JP3126307B2 - Optical fiber resin coating method - Google Patents

Optical fiber resin coating method

Info

Publication number
JP3126307B2
JP3126307B2 JP08042324A JP4232496A JP3126307B2 JP 3126307 B2 JP3126307 B2 JP 3126307B2 JP 08042324 A JP08042324 A JP 08042324A JP 4232496 A JP4232496 A JP 4232496A JP 3126307 B2 JP3126307 B2 JP 3126307B2
Authority
JP
Japan
Prior art keywords
coating
optical fiber
resin
pressure
outer diameter
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
Application number
JP08042324A
Other languages
Japanese (ja)
Other versions
JPH09236732A (en
Inventor
真二 鈴木
秀夫 平沢
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.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP08042324A priority Critical patent/JP3126307B2/en
Publication of JPH09236732A publication Critical patent/JPH09236732A/en
Application granted granted Critical
Publication of JP3126307B2 publication Critical patent/JP3126307B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

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

【0001】[0001]

【発明の属する技術分野】本発明は光ファイバー表面に
樹脂被覆する際に光ファイバの被覆外径のばらつきを最
小限に抑え、さらに樹脂被覆中への気泡混入のない光フ
ァイバの樹脂被覆方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for coating an optical fiber with a resin, which minimizes variations in the outer diameter of the optical fiber when the resin is coated on the surface of the optical fiber, and which does not contain bubbles in the resin coating. It is.

【0002】[0002]

【従来の技術】被覆光ファイバは図4のようにして製造
されている。すなわち、線引炉12で加熱された光ファイ
バプリフォーム11から光ファイバ13が線引され、外径測
定機14で光ファイバの外径を測定した後、冷却管15で冷
却され、樹脂被覆装置16の加圧ダイス20で光ファイバに
液状の被覆樹脂を被覆し、偏心モニタ17を通り、被覆材
料をUV照射装置18で硬化させ、このようにして得られた
被覆光ファイバをキャプスタン21で引き取り、ドラムに
巻き取っている。光ファイバの外径はキャプスタン21の
引き取り速度により制御される。図3に光ファイバの樹
脂被覆装置の加圧ダイスを示す。加圧ダイスはホルダ27
の底部に円錐状のダイス22を配置し、その上方に円錐状
のニップル23が配置されて形成される。樹脂槽から樹脂
供給管を通して大気圧より高い圧力で圧送された樹脂
は、ホルダ中央部の樹脂供給孔24からダイス22とニップ
ル23間に形成される樹脂付着部25へ供給され、走行する
光ファイバ3に樹脂被覆され、被覆光ファイバは先端ノ
ズル26より出てくる。
2. Description of the Related Art A coated optical fiber is manufactured as shown in FIG. That is, the optical fiber 13 is drawn from the optical fiber preform 11 heated in the drawing furnace 12, the outer diameter of the optical fiber is measured by an outer diameter measuring device 14, then cooled by a cooling pipe 15, and the resin coating device is used. The optical fiber is coated with the liquid coating resin by the 16 pressing dies 20, the coating material is cured by the UV irradiation device 18 through the eccentricity monitor 17, and the coated optical fiber obtained in this manner is We take and take up on drum. The outer diameter of the optical fiber is controlled by the take-up speed of the capstan 21. FIG. 3 shows a pressure die of the optical fiber resin coating apparatus. Pressing die is holder 27
A conical die 22 is disposed at the bottom of the nipple, and a conical nipple 23 is disposed above the conical die 22. The resin pressure-fed from the resin tank through the resin supply pipe at a pressure higher than the atmospheric pressure is supplied from the resin supply hole 24 in the center of the holder to the resin attachment portion 25 formed between the die 22 and the nipple 23, and the traveling optical fiber 3 is coated with a resin, and the coated optical fiber emerges from the tip nozzle 26.

