JPS624333B2 - - Google Patents
Info
- Publication number
- JPS624333B2 JPS624333B2 JP4312583A JP4312583A JPS624333B2 JP S624333 B2 JPS624333 B2 JP S624333B2 JP 4312583 A JP4312583 A JP 4312583A JP 4312583 A JP4312583 A JP 4312583A JP S624333 B2 JPS624333 B2 JP S624333B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- core tube
- fiber
- gas
- helium
- 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
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
- C03B37/029—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
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)
Description
【発明の詳細な説明】
本発明は光フアイバの線引き方法において、使
用する炉の炉内構成材料のカーボンの酸化消耗を
防止し炉内雰囲気を清浄化した線引き方法に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an optical fiber drawing method that prevents the oxidative consumption of carbon in the constituent materials of the furnace used and cleans the atmosphere inside the furnace.
石英系ガラスのフアイバ素材からフアイバを線
引する方法において、従来使用された線引き炉は
カーボンを主体とした材料で構成されており、石
英系フアイバの線引きに必要な2000℃以上の高温
では酸化防止のためのアルゴンや窒素などの不活
性ガスを流入させている。発熱体内部に炉心管を
有する炉においては、窒素ガスと石英との反応生
成物を考慮しアルゴンガスを流入させているのが
普通である。炉心管内部にアルゴンガスを流入さ
せた場合、長時間の連続した線引きでは、その線
引き期間中にわたつてカーボンの酸化消耗や石英
とカーボンとの反応によるダストの発生を防止し
きれず、時間とともにダスト量が増加する。その
ため発生したダストによつてフアイバ表面が汚染
され、フアイバの破断強度の低下要因となる傷が
形成され、従つて長尺の高強度フアイバが得られ
ないという欠点があつた。 In the method of drawing fibers from silica-based fiber materials, the drawing furnaces used in the past are made of carbon-based materials, which prevent oxidation at the high temperatures of 2000°C or higher required for drawing silica-based fibers. An inert gas such as argon or nitrogen is injected for this purpose. In a furnace having a core tube inside the heating element, argon gas is usually introduced in consideration of reaction products between nitrogen gas and quartz. When argon gas is allowed to flow into the core tube, continuous drawing over a long period of time will not prevent the oxidation and consumption of carbon and the generation of dust due to the reaction between quartz and carbon. The amount increases. As a result, the generated dust contaminates the surface of the fiber, forming scratches that reduce the breaking strength of the fiber, resulting in the disadvantage that a long, high-strength fiber cannot be obtained.
本発明はこれらの欠点を除去するため、炉心管
内部にヘリウムガスを混ぜたアルゴンガスを流入
させてその雰囲気の中で線引きを行なうことを特
徴とし、長時間にわたつて線引き炉内雰囲気を清
浄に保つことにより、長尺の高強度フアイバを得
ることを目的とした光フアイバ線引き方法に関す
るもので、以下図面により詳細説明する。 In order to eliminate these drawbacks, the present invention is characterized in that argon gas mixed with helium gas is flowed into the furnace core tube and drawing is performed in that atmosphere, thereby cleaning the atmosphere inside the drawing furnace for a long period of time. The present invention relates to an optical fiber drawing method for the purpose of obtaining a long, high-strength fiber by maintaining the same temperature, and will be explained in detail below with reference to the drawings.
第1図は本発明の1実施例である線引き炉の構
成を説明する断面図であつて、1は炉体、2は上
部突出室、3は上部突出室上面の上部開口、4は
下部突出室、5は下部突出室下面の下部開口、6
は母材、7はフアイバー、8はカーボンからなる
円筒状の炉心管、9は炉心管内部、10は炉体1
内の炉心管外部、11はヒータ、12はヘリウム
ガスボンベ、13はアルゴンガスボンベ、14は
混合器、15はガス入口、16はガス出口、であ
る。 FIG. 1 is a sectional view illustrating the configuration of a drawing furnace according to an embodiment of the present invention, in which 1 is a furnace body, 2 is an upper protrusion chamber, 3 is an upper opening on the upper surface of the upper protrusion chamber, and 4 is a lower protrusion. Chamber, 5 is a lower opening on the lower surface of the lower protruding chamber, 6
7 is a base material, 7 is a fiber, 8 is a cylindrical furnace tube made of carbon, 9 is the inside of the furnace tube, 10 is a furnace body 1
11 is a heater, 12 is a helium gas cylinder, 13 is an argon gas cylinder, 14 is a mixer, 15 is a gas inlet, and 16 is a gas outlet.
