JPS60246232A - Manufacture of optical fiber preform - Google Patents

Manufacture of optical fiber preform

Info

Publication number
JPS60246232A
JPS60246232A JP9986984A JP9986984A JPS60246232A JP S60246232 A JPS60246232 A JP S60246232A JP 9986984 A JP9986984 A JP 9986984A JP 9986984 A JP9986984 A JP 9986984A JP S60246232 A JPS60246232 A JP S60246232A
Authority
JP
Japan
Prior art keywords
soot
discharge tube
base material
glass
excess
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
Application number
JP9986984A
Other languages
Japanese (ja)
Inventor
Toshiro Ikuma
伊熊 敏郎
Shozo Morimoto
詔三 森本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Sheet Glass Co Ltd
Original Assignee
Nippon Sheet Glass Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Sheet Glass Co Ltd filed Critical Nippon Sheet Glass Co Ltd
Priority to JP9986984A priority Critical patent/JPS60246232A/en
Publication of JPS60246232A publication Critical patent/JPS60246232A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • C03B37/012Manufacture of preforms for drawing fibres or filaments
    • C03B37/014Manufacture 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]
    • C03B37/0144Means 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)

Abstract

PURPOSE:To keep the inner diameter of an exhaustion tube at nearly definite level, and to obtain an optical fiber preform having uniform characteristics along the longitudinal direction, by oscillating the discharge tube wall after forming a specific porous preform, thereby removing the excess fine glass particles attached to the discharge tube. CONSTITUTION:The core nozzle 1A of the burner 1 is supplied with a glass- forming gas such as SiCl4, GeCl4, etc., and the annular nozzle 1B is supplied with combustible gas, etc. such as O2, H2, etc. The glass-forming gas is hydrolyzed in the oxyhydrogen flame 2 to fine glass particles 3 (soot) depositing on the starting substrate ascending under rotation, to form a porous preform 4. The deposition of the soot on the growth surface 4A is continued, and the excess soot 3A (about 30% of the whole soot) failed to deposit is discharged from the reaction system through the discharge tube 5, and sent to the scrubber, etc. The excess soot 3A accumulated gradually on the inner surface of the discharge tube 5 is removed by applying small vibration 7 to the wall of the discharge tube 5 continuously or intermittently by driving the vibrator 6 attached closely to the outer wall.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は気相軸付法による光フアイバ心材の製造方法の
改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to an improvement in a method for manufacturing an optical fiber core material by a vapor phase axial method.

〔従来技術の説明〕[Description of prior art]

光フアイバ母材の製造方法の/−)として気相軸付法が
知られている。
A vapor phase axial method is known as a method for manufacturing optical fiber base materials.

この気相軸付法テ(」、5ICJ4 、GeC1,1”
3のガラス形成原料ガスを酸素および水素を含むi11
燃ガガス燃焼バーナーに供給し、火炎中でこれらガラス
形成原料を加水分解反+1’[、、させること1よって
ガラス微粒子(以下型K[スート1とよふ)を生成12
、棒状の出発基材の先端からその軸方向1前記スートを
付着成長させることによって略円II状の多孔質母材を
得た後、この多孔FiI母材を高温で加熱焼結して透明
なガラス[Jノドとする。
This gas phase axis method (", 5ICJ4, GeC1,1"
I11 containing oxygen and hydrogen
Gas is supplied to a combustion burner and these glass forming raw materials are hydrolyzed in a flame to produce glass fine particles (hereinafter referred to as type K [soot 1]).
After obtaining a porous base material in the shape of a circle II by depositing and growing the soot in the axial direction from the tip of a rod-shaped starting base material, this porous FiI base material is heated and sintered at a high temperature to form a transparent material. Glass [J throat.

1記透明ガラスロッドを細径に加熱台IL伸4−ること
により光伝送ファイバを得ることができる。1述した気
相軸fJ法は、ガラスバイブの内(lUj V(スlを
堆積する内イ」法あるいはガラスu]l゛の外周にスー
トを堆積さセる外付法等の他の多什質It r4成形方
法に比べて長さの制約が少ないという大きな利点があり
、超長尺ファイバの製f1も検111されている。
1. An optical transmission fiber can be obtained by IL-stretching the transparent glass rod to a small diameter on a heating table. The vapor axis fJ method described in 1 can be used in many other ways, such as the inside method of depositing soot inside a glass vibrator or the external method of depositing soot on the outer periphery of the glass vibrator. It has the great advantage that there are fewer restrictions on length compared to the high-quality Itr4 forming method, and the production of ultra-long fibers f1 has also been investigated.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