【0003】[0003]

【発明が解決しようとする課題】光ファイバの被覆外径
は裸光ファイバ径が変わらない場合は、被覆樹脂圧力、
被覆樹脂の保持温度、線引速度によって変化する。特に
被覆樹脂の粘度は、保持温度によって大幅に変化するた
め、所要温度に制御しておく必要がある。光ファイバの
被覆外径のばらつきはマイクロベンディング・ロスを増
加させるため、光ファイバの伝送損失を悪化させる。ま
た、線引条件、特に被覆樹脂圧力条件によっては樹脂被
覆中に気泡が混入してしまい、これもまた伝送損失を悪
化させる問題がある。本発明の目的は、上記のような問
題点に鑑み、光ファイバの被覆外径のばらつきを最小限
に抑え、かつ樹脂被覆中への気泡混入のない伝送特性の
すぐれた光ファイバの樹脂被覆方法を提供するものであ
る。
When the bare optical fiber diameter does not change, the coating outer diameter of the optical fiber is set to the coating resin pressure.
It changes depending on the holding temperature of the coating resin and the drawing speed. In particular, since the viscosity of the coating resin greatly changes depending on the holding temperature, it is necessary to control the viscosity to a required temperature. Variations in the outer diameter of the coating of the optical fiber increase the microbending loss, thereby worsening the transmission loss of the optical fiber. Also, depending on the drawing conditions, especially the pressure of the coating resin, air bubbles are mixed in the resin coating, which also has a problem that transmission loss is deteriorated. SUMMARY OF THE INVENTION An object of the present invention is to provide a resin coating method for an optical fiber having excellent transmission characteristics that minimizes variation in the coating outer diameter of the optical fiber and does not cause air bubbles to enter the resin coating in view of the above problems. Is provided.

【0004】[0004]

【課題を解決するための手段】本発明は、大気圧より高
い圧力の被覆樹脂が供給された加圧ダイス中を走行し,
先端ノズルから引出される光ファイバ表面に樹脂を被覆
する光ファイバの樹脂被覆方法において、光ファイバの
被覆外径が被覆樹脂圧力の0.6乗に比例し、被覆樹脂粘
度に逆比例し、線引速度の0.7乗に逆比例する関係に基
づいて、被覆樹脂圧力および/または被覆樹脂粘度を調
整することにより、光ファイバの被覆外径の制御を行な
うことを特徴とする光ファイバの樹脂被覆方法を要旨と
するものである。なお本発明においては、被覆樹脂圧
力はすべてゲージ圧(真の圧力から大気圧を引いた値)
で表すものとする。
SUMMARY OF THE INVENTION According to the present invention, there is provided a vehicle which travels in a pressing die supplied with a coating resin having a pressure higher than the atmospheric pressure .
Coating resin on optical fiber surface drawn from tip nozzle
In the resin coating process of optical fibers, the coating outer diameter of the optical fiber is proportional to 0.6 square of the coating resin pressure, inversely proportional to the coating resin viscosity, based on the inversely related to the 0.7 power of the drawing speed, the coating Adjust resin pressure and / or coating resin viscosity
The gist of the present invention is to provide a resin coating method for an optical fiber, wherein the outer diameter of the coating of the optical fiber is controlled by adjusting the diameter. In the present invention, all coating resin pressures are gauge pressures (true pressure minus atmospheric pressure).
In shall be I table.

【0005】[0005]

【発明の実施の形態】加圧ダイスを用いる光ファイバの
樹脂被覆方法において、光ファイバの被覆外径Dcを制御
する因子として、被覆樹脂圧力P、被覆樹脂粘度μ、線
引速度Vfが挙げられる。そこでこの3つ因子と光ファ
イバの被覆外径Dcの関係を調べたところ、光ファイバの
被覆外径Dc(μm)は被覆樹脂圧力P(kg/cm 2 の0.6
乗に比例し、被覆樹脂粘度μ(poise)に逆比例し、線
引速度Vf(m/min)の0.7乗に逆比例することを見いだ
した。そこで外径125μmの光ファイバについて被覆外
径DcとP0.6/μVf0.7の関係を調べたところ図2に示
す結果(図中点で示す)が得られ、これらの値より近
似線(実線で示す)を求め光ファイバの被覆外径Dcを算
出する式を求めたところ次に示す式(1)が得られた。 Dc=k(P0.6/μVf0.7)+C (k,Cは定数を表す)…(1) なお図2においてk,Cはそれぞれk=0.012、C=1
89であった。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In a resin coating method for an optical fiber using a pressing die, factors controlling the coating outer diameter Dc of the optical fiber include a coating resin pressure P, a coating resin viscosity μ, and a drawing speed Vf. . So it was examined a relationship between the coating outer diameter Dc of the three factors and the optical fiber, 0.6 of the coating outside diameter Dc of the optical fiber ([mu] m) of the coating resin pressure P (kg / cm 2)
It was found to be proportional to the power, inversely proportional to the coating resin viscosity μ (poise), and inversely proportional to the drawing speed Vf (m / min) to the 0.7th power. Then, when the relationship between the coating outer diameter Dc and P 0.6 / μVf 0.7 was examined for an optical fiber having an outer diameter of 125 μm, the results shown in FIG. 2 (indicated by dots in the figure) were obtained, and an approximate line (solid line) was obtained from these values. The following equation (1) was obtained when an equation for calculating the coating outer diameter Dc of the optical fiber was obtained. Dc = k (P 0.6 / μVf 0.7) + C (k, C represents a constant) ... (1) where, k, C each k = 0.012 in FIG. 2, C = 1
89.

