gas flow rate or lower the temperature of the gas, but there is always a limit when the gas temperature is lowered, and the fiber is cooled. If this is done, the gas temperature will gradually rise, and therefore there is only a way to increase the gas flow rate in order to perform cooling that follows the increase in the drawing speed. However, when the gas flow rate is increased, the problem of fiber line blurring occurs.
また冷却される時間又は距離を延長して奪う熱量を大
きくしようとすると、装置の高さを高くすることにな
り、装置コストが増大してしまい、生産性向上の目的に
は好ましくない。Further, if it is attempted to increase the amount of heat to be taken by extending the cooling time or distance, the height of the device is increased and the device cost is increased, which is not preferable for the purpose of improving productivity.
本発明はこのような現状に鑑みてなされたものであつ
て、線引速度を増大しても上記のような困難を解消し
て、線ブレなく効果的に又装置コストも低廉に充分な冷
却が可能で高品質の光フアイバを製造できる方法を提供
することを目的とする。The present invention has been made in view of the above circumstances, and even if the drawing speed is increased, the above-mentioned difficulties are solved, effectively without line blurring, and at a low device cost, sufficient cooling is achieved. It is an object of the present invention to provide a method capable of producing a high-quality optical fiber that can be manufactured.
本発明は、加熱源により加熱溶融された光フアイバ母
材先端から一定の張力でフアイバを線引きすると共に線
引きされたフアイバの表面に樹脂被覆を施して光フアイ
バを形成させる方法において、上記加熱源を出た後で樹
脂被覆前のフアイバを管状冷却部内を通過させつつ該管
状冷却部の上部液溜めより該管状冷却部内に室温より低
い温度域に沸点を有する液体を落下させて、該液体の蒸
発ガス又は該液体の蒸発熱により該管状冷却部内を冷却
することによりフアイバ表面を冷却することを特徴とす
る光フアイバの製造方法を提供するものである。The present invention is a method of forming an optical fiber by applying a resin coating on the surface of the drawn fiber with a constant tension from the fiber end of the optical fiber base material heated and melted by a heating source, and forming the optical fiber in the method. After passing through the tubular cooling section after passing through the resin-coated fiber, a liquid having a boiling point in a temperature range lower than room temperature is dropped into the tubular cooling section from the upper liquid reservoir of the tubular cooling section to evaporate the liquid. The present invention provides a method for producing an optical fiber, characterized in that the inside of the tubular cooling part is cooled by the heat of vaporization of the gas or the liquid to cool the fiber surface.
本発明のさらに好ましい実施態様としては、該管状冷
却部上部液溜め中の液体から蒸発した気体を加熱源を出
た後で樹脂被覆前の光フアイバに吹きつけて行なう上記
方法が挙げられる。また室温より低い温度域に沸点を有
する液体として液体窒素又は液体アルゴンを用いること
が特に好ましい。As a further preferred embodiment of the present invention, there is mentioned the above method in which the gas evaporated from the liquid in the liquid reservoir in the upper portion of the tubular cooling unit is blown onto the optical fiber before resin coating after leaving the heating source. Further, it is particularly preferable to use liquid nitrogen or liquid argon as the liquid having a boiling point in a temperature range lower than room temperature.
