JPS62226834A - Optical fiber drawing device - Google Patents
Optical fiber drawing deviceInfo
- Publication number
- JPS62226834A JPS62226834A JP6853486A JP6853486A JPS62226834A JP S62226834 A JPS62226834 A JP S62226834A JP 6853486 A JP6853486 A JP 6853486A JP 6853486 A JP6853486 A JP 6853486A JP S62226834 A JPS62226834 A JP S62226834A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- core tube
- optical fiber
- preform
- 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.)
- Pending
Links
- 239000013307 optical fiber Substances 0.000 title claims abstract description 21
- 238000012681 fiber drawing Methods 0.000 title claims description 8
- 239000007789 gas Substances 0.000 claims abstract description 26
- 239000011261 inert gas Substances 0.000 claims abstract description 16
- 238000001514 detection method Methods 0.000 claims description 7
- 238000005491 wire drawing Methods 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 2
- 230000008018 melting Effects 0.000 abstract 1
- 238000002844 melting Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000005452 bending Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
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
- C03B37/029—Furnaces therefor
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2205/00—Fibre drawing or extruding details
- C03B2205/60—Optical fibre draw furnaces
- C03B2205/90—Manipulating the gas flow through the furnace other than by use of upper or lower seals, e.g. by modification of the core tube shape or by using baffles
- C03B2205/91—Manipulating the gas flow through the furnace other than by use of upper or lower seals, e.g. by modification of the core tube shape or by using baffles by controlling the furnace gas flow rate into or out of the furnace
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は光ファイバ線引装置に係り、特に線引炉の内圧
を安定化する制御装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an optical fiber drawing device, and particularly to a control device for stabilizing the internal pressure of a drawing furnace.
[従来の技術]
従来の光ファイバ線引装置の溝成を第3図に示す。線引
炉31内に設置された炉心管32の内部にプリフォーム
33を挿入し、炉心管32の外周部に位置するヒータ3
4により炉心管32内を加熱しながらプリフォーム33
を線引きして光ファイバ35を得ていた。このとき、プ
リフォーム33を安定して溶融線引きするためにガス吹
き出し器36及び37から炉心管32内にAr等の不活
性ガスを導入していた。[Prior Art] FIG. 3 shows the groove configuration of a conventional optical fiber drawing device. A preform 33 is inserted into a furnace core tube 32 installed in a drawing furnace 31, and a heater 3 is placed on the outer periphery of the furnace core tube 32.
4, the preform 33 is heated while heating the inside of the furnace tube 32.
The optical fiber 35 was obtained by drawing. At this time, in order to stably melt and draw the preform 33, an inert gas such as Ar was introduced into the furnace tube 32 from gas blowers 36 and 37.
[発明が解決しようとする問題点1
しかしながら、炉心管32内を流れる不活性ガス流は種
々の要因によって変動しやすく、イの結果炉心管32の
内圧も変動して線引きにより1!?られた光ファイバ3
5の外径が不均一となるという問題点を生じていた。[Problem to be Solved by the Invention 1] However, the inert gas flow flowing inside the reactor core tube 32 tends to fluctuate due to various factors, and as a result of (a), the internal pressure of the reactor core tube 32 also fluctuates, resulting in 1! ? optical fiber 3
A problem has arisen in that the outer diameter of the tube 5 is non-uniform.
不活性ガス流の変動の要因としては、■ヒータ34を作
動させる供給電流の変動やヒータ3/Iの劣化による炉
心管32内の温度変動、■プリフォーム33の曲がりや
その表面上の凹凸、■不活性ガス供給圧力の変動等が挙
げられる。The causes of fluctuations in the inert gas flow include: (1) temperature fluctuations in the core tube 32 due to fluctuations in the supply current that operates the heater 34 and deterioration of the heater 3/I; (2) bending of the preform 33 and irregularities on its surface; ■Changes in inert gas supply pressure, etc.