気相軸付法においては、火炎加水分解で生成するスート
は必ずしも全てが多孔質母材に堆積するわけではなく、
その30%前後は排ガスとともに、反応室に接続された
排出管を通してスクラバー等の排ガス処理装置に導かれ
る。このため排出管内には排ガス中に混在する余剰スー
トが付着し、排出管の実効的内径が経時的に変化するた
め排気量や反応部の圧力が変動し、それに伴ないバーナ
からのスート流の方向も微妙VC揺れ動くことになる。
In the gas-phase axial method, not all of the soot generated by flame hydrolysis is deposited on the porous base material;
Approximately 30% of the exhaust gas is led to an exhaust gas treatment device such as a scrubber through an exhaust pipe connected to the reaction chamber. For this reason, excess soot mixed in the exhaust gas adheres to the inside of the exhaust pipe, and the effective inner diameter of the exhaust pipe changes over time, causing fluctuations in the exhaust volume and pressure in the reaction section, which in turn causes the soot flow from the burner to change. The direction of VC will also fluctuate slightly.

このように多孔質母材に向うスート流の流れ方向が不安
定であると、生成される多孔質母材の特性が長さ方向に
不均一になる。L記問題の対策として排気量を一定に保
つ方法や、反応部の圧力を測定し排気量を制御すること
により反応部の圧力を一定に保つ方法などが提案されて
いる。しかしながら排出管に付着するスートの厚みは必
ずしも均一にならないため排ガス流の中心は経時的に変
動すること、および反応部の内圧を一定に保つても排出
管の実効的内径が変化することに起因1.て排ガスの流
速が大きく変動するという問題がある。
If the flow direction of the soot flow toward the porous base material is unstable in this way, the properties of the generated porous base material will be non-uniform in the length direction. As a countermeasure to the L problem, a method of keeping the exhaust volume constant, and a method of keeping the pressure of the reaction part constant by measuring the pressure of the reaction part and controlling the exhaust volume have been proposed. However, the thickness of the soot adhering to the exhaust pipe is not necessarily uniform, so the center of the exhaust gas flow changes over time, and even if the internal pressure of the reaction section is kept constant, the effective inner diameter of the exhaust pipe changes. 1. There is a problem in that the flow velocity of exhaust gas fluctuates greatly.

このような排気系の乱れ(」母材成長面のn、A rV
や、スート流と母材成長面の位I?j関係等に経時的な
乱れを与え、その結果長さ方向に安定な特性をイI4る
多孔質母材を作成することは困麺になる。
Such turbulence in the exhaust system (n of the base metal growth surface, A rV
What about the soot flow and base material growth? It is difficult to create a porous base material that has stable properties in the length direction by disturbing the j relationship over time.

特に最近開発に注力されている尤−ノアイバ母材の高速
合成においては原料供給量が増大し反応系外に排出され
るスート量も多量であるため、1.述した問題は一層重
大になってきている。
In particular, in the high-speed synthesis of the Noiba base material, which has been a focus of recent development, the amount of raw materials supplied increases and the amount of soot discharged outside the reaction system is also large. The problems mentioned are becoming more and more important.

〔発明の目的〕[Purpose of the invention]

本発明の目的は気相軸付法において、反応糸から排出さ
れる余剰スートの付着による排出管の実効的内径の経時
変化を極力無くすることにより、燃焼バーナからのスー
ト流を安定させ、長さ方向に安定した特性を有する光フ
アイバ母材を製造−する方法を提供することにある。
The purpose of the present invention is to stabilize the soot flow from the combustion burner in the vapor phase shafting method by eliminating as much as possible the change in the effective inner diameter of the discharge pipe over time due to the adhesion of excess soot discharged from the reaction yarn. An object of the present invention is to provide a method for manufacturing an optical fiber preform having stable properties in the transverse direction.

〔発明の概要〕[Summary of the invention]

1紀の目的を達成する本発明方法は、揮発性のガラス形
成原料を火炎中で反応させることにより得られるガラス
微粒子を基材に堆積させて多孔質母材を成形した後、こ
の多孔質母材を加熱焼結して透明ガラス化する光フアイ
バ母材の製造方法において、反応系外へ余剰ガラス微粒
子を導く排出管に付着するガラス微粒子を、前記堆積処
理の間連続的または間けつ的に除去することを要旨とし
ている。
The method of the present invention which achieves the first objective is to deposit glass fine particles obtained by reacting volatile glass-forming raw materials in a flame on a base material to form a porous base material, and then to form a porous base material. In a method for producing an optical fiber base material in which a material is heated and sintered to make it transparent, glass particles adhering to a discharge pipe that guides excess glass particles out of the reaction system are removed continuously or intermittently during the deposition process. The purpose is to remove it.