【0006】式(1)の関係を用いれば、例えば被覆樹
脂の温度、あるいは線引速度の変化によって、被覆外径
が変動した場合、その温度における粘度、あるいは線引
速度の変化量に応じた被覆樹脂圧力を式(1)より計算
し、圧力調整を行うことで被覆外径を所定径に保持する
ことができる。実際の線引工程においては、光ファイバ
の被覆外径を外径測定機にて計測し、所定の被覆外径に
対する差分量を基に適正な被覆樹脂圧力を式(1)によ
り算出し、加圧力制御部によって被覆樹脂圧力を制御
し、被覆外径を所定の径に保持する。さらに式(1)に
より光ファイバの被覆外径の変動に対して、被覆樹脂粘
度や、あるいは被覆樹脂圧力と被覆樹脂粘度を調整する
ことで、被覆外径を所定の径に保持するよう制御する。
このようにして加圧ダイス内の被覆樹脂に加える圧力
を、式(1)を満たすように調整することにより、光フ
ァイバの線引速度が高速でも低速でも、また被覆樹脂の
温度が高くても低くても光ファイバに被覆する被覆径を
所定の径に制御できるので、本発明は光ファイバの線引
速度または被覆樹脂の粘度がどのような値であっても加
圧ダイス内に供給される被覆樹脂圧力を調整することに
より被覆光ファイバ外径を所定の径に保てる。
If the relationship of the formula (1) is used, for example, when the coating outer diameter fluctuates due to a change in the temperature of the coating resin or the drawing speed, it depends on the viscosity at that temperature or the amount of change in the drawing speed. The coating resin pressure is calculated from equation (1), and the coating outer diameter can be maintained at a predetermined value by adjusting the pressure. In the actual drawing step, the coating outer diameter of the optical fiber is measured by an outer diameter measuring device, and an appropriate coating resin pressure is calculated by equation (1) based on a difference amount with respect to a predetermined coating outer diameter. The coating resin pressure is controlled by the pressure control unit, and the coating outer diameter is maintained at a predetermined diameter. Further, by controlling the coating resin viscosity or the coating resin pressure and the coating resin viscosity with respect to the fluctuation of the coating outer diameter of the optical fiber according to the equation (1), the coating outer diameter is controlled to be maintained at a predetermined diameter. .
By adjusting the pressure applied to the coating resin in the pressing die so as to satisfy Equation (1) in this manner, even if the drawing speed of the optical fiber is high or low, or if the temperature of the coating resin is high, Since the coating diameter for coating the optical fiber can be controlled to a predetermined diameter even if it is low, the present invention is supplied into the pressure die regardless of the drawing speed of the optical fiber or the viscosity of the coating resin whatever the value. By adjusting the coating resin pressure, the outer diameter of the coated optical fiber can be maintained at a predetermined value.

【0007】本発明においては、被覆樹脂圧力を、被覆
樹脂圧力を低下させた際樹脂が枯渇状態になる圧力の1.
7 倍〜5倍の圧力とすれば、樹脂被覆中への気泡混入が
なくなるので、気泡の混入のない光ファイバが製造でき
る。被覆樹脂圧力が、樹脂が枯渇状態になる圧力の1.7
倍未満では樹脂被覆中への気泡混入の問題があり、樹脂
が枯渇状態になる圧力の5倍を超えると加圧ダイスのニ
ップル上部より被覆樹脂があふれ出す問題がある。
[0007] In the present invention, the coating resin pressure is set at 1.
If the pressure is 7 to 5 times, no air bubbles are mixed into the resin coating, so that an optical fiber free of air bubbles can be manufactured. The coating resin pressure is 1.7 times the pressure at which the resin is depleted.
If the pressure is less than twice, there is a problem of air bubbles in the resin coating. If the pressure exceeds five times the pressure at which the resin is depleted, the coating resin overflows from the upper portion of the nipple of the pressing die.