以下図面を参照して本発明を詳細に説明する。第1図
は本発明の実施例を説明する概略構成図であつて、同図
中1〜5,7,8及び15は第2図、第3図と同じを意味す
る。9は室温より低い温度域に沸点を有する液体であ
り、10は該液体9の補給タンクであつて補給パイプ11、
バルブ12を介して管状冷却部13内の上部液溜め17に通じ
ている。なおタンク10、パイプ11、バルブ12は保温材14
によつて保温されている。光フアイバの軸方向に延在す
る管状冷却部13の上端にはガス吹出口18が設けられてお
り、管状冷却部13内の中空部分がフアイバ冷却部16であ
り、その下端には液受け部19が設けられている。該管状
冷却部13の上下端及び上部液溜め17底面の中央部分には
線引きフアイバ4の通過用穴があけてあり、上部液溜め
17のフアイバ冷却部16側の底面には細かい孔を設けてあ
る。また管状冷却部の下部近くには液通過用穴21が設け
てあり、20はオーバーフロー受け、24は液抜きである。Hereinafter, the present invention will be described in detail with reference to the drawings. FIG. 1 is a schematic configuration diagram for explaining an embodiment of the present invention, in which 1 to 5, 7, 8, and 15 mean the same as in FIGS. 2 and 3. 9 is a liquid having a boiling point in a temperature range lower than room temperature, 10 is a replenishment tank for the liquid 9, and a replenishment pipe 11,
It communicates with the upper liquid reservoir 17 in the tubular cooling section 13 via the valve 12. The tank 10, pipe 11 and valve 12 are
It is kept warm by. A gas outlet 18 is provided at the upper end of the tubular cooling portion 13 extending in the axial direction of the optical fiber, the hollow portion inside the tubular cooling portion 13 is the fiber cooling portion 16, and the liquid receiving portion is at the lower end thereof. 19 are provided. The upper and lower ends of the tubular cooling section 13 and the central portion of the bottom surface of the upper liquid reservoir 17 are provided with passage holes for the drawing fiber 4.
A fine hole is provided on the bottom surface of the fiber cooling unit 16 side of 17. Further, a liquid passage hole 21 is provided near the lower portion of the tubular cooling unit, 20 is an overflow receiving member, and 24 is a liquid removing member.
本発明によつて光フアイバを製造するには母材1は加
熱炉2で加熱された炉心管3内に送り出され、炉心管3
内で加熱溶融された母材1の先端に一定の張力を加えて
軸方向に線引きし、フアイバ4を引き出す。In order to manufacture an optical fiber according to the present invention, the base material 1 is sent into the furnace core tube 3 heated in the heating furnace 2, and the core tube 3
A constant tension is applied to the front end of the base material 1 which is heated and melted inside to draw in the axial direction, and the fiber 4 is drawn out.
このようにして引き出された線引きフアイバ4は、コ
ーテイングダイス5に送入される前に、まず管状冷却部
13を通過する。該管状冷却部13内では、タンク10より上
部液溜め17に供給された液体9が細孔を通つてフアイバ
冷却部16へと落下してくるが、落下途中で蒸発すること
により冷たいガスを発生し、又その蒸発熱により該フア
イバ冷却部16内を冷却する。線引きフアイバ4はこの冷
えたフアイバ冷却部16内を通過することにより冷却され
る。このとき、上部液溜め17においても液体9の蒸発が
起るので図示の方法のように上部液溜め17にガス吹出口
18を設けておくと、線引きフアイバ4は管状冷却部13に
入る手前でも冷却されるという効果が得られる。液体9
が液受け部19に到達する以前に全て蒸発するようにタン
ク10からの補給量をバルブ12で調整するが、安全のため
蒸発しきれなかつた液体9を液受け部19にて捕集し、さ
らに集めた液体9が液受け部19から溢れてダイス5に入
るのを防ぐために、液通過用穴21からオーバーフロー受
けに入るようにしておく。また管状冷却部13は冷やされ
るので、凝縮した空気中の水分がダイス5に落ちるのを
防ぐために、断熱材22をはさんでフランジパイプ23を取
り付けておくことが好ましい。また管状冷却部13の外面
は保温又は2重構造にするなどして冷却したほうがより
効果的であり好ましい。The wire drawing fiber 4 thus drawn out is first fed into the coating die 5 before being fed into the tubular cooling part.
Pass thirteen. In the tubular cooling section 13, the liquid 9 supplied from the tank 10 to the upper liquid reservoir 17 passes through the pores and drops into the fiber cooling section 16, but vaporizes during the drop to generate a cold gas. In addition, the inside of the fiber cooling unit 16 is cooled by the heat of vaporization. The wire drawing fiber 4 is cooled by passing through the inside of the cooled fiber cooling section 16. At this time, the liquid 9 evaporates also in the upper liquid reservoir 17, so that a gas outlet is provided in the upper liquid reservoir 17 as shown in the figure.