〔発明の作用効果〕[Function and effect of the invention]

上述した方法によれば、排出管内面に付着する余剰スー
トが多孔5を母材の成形処理の間常時除去されるため排
出管の実効的内径はけば一定に保持され、したがって前
述した圧力制御あるいは排気量制御と組み合せることに
より燃焼バーナからのスート流の乱れを従来に比して小
さい範囲に抑制することができ、長さ方向に特性が均一
な多孔質母材を製造することができる。
According to the above-mentioned method, the excess soot adhering to the inner surface of the discharge pipe is constantly removed during the molding process of the base material through the pores 5, so that the effective inner diameter of the discharge pipe is kept constant. Alternatively, by combining it with displacement control, it is possible to suppress the turbulence of the soot flow from the combustion burner to a smaller range than before, and it is possible to manufacture a porous base material with uniform properties in the length direction. .

〔実 施 例〕〔Example〕

以下本発明を図面に示した実施例について詳細に説明す
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to embodiments shown in the drawings.

図において/はバーナであり、このバーナ/の中心/ス
ル部/AKS]Ce4.GeCe4等ノ1f−yス形成
原料ガスが01給され、また中心ノズル部/Aを囲む環
状/ズル部/BK酸素、水素等の可燃ガスおよび必要に
応じてアルゴンガス等の不活性ガスが供給される。上2
のガラス形成原料はバーナ/で生成される酸水素火炎λ
中で加水分解反応によりスー)JK転化し、このスート
3は図外上方にあるl111転しながら上昇する出発基
材」−に堆積して多孔質母材qが生成され、以後母材の
成長面4’AK順次堆積していく。多孔質母材lに堆積
し1(か、)だ余剰スー)JAは排出管Sで反応系外に
導かれ、スクラバ等の排ガス処理設備へ送られる。そし
て従来技術では第3図に示すように排出管Sを辿る余剰
スートJAが時間の経過とともに排出管Sの内面に付着
堆積して前述の問題を生じる。
In the figure, / is a burner, and the center of this burner/through part/AKS]Ce4. 1f-y gas forming raw material gas such as GeCe4 is supplied, and combustible gases such as oxygen and hydrogen and inert gases such as argon gas are supplied as necessary. be done. Top 2
The glass forming raw material is the oxyhydrogen flame λ generated in the burner/
The soot 3 is converted into JK by a hydrolysis reaction, and this soot 3 is deposited on the starting base material (not shown) which rises while rotating, producing a porous base material q, and thereafter the growth of the base material. It is deposited sequentially on surface 4'AK. The excess soot (1) JA deposited on the porous base material L is led out of the reaction system through a discharge pipe S and sent to exhaust gas treatment equipment such as a scrubber. In the prior art, as shown in FIG. 3, excess soot JA following the discharge pipe S adheres and accumulates on the inner surface of the discharge pipe S over time, causing the above-mentioned problem.

そこで本実施例では排出管の外壁に密着して娠動子乙を
取りつけ、この振動f−乙を駆動して排出管壁Ky&小
振動7全連続的または間(1つ的にりλる。これにより
排出管の入[1端あるいは内壁面に余剰スー13Aが付
着したとしてもすぐKIkRり落とされ従来のように厚
い層に堆積することはない。
Therefore, in the present embodiment, the impeller A is attached in close contact with the outer wall of the discharge pipe, and this vibration f-B is driven to generate the discharge pipe wall Ky and small vibrations 7 either continuously or intermittently (one time λ). As a result, even if excess soot 13A adheres to the inlet end or the inner wall surface of the discharge pipe, the KIkR immediately falls off and does not accumulate in a thick layer as in the conventional case.

したがって排出管jの実効内径は常時一定に保持され、
通過する気流の流速は一定に保たれる。
Therefore, the effective inner diameter of the discharge pipe j is always kept constant,
The flow rate of the passing airflow remains constant.

これにより多孔質母材4IVC堆積する有効なスートの
流れは母材の生成の全期間を通して流速が安定しており
、母材長さ方向の特性を高度に均一化することができる
As a result, the effective soot flow for depositing the porous base material 4IVC has a stable flow rate throughout the entire period of base material formation, and the properties in the longitudinal direction of the base material can be made highly uniform.

以」−に説明した実施例では排出管壁に振動を与えて付
着スートを除去するようにしたが、本発明方法はスート
除去の具体的方法について何ら制限するものではない。
In the embodiments described below, the attached soot is removed by applying vibration to the wall of the discharge pipe, but the method of the present invention is not intended to limit the specific method of soot removal.

