JPS6232139B2 - - Google Patents
Info
- Publication number
- JPS6232139B2 JPS6232139B2 JP50678A JP50678A JPS6232139B2 JP S6232139 B2 JPS6232139 B2 JP S6232139B2 JP 50678 A JP50678 A JP 50678A JP 50678 A JP50678 A JP 50678A JP S6232139 B2 JPS6232139 B2 JP S6232139B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction vessel
- exhaust
- burner
- optical fiber
- valve
- 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
- C03B37/012—Manufacture of preforms for drawing fibres or filaments
- C03B37/014—Manufacture of preforms for drawing fibres or filaments made entirely or partially by chemical means, e.g. vapour phase deposition of bulk porous glass either by outside vapour deposition [OVD], or by outside vapour phase oxidation [OVPO] or by vapour axial deposition [VAD]
- C03B37/0144—Means for after-treatment or catching of worked reactant gases
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General 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】
本発明は通信用光フアイバ用母材の製造装置に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for manufacturing a preform for communication optical fiber.
第1図は従来のこの種装置の断面図で、水素、
メタン、プロパンなどの可燃性ガスを酸素と共に
燃焼させるバーナ10に、SiCl4,GeCl4,BCl3,
PCl3,AlCl3,GaCl3などのようなSi,Ge,B,
P,Al,Gaなどの化合物ガラス原料を吹き込
み、火炎中でガラス微粒子を合成し、これを回転
しながら上方に移動する石英ガラスなどの耐火物
で作られた出発棒11の一端に吹き付け、堆積さ
せて、棒状に多孔質ガラス棒12を成長させる。
このガラス合成反応、堆積を行う部分は外気によ
る多孔質ガラスの汚染を防止するために反応容器
13の中で行う。合成反応によつて発生する水蒸
気、塩素、塩化水素などのガスは、排気口14よ
り排出される。 Figure 1 is a cross-sectional view of a conventional device of this type.
A burner 10 that burns flammable gases such as methane and propane together with oxygen contains SiCl 4 , GeCl 4 , BCl 3 ,
Si, Ge, B, such as PCl 3 , AlCl 3 , GaCl 3 etc.
Compound glass raw materials such as P, Al, and Ga are injected to synthesize glass fine particles in a flame, which are then blown onto one end of the starting rod 11 made of refractory material such as quartz glass, which moves upward while rotating, and is deposited. This causes the porous glass rod 12 to grow into a rod shape.
The glass synthesis reaction and deposition portions are performed in a reaction vessel 13 in order to prevent the porous glass from being contaminated by outside air. Gases such as water vapor, chlorine, and hydrogen chloride generated by the synthesis reaction are exhausted from the exhaust port 14.
このようにして作られた多孔質ガラスは、出発
材と同軸上に設置された加熱炉15で加熱溶融、
脱泡し、透明な光フアイバ母材またはガラス棒と
する。これらの工程は連続的に行われる。 The porous glass thus produced is heated and melted in a heating furnace 15 installed coaxially with the starting material.
Degassed and made into a transparent optical fiber base material or glass rod. These steps are performed continuously.
この従来の装置では、反応容器からの排気は自
然排気または単なる強制排気によつていたので、
反応容器内の圧力が変動すると、ガラス微粒子を
合成する火炎が不安定となり、多孔質ガラス棒の
先端に付着するガラス微粒子の堆積率が変わり、
作られる多孔質ガラス棒の外径が変動したり、多
孔質体の密度が変動するという問題があつた。 In this conventional device, exhaust from the reaction vessel was by natural exhaust or simply forced exhaust;
When the pressure inside the reaction vessel fluctuates, the flame that synthesizes the glass particles becomes unstable, and the deposition rate of the glass particles that adhere to the tip of the porous glass rod changes.
There were problems in that the outer diameter of the porous glass rod produced varied and the density of the porous body varied.
反応容器内の圧力変動の原因としては、外部気
圧の変化、バーナへの供給ガス量の変動、バーナ
先端部へのガラス微粒子の付着等がある。 Causes of pressure fluctuations within the reaction vessel include changes in external atmospheric pressure, fluctuations in the amount of gas supplied to the burner, and adhesion of glass particles to the tip of the burner.
