JP5170038B2 - Optical fiber drawing method - Google Patents

Optical fiber drawing method Download PDF

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JP5170038B2
JP5170038B2 JP2009196873A JP2009196873A JP5170038B2 JP 5170038 B2 JP5170038 B2 JP 5170038B2 JP 2009196873 A JP2009196873 A JP 2009196873A JP 2009196873 A JP2009196873 A JP 2009196873A JP 5170038 B2 JP5170038 B2 JP 5170038B2
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optical fiber
furnace
drawing furnace
inert gas
fiber preform
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JP2011046563A (en
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徹 山田
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Sumitomo Electric Industries Ltd
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    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B37/00Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
    • C03B37/01Manufacture of glass fibres or filaments
    • C03B37/02Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor
    • C03B37/025Manufacture 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
    • C03B37/027Fibres composed of different sorts of glass, e.g. glass optical fibres
    • C03B37/02736Means for supporting, rotating or feeding the tubes, rods, fibres or filaments to be drawn, e.g. fibre draw towers, preform alignment, butt-joining preforms or dummy parts during feeding
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B37/00Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
    • C03B37/01Manufacture of glass fibres or filaments
    • C03B37/02Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor
    • C03B37/025Manufacture 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
    • C03B37/029Furnaces therefor
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2205/00Fibre drawing or extruding details
    • C03B2205/60Optical fibre draw furnaces
    • C03B2205/80Means for sealing the preform entry or upper end of the furnace

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  • Chemical & Material Sciences (AREA)
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  • Manufacture, Treatment Of Glass Fibers (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for drawing an optical fiber by which a high-quality optical fiber can be obtained by suppressing the variation in outside diameter, and the cost is reduced by decreasing the consumption of an inert gas. <P>SOLUTION: An optical fiber drawing furnace 10 includes: a drawing furnace 11 housing an optical fiber preform 1 to be freely movable vertically; a plurality of partition plates 12-16 movable along a dummy rod 26 in the drawing furnace 11; a heater 17 for heating the optical fiber preform 1; a gas supply means 18 for supplying the inert gas into the drawing furnace 11; and a furnace internal pressure measuring instrument 20 for measuring the internal pressure of the drawing furnace 11. The quantity of the inert gas to be supplied by a gas supply means 18 is gradually reduced with the reduction of the volume in the drawing furnace 11 by being partitioned by the partition plates 12-16 by a control means 21 so that the pressure of the drawing furnace 11 is kept constant according to the measured value by the furnace internal pressure measuring instrument 20. <P>COPYRIGHT: (C)2011,JPO&amp;INPIT

Description

本発明は、光ファイバ母材を加熱溶融させながら光ファイバを線引きする光ファイバの線引方法に関する。   The present invention relates to an optical fiber drawing method for drawing an optical fiber while heating and melting an optical fiber preform.

従来の光ファイバの線引方法の一例として、線引炉内圧を検出する圧力検出手段と、圧力が所定値になるように線引炉内に導入する不活性ガス流量を制御する制御手段を備えた線引装置が提案されている(例えば、特許文献1参照)。   As an example of a conventional optical fiber drawing method, a pressure detection means for detecting the drawing furnace internal pressure and a control means for controlling the flow rate of the inert gas introduced into the drawing furnace so that the pressure becomes a predetermined value are provided. A drawing apparatus has been proposed (see, for example, Patent Document 1).

また、従来の光ファイバの線引方法の別の例として、上下に昇降可能な光ファイバ母材取付用のダミー棒と、ダミー棒に取り付けられた光ファイバ母材の下端を加熱するヒータと、ダミー棒に沿って摺動可能な複数枚の仕切板を備えた光ファイバ線引炉が提案されている(例えば、特許文献2参照)。   Also, as another example of a conventional optical fiber drawing method, a dummy rod for attaching an optical fiber preform that can be moved up and down, a heater that heats the lower end of the optical fiber preform attached to the dummy rod, An optical fiber drawing furnace provided with a plurality of partition plates slidable along a dummy rod has been proposed (see, for example, Patent Document 2).