例えば第2図に示すように排出管Sの出1]側から掻き
落し部材ざを入れ込み、この掻き落し部材ざを排出管内
壁に接触させた状態で適宜駆動装置11により排出領S
の長さ方向および管周方向に移動させて付着するスート
を掻き落すようにしてもよい。
For example, as shown in FIG. 2, a scraping member groove is inserted from the outlet 1 side of the discharge pipe S, and with the scraping member groove in contact with the inner wall of the discharge pipe, the drive device 11 is operated as appropriate to discharge the discharge area S.
The attached soot may be scraped off by moving the tube in the longitudinal direction and circumferential direction.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の一実施例を示す縦断面図、第2図は本
発明の他の実施例を示す縦断面図、第3図は従来の状態
を示す要部断面図である。 (7) /0.。バーナ 2.+・火炎 3・・0スート 3A・・・余剰スー1q・・・多孔質
母材 qA・・・成長面S・・・排出管 乙・・・振動
子 ざ・・・掻き落し部材 (g) 第1図 小
FIG. 1 is a longitudinal sectional view showing one embodiment of the present invention, FIG. 2 is a longitudinal sectional view showing another embodiment of the invention, and FIG. 3 is a sectional view of essential parts showing a conventional state. (7) /0. . Burner 2. +・Flame 3...0 soot 3A...excess soot 1q...porous base material qA...growth surface S...discharge pipe B...vibrator zone...scraping member (g) Figure 1 Small

Claims (1)

【特許請求の範囲】[Claims] (1)揮発性のガラス形成原料を火炎中で反応させるこ
とにより得られるガラス微粒子を基材に堆積させて多孔
質母材を成形した後、この多孔質母材を加熱焼結して透
明ガラス化する光7アイバ母材の製造方法において、反
応系外へ余剰ガラス微粒子を導く排出管に付着するガラ
ス微粒子を、前記堆積処理の間連続的または間けつ的に
除去することを特徴とする光フアイバ母材の製造方法。 (2、特許請求の範囲第7項において、排出管に付着も
するガラス微粒子の除去を、排出管壁に振動を与えるこ
とにより行なう光フアイバ母材の製造方法。
(1) Glass particles obtained by reacting volatile glass-forming raw materials in a flame are deposited on a base material to form a porous base material, and then this porous base material is heated and sintered to create a transparent glass. 7. A method for producing an Ivar base material, characterized in that glass particles adhering to a discharge pipe that guides excess glass particles out of the reaction system are removed continuously or intermittently during the deposition process. Method for manufacturing fiber matrix. (2. The method for manufacturing an optical fiber base material according to claim 7, wherein the removal of glass particles also adhering to the discharge tube is carried out by applying vibration to the discharge tube wall.
JP9986984A 1984-05-18 1984-05-18 Manufacture of optical fiber preform Pending JPS60246232A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9986984A JPS60246232A (en) 1984-05-18 1984-05-18 Manufacture of optical fiber preform

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9986984A JPS60246232A (en) 1984-05-18 1984-05-18 Manufacture of optical fiber preform

Publications (1)

Publication Number Publication Date
JPS60246232A true JPS60246232A (en) 1985-12-05

Family

ID=14258812

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9986984A Pending JPS60246232A (en) 1984-05-18 1984-05-18 Manufacture of optical fiber preform

Country Status (1)

Country Link
JP (1) JPS60246232A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5717439A (en) * 1980-07-04 1982-01-29 Hitachi Ltd Manufacture of base material for optical fiber
JPS5752538B2 (en) * 1974-08-14 1982-11-08
JPS6041539A (en) * 1983-08-16 1985-03-05 Sumitomo Electric Ind Ltd Apparatus for removing automatically deposited product
JPS6041537A (en) * 1983-08-16 1985-03-05 Sumitomo Electric Ind Ltd Apparatus for removing automatically deposited product
JPS6041540A (en) * 1983-08-16 1985-03-05 Sumitomo Electric Ind Ltd Apparatus for removing automatically deposited product

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5752538B2 (en) * 1974-08-14 1982-11-08
JPS5717439A (en) * 1980-07-04 1982-01-29 Hitachi Ltd Manufacture of base material for optical fiber
JPS6041539A (en) * 1983-08-16 1985-03-05 Sumitomo Electric Ind Ltd Apparatus for removing automatically deposited product
JPS6041537A (en) * 1983-08-16 1985-03-05 Sumitomo Electric Ind Ltd Apparatus for removing automatically deposited product
JPS6041540A (en) * 1983-08-16 1985-03-05 Sumitomo Electric Ind Ltd Apparatus for removing automatically deposited product

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