本発明は前述の問題を解決するため、排気口1
4から排出されるガスの流量を一定にし、安定な
条件で多孔質ガラスを成長させることにより、均
一な寸法を有する多孔質ガラスまたは透明ガラス
棒を製造しようとするものである。以下図面によ
り本発明を詳細に説明する。 In order to solve the above-mentioned problem, the present invention provides an exhaust port 1
By keeping the flow rate of the gas discharged from 4 constant and growing porous glass under stable conditions, it is attempted to produce porous glass or transparent glass rods having uniform dimensions. The present invention will be explained in detail below with reference to the drawings.
第2図は本発明の一実施例図で、20はバー
ナ、21は出発棒、22は多孔質ガラス棒、23
は反応容器、24は排気口、25は加熱炉であ
る。第2図において、前述のように、多孔質ガラ
ス棒を成長させると共に、排気口24に接続され
た弁26を置き、弁26の開閉度を同じ配管系中
に置かれたガス流計測装置27によつて、ガス流
量を測定し、この信号を増幅器28で増幅し、弁
を開閉するモータ29を駆動する。排気ガス流量
が増加した時は弁26が閉じる方向に、逆に流量
が減少した時は弁26が開く方向に、モータ29
が動くようにしてある。このような回路で、増幅
器28により、排気ガス流量が最初に設定した一
定のガス流量に保たれる。ガラス合成反応容器2
3は、前述のような排気ガス流量を一定値に制御
する代わりに、反応容器23の内部圧力を一定に
保つことによつても、多孔質ガラスの外径は一定
の太さに保つことができる。 FIG. 2 shows an embodiment of the present invention, in which 20 is a burner, 21 is a starting rod, 22 is a porous glass rod, 23
24 is an exhaust port, and 25 is a heating furnace. In FIG. 2, as described above, a porous glass rod is grown, a valve 26 connected to an exhaust port 24 is placed, and the opening/closing degree of the valve 26 is measured by a gas flow measuring device 27 placed in the same piping system. , the gas flow rate is measured, and this signal is amplified by an amplifier 28 to drive a motor 29 that opens and closes the valve. The motor 29 moves the valve 26 in the direction in which it closes when the exhaust gas flow rate increases, and in the direction in which the valve 26 opens when the flow rate decreases.
is set to move. In such a circuit, the amplifier 28 maintains the exhaust gas flow rate at an initially set constant gas flow rate. Glass synthesis reaction vessel 2
3, the outer diameter of the porous glass can be kept constant by keeping the internal pressure of the reaction vessel 23 constant instead of controlling the exhaust gas flow rate to a constant value as described above. can.
30は反応容器に取り付けられた圧力検知器
で、反応容器内の圧力を電気信号として取り出
し、前述の実施例と同様の増幅器28に入れ、設
定圧力より高い場合には、弁26が開くようにモ
ータ29を駆動させ、逆に低い場合には弁26を
閉じるようにモータ29を駆動させる。 Reference numeral 30 denotes a pressure sensor attached to the reaction vessel, which picks up the pressure inside the reaction vessel as an electrical signal and inputs it into the same amplifier 28 as in the previous embodiment, so that if the pressure is higher than the set pressure, the valve 26 is opened. The motor 29 is driven, and if the temperature is low, the motor 29 is driven to close the valve 26.
以上説明したように、本発明の光フアイバ用母
材の製造装置は、排気口に接続された弁を制御す
ることにより、ガラス合成反応によつて生成され
た水蒸気、塩素、塩化水素などの排気量を一定に
保ち、反応容器23内のガス流を安定化して、多
孔質ガラス棒22の成長を一定状態で行うので、
多孔質ガラス棒22の外径、密度等を均質化する
ことができる。 As explained above, the optical fiber base material manufacturing apparatus of the present invention exhausts water vapor, chlorine, hydrogen chloride, etc. generated by the glass synthesis reaction by controlling the valve connected to the exhaust port. Since the amount is kept constant and the gas flow inside the reaction vessel 23 is stabilized, the growth of the porous glass rod 22 is performed in a constant state.
The outer diameter, density, etc. of the porous glass rod 22 can be made uniform.
