JPH01308842A - Drawing furnace for optical fiber - Google Patents
Drawing furnace for optical fiberInfo
- Publication number
- JPH01308842A JPH01308842A JP13934988A JP13934988A JPH01308842A JP H01308842 A JPH01308842 A JP H01308842A JP 13934988 A JP13934988 A JP 13934988A JP 13934988 A JP13934988 A JP 13934988A JP H01308842 A JPH01308842 A JP H01308842A
- Authority
- JP
- Japan
- Prior art keywords
- preform
- gas
- drawing furnace
- optical fiber
- furnace
- 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 29
- 239000007789 gas Substances 0.000 claims abstract description 54
- 239000011261 inert gas Substances 0.000 claims abstract description 15
- 238000012681 fiber drawing Methods 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims description 13
- 239000000155 melt Substances 0.000 claims description 3
- 239000000835 fiber Substances 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 5
- 238000011109 contamination Methods 0.000 abstract description 2
- 238000007664 blowing Methods 0.000 abstract 1
- 238000003780 insertion Methods 0.000 description 3
- 230000037431 insertion Effects 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000005491 wire drawing Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007921 spray Substances 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
- C03B37/0253—Controlling or regulating
-
- 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
- C03B37/02736—Means 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
-
- 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
- C03B2205/30—Means for continuous drawing from a preform
-
- 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
- C03B2205/62—Heating means for drawing
- C03B2205/63—Ohmic resistance heaters, e.g. carbon or graphite resistance heaters
-
- 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
-
- 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
- C03B2205/98—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 using annular gas inlet distributors
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】
〈産業上の利用分計〉
本発明は、線径変動及び強度低下の少ない光ファイバを
得ろことができる光ファイバ線引炉に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application> The present invention relates to an optical fiber drawing furnace capable of producing optical fibers with less variation in wire diameter and less decrease in strength.
〈従来の技術〉
従来より光ファイバ母材(息下、プリフォームと称す)
を加熱溶融し、線引きして光ファイバを得る光ファイバ
線引炉においては、当該線引炉内の雰囲気の乱れを防止
して径変動のない光ファイバを製造するとともに外気の
当該線引炉内への混入によるヒータ等の酸化劣化を防止
するために、当該線引炉へのプリフォームの入口にガス
カーテンを形成したり、ヒータを有する加熱炉をシール
したりしている。<Conventional technology> Conventionally, optical fiber base material (referred to as preform)
In an optical fiber drawing furnace that heats and melts and draws optical fibers, it is possible to prevent disturbances in the atmosphere inside the drawing furnace to produce optical fibers with no diameter variation, and to prevent outside air from entering the drawing furnace. In order to prevent oxidative deterioration of the heater and the like due to contamination, a gas curtain is formed at the entrance of the preform to the drawing furnace, or a heating furnace containing the heater is sealed.
このようなガスカーテンを形成しうる線引炉の一例を第
2図に示す。同図に示すように、線引炉本体1はプリフ
ォーム2が導入される炉芯管3と加熱ヒータ4とを有し
ており、当該線引炉本体1の入口1aには炉芯管3の内
径とほぼ同寸法の内径を有する環状のガスカーテン装置
5が設けられている。このガスカーテン装置5の内周面
には溝状のガス噴出口5aが周方向に亘って形成されて
おり、このガス噴出口5aを介して、外部から導入され
ろ不活性ガス6をプリフォーム2の外周面に向って噴出
するように構成されている。かかるガスカーテン装置5
のガス噴出口5aから噴出される例えば窒素ガスなどの
不活性ガス6はプリフォーム2の外周面に吹き付けられ
た後上下方向に分配され、炉内方向に向ったガスは炉内
を通過して炉下部から排出されるガスの流れを形成する
。これにより、炉内に一定の雰囲気ガスの流れを形成す
るとともに外気が炉内に流入するのを防止している。な
お、プリフォーム2はダミー棒7に溶着されて母材挿入
装置8により炉内に挿入されている。An example of a drawing furnace capable of forming such a gas curtain is shown in FIG. As shown in the figure, the drawing furnace main body 1 has a furnace core tube 3 into which the preform 2 is introduced and a heater 4. An annular gas curtain device 5 having an inner diameter approximately the same as the inner diameter of the gas curtain device 5 is provided. A groove-shaped gas outlet 5a is formed in the inner peripheral surface of the gas curtain device 5 in the circumferential direction, and an inert gas 6 introduced from the outside is passed through the gas outlet 5a to form a preform. It is configured to eject toward the outer circumferential surface of No. 2. Such a gas curtain device 5
An inert gas 6 such as nitrogen gas is ejected from the gas ejection port 5a of the preform 2, and after being blown onto the outer peripheral surface of the preform 2, it is distributed in the vertical direction, and the gas directed toward the inside of the furnace passes through the inside of the furnace. Forms a flow of gas that is discharged from the lower part of the furnace. This creates a constant flow of atmospheric gas within the furnace and prevents outside air from flowing into the furnace. Note that the preform 2 is welded to a dummy rod 7 and inserted into the furnace by a base material insertion device 8.