【0008】図1は本発明の実施態様の一例の線引装置
の構成図である。まず、光ファイバ母材1は電気炉2に
挿入され、加熱溶融されて光ファイバ3に線引される。
線引された光ファイバは冷却管5を通り樹脂被覆装置6
に挿入され、図3に示す内部が円錐状のダイス22と、そ
の下端部が細径の先端ノズル26を形成する加圧ダイス10
中を通り樹脂被覆され、樹脂被覆された光ファイバは偏
心モニタ7を通りUV照射装置8で硬化され、ドラム(図
示せず)にて巻き取られる。この時、光ファイバの外径
および光ファイバの被覆外径は、それぞれ光ファイバ外
径測定機4および被覆外径測定機9で測定される。ま
た、被覆樹脂温度、線引速度Vfがそれぞれ温度計測部、
線引速度計測部で計測される。ここで光ファイバの被覆
外径Dcの計測データは計算部へ送られ、また、このとき
同時に被覆樹脂の温度(被覆樹脂粘度μに変換され
る)、線引速度Vfの計測データも計算部へ送られ、光フ
ァイバの被覆外径Dcと設定した被覆径との差が、0にな
るような被覆樹脂圧力P を計算し、加圧力制御部にフィ
ードバックされる。この被覆光ファイバ径Dc、粘度μ、
線引速度Vfの計測データをもとに適正な被覆樹脂圧力が
計算され、加圧力制御部にて被覆樹脂圧力P が調整され
る。光ファイバの被覆外径が設定した径になれば、被覆
樹脂圧力は保持される。したがって、光ファイバの線引
速度が変動しても、またはコーティング材の温度(粘
度)が変動した場合でもそのときの線引速度、粘度に対
応して光ファイバの被覆外径が常に設定の径になるよう
に被覆樹脂圧力が調整される。
FIG. 1 is a configuration diagram of a drawing apparatus according to an embodiment of the present invention. First, the optical fiber preform 1 is inserted into an electric furnace 2, heated and melted, and drawn into an optical fiber 3.
The drawn optical fiber passes through a cooling pipe 5 and a resin coating device 6.
3 and a press die 10 having a conical inside as shown in FIG.
The resin-coated optical fiber passing through the inside is cured by an UV irradiation device 8 through an eccentricity monitor 7 and wound up by a drum (not shown). At this time, the outer diameter of the optical fiber and the outer diameter of the coating of the optical fiber are measured by the optical fiber outer diameter measuring device 4 and the coating outer diameter measuring device 9, respectively. In addition, the coating resin temperature and the drawing speed Vf are respectively the temperature measurement unit,
It is measured by the drawing speed measuring unit. Here, the measurement data of the coating outer diameter Dc of the optical fiber is sent to the calculation unit, and at the same time, the measurement data of the coating resin temperature (converted to coating resin viscosity μ) and the drawing speed Vf are also sent to the calculation unit. The coating resin pressure P is calculated so that the difference between the coating outer diameter Dc of the optical fiber and the set coating diameter becomes zero, and is fed back to the pressing force controller. This coated optical fiber diameter Dc, viscosity μ,
An appropriate coating resin pressure is calculated based on the measurement data of the drawing speed Vf, and the coating resin pressure P is adjusted by the pressing force control unit. When the coating outer diameter of the optical fiber reaches the set diameter, the coating resin pressure is maintained. Therefore, even if the drawing speed of the optical fiber fluctuates or the temperature (viscosity) of the coating material fluctuates, the coating outer diameter of the optical fiber always corresponds to the drawing speed and viscosity at that time. The coating resin pressure is adjusted so that

【0009】[0009]