かくして本゛発明の目的は上記従来技術の問題f+(を
解澗し、光ファイバ外径の均一化を図ることのできる光
ファイバ線引装置を提供することにある。SUMMARY OF THE INVENTION It is therefore an object of the present invention to provide an optical fiber drawing apparatus that can solve the problem f+ (of the prior art described above) and make the outer diameter of the optical fiber uniform.
[問題点を解決するための手段]
本発明の光フン・イバ線引装置は上記目的を達成するた
めに、線引炉の内圧を検出する圧力検出手段と、この圧
力検出手段で検出された内圧が所定の圧力値となるよう
にこれら両者の差分をとり、この差分に基づいて線引炉
内に導入する不活性ガスの流山を制御する制御手段とを
設けたものである。[Means for Solving the Problems] In order to achieve the above-mentioned object, the optical furnace/iva wire drawing apparatus of the present invention includes a pressure detection means for detecting the internal pressure of the drawing furnace, and a pressure detection means for detecting the internal pressure of the drawing furnace. A control means is provided for calculating the difference between the two so that the internal pressure becomes a predetermined pressure value, and controlling the flow rate of the inert gas introduced into the drawing furnace based on this difference.
[作 用1
以上のような構成とすることにより、線引炉の内圧が圧
力検出手段で検出され、この内圧と所定の圧力値(設定
値)との差分に基づいて制御手段により線引炉内に導入
する不活性ガス流qが制御される。その結果、不活性ガ
ス流の変動が抑制され、プリフォームが安定して溶融線
引きされるので、外径の均一な光ファイバを得ることが
できる。[Operation 1] With the above configuration, the internal pressure of the drawing furnace is detected by the pressure detection means, and the drawing furnace is controlled by the control means based on the difference between this internal pressure and a predetermined pressure value (set value). The inert gas flow q introduced into the chamber is controlled. As a result, fluctuations in the inert gas flow are suppressed and the preform is melt-drawn in a stable manner, making it possible to obtain an optical fiber with a uniform outer diameter.
[実施例] 以下、本発明の実施例を添付図面に従って説明する。[Example] Embodiments of the present invention will be described below with reference to the accompanying drawings.
第1図は本発明の一実施例に係る光ファイバ線引装置の
構成図である。線引炉1内にカーボン質炉心菅2が設【
ノられ、この炉心管2の外周部に加熱用のヒータ3が配
置されている。炉心管2の上部及び下部にはそれぞれガ
ス吹き出し器4及び5が設置され、これらのガス吹き出
し器4及び5には供給管を介してガス流R調節悉6が接
続されている。さらに、このガス流m調節器6に不活性
ガス供給VS7が接続されている。また、炉心管2の下
部には管内の圧力を検出するための取出し口8が開口し
ており、この取出し口8に圧力計9が設けられている。FIG. 1 is a block diagram of an optical fiber drawing apparatus according to an embodiment of the present invention. A carbon core tube 2 is installed in the drawing furnace 1.
A heater 3 for heating is arranged on the outer periphery of the furnace core tube 2. Gas blowers 4 and 5 are installed at the upper and lower portions of the furnace core tube 2, respectively, and a gas flow R adjustment lever 6 is connected to these gas blowers 4 and 5 via a supply pipe. Furthermore, an inert gas supply VS7 is connected to this gas flow m regulator 6. Further, an outlet 8 for detecting the pressure inside the tube is opened at the lower part of the core tube 2, and a pressure gauge 9 is provided at the outlet 8.
そして、圧力計9の出力が制御器10に接続され、制t
Il器10の出力がガス流I11調節器6に接続されて
いる。Then, the output of the pressure gauge 9 is connected to the controller 10, and the output of the pressure gauge 9 is connected to the controller 10.
The output of Il device 10 is connected to gas flow I11 regulator 6.
なお、取出し口8は炉心管2内のガス流に影響を及ぼさ
ないように炉心管2の下部に設けられることが望ましい
。Note that it is desirable that the outlet 8 be provided at the lower part of the furnace core tube 2 so as not to affect the gas flow within the furnace core tube 2.
