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JPH033617B2 - - Google Patents
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JPH033617B2 - - Google Patents

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Publication number
JPH033617B2
JPH033617B2 JP4245483A JP4245483A JPH033617B2 JP H033617 B2 JPH033617 B2 JP H033617B2 JP 4245483 A JP4245483 A JP 4245483A JP 4245483 A JP4245483 A JP 4245483A JP H033617 B2 JPH033617 B2 JP H033617B2
Authority
JP
Japan
Prior art keywords
growth rate
torch
base material
glass
porous glass
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 - Lifetime
Application number
JP4245483A
Other languages
Japanese (ja)
Other versions
JPS59169950A (en
Inventor
Fumiaki Hanawa
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.)
NTT Inc
Original Assignee
Nippon Telegraph and Telephone Corp
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 Telegraph and Telephone Corp filed Critical Nippon Telegraph and Telephone Corp
Priority to JP4245483A priority Critical patent/JPS59169950A/en
Publication of JPS59169950A publication Critical patent/JPS59169950A/en
Publication of JPH033617B2 publication Critical patent/JPH033617B2/ja
Granted 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]
    • C03B37/01413Reactant delivery systems
    • C03B37/0142Reactant deposition burners
    • 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]
    • C03B37/01486Means for supporting, rotating or translating the preforms being formed, e.g. lathes
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/42Assembly details; Material or dimensions of burner; Manifolds or supports
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/60Relationship between burner and deposit, e.g. position
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/70Control measures

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、気相軸付け法による光フアイバ用母
材の製造方法において、任意の屈折率分布を再現
性よく製造し、光学特性のロツト間変動を改善す
ることを目的とした光フアイバ用母材の製造方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention aims to manufacture an arbitrary refractive index distribution with good reproducibility and improve lot-to-lot variations in optical properties in a method for manufacturing an optical fiber base material using a vapor phase axising method. The present invention relates to a method for manufacturing the target optical fiber base material.

気相軸付け法(以下、VAD法と称す。)は
SiCl4、GeCl4、POCl3などのガラス形成原料を微
粒子合成トーチ(以下、トーチと称す。)に送り
込み、トーチの吹出し口の前方に形成される酸水
素火炎によつて火炎加水分解反応せしめてSiO2
GeO2、P2O5などのガラス微粒子を生成し、これ
を回転する棒状出発材の片端面に吹き付けて棒状
出発材の回転軸方向に堆積成長させて多孔質ガラ
ス体を形成した後、連続的にまたは非連続的に高
温炉に挿入させて脱泡透明ガラス化して光フアイ
バ用母材を得る方法である。この方法は、長尺、
大型の光フアイバ用母材が連続的に製造可能であ
るし、光学的特性においては低損失、広帯域な特
性を有する光フアイバが得られている。しかしな
がら、VAD法によつて広帯域光フアイバを製造
するには、多孔質母材製造時に屈折率分布を最適
形状にしなければならない。分布係数αと帯域の
関係を示す第1図によれば、分布係数α=1.99±
0.02の時が最適屈折率分布となるが、最適α値か
ら若干ずれると帯域特性は著しく劣化する。従つ
て、特に広帯域光フアイバを製造するには、分布
係数α=2となるように多孔質母材の製造条件を
探索しなければならない。また、広帯域光フアイ
バ用母材を再現性良く製造する(歩留りを向上さ
せる)には、最適製造条件を常に一定に保ちなが
ら多孔質母材を製造しなければならない。
The vapor phase axial method (hereinafter referred to as the VAD method) is
Glass-forming raw materials such as SiCl 4 , GeCl 4 , and POCl 3 are fed into a fine particle synthesis torch (hereinafter referred to as the torch), and a flame hydrolysis reaction is caused by an oxyhydrogen flame formed in front of the torch's outlet. SiO2 ,
Glass particles such as GeO 2 and P 2 O 5 are generated, and these are sprayed onto one end surface of a rotating rod-shaped starting material to deposit and grow in the direction of the rotational axis of the rod-shaped starting material to form a porous glass body. In this method, the fiber is inserted into a high-temperature furnace either continuously or discontinuously to remove bubbles and turn it into transparent glass to obtain a preform for optical fiber. This method uses long
Large-sized optical fiber preforms can be manufactured continuously, and optical fibers with low loss and broadband optical properties can be obtained. However, in order to manufacture a broadband optical fiber by the VAD method, the refractive index distribution must be optimized during manufacturing of the porous base material. According to Figure 1, which shows the relationship between distribution coefficient α and band, distribution coefficient α=1.99±
When the α value is 0.02, the optimum refractive index distribution is obtained, but if there is a slight deviation from the optimum α value, the band characteristics deteriorate significantly. Therefore, in order to manufacture a broadband optical fiber in particular, it is necessary to search for manufacturing conditions for the porous base material so that the distribution coefficient α=2. Furthermore, in order to manufacture a broadband optical fiber preform with good reproducibility (improve the yield), the porous preform must be manufactured while keeping the optimum manufacturing conditions constant.