上記特許文献2に開示された光ファイバの線引方法では、光ファイバ母材であるプリフォームを線引きするにつれてプリフォームの残長が減少することに伴い、炉内の容積に変動を生じて炉内圧力が変動することを防止するために、炉内を段階的に仕切る複数枚の仕切板が設けられている。   In the optical fiber drawing method disclosed in Patent Document 2 described above, the remaining length of the preform decreases as the preform, which is the optical fiber preform, is drawn. In order to prevent the internal pressure from fluctuating, a plurality of partition plates for partitioning the inside of the furnace in stages are provided.

特開昭62−226834号公報JP-A-62-226834 特開2002−68773号公報JP 2002-68773 A

しかしながら、上記特許文献1に開示された従来の光ファイバ線引装置では、炉内圧力が一定になるように制御してはいるものの、フィードバック制御であるため、大きく容積の変わるような状況で制御を素早く追従させるのは難しく、時間遅れが生じていた。このため、制御が追い着かず、炉内の気流が乱れて、線引きされる光ファイバの外径に許容範囲を超える外径変動を発生させる場合があった。また、結果的に過剰な不活性ガスを供給していた場合があった。   However, the conventional optical fiber drawing apparatus disclosed in Patent Document 1 is controlled so that the pressure in the furnace is constant, but is feedback control, so control is performed in a situation where the volume changes greatly. It was difficult to make it follow quickly, causing a time delay. For this reason, the control could not catch up, the airflow in the furnace was disturbed, and the outer diameter of the optical fiber to be drawn sometimes caused an outer diameter fluctuation exceeding the allowable range. As a result, excessive inert gas may have been supplied.

また、上記特許文献2に開示された従来の光ファイバの線引方法では、炉内へのパージガスの供給量が一定であるので、炉内圧力を一定に保持することは難しく、炉内で圧力変動が生じ、線引きされる光ファイバの外径に許容範囲を超える外径変動を発生させる場合があった。また、所定量の不活性ガスを常時供給するため、過剰な不活性ガスを供給していた場合があった。
通常、ガラス径の変動は、中心値に対して0.1μm以下の変動幅であるが、炉内の気流が乱れた場合、0.5μm以上の変動幅となってしまう。
Further, in the conventional optical fiber drawing method disclosed in Patent Document 2, since the supply amount of purge gas into the furnace is constant, it is difficult to keep the furnace pressure constant. In some cases, fluctuations have occurred and the outer diameter of the optical fiber to be drawn has an outer diameter fluctuation that exceeds an allowable range. In addition, since a predetermined amount of inert gas is constantly supplied, excessive inert gas may be supplied.
Usually, the fluctuation of the glass diameter is a fluctuation width of 0.1 μm or less with respect to the center value, but when the airflow in the furnace is disturbed, the fluctuation width is 0.5 μm or more.

本発明の目的は、上述した事情に鑑みてなされたものであり、外径変動を抑制して高品質な光ファイバを得ることができるとともに、不活性ガスの使用量を低減することによりコスト削減を図ることができる光ファイバの線引方法を提供することにある。   The object of the present invention has been made in view of the above-described circumstances, and can reduce the cost by reducing the amount of inert gas used while suppressing fluctuations in the outer diameter to obtain a high-quality optical fiber. An object of the present invention is to provide an optical fiber drawing method capable of achieving the above.

上記課題を解決することができる本発明に係る光ファイバの線引方法は、線引炉内に光ファイバ母材と光ファイバ母材取付け用ダミー棒とを上下に昇降自在に収容し、前記線引炉の上部空間内を前記ダミー棒に沿って摺動可能な複数の仕切板により仕切りながら前記光ファイバ母材を加熱し、前記線引炉内に不活性ガスを供給して前記光ファイバ母材の下端から光ファイバを線引きする光ファイバの線引方法であって、前記線引炉内の圧力を一定に保つように、前記仕切板によって仕切られることによる前記線引炉内容積の減少に従い、線引き開始からの時間経過に応じて予め格納されているテーブルに基づいて、徐々に前記不活性ガスの供給量を減少させることを特徴としている。 An optical fiber drawing method according to the present invention that can solve the above-described problem is that an optical fiber preform and a dummy rod for attaching an optical fiber preform are accommodated in a draw furnace so as to be movable up and down. The optical fiber preform is heated while being partitioned by a plurality of partition plates slidable along the dummy rod in the upper space of the draw furnace, and an inert gas is supplied into the draw furnace to supply the optical fiber preform. An optical fiber drawing method for drawing an optical fiber from a lower end of a material, wherein the drawing furnace volume is reduced by being partitioned by the partition plate so as to keep the pressure in the drawing furnace constant. The supply amount of the inert gas is gradually decreased based on a table stored in advance with the passage of time from the start of drawing .