次に、本実施例の動作を説明する。Next, the operation of this embodiment will be explained.
まず、不活性ガス供給器7からガス流m調節器6及びガ
ス吹き出し器4.5を介してHe−Arf1合ガス全ガ
ス管2内に導入する。このどき、炉心管2内の圧力が圧
力計9によって検出され、この圧力値を示す検出信号が
圧力計9から制御器10に出力される。検出信号を入力
した制御器10では検出された圧力値と予め設定されて
いる設定値どの差分がとられ、さらにこの差分に基づい
たガス流量を指定する制御信号がガス流ff1UA節器
6に出力される。そして、ガス流量調節器6において制
m信号に基づき炉心管2へ導入するガス流量が制御され
る。このようにして、炉心管2の内圧は常時設定値に保
持されている。First, a combined He-Arf1 gas is introduced into the entire gas pipe 2 from the inert gas supply device 7 via the gas flow m regulator 6 and the gas blower 4.5. At this time, the pressure inside the reactor core tube 2 is detected by the pressure gauge 9, and a detection signal indicating this pressure value is outputted from the pressure gauge 9 to the controller 10. The controller 10 to which the detection signal is input calculates the difference between the detected pressure value and a preset value, and further outputs a control signal specifying the gas flow rate based on this difference to the gas flow regulator 6. be done. Then, the gas flow rate controller 6 controls the gas flow rate introduced into the reactor core tube 2 based on the m control signal. In this way, the internal pressure of the furnace tube 2 is always maintained at the set value.
この状態で多層のガラス質材料からなるプリフォーム1
1を炉心管2上部から管内に挿入すると共にヒータ3を
作動させて炉心管2を2000℃以上の高温に加熱する
。これによりプリフォーム11を溶融しつつ線引ぎして
炉心管2下部から光ファイバ12を引き出す。In this state, the preform 1 made of multilayer glass material
1 is inserted into the furnace core tube 2 from above and the heater 3 is activated to heat the furnace core tube 2 to a high temperature of 2000° C. or higher. As a result, the preform 11 is melted and drawn, and the optical fiber 12 is pulled out from the lower part of the furnace tube 2.
なお、このときプリフォーム11に曲がりや凹凸が生じ
ていたりあるいはヒータ3による加熱温度に変動が発生
したとしても、上述したように圧力計9.制御器10及
びガス流量調節器6によって炉心管2の内圧は設定値に
保持されるので、光ファイバ12の外径の変動が抑制さ
れる。At this time, even if the preform 11 is bent or uneven, or the heating temperature by the heater 3 fluctuates, the pressure gauge 9. Since the internal pressure of the reactor core tube 2 is maintained at a set value by the controller 10 and the gas flow rate regulator 6, fluctuations in the outer diameter of the optical fiber 12 are suppressed.
第1図に示寸装置を用い、ブリフt−ム11の外径20
mm、光ファイバ12の外径125tI11.引出速度
GO1rL/1ainとして線引作業を行なった。従来
のようにガス流jの制御を行なわなかった場合には、第
2図(a)に示すごとく光ファイバ12の外径変動が最
大1.5Imであった。これに対して、本発明に基づぎ
内圧の設定値を5#1111120 、流但変化示を上
250cm3/n1inとしてガス流通の制御を行なっ
た場合には、第2図(b)に示すごとく光ファイバ12
の外径変動が最大0.5pであった。Using a sizing device as shown in FIG.
mm, the outer diameter of the optical fiber 12 is 125tI11. The wire drawing operation was performed at a drawing speed of GO1rL/1ain. When the gas flow j was not controlled as in the conventional case, the maximum variation in the outer diameter of the optical fiber 12 was 1.5 Im, as shown in FIG. 2(a). On the other hand, when the gas flow is controlled based on the present invention by setting the internal pressure to 5#1111120 and setting the flow rate change to 250cm3/n1in, as shown in Fig. 2(b). optical fiber 12
The outer diameter variation was 0.5p at maximum.