【実施例】【Example】

実施例 図1の線引き装置を用い、図3の加圧ダイスの先端ノズ
ル径を0.25mmとして、被覆樹脂としてアクリル・ウレタ
ン系UV硬化樹脂を用いて粘度を15ポイズ(40℃)に設定
し線引速度120m/ 分で被覆線引を行った。被覆樹脂圧力
は、被覆樹脂圧力を低下させた際の樹脂が枯渇状態にな
る圧力0.3kg/cm2 の1.7 倍の0.5kg/cm2のゲージ圧に設
定して行った。なおこのとき光ファイバの外径を125 μ
m 、被覆外径を200 μm に設定し、式(1)により被覆
樹脂圧力を制御して10km線引を行った。得られた被覆光
ファイバの被覆外径のばらつきは±0.24μm であり、伝
送損失も0.34dB/km (波長1.3 μm )、0.20dB/km (波
長1.55μm )と極めて良好な値となり、また樹脂被覆中
には気泡の混入が全く確認されなかった。なお比較例と
して、図4の従来法による線引き装置を用いて線引速度
100m/ 分で10km線引を行ったところ、被覆外径のばらつ
きは±1.0 μm であった。
Example Using the drawing apparatus shown in FIG. 1, the pressure nozzle of FIG. 3 was made to have a tip nozzle diameter of 0.25 mm, and an acrylic / urethane UV curing resin was used as a coating resin, and the viscosity was set to 15 poise (40 ° C.). The coated wire was drawn at a drawing speed of 120 m / min. Coating resin pressure was performed by setting 1.7 times the 0.5 kg / cm 2 gauge pressure in the pressure 0.3 kg / cm 2 where the resin at the time of lowering the coating resin pressure becomes depleted. At this time, the outer diameter of the optical fiber was 125 μ
m, the outer diameter of the coating was set to 200 μm, and the pressure of the coating resin was controlled by equation (1) to draw 10 km. The dispersion of the outer diameter of the obtained coated optical fiber is ± 0.24 μm, and the transmission loss is 0.34 dB / km (wavelength 1.3 μm) and 0.20 dB / km (wavelength 1.55 μm), which are extremely good values. No air bubbles were mixed during the coating. As a comparative example, the drawing speed was determined using the conventional drawing apparatus shown in FIG.
When a 10 km line was drawn at 100 m / min, the variation in coating outer diameter was ± 1.0 μm.

【0010】[0010]

【発明の効果】本発明によれば、被覆光ファイバ外径が
常に一定の値になるように調整するために、線引速度や
粘度の変動による被覆径のばらつきを最小限に押さえる
ことが出来るので、光ファイバの被覆外径のばらつきに
起因するマイクロベンディングロスがなく気泡の混入の
ない高品質な被覆光ファイバを製造することができる。
According to the present invention, since the outer diameter of the coated optical fiber is always adjusted to a constant value, variations in the coated diameter due to fluctuations in drawing speed and viscosity can be minimized. Therefore, it is possible to manufacture a high-quality coated optical fiber having no microbending loss due to the variation in the coating outer diameter of the optical fiber and free of bubbles.

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

【図1】本発明による線引装置の構成図。FIG. 1 is a configuration diagram of a drawing apparatus according to the present invention.

【図2】本発明における、光ファイバの外径125 μm に
おける、被覆外径と被覆樹脂圧力・被覆樹脂粘度・線引
速度の関係を示す図。
FIG. 2 is a diagram showing the relationship between coating outer diameter, coating resin pressure, coating resin viscosity, and drawing speed at an optical fiber outer diameter of 125 μm in the present invention.

【図3】加圧ダイスの説明図。FIG. 3 is an explanatory view of a pressing die.

【図4】従来法による線引装置の構成図。FIG. 4 is a configuration diagram of a drawing apparatus according to a conventional method.

【符号の説明】[Explanation of symbols]

1、11…光ファイバ母材 2、12…電気炉 3、13…光ファイバ 4、14…光ファイバ外径測定機 5、15…冷却管 6、16…樹脂被覆装置 7、17…偏心モニタ 8、18…UV照射装置 9、19…被覆外径測定機 10、20…加圧ダイス 21…キャプスタン 22…ダイス 23…ニップル 24…樹脂供給孔 25…樹脂付着部 26…先端ノズル 27…ホルダ 1, 11: Optical fiber preform 2, 12, Electric furnace 3, 13, Optical fiber 4, 14, Optical fiber outer diameter measuring device 5, 15, Cooling pipe 6, 16, Resin coating device 7, 17 ... Eccentric monitor 8 , 18… UV irradiation device 9,19… Coating outer diameter measuring machine 10,20… Pressure die 21… Capstan 22… Die 23… Nipple 24… Resin supply hole 25… Resin adhesion part 26… Tip nozzle 27… Holder