〈発明が解決しようとする課題〉
前述した線引炉においては、通常、導入されるプリフォ
ーム2とダミー棒7との外径差のため、線引きされた光
ファイバに線径変動が生じ、また、外気が炉内に混入さ
れて炉芯管3等に酸化劣化が生じろという問題がある。<Problems to be Solved by the Invention> In the above-mentioned drawing furnace, normally, due to the difference in the outer diameter between the introduced preform 2 and the dummy rod 7, a wire diameter variation occurs in the drawn optical fiber. There is a problem in that outside air is mixed into the furnace, causing oxidative deterioration of the furnace core tube 3 and the like.
このような問題は、プリフォーム毎の外径差やプリフォ
ームの長手方向に亘っての外径差によっても発生する。Such problems also occur due to differences in outer diameter between preforms or differences in outer diameter in the longitudinal direction of the preforms.
本発明はこのような事情に鑑み、プリフォームの外径の
変化に起因する光ファイバの外径に変化及び外気の混入
を防止することができる光ファイバ線引炉を提供するこ
とを目的とする。In view of these circumstances, it is an object of the present invention to provide an optical fiber drawing furnace that can prevent changes in the outer diameter of the optical fiber caused by changes in the outer diameter of the preform and prevent entry of outside air. .
く課題を解決するための手段〉
前記目的を達成する本発明の光ファイバ線引炉は、光フ
ァイバ母材を加熱溶融して線引きする線引炉本体を有す
る光ファイバ線引炉において、当該線引炉本体の母材入
口近傍にて当該母材の外周面に不活性ガスを吹き付けて
当該線引炉本体内への外気の流入を防止するガスカーテ
ン装置と、当該線引炉本体に導入される母材の外径を測
定する外径測定装置と、この外径測定装置により測定さ
れた母材の外径に応じて上記ガスカーテン装置から吹き
出されろ不活性ガスの流量を制御する制御手段とを有す
ることを特徴とする。Means for Solving the Problems〉 The optical fiber drawing furnace of the present invention that achieves the above object is an optical fiber drawing furnace that has a drawing furnace body that heats and melts an optical fiber preform to draw the wire. A gas curtain device that sprays an inert gas onto the outer peripheral surface of the base material near the base material inlet of the drawing furnace body to prevent outside air from flowing into the wire drawing furnace body; an outer diameter measuring device for measuring the outer diameter of the base material; and a control means for controlling the flow rate of the inert gas blown out from the gas curtain device according to the outer diameter of the base material measured by the outer diameter measuring device. It is characterized by having the following.
く作 用〉
ガスカーテン装置から吹き出された不活性ガスは光ファ
イバ母材の外周面に当った後当該母材の外周面軸方向に
沿って炉内方向及び炉外方向へ流れる。光ファイバ母材
の外径が変化するとそれに応じて不活性ガスの流量が制
御されて炉内方向へ流れる不活性ガスの流量が一定に制
御され、炉内雰囲気が一定に保持される。Function> The inert gas blown out from the gas curtain device hits the outer circumferential surface of the optical fiber preform and then flows toward the inside of the furnace and toward the outside of the furnace along the axial direction of the outer circumferential surface of the preform. When the outer diameter of the optical fiber preform changes, the flow rate of the inert gas is controlled accordingly, so that the flow rate of the inert gas flowing toward the inside of the furnace is controlled to be constant, and the atmosphere inside the furnace is maintained constant.
く実 施 例〉
以下、本発明の好適な一実施例を図面を参照しながら説
明する。Embodiment A preferred embodiment of the present invention will be described below with reference to the drawings.
第1図には、本実施例にかかる光ファイバ線引炉の構成
を示すが、第2図に示した従来の線引炉と同一部材には
同一符号を付して重複した説明は省略する。FIG. 1 shows the configuration of the optical fiber drawing furnace according to this embodiment, but the same members as those in the conventional drawing furnace shown in FIG. .