このように構成された光ファイバの線引方法によれば、線引炉内の圧力を一定に保つように、前記仕切板によって仕切られることによる前記線引炉内容積の減少に従い、線引き開始からの時間経過に応じて予め格納されているテーブルに基づいて、徐々に不活性ガスの供給量を減少させる。これにより、線引中に炉内の熱による対流によって炉内の気流が乱れることはなく、外径変動を抑制した高品質な光ファイバを製造することができる。また、線引炉内の容積の減少に従い、不活性ガスの供給量を減少させるので、不活性ガスの供給量を節約することができ、コスト削減を図ることができる。
According to the optical fiber drawing method configured in this way, from the start of drawing according to the decrease in the drawing furnace volume by being partitioned by the partition plate so as to keep the pressure in the drawing furnace constant. The supply amount of the inert gas is gradually reduced based on a table stored in advance as time elapses . Thereby, the airflow in the furnace is not disturbed by convection due to the heat in the furnace during drawing, and a high-quality optical fiber that suppresses fluctuations in the outer diameter can be manufactured. Further, since the supply amount of the inert gas is reduced according to the decrease in the volume in the drawing furnace, the supply amount of the inert gas can be saved, and the cost can be reduced.

本発明に係る光ファイバの線引方法によれば、外径変動を抑制して高品質な光ファイバを得ることができるとともに、不活性ガスの使用量を低減することによりコスト削減を図ることができる。   According to the method for drawing an optical fiber according to the present invention, it is possible to obtain a high-quality optical fiber by suppressing fluctuations in the outer diameter, and to reduce costs by reducing the amount of inert gas used. it can.

本発明に係る一実施形態の光ファイバの線引方法を適用された光ファイバ線引炉の縦断面図である。1 is a longitudinal sectional view of an optical fiber drawing furnace to which an optical fiber drawing method according to an embodiment of the present invention is applied.

以下、本発明の一実施形態に係る光ファイバの線引方法について図面を参照して説明する。   Hereinafter, an optical fiber drawing method according to an embodiment of the present invention will be described with reference to the drawings.

図1に示すように、本発明の一実施形態である光ファイバの線引方法を適用した光ファイバ線引炉10は、光ファイバ母材1から光ファイバ2を線引きするもので、光ファイバ母材1を上下に昇降自在に収容した線引炉11と、線引炉11内を後述するダミー棒26に沿って移動可能な複数の仕切板12,13,14,15,16を備えている。
また、光ファイバ線引炉10は、光ファイバ母材1を加熱する主ヒータ17と、線引炉11内に不活性ガス(例えば、He等)を供給するガス供給手段18と、線引炉11の内圧を測定する炉内圧測定器20と、炉内圧に基づいて不活性ガスの供給量を制御する制御手段21を備えている。
As shown in FIG. 1, an optical fiber drawing furnace 10 to which an optical fiber drawing method according to an embodiment of the present invention is applied draws an optical fiber 2 from an optical fiber preform 1. A drawing furnace 11 that accommodates the material 1 so as to be movable up and down, and a plurality of partition plates 12, 13, 14, 15, and 16 that can move in the drawing furnace 11 along a dummy rod 26 described later. .
The optical fiber drawing furnace 10 includes a main heater 17 for heating the optical fiber preform 1, a gas supply means 18 for supplying an inert gas (for example, He) into the drawing furnace 11, and a drawing furnace. And a control means 21 for controlling the supply amount of the inert gas based on the furnace pressure.