フロントページの続き (56)参考文献 特開 昭59−131417(JP,A) 実開 平2−51218(JP,U) (58)調査した分野(Int.Cl.7,DB名) G02B 6/00 - 6/54 Continuation of the front page (56) References JP-A-59-131417 (JP, A) JP-A-2-51218 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) G02B 6 / 00-6/54

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 大気圧より高い圧力の被覆樹脂が供給さ
れた加圧ダイス中を走行し、先端ノズルから引出される
光ファイバ表面に樹脂を被覆する光ファイバの樹脂被覆
方法において、光ファイバの被覆外径が被覆樹脂圧力の
0.6乗に比例し、被覆樹脂粘度に逆比例し、線引速度の
0.7乗に逆比例する関係に基づいて、被覆樹脂圧力およ
び/または被覆樹脂粘度を調整することにより、光ファ
イバの被覆外径の制御を行なうことを特徴とする光ファ
イバの樹脂被覆方法。
1. A vehicle travels in a pressure die to which a coating resin having a pressure higher than the atmospheric pressure is supplied, and is drawn out from a tip nozzle.
In a resin coating method for an optical fiber in which a resin is coated on the surface of an optical fiber, the outer diameter of the coating of the optical fiber is determined by the pressure of the coating resin.
It is proportional to the 0.6 power, inversely proportional to the coating resin viscosity,
Based on the relationship inversely proportional to the power of 0.7 , the coating resin pressure and
And / or adjusting the coating resin viscosity to control the coating outer diameter of the optical fiber.
【請求項2】 被覆樹脂圧力P(kg/cm 2 、光ファイ
バの線引速度Vf(m/min.)、被覆樹脂の粘度μ(pois
e)について、光ファイバの被覆外径Dc(μm)が(1)
式、 Dc=k(P0.6/μVf0.7)+C (k,Cは定数を表す)…(1) の関係を満足するように線引速度Vfと被覆樹脂粘度μの
変動に対応して、常に光ファイバの被覆外径を所定の径
に保持するよう被覆樹脂圧力Pおよび/または被覆樹脂
粘度μを制御する請求項1に記載の光ファイバの樹脂被
覆方法。
2. Coating resin pressure P (kg / cm 2 ) , optical fiber drawing speed Vf (m / min.) , Coating resin viscosity μ (pois
For e) , the coating outer diameter Dc (μm ) of the optical fiber is (1)
Formula: Dc = k (P 0.6 / μVf 0.7 ) + C (k and C represent constants) (1) In order to satisfy the relationship, the drawing speed Vf and the variation of the coating resin viscosity μ are always satisfied. 2. The resin coating method for an optical fiber according to claim 1, wherein the coating resin pressure P and / or the coating resin viscosity μ are controlled so that the coating outer diameter of the optical fiber is maintained at a predetermined diameter.
【請求項3】 被覆樹脂圧力を、被覆樹脂圧力を低下さ
せ樹脂が枯渇状態になるときの圧力の1.7倍〜5倍の圧
力とする請求項1または2に記載の光ファイバの樹脂被
覆方法。
3. The optical fiber resin coating method according to claim 1, wherein the coating resin pressure is 1.7 to 5 times the pressure when the coating resin pressure is reduced and the resin is depleted.
JP08042324A 1996-02-29 1996-02-29 Optical fiber resin coating method Expired - Fee Related JP3126307B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08042324A JP3126307B2 (en) 1996-02-29 1996-02-29 Optical fiber resin coating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08042324A JP3126307B2 (en) 1996-02-29 1996-02-29 Optical fiber resin coating method

Publications (2)

Publication Number Publication Date
JPH09236732A JPH09236732A (en) 1997-09-09
JP3126307B2 true JP3126307B2 (en) 2001-01-22

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ID=12632838

Family Applications (1)

Application Number Title Priority Date Filing Date
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JP (1) JP3126307B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100702293B1 (en) * 2005-06-03 2007-03-30 엘에스전선 주식회사 Method of coating and drawing optical fiber for preventing badness loss
DK2146233T3 (en) * 2007-05-08 2020-12-07 Furukawa Electric Co Ltd Process for the production of optical fiber and plants for the production of optical fiber

Also Published As

Publication number Publication date
JPH09236732A (en) 1997-09-09

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