屈折率分布を制御するための製造条件として
は、 (1) トーチに導入する原料ガス(SiCl4、GeCl4)、
H2ガス、O2ガス、Arガスを制御する。
The manufacturing conditions for controlling the refractive index distribution include (1) raw material gases (SiCl 4 , GeCl 4 ) introduced into the torch;
Controls H2 gas, O2 gas, Ar gas.

(2) 多孔質母材成長面の温度分布を制御する。(2) Control the temperature distribution on the growth surface of the porous base material.

(3) 使用するトーチの設置位置および角度を最適
にする。
(3) Optimize the installation position and angle of the torch to be used.

があるが、以上の3点を調整することにより最適
屈折率分布(α=2)を有する母材を製造するこ
とができる。従つて、広帯域用母材を再現性良く
製造するには、(1)、(2)、(3)により得られた最適条
件を常に一定に保てばよい訳であるが、(1)の条件
はマスフローメーター・コントローラーで精密に
制御できるとともに一定条件に保つことができる
ものの、(2)、(3)の条件、特に(3)の条件については
最適条件は見出せるが、これを一定に保つのが難
かしい。現状のVAD技術においては、(3)の最適
条件を一定に保つことが困難なことに原因して帯
域特性が大きなバラツキを生じる結果となつてい
る。
However, by adjusting the above three points, a base material having an optimal refractive index distribution (α=2) can be manufactured. Therefore, in order to manufacture broadband base materials with good reproducibility, it is sufficient to keep the optimal conditions obtained in (1), (2), and (3) constant. Although the conditions can be precisely controlled and kept constant using a mass flow meter/controller, optimal conditions can be found for conditions (2) and (3), especially condition (3), but these conditions cannot be kept constant. It's difficult. In the current VAD technology, it is difficult to keep the optimal condition (3) constant, which results in large variations in band characteristics.

(3)の最適条件を一定にすることが困難なのは以
下に述べる理由による。すなわち (イ) 通常使用されてちるトーチは石英ガラス製で
あるため、トーチ外観が真円のものが得難く、
従つてトーチを洗浄する等においてトーチ用ホ
ルダーからトーチを取りはずし、再度トーチを
取り付ける際にもとの位置(最適位置)より若
干ずれてしまう。このずれはトーチ用ホルダー
の精度によつても生ずる。
The reason why it is difficult to keep the optimum condition (3) constant is as follows. In other words, (a) Since the commonly used chiru torches are made of quartz glass, it is difficult to obtain a torch with a perfectly round appearance.
Therefore, when the torch is removed from the torch holder when cleaning the torch, etc., and when the torch is reattached, the torch will be slightly shifted from its original position (optimal position). This deviation also occurs due to the accuracy of the torch holder.

(ロ) 反応容器の排気口からの排気量の変動によ
り、トーチの前方に形成される火炎流の中心軸
がわずかに移動し、最適条件からずれてしま
う。この現象はトーチが最適位置に設置されて
いても((ロ)で述べた現象が生じなくとも)生ず
る。けだし排気量の変動は、余剰ガラス微粒子
が排気口の内面に付着するために長時間の間に
少しずつ変動するからである。
(b) Due to fluctuations in the amount of exhaust from the exhaust port of the reaction vessel, the central axis of the flame flow formed in front of the torch shifts slightly, causing deviation from the optimal conditions. This phenomenon occurs even if the torch is installed at the optimal position (even if the phenomenon described in (b) does not occur). This is because the amount of discharged air fluctuates little by little over a long period of time because excess glass particles adhere to the inner surface of the exhaust port.

(ハ) 多孔質母材が成長するに従つて反応容器内部
の圧力が変化し、これに原因して火炎流の中心
軸がわずかに移動し、最適条件からずれてしま
う。この変動は短時間の間に生ずる。
(c) As the porous base material grows, the pressure inside the reaction vessel changes, which causes the central axis of the flame flow to shift slightly and deviate from the optimal conditions. This variation occurs over a short period of time.