線引炉11は、その上部を蓋部材22により閉塞された外筒管23と、外筒管23の下側に配設された炉心管24と、炉心管24の下側に配設された炉心管下方延長部25を備えている。外筒管23は、蓋部材22の中央部にダミー棒26を挿通している。
ダミー棒26は、連結部材27を介して光ファイバ母材1を組み付けている。仕切板12,13,14,15,16は、ダミー棒26に挿通されて連結部材27の上部に配置されている。
The drawing furnace 11 has an outer tube 23 whose upper portion is closed by a cover member 22, a core tube 24 disposed below the outer tube 23, and a lower portion of the core tube 24. A core tube lower extension 25 is provided. The outer tube 23 has a dummy rod 26 inserted through the center of the lid member 22.
The dummy rod 26 is assembled with the optical fiber preform 1 via the connecting member 27. The partition plates 12, 13, 14, 15, and 16 are inserted into the dummy bar 26 and disposed on the upper portion of the connecting member 27.

光ファイバ2の線引きが進行して光ファイバ母材1が短くなった際に、光ファイバ部材1がダミー棒26とともに下降する。これに伴って、仕切板12,13,14,15,16は、外筒管23の内周部の上下に所定間隔を保って形成された段部28,29,30,31,32に段階的に係合される。   When the drawing of the optical fiber 2 proceeds and the optical fiber preform 1 is shortened, the optical fiber member 1 is lowered together with the dummy rod 26. Accordingly, the partition plates 12, 13, 14, 15, 16 are stepped into step portions 28, 29, 30, 31, 32 formed at predetermined intervals above and below the inner peripheral portion of the outer tube 23. Engaged.

複数の仕切板12,13,14,15,16を配置することで、外筒管23内の炉内空間容積を略一定にしている。これにより、外筒管23内の上下方向での温度差による対流の発生を抑止して、光ファイバ2の外径変動を抑制している。   By arranging the plurality of partition plates 12, 13, 14, 15, 16, the furnace space volume in the outer tube 23 is made substantially constant. Thereby, generation | occurrence | production of the convection by the temperature difference in the up-down direction in the outer cylinder pipe 23 is suppressed, and the outer-diameter fluctuation | variation of the optical fiber 2 is suppressed.

主ヒータ17は、炉芯管24の外側に組み付けられている。
なお、外筒管23の最上部に補助ヒータ33を組み付けている。補助ヒータ33は、光ファイバ母材1の下端部を加熱溶融させるための主ヒータ17とは違い、線引炉11内の気流の安定化をより一層図るために配設されている。
The main heater 17 is assembled to the outside of the furnace core tube 24.
An auxiliary heater 33 is assembled on the uppermost part of the outer tube 23. Unlike the main heater 17 for heating and melting the lower end portion of the optical fiber preform 1, the auxiliary heater 33 is disposed to further stabilize the airflow in the drawing furnace 11.

ガス供給手段18は、外筒管23に連通接続されている。ガス供給手段18は、線引中の主ヒータ17による加熱に伴う炉心管24の酸化劣化を抑制するための不活性ガスを線引炉11内に供給する。ガス供給手段18は、制御手段21によって不活性ガスの供給量が制御されている。   The gas supply means 18 is connected in communication with the outer tube 23. The gas supply means 18 supplies an inert gas into the drawing furnace 11 for suppressing oxidation deterioration of the furnace core tube 24 due to heating by the main heater 17 during drawing. In the gas supply means 18, the supply amount of the inert gas is controlled by the control means 21.

炉内圧測定器20は、圧力変動の少ない炉心管下方延長部25の下端部近傍に取り付けられている。炉内圧測定器20は、炉内圧を所定の時間間隔で測定して、その測定情報を制御手段21に送る。なお、炉内圧測定器20の取り付け位置は、炉心管下方延長部25の上端部に取り付けられても良い。   The in-furnace pressure measuring device 20 is attached in the vicinity of the lower end portion of the core tube lower extension 25 with little pressure fluctuation. The in-furnace pressure measuring device 20 measures the in-furnace pressure at predetermined time intervals and sends the measurement information to the control means 21. It should be noted that the attachment position of the furnace pressure measuring device 20 may be attached to the upper end portion of the core tube lower extension 25.