図から分るように炉体1には、中央上部に上部
突出室2が設けられ、該上部突出室2の上面に
は、炉外から母材6を懸垂できるように上部開口
3が設けられており、また中央下部に下部突出室
4が設けられ、該下部突出室4の下面には、線引
きされたフアイバ7を炉外に牽引できるように下
部開口5が設けられている。また炉体1内にてそ
の中心に円筒状の炉心管8が上部突出室2と下部
突出室4を連結しており、該炉心管8の炉心管内
部9が炉心管外部10に気密になるように設けら
れている。炉心管外部10において円筒状発熱体
よりなるヒータ11が炉心管8の周囲に設けられ
ている。下部突出室4の側面にはガス入口15が
設けられ、ガス入口15にはヘリウムガスボンベ
12とアルゴンガスボンベ13が混合器14を介
して連結されている。上部突出室2の側面にはガ
ス出口16が設けられており、図示していないが
ガス出口16には排出ガスの処理装置が設けられ
ている。 As can be seen from the figure, the furnace body 1 is provided with an upper protrusion chamber 2 at the upper center, and an upper opening 3 is provided on the upper surface of the upper protrusion chamber 2 so that a base material 6 can be suspended from outside the furnace. A lower protruding chamber 4 is provided at the lower center, and a lower opening 5 is provided on the lower surface of the lower protruding chamber 4 so that the drawn fiber 7 can be pulled out of the furnace. In addition, a cylindrical furnace core tube 8 is located at the center of the furnace body 1 and connects the upper projecting chamber 2 and the lower projecting chamber 4, and the inside 9 of the furnace tube 8 is airtight to the outside 10 of the furnace tube. It is set up like this. A heater 11 made of a cylindrical heating element is provided around the core tube 8 at the outside of the core tube 10 . A gas inlet 15 is provided on the side surface of the lower projecting chamber 4 , and a helium gas cylinder 12 and an argon gas cylinder 13 are connected to the gas inlet 15 via a mixer 14 . A gas outlet 16 is provided on the side surface of the upper projecting chamber 2, and although not shown, the gas outlet 16 is provided with an exhaust gas processing device.
以上の様に線引き炉を構成したので、炉外から
母材6を懸垂し、炉体1内の炉心管外部10と気
密性が保持された炉心管内部9において、高温状
態で母材6を線引きしフアイバー7として下部突
出室4の下部開口5から炉外に牽引するととも
に、ヘリウムガスボンベ12からのヘリウムガス
とアルゴンガスボンベ13からのアルゴンガスを
混合器14により所定の流量比で混合しガス入口
15から流入せしめ炉心管内部9の清浄な雰囲気
として使用しガス出口16より流出させることが
できる。 Since the wire drawing furnace is configured as described above, the base material 6 is suspended from outside the furnace, and the base material 6 is drawn in a high temperature state in the core tube outside 10 in the furnace body 1 and the core tube interior 9 which is kept airtight. The drawn fiber 7 is pulled out of the furnace from the lower opening 5 of the lower protrusion chamber 4, and the helium gas from the helium gas cylinder 12 and the argon gas from the argon gas cylinder 13 are mixed at a predetermined flow rate ratio by the mixer 14, and the gas is inlet. The gas can be made to flow in from 15 and used as a clean atmosphere inside the furnace tube 9, and can be made to flow out from the gas outlet 16.
母材の外径を25mmとし、内径40mmの炉心管内部
3の線引き開始後3時間のダスト発生量とアルゴ
ンに対するヘリウムの流量比との関係を調べた。 The outer diameter of the base material was 25 mm, and the relationship between the amount of dust generated for 3 hours after the start of drawing in the inner diameter of the core tube 3 with an inner diameter of 40 mm and the flow rate ratio of helium to argon was investigated.
ガス出口16から採取した炉内雰囲気のクリー
ン度は、ヘリウムの流量比0ではクラス5000〜
10000であるのに対し、ヘリウムを混合すると流
量比0.05からクリーン度が向上しはじめ流量比
0.3でほぼ一定値、クラス100〜300まで減少し
た。ヘリウムの流量比を増すと線径変動が生じる
ため流量比の限度は0.6である。 The cleanliness of the atmosphere inside the furnace sampled from the gas outlet 16 is class 5000 or higher when the helium flow rate ratio is 0.
10,000, but when helium is mixed, the cleanliness starts to improve from a flow rate ratio of 0.05.
It remained almost constant at 0.3 and decreased to classes 100-300. If the helium flow rate is increased, the wire diameter will fluctuate, so the limit on the flow rate is 0.6.
ヘリウムの流量比0.3で母材の外径25mmの合成
石英ガラス棒を線引きし、公知の被覆法によりシ
リコン被覆した外径125±1μm、シリコン被覆
外径400μm、単長10.7Kmのフアイバーを、ゲー
ジ長100m、引張り速度10%/min.で引張り試験
した結果、最小値は5.3Kg、最大値は6.6Kg、平均
6.2Kgであつた。 A synthetic quartz glass rod with an outer diameter of 25 mm as a base material was drawn at a helium flow rate ratio of 0.3, and a fiber with an outer diameter of 125 ± 1 μm, a silicon coated outer diameter of 400 μm, and a single length of 10.7 km was coated with silicon using a known coating method. As a result of a tensile test with a length of 100 m and a tensile speed of 10%/min, the minimum value was 5.3Kg, the maximum value was 6.6Kg, and the average
It weighed 6.2Kg.