第1図に示すように、本実施例の光ファイバ線引炉は線
引炉本体1に設けられているガスカーテン装置5の上方
に外径測定器11を具えたものである。この外径測定器
11は1(8−Neレーザー等によりプリフォーム2あ
るいはダミー棒7の外径を測定するものであり、この測
定データは、ガスカーテン装置5に送られる不活性ガス
6の流量を調節しうる電磁バルブ等からなるガス流量調
節器12を制御する制御手段となる演算器13に入力さ
れる。As shown in FIG. 1, the optical fiber drawing furnace of this embodiment is equipped with an outer diameter measuring device 11 above a gas curtain device 5 provided in a drawing furnace main body 1. As shown in FIG. This outer diameter measuring device 11 measures the outer diameter of the preform 2 or the dummy rod 7 using 1 (8-Ne laser, etc.), and this measurement data is based on the flow rate of the inert gas 6 sent to the gas curtain device 5. The data is input to a computing unit 13, which serves as a control means for controlling a gas flow rate regulator 12, which is composed of an electromagnetic valve or the like that can adjust the flow rate.
この演算器13では測定データと別途入力される基準外
径14との偏差をとり、その変化した外径に対応したガ
ス流量となるように流量調節器12を制御し、ガスカー
テン装置5のガスカーテン効果が常に一定になるように
している。このとき、演算器13は同時に、外径測定位
置とエアカーテン装置5との距離並びにそのときの母材
挿入装置8によるプリフォーム送り速度から、現在の外
径測定部分がガスカーテン装置5に入る時間を求め、こ
れに対応して流量調節器12を制御している。This calculator 13 calculates the deviation between the measured data and the separately input reference outer diameter 14, controls the flow rate regulator 12 so that the gas flow rate corresponds to the changed outer diameter, and controls the gas flow rate of the gas curtain device 5. The curtain effect is always constant. At this time, the calculator 13 simultaneously determines that the current outer diameter measurement portion enters the gas curtain device 5 based on the distance between the outer diameter measurement position and the air curtain device 5 and the preform feed rate by the base material insertion device 8 at that time. The time is determined and the flow rate regulator 12 is controlled accordingly.
すなわち、ガスカーテン装置S内にてブリフオーム2の
外径が変化する際に、その変化する外径に対応してガス
流量が調節されるようになっている。That is, when the outer diameter of the brifome 2 changes within the gas curtain device S, the gas flow rate is adjusted in accordance with the changing outer diameter.
このような本実施例の線引炉における作用を説明する。The operation of the drawing furnace of this embodiment will be explained.
基準外径14に対して実際のプリフォーム径が小さくな
った場合には、ガス流量を一定のままにすると、プリフ
ォーム2の外周面に当った後線引炉内方向(下方)に向
って流れる不活性ガス6の流れが小さくなってガスカー
テン効果が弱まるが、本実施例の線引炉ではプリフォー
ム径が小さ(なった部分がガスカーテン装置5に入った
際に、ガス流量がその径に応じて増加するように調節サ
レるので、線引炉内に向って流れろガス流量が一定に保
たれる。一方、プリフォーム径が大きくなった場合には
、ガス流量を一定のままにすると、線引炉内方向に向っ
て流れる不活性ガス6の流れが大きくなるが、本実施例
の線引炉ではプリフォーム径が大きくなった部分がガス
カーテン装置5に入った際に、ガス流量がその径に応じ
て減少するように調節されるので、線引炉内に向って流
れるガス流量が一定に保たれろ。If the actual preform diameter is smaller than the reference outer diameter 14, if the gas flow rate is kept constant, the gas will flow inward (downward) into the drawing furnace after hitting the outer peripheral surface of the preform 2. The flow of the flowing inert gas 6 becomes smaller and the gas curtain effect is weakened, but in the drawing furnace of this embodiment, the preform diameter is small (when the small part enters the gas curtain device 5, the gas flow rate is Since the preform is adjusted so that it increases according to the diameter, the gas flow rate toward the inside of the drawing furnace is kept constant.On the other hand, when the preform diameter increases, the gas flow rate remains constant. As a result, the flow of the inert gas 6 flowing toward the inside of the drawing furnace increases, but in the drawing furnace of this embodiment, when the portion of the preform with a large diameter enters the gas curtain device 5, the gas The flow rate of the gas flowing into the drawing furnace remains constant since the flow rate is adjusted to decrease depending on its diameter.