制御手段21は、不図示の演算回路等を内蔵した電子部品を備えている。制御手段21は、線引き開始からの時間経過に応じ、予め格納されているテーブルに基づいて不活性ガスの供給量を決定する。前記テーブルは、炉内圧測定器20の炉内圧の測定値を用いて補正され、次回の線引き時の流量制御に反映される。そして、ガス供給手段18が決定された供給量の不活性ガスを供給する。   The control means 21 includes an electronic component with a built-in arithmetic circuit (not shown). The control means 21 determines the supply amount of the inert gas based on a prestored table as time elapses from the start of drawing. The table is corrected by using the measured value of the furnace pressure of the furnace pressure measuring device 20, and is reflected in the flow rate control at the next drawing. The gas supply means 18 supplies the determined supply amount of inert gas.

次に、光ファイバ線引炉10を用いた光ファイバの線引方法について説明する。   Next, an optical fiber drawing method using the optical fiber drawing furnace 10 will be described.

先ず、ダミー棒26の下端に連結部材27を介して光ファイバ母材1を取り付け、光ファイバ母材1の下端を主ヒータ17で加熱溶融させる。そして、加熱溶融されている光ファイバ母材1の下端から光ファイバ2を線引きする。光ファイバ母材1は、光ファイバ2の線引きが進むと短くなるのでダミー棒26を下降させて光ファイバ母材1の下端が主ヒータ17によって常に加熱されるようにする。   First, the optical fiber preform 1 is attached to the lower end of the dummy rod 26 via the connecting member 27, and the lower end of the optical fiber preform 1 is heated and melted by the main heater 17. And the optical fiber 2 is drawn from the lower end of the optical fiber preform 1 heated and melted. Since the optical fiber preform 1 becomes shorter as the drawing of the optical fiber 2 progresses, the dummy rod 26 is lowered so that the lower end of the optical fiber preform 1 is always heated by the main heater 17.

主ヒータ17による加熱溶融が始まると、制御手段21は、線引き開始からの時間経過に応じて予め格納されているテーブルに基づいて、不活性ガスの供給量を決定する。そして、ガス供給手段18が決定された所定量の不活性ガスを供給する。   When heating and melting by the main heater 17 starts, the control means 21 determines the supply amount of the inert gas based on a table stored in advance as time elapses from the start of drawing. And the gas supply means 18 supplies the determined predetermined amount of inert gas.

このとき、外筒管23内の炉内空間容積を略一定にするように、仕切板12,13,14,15,16によって、炉内空間は段階的に仕切られる。この線引炉11内の容積の減少に伴って、不活性ガスの供給量を徐々に減少させる。これにより、線引中に炉内の熱による対流によって炉内の気流が乱れることはなく、線引きされる光ファイバ2の外径変動を抑制することができる。   At this time, the furnace space is partitioned in stages by the partition plates 12, 13, 14, 15, and 16 so that the furnace space volume in the outer tube 23 is substantially constant. As the volume in the drawing furnace 11 decreases, the supply amount of the inert gas is gradually decreased. Thereby, the airflow in a furnace is not disturbed by the convection by the heat in a furnace during drawing, and the outer diameter fluctuation | variation of the optical fiber 2 drawn can be suppressed.

次に、本発明に係る光ファイバの線引方法の作用効果を確認するために行った実施例について説明する。   Next, an example carried out to confirm the operation and effect of the optical fiber drawing method according to the present invention will be described.