第1図は従来の光フアイバ用母材の製造装置の
断面図、第2図は本発明の一実施例図である。
20…バーナー、21…出発棒、22…多孔質
ガラス棒、23…反応容器、24…排気口、25
…加熱炉、26…弁、27…ガス流計測装置、2
8…増幅器、29…モータ、30…圧力検知器。
FIG. 1 is a sectional view of a conventional optical fiber base material manufacturing apparatus, and FIG. 2 is a diagram showing an embodiment of the present invention. 20...Burner, 21...Starting rod, 22...Porous glass rod, 23...Reaction container, 24...Exhaust port, 25
...Heating furnace, 26...Valve, 27...Gas flow measuring device, 2
8...Amplifier, 29...Motor, 30...Pressure detector.
Claims (1)
能に保持された出発棒と、該出発棒の先端にガラ
ス微粒子を堆積させるためのガラス微粒子合成用
バーナと、該バーナへ化合物ガラス原料および可
燃性ガス、酸素ガスを供給する供給系と、前記反
応容器に備えられ、反応容器内で生ずるガスを排
出する排気系を備えた光フアイバ用母材の製造装
置において、該排気系が排気系内に設置した排気
ガス流量計もしくは反応容器に設置した圧力検知
器に連動して排気量を制御し、反応容器内の圧力
を一定に保つ弁を備えたことを特徴とする光フア
イバ用母材の製造装置。1. A reaction vessel, a starting rod rotatably held in the reaction vessel so that it can be pulled up, a burner for synthesizing glass particles for depositing glass particles on the tip of the starting rod, and a compound glass raw material and a combustible material being fed to the burner. In an apparatus for manufacturing an optical fiber base material, the apparatus includes a supply system for supplying reactive gas and oxygen gas, and an exhaust system that is provided in the reaction vessel and exhausts gas generated in the reaction vessel, wherein the exhaust system is provided in the exhaust system. A base material for optical fiber, characterized in that it is equipped with a valve that controls the exhaust amount in conjunction with an exhaust gas flow meter installed in the chamber or a pressure detector installed in the reaction vessel, and keeps the pressure in the reaction vessel constant. Manufacturing equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50678A JPS5494049A (en) | 1978-01-09 | 1978-01-09 | Mother material producing apparatus for optical fibers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50678A JPS5494049A (en) | 1978-01-09 | 1978-01-09 | Mother material producing apparatus for optical fibers |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5494049A JPS5494049A (en) | 1979-07-25 |
| JPS6232139B2 true JPS6232139B2 (en) | 1987-07-13 |
Family
ID=11475643
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50678A Granted JPS5494049A (en) | 1978-01-09 | 1978-01-09 | Mother material producing apparatus for optical fibers |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5494049A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS642940U (en) * | 1987-06-25 | 1989-01-10 | ||
| JPH01151548U (en) * | 1988-03-31 | 1989-10-19 | ||
| JPH0218847U (en) * | 1988-07-21 | 1990-02-07 | ||
| JPH0460056A (en) * | 1990-06-28 | 1992-02-26 | Asahi Utsudo Tec Kk | Sound insulating wooden floor material |
| JPH0460057A (en) * | 1990-06-28 | 1992-02-26 | Asahi Utsudo Tec Kk | Sound insulating wooden floor material |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5626737A (en) * | 1979-08-14 | 1981-03-14 | Nippon Telegr & Teleph Corp <Ntt> | Exhaust adjuster for optical fiber base material manufacturing apparatus |
-
1978
- 1978-01-09 JP JP50678A patent/JPS5494049A/en active Granted
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS642940U (en) * | 1987-06-25 | 1989-01-10 | ||
| JPH01151548U (en) * | 1988-03-31 | 1989-10-19 | ||
| JPH0218847U (en) * | 1988-07-21 | 1990-02-07 | ||
| JPH0460056A (en) * | 1990-06-28 | 1992-02-26 | Asahi Utsudo Tec Kk | Sound insulating wooden floor material |
| JPH0460057A (en) * | 1990-06-28 | 1992-02-26 | Asahi Utsudo Tec Kk | Sound insulating wooden floor material |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5494049A (en) | 1979-07-25 |
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