[発明の効果]
以上説明したように本発明によれば、次のごとぎ優れた
効果を発揮する。[Effects of the Invention] As explained above, according to the present invention, the following excellent effects are exhibited.
線引炉内に導入する不活性ガス流岳を制御することによ
り線引炉の内圧を所定の圧力値に保持させることができ
る。従って、ヒータへの供給電流の変V」やヒータの劣
化、プリフォームの曲がりや凹凸、不活性ガス供給圧力
の変動等が生じても線引炉内は一定圧に保持され、その
結果線引きして得られる光ファイバの外径の均一化が向
上する。By controlling the amount of inert gas introduced into the drawing furnace, the internal pressure of the drawing furnace can be maintained at a predetermined pressure value. Therefore, even if there is a change in the current supplied to the heater, deterioration of the heater, bending or unevenness of the preform, fluctuations in the inert gas supply pressure, etc., the pressure inside the drawing furnace is maintained at a constant level, and as a result, the drawing furnace is maintained at a constant pressure. This improves the uniformity of the outer diameter of the optical fiber obtained.
第1図は本発明の一実施例に係る光ファイバ線引装置の
構成図、第2図(a)及び(b)はそれぞれ従来法及び
本発明の装置によりlqられた光ファイバの外径変動を
示す説明図、第3図は従来例の構成図である。
図中、1は線引炉、6はガス流■調節器、9は圧力計、
10は制御器、11はプリフォームである。FIG. 1 is a block diagram of an optical fiber drawing device according to an embodiment of the present invention, and FIGS. 2(a) and (b) show variations in the outer diameter of an optical fiber drawn by the conventional method and the device of the present invention, respectively. FIG. 3 is a configuration diagram of a conventional example. In the figure, 1 is a drawing furnace, 6 is a gas flow regulator, 9 is a pressure gauge,
10 is a controller, and 11 is a preform.
Claims (1)
にてプリフォームを線引きする光ファイバ線引装置にお
いて、上記線引炉の内圧を検出する圧力検出手段と、該
圧力検出手段で検出された内圧が所定の圧力値となるよ
うに上記内圧と上記所定の圧力値との差分をとり、該差
分に基づいて上記線引炉内に導入する上記不活性ガスの
流量を制御する制御手段とを備えたことを特徴とする光
ファイバ線引装置。In an optical fiber drawing apparatus that introduces an inert gas into a drawing furnace and draws a preform in the gas atmosphere, a pressure detection means detects the internal pressure of the drawing furnace, and the pressure detection means detects the internal pressure of the drawing furnace. A control means for calculating the difference between the internal pressure and the predetermined pressure value so that the internal pressure obtained becomes a predetermined pressure value, and controlling the flow rate of the inert gas introduced into the drawing furnace based on the difference. An optical fiber drawing device comprising:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6853486A JPS62226834A (en) | 1986-03-28 | 1986-03-28 | Optical fiber drawing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6853486A JPS62226834A (en) | 1986-03-28 | 1986-03-28 | Optical fiber drawing device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62226834A true JPS62226834A (en) | 1987-10-05 |
Family
ID=13376496
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6853486A Pending JPS62226834A (en) | 1986-03-28 | 1986-03-28 | Optical fiber drawing device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62226834A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011046563A (en) * | 2009-08-27 | 2011-03-10 | Sumitomo Electric Ind Ltd | Method for drawing optical fiber |
JP2017214256A (en) * | 2016-06-01 | 2017-12-07 | 住友電気工業株式会社 | Wire drawing method for optical fiber |
-
1986
- 1986-03-28 JP JP6853486A patent/JPS62226834A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011046563A (en) * | 2009-08-27 | 2011-03-10 | Sumitomo Electric Ind Ltd | Method for drawing optical fiber |
JP2017214256A (en) * | 2016-06-01 | 2017-12-07 | 住友電気工業株式会社 | Wire drawing method for optical fiber |
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