本発明に係る光ファイバの線引方法により光ファイバの線引を行った。
実施例では、Heガスを徐々に減らしながら線引を行い、線引開始から1時間間隔でガラス外径(変動)を線引炉下の外径測定器により測定した。また、この時の炉内圧力を測定した。一方、従来の線引方法である比較例では、Heガスを一定量供給しながら炉内圧力とガラス外径(変動)を同様な方法で測定した。その結果を表1に示す。なお、Heガスは、実施例、比較例とも線引開始時の流量を100(l/分)とし、変化量は、線引開始時の初期流量からの差分Δで表している。
The optical fiber was drawn by the optical fiber drawing method according to the present invention.
In the examples, drawing was performed while gradually reducing the He gas, and the glass outer diameter (fluctuation) was measured at an interval of 1 hour from the start of drawing with an outer diameter measuring device under the drawing furnace. Further, the pressure in the furnace at this time was measured. On the other hand, in the comparative example which is a conventional drawing method, the furnace pressure and the glass outer diameter (variation) were measured by the same method while supplying a certain amount of He gas. The results are shown in Table 1. In the He gas, the flow rate at the start of drawing is 100 (l / min) in both the examples and the comparative examples, and the amount of change is represented by a difference Δ from the initial flow rate at the start of drawing.

Figure 0005170038
Figure 0005170038

表1に示すように、He流量を徐々に減らした実施例では、炉内圧は略一定となり、ガラス外径の変動が小さいことがわかる。一方、Heガスの供給量を一定にした従来例では、線引きが進むにつれて炉内圧が徐々に高くなり、それにつれてガラス外径の変動も大きくなっていることがわかる。   As shown in Table 1, it can be seen that in the example in which the He flow rate was gradually reduced, the furnace pressure was substantially constant, and the fluctuation of the glass outer diameter was small. On the other hand, in the conventional example in which the supply amount of He gas is constant, it can be seen that the furnace pressure gradually increases as the drawing progresses, and the fluctuation of the glass outer diameter increases accordingly.

なお、本発明は、上述した実施形態に限定されるものではなく、適宜、変形、改良等が自在である。その他、上述した実施形態における各構成要素の材質、形状、寸法、数値、形態、数、配置場所、等は本発明を達成できるものであれば任意であり、限定されない。   In addition, this invention is not limited to embodiment mentioned above, A deformation | transformation, improvement, etc. are possible suitably. In addition, the material, shape, dimension, numerical value, form, number, arrangement location, and the like of each component in the above-described embodiment are arbitrary and are not limited as long as the present invention can be achieved.

1 光ファイバ母材
2 光ファイバ
10 光ファイバ線引炉
11 線引炉
12〜16 仕切板
17 ヒータ
18 ガス供給手段
20 炉内圧測定器
21 制御手段
DESCRIPTION OF SYMBOLS 1 Optical fiber base material 2 Optical fiber 10 Optical fiber drawing furnace 11 Drawing furnace 12-16 Partition plate 17 Heater 18 Gas supply means 20 Furnace pressure measuring instrument 21 Control means

Claims (1)

線引炉内に光ファイバ母材と光ファイバ母材取付け用ダミー棒とを上下に昇降自在に収容し、前記線引炉の上部空間内を前記ダミー棒に沿って摺動可能な複数の仕切板により仕切りながら前記光ファイバ母材を加熱し、前記線引炉内に不活性ガスを供給して前記光ファイバ母材の下端から光ファイバを線引きする光ファイバの線引方法であって、
前記線引炉内の圧力を一定に保つように、前記仕切板によって仕切られることによる前記線引炉内容積の減少に従い、線引き開始からの時間経過に応じて予め格納されているテーブルに基づいて、徐々に前記不活性ガスの供給量を減少させることを特徴とする光ファイバの線引方法。
An optical fiber preform and an optical fiber preform mounting dummy rod are accommodated in the drawing furnace so as to be movable up and down, and a plurality of partitions are slidable along the dummy rod in the upper space of the drawing furnace. Heating the optical fiber preform while partitioning by a plate, supplying an inert gas into the drawing furnace, and drawing an optical fiber from a lower end of the optical fiber preform,
Based on a table stored in advance as time elapses from the start of drawing, according to a decrease in the volume of the drawing furnace by being partitioned by the partition plate so as to keep the pressure in the drawing furnace constant. , line引方technique of the fiber, characterized in that to gradually decrease the supply amount of the inert gas.
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