このように本実施例の線引炉ではプリフォーム2あるい
はダミー棒7の径が変化しても、ガスカーテン装置5か
ら吹き出してプリフォーム2等の外周面に当った後線引
炉内に向って流れるガス流量が一定に保たれ、ガスカー
テン効果が一定となるので、炉内の雰囲気に乱れが生じ
るのが防止され、且つ炉内に外気が混入する乙ともない
。In this way, in the drawing furnace of this embodiment, even if the diameter of the preform 2 or the dummy rod 7 changes, the gas blows out from the gas curtain device 5, hits the outer peripheral surface of the preform 2, etc., and then heads into the drawing furnace. Since the flow rate of the gas flowing through the furnace is kept constant and the gas curtain effect is constant, disturbances in the atmosphere inside the furnace are prevented, and outside air does not get mixed into the furnace.
〈試 験 例〉
上記実施例の線引炉において、外径が長手方向に亘って
26mmφ〜23mmφで変動するプリフォームを用い
て線引きした。基準外径を25間φに設定し、このとき
の不活性ガス(N2)流量を101/分とし、プリフォ
ーム外径差1+mφに対してガス流量を11/分変化す
るように設定した。すなわち、プリフォーム外径が1f
flφ大きくなったときにガス流量が11/分小さくな
り、プリフォーム外径が1mmφ小さくなったときにガ
ス流量がlj/分大きくなるように設定した。<Test Example> In the drawing furnace of the above example, wire was drawn using a preform whose outer diameter varied from 26 mmφ to 23 mmφ in the longitudinal direction. The reference outer diameter was set to 25 φ, the inert gas (N2) flow rate at this time was 101/min, and the gas flow rate was set to change by 11/min for a preform outer diameter difference of 1+mφ. That is, the preform outer diameter is 1f.
The gas flow rate was set so that when flφ increased, the gas flow rate decreased by 11/min, and when the preform outer diameter decreased by 1 mmφ, the gas flow rate increased by lj/min.
この線引きの際に、炉の下部から流出するガス流量を測
定したところ、プリフォーム径が変化しても6!/分と
一定であり、線引きされた光ファイバについても径変動
が125±0.5μmと小さく、強度低下も検出されな
かった。When we measured the gas flow rate flowing out from the bottom of the furnace during this wire drawing, we found that it was 6! even if the preform diameter changed. The diameter variation of the drawn optical fiber was as small as 125±0.5 μm, and no decrease in strength was detected.
一方、比較のため、第2図に示すような従来の線引炉を
用い、同様に26〜23朧φで径が変動するプリフォー
ムをガス流量101/分と一定にして線引きしたところ
、炉の下部から流出するガス流量が717分〜41/分
の間で変化し、光ファイバの径変動も125±1.0μ
mと約2倍に大きくなった。また、炉の下部からの流出
するガスが417分になった際に炉下部から空気が混入
したためか、炉内構成材料が酸化されてしまった。On the other hand, for comparison, we used a conventional drawing furnace as shown in Fig. 2 to draw a preform with a diameter varying from 26 to 23 φ at a constant gas flow rate of 101/min. The gas flow rate flowing out from the bottom of the fiber varies between 717 min and 41 min, and the diameter variation of the optical fiber is 125 ± 1.0μ.
It has become about twice as large as m. Furthermore, when the gas flowing out from the lower part of the furnace reached 417 minutes, air was mixed in from the lower part of the furnace, and the materials constituting the furnace were oxidized.
〈発明の効果〉
以上説明したように、本発明にかかる光ファイバ線引炉
によれば、プリフォーム径が変動しても、線引炉内に流
れる不活性ガスの量が常に一定に保たれるとともに外気
の混入も防止されるので、線引きされる光ファイバの径
変動の増加や強度低下が防止され、生産性が向上されろ
。<Effects of the Invention> As explained above, according to the optical fiber drawing furnace of the present invention, even if the preform diameter changes, the amount of inert gas flowing into the drawing furnace can be kept constant. At the same time, the mixing of outside air is also prevented, which prevents an increase in diameter variation and a decrease in strength of the optical fiber being drawn, and improves productivity.
第1図は本発明の一実施例にかかる光ファイバ線引炉を
示す構成図、第2図は従来技術にかかる光ファイバ線引
炉を示す構成図である。
図面中、
1は線引炉本体、
2はプリフォーム(光ファイバ母材)、3は炉芯管、
4は加熱ヒータ、
5はガスカーテン装置、
7はダミー棒、
8は母材挿入装置、
11は外径測定器、
12は流量調節器、
13は演算器である。FIG. 1 is a block diagram showing an optical fiber drawing furnace according to an embodiment of the present invention, and FIG. 2 is a block diagram showing an optical fiber drawing furnace according to the prior art. In the drawings, 1 is the drawing furnace body, 2 is the preform (optical fiber base material), 3 is the furnace core tube, 4 is the heater, 5 is the gas curtain device, 7 is the dummy rod, 8 is the base material insertion device, 11 is an outer diameter measuring device, 12 is a flow rate regulator, and 13 is a computing unit.