以上詳細説明したように炉心管内部にヘリウム
ガスを混合したアルゴンガスを流入させる本発明
を実施することによつて、高温状態において母材
からフアイバーを線引きする炉心管内部を清浄に
保つことができるため、長尺の高強度フアイバー
が得られるという効果がある。 As explained in detail above, by carrying out the present invention in which argon gas mixed with helium gas is flowed into the inside of the reactor core tube, the inside of the reactor core tube where fibers are drawn from the base material can be kept clean in a high temperature state. Therefore, there is an effect that a long high-strength fiber can be obtained.
第1図は本発明の1実施例を説明する断面図。
1:炉体、2:上部突出室、4:下部突出室、
6:母材、7:フアイバー、8:炉心管、11:
ヒータ、12:ヘリウムガスボンベ、13:アル
ゴンガスボンベ、14:混合器、15:ガス入
口、16:ガス出口。
FIG. 1 is a sectional view illustrating one embodiment of the present invention. 1: Furnace body, 2: Upper protrusion chamber, 4: Lower protrusion chamber,
6: Base metal, 7: Fiber, 8: Furnace tube, 11:
Heater, 12: Helium gas cylinder, 13: Argon gas cylinder, 14: Mixer, 15: Gas inlet, 16: Gas outlet.
Claims (1)
母材を加熱延伸してフアイバに線引きする方法に
おいて、使用する炉には、円筒状発熱体内部にカ
ーボンから成る円筒状の炉心管を有し、この炉心
管によつて炉心管内部が炉体内の炉心管外部と気
密性が保たれており、かつ、炉内雰囲気の制御の
ため炉心管内部に流入させる雰囲気ガスがアルゴ
ンを主成分としこれにヘリウムを0.05〜0.6の流
量比であることを特徴とする光フアイバ線引き方
法。1. In the method of heating and stretching a rod-shaped fiber base material mainly composed of quartz glass and drawing it into a fiber, the furnace used has a cylindrical furnace core tube made of carbon inside a cylindrical heating element, This core tube maintains airtightness between the inside of the core tube and the outside of the core tube inside the furnace body, and the atmospheric gas that is introduced into the core tube to control the furnace atmosphere is mainly composed of argon. A method for drawing an optical fiber, characterized by using helium at a flow rate ratio of 0.05 to 0.6.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4312583A JPS59169951A (en) | 1983-03-17 | 1983-03-17 | Drawing of optical fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4312583A JPS59169951A (en) | 1983-03-17 | 1983-03-17 | Drawing of optical fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59169951A JPS59169951A (en) | 1984-09-26 |
| JPS624333B2 true JPS624333B2 (en) | 1987-01-29 |
Family
ID=12655119
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4312583A Granted JPS59169951A (en) | 1983-03-17 | 1983-03-17 | Drawing of optical fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59169951A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0849232B1 (en) * | 1996-12-17 | 1999-05-26 | Alcatel | Process and apparatus for drawing an optical fibre from a preform |
-
1983
- 1983-03-17 JP JP4312583A patent/JPS59169951A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59169951A (en) | 1984-09-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6319550B1 (en) | Method and apparatus for treating silica granules using porous graphite crucible | |
| EP0032594A2 (en) | Method for producing silica glass | |
| US2285017A (en) | Coating apparatus | |
| JPS624333B2 (en) | ||
| GB806697A (en) | Improvements in or relating to processes for fusing powdered semi-conductor materials | |
| JPS637269A (en) | Sintering furnace | |
| US2328422A (en) | Method for coating bodies with carbon | |
| JPH0640544B2 (en) | Method for forming an oxide layer on a semiconductor substrate | |
| JPH0435399Y2 (en) | ||
| US3341285A (en) | Process for preparing alumina wool | |
| JP2001521871A (en) | Apparatus and method for drawing waveguide fiber | |
| JPH0332502Y2 (en) | ||
| JP2557651B2 (en) | Optical fiber base material manufacturing method | |
| JP2007070189A (en) | Optical fiber drawing device and drawing furnace sealing method | |
| JPH05279070A (en) | Optical fiber drawing furnace | |
| JP2951426B2 (en) | Optical fiber drawing method | |
| JPS59137334A (en) | Manufacturing apparatus of base material for optical fiber | |
| JPH01275443A (en) | Optical fiber drawing furnace | |
| JP3137141B2 (en) | Fluoride optical fiber drawing furnace | |
| JPS60155540A (en) | Heating furnace for drawing optical glass rod | |
| JPS61132534A (en) | Optical fiber drawing method and drawing device | |
| JPS63285185A (en) | Apparatus for pulling up silicon single crystal | |
| JPH026348A (en) | Optical fiber drawing furnace | |
| JPH0532510Y2 (en) | ||
| JPS6360124A (en) | Wire drawing furnace for optical fiber |