The provision of 18 has the effect that the drawing fiber 4 is cooled even before it enters the tubular cooling section 13. Liquid 9
The amount of replenishment from the tank 10 is adjusted by the valve 12 so that all of the liquid 9 evaporates before reaching the liquid receiving portion 19. Further, in order to prevent the collected liquid 9 from overflowing the liquid receiving portion 19 and entering the die 5, the liquid receiving hole 21 is made to enter the overflow receiving portion. Further, since the tubular cooling section 13 is cooled, it is preferable to attach the flange pipe 23 with the heat insulating material 22 interposed therebetween in order to prevent the condensed water in the air from falling into the die 5. Further, it is more effective and preferable to cool the outer surface of the tubular cooling section 13 by keeping it warm or by forming a double structure.
本発明における沸点が室温より低い温度域にある液体
としては、例えば液体窒素(沸点−195.82℃)、液体ア
ルゴン(沸点−185.87℃)等を用いることができる。As the liquid having a boiling point in the temperature range lower than room temperature in the present invention, for example, liquid nitrogen (boiling point −195.82 ° C.), liquid argon (boiling point −185.87 ° C.) and the like can be used.
このように、本発明においては従来法のようにガスを
流すことはなく、しかも連続的にフアイバを冷却する目
的で、室温より低い温度域に沸点を持つ液体を管状冷却
部内で連続的に蒸発させることにより、冷たいガスを発
生させまたその蒸発熱で管状冷却部内のガスを冷やし
て、この冷たいガスにより線引きフアイバをその周囲か
ら冷却する。つまり熱い線引きフアイバと管状冷却部内
の周囲のガスの間で熱交換を行わせるわけである。その
周囲ガスは液体の冷たい蒸気でフアイバにより暖められ
るが、その熱を液体を蒸発させることにより奪い、常に
冷たい状態に保つことができる。これによつてガスを流
すのと同様に線引きフアイバの冷却が可能で、しかもガ
ス流れによる線ブレの心配はなく、装置の大型化なしに
連続的かつ高速な冷却ができる。As described above, in the present invention, unlike the conventional method, gas is not passed, and for the purpose of continuously cooling the fiber, a liquid having a boiling point in a temperature range lower than room temperature is continuously evaporated in the tubular cooling section. By doing so, cold gas is generated and the heat of vaporization cools the gas in the tubular cooling section, and the cold gas cools the wire drawing fiber from its surroundings. In other words, heat is exchanged between the hot drawing fiber and the surrounding gas in the tubular cooling section. The ambient gas is warmed by the fiber with the cold vapor of the liquid, but its heat is taken away by evaporating the liquid and can always be kept cold. As a result, the wire drawing fiber can be cooled in the same manner as gas is flowed, and there is no concern about line blurring due to gas flow, and continuous and high-speed cooling can be performed without increasing the size of the device.
以上の説明から明らかなように、本発明の光フアイバ
の製造方法によれば、 加熱溶融した母材から線引きしたフアイバを従来の
光フアイバの製造方法の場合よりも、冷却効果を大幅に
向上できるだけでなく、フアイバの線引き速度を上げて
も、線ブレを起こすことなく冷却を十分に行うことがで
きるから光フアイバの生産効率を大幅に向上させること
ができる。As is clear from the above description, according to the method for manufacturing an optical fiber of the present invention, the fiber drawn from the heated and melted base material can greatly improve the cooling effect as compared with the case of the conventional method for manufacturing an optical fiber. Not only that, even if the fiber drawing speed is increased, sufficient cooling can be performed without causing line blurring, so that the production efficiency of the optical fiber can be significantly improved.
さらに、使用する飽和温度の低い液体から発生した
ガスを、線引きフアイバの通過路中に充満させるから、
フアイバ周囲の雰囲気を清浄に保持でき、作製される光
フアイバの表面に傷がなく強度の高い光フアイバを作る
ことができる。Furthermore, since the gas generated from the liquid with a low saturation temperature used is filled in the passage of the drawing fiber,
The atmosphere around the fiber can be kept clean, and the optical fiber to be produced has no damage on the surface thereof and can be made to have high strength.