Claims (1)
有する光ファイバ線引炉において、当該線引炉本体の母
材入口近傍にて当該母材の外周面に不活性ガスを吹き付
けて当該線引炉本体内への外気の流入を防止するガスカ
ーテン装置と、当該線引炉本体に導入される母材の外径
を測定する外径測定装置と、この外径測定装置により測
定された母材の外径に応じて上記ガスカーテン装置から
吹き出される不活性ガスの流量を制御する制御手段とを
有することを特徴とする光ファイバ線引炉。In an optical fiber drawing furnace having a drawing furnace body that heats and melts an optical fiber preform to draw the fiber, an inert gas is blown onto the outer circumferential surface of the preform near the inlet of the preform in the drawing furnace main body. A gas curtain device that prevents outside air from entering the drawing furnace body, an outer diameter measuring device that measures the outer diameter of the base material introduced into the drawing furnace body, and an outer diameter measuring device that measures the outer diameter of the base material introduced into the drawing furnace body. An optical fiber drawing furnace comprising: a control means for controlling the flow rate of the inert gas blown out from the gas curtain device according to the outer diameter of the base material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13934988A JPH01308842A (en) | 1988-06-08 | 1988-06-08 | Drawing furnace for optical fiber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13934988A JPH01308842A (en) | 1988-06-08 | 1988-06-08 | Drawing furnace for optical fiber |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01308842A true JPH01308842A (en) | 1989-12-13 |
Family
ID=15243259
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13934988A Pending JPH01308842A (en) | 1988-06-08 | 1988-06-08 | Drawing furnace for optical fiber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01308842A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108929031A (en) * | 2018-07-27 | 2018-12-04 | 长飞光纤光缆股份有限公司 | A kind of device and method of VAD preparation optical fiber preform base material |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6385025A (en) * | 1986-09-26 | 1988-04-15 | Sumitomo Electric Ind Ltd | Drawing of optical fiber |
-
1988
- 1988-06-08 JP JP13934988A patent/JPH01308842A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6385025A (en) * | 1986-09-26 | 1988-04-15 | Sumitomo Electric Ind Ltd | Drawing of optical fiber |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108929031A (en) * | 2018-07-27 | 2018-12-04 | 长飞光纤光缆股份有限公司 | A kind of device and method of VAD preparation optical fiber preform base material |
CN108929031B (en) * | 2018-07-27 | 2021-11-09 | 长飞光纤光缆股份有限公司 | Device and method for preparing optical fiber preform base material by VAD |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4101300A (en) | Method and apparatus for drawing optical fiber | |
EP0846665B1 (en) | Process and apparatus for manufacturing a glass preform for optical fibres by drawing a preform | |
JP3654494B2 (en) | Method and system for steam delivery control in optical preform manufacture | |
KR940014216A (en) | Drawing method of glass product and its device | |
JPH06229854A (en) | Measuring method of tension of moving optical fiber | |
JPH01308842A (en) | Drawing furnace for optical fiber | |
JPH0617788B2 (en) | Device for measuring the diameter of continuous or rod-shaped products in the tobacco processing industry | |
US5346530A (en) | Method for atomizing liquid metal utilizing liquid flow rate sensor | |
US20060107698A1 (en) | Automatic pressure control device for quartz tube | |
JPS63195139A (en) | Apparatus for drawing glass rod | |
JP2000063142A (en) | Furnace for drawing optical fiber and method for drawing optical fiber | |
JP2005075664A (en) | Method for drawing optical fiber | |
JP3166483B2 (en) | Optical fiber temperature measuring device | |
JP2818661B2 (en) | Optical fiber manufacturing method | |
JPH05180492A (en) | Ion concentration controller in air conditioning room | |
JPH08710B2 (en) | Sealing method for optical fiber drawing furnace | |
JPS63285133A (en) | Furnace for drawing optical fiber | |
JPS62162647A (en) | Drawing device for optical fiber | |
JPS63159232A (en) | Production apparatus for optical fiber preform | |
JPH01305829A (en) | Method for drawing optical fiber | |
JP3667363B2 (en) | Glass tube outer diameter control device | |
JPS61136931A (en) | Manufacture of glass capillary tube | |
JPH01186281A (en) | Welding method | |
JP3495395B2 (en) | Optical fiber drawing method | |
EE03915B1 (en) | Apparatus and method for dispensing a stream of glass |