第1図は本発明の実施例を説明する概略構成図である。 第2図及び第3図は従来法とその改良例を説明する概略
構成図である。FIG. 1 is a schematic configuration diagram illustrating an embodiment of the present invention. 2 and 3 are schematic configuration diagrams illustrating a conventional method and an improved example thereof.
Claims (3)
材先端から一定の張力でフアイバを線引きすると共に線
引きされたフアイバの表面に樹脂被覆を施して光フアイ
バを形成させる方法において、上記加熱源を出た後で樹
脂被覆前のフアイバを管状冷却部内を通過させつつ該管
状冷却部の上部液溜めより該管状冷却部内に室温より低
い温度域に沸点を有する液体を落下させて、該液体の蒸
発ガス又は該液体の蒸発熱により該管状冷却部内を冷却
することによりフアイバ表面を冷却することを特徴とす
る光フアイバの製造方法。1. A method for forming an optical fiber by drawing a fiber from the tip of an optical fiber base material heated and melted by a heating source with a constant tension and applying a resin coating on the surface of the drawn fiber to form an optical fiber. After passing through the inside of the tubular cooling part, the liquid having a boiling point in a temperature range lower than room temperature is dropped into the tubular cooling part from the upper liquid reservoir of the tubular cooling part while passing the fiber before resin coating through the tubular cooling part. A method for producing an optical fiber, characterized in that the fiber surface is cooled by cooling the inside of the tubular cooling section with the heat of vaporization of the vaporized gas or the liquid.
した気体を加熱源を出た後で樹脂被覆前のフアイバに吹
きつけて行なう特許請求の範囲第1項に記載の光フアイ
バの製造方法。2. The optical fiber according to claim 1, wherein the gas evaporated from the liquid in the liquid reservoir in the upper portion of the tubular cooling section is blown onto the fiber before resin coating after leaving the heating source. Production method.
して液体窒素又は液体アルゴンを用いる特許請求の範囲
第1項又は第2項に記載される光フアイバの製造方法。3. The method for producing an optical fiber according to claim 1 or 2, wherein liquid nitrogen or liquid argon is used as the liquid having a boiling point in a temperature range lower than room temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62083065A JP2547764B2 (en) | 1987-04-06 | 1987-04-06 | Optical fiber manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62083065A JP2547764B2 (en) | 1987-04-06 | 1987-04-06 | Optical fiber manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63248742A JPS63248742A (en) | 1988-10-17 |
| JP2547764B2 true JP2547764B2 (en) | 1996-10-23 |
Family
ID=13791779
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62083065A Expired - Fee Related JP2547764B2 (en) | 1987-04-06 | 1987-04-06 | Optical fiber manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2547764B2 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2618424B2 (en) * | 1988-03-02 | 1997-06-11 | 古河電気工業株式会社 | Manufacturing method of optical fiber core |
| US5043001A (en) * | 1990-05-29 | 1991-08-27 | Corning Incorporated | Method and apparatus for fiber cooling |
| DE19644350A1 (en) * | 1996-10-25 | 1998-04-30 | Alsthom Cge Alcatel | Method and device for producing an optical glass fiber |
| CN107311446B (en) * | 2017-06-28 | 2023-08-04 | 江东科技有限公司 | An optical fiber drawing cooling device |
| CN108002697B (en) * | 2017-11-30 | 2020-04-14 | 长飞光纤光缆股份有限公司 | Spray type cooling device and method for online cooling of optical fiber |
| CN108793726B (en) * | 2018-06-20 | 2019-07-30 | 江苏永鼎光纤科技有限公司 | A kind of optical fiber cooling apparatus and cooling method is carried out to optical fiber |
| CN115818984B (en) * | 2022-12-30 | 2024-09-10 | 长飞光纤光缆股份有限公司 | Evaporation natural cooling type solidifying equipment |
-
1987
- 1987-04-06 JP JP62083065A patent/JP2547764B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63248742A (en) | 1988-10-17 |
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