以上の(イ)、(ロ)、(ハ)の理由によりトーチの最適位
置および角度、すなわちトーチの前方に形成され
る火炎流の最適中心軸が若干ずれてしまうために
広帯域用母材を再現性良く製造するのが困難であ
る。また、最適位置かどうかはVAD法の場合、
空間的に屈折率分布が形成されているため、その
都度測定する技術が確立されておらず、製造した
母材をフアイバ化して帯域特性を測定してみなけ
ればわからないのが実状である。
Due to reasons (a), (b), and (c) above, the optimal position and angle of the torch, that is, the optimal central axis of the flame flow formed in front of the torch, is slightly shifted, so we reproduced the broadband base material. It is difficult to manufacture with good performance. In addition, in the case of VAD method, whether it is the optimal position or not,
Because the refractive index distribution is formed spatially, there is no established technology for measuring it each time, and the reality is that it is impossible to know unless the manufactured base material is made into a fiber and the band characteristics are measured.

本発明は、かかる実状に鑑みて提案されたもの
であつて、トーチの最適位置および角度、すなわ
ち火炎流の中心軸と多孔質母材の中心軸が交わる
点が若干ずれることにより多孔質母材の成長速度
が変化することに着目し、多孔質ガラス体の成長
速度設定部と多孔質ガラス体の成長速度検出部お
よび前後、左右に移動する機能をそなえたトーチ
用ホルダーにより、あらかじめ設定した多孔質ガ
ラス体の成長速度に対して多孔質ガラス体の成長
速度検出吹から検出される速度が等しくなるよう
にトーチ用ホルダーの位置保持し、火炎流の中心
軸と多孔質母材の中心軸が交わる点および角度を
一定となるように制御することを特徴とし、
VAD法における欠点を解決してロツト間変動の
極めて少ない再現性のある光フアイバ用母材の製
造方法を提供せんとする。
The present invention has been proposed in view of the above-mentioned circumstances. Focusing on the fact that the growth rate of the porous glass changes, we use a porous glass growth rate setting section, a porous glass growth rate detection section, and a torch holder that has the ability to move back and forth and left and right to control the growth rate of the preset pores. The torch holder is held in position so that the growth rate detected from the porous glass body is equal to the growth rate of the porous glass body, and the central axis of the flame flow and the central axis of the porous base material are aligned. It is characterized by controlling the intersection point and angle to be constant,
The present invention aims to solve the drawbacks of the VAD method and provide a method for manufacturing an optical fiber base material with extremely low lot-to-lot variation and reproducibility.

以下、図面に示した実施例にもとずき、本発明
に係る光フアイバ用母材の製造方法について説明
する。
Hereinafter, a method for manufacturing an optical fiber base material according to the present invention will be explained based on the embodiments shown in the drawings.

本発明者らは、グレーデツド形光フアイバ用母
材の製造において、まずトーチ(火炎流)と多孔
質ガラス体の成長面の相対的な位置関係に対する
帯域特性のロツト間変動について検討した。この
結果、初期に設定したトーチ(火炎流)と多孔質
ガラス体成長面の位置が約100μmずれることに
より帯域特性が著しく劣化することが明らかにな
つた。このずれは、余剰微粒子を排気する排気口
の流速変化や、反応容器内の圧力変動などによつ
て起こるが、最も著しいのはトーチを洗浄するた
めにトーチ用ホルダーからトーチを取りはずし、
再度取り付ける時である。通常のトーチは石英ガ
ラス製であるため、外観の寸法精度があまりよく
なく、従つて再度の取り付け時に100μm程度、
もしくはそれ以上の位置ずれが容易に生じる。し
かし、トーチもしくはトーチの吹出し口前方に成
形される火炎流と多孔質ガラス体は空間的に配置
されているため、初期の位置設定に対するずれを
測定することが非常に困難であり、これがロツト
間毎の帯域特性劣化の解消に大きな支障となつて
いることが明らかになつた。本発明者らは、上記
問題解決のため更に検討を行なつた結果、多孔質
ガラス体の成長面に対するトーチもしくはトーチ
の前方に成形される火炎流の位置が若干ずれる
と、多孔質ガラス体の成長速度もずれに応じて変
化することを見出した。この現象は、多孔質ガラ
ス体を細く形成する(10mmφ〜15mmφ)単一モー
ド光フアイバ用母材の製造においても同様であ
り、この場合には、上記現象はさらに著しく現わ
れた。
In manufacturing a preform for a graded optical fiber, the present inventors first studied the inter-lot variation in band characteristics with respect to the relative positional relationship between the torch (flame flow) and the growth surface of the porous glass body. As a result, it was revealed that the band characteristics were significantly deteriorated due to a misalignment of approximately 100 μm between the initially set torch (flame flow) and the porous glass growth surface. This deviation occurs due to changes in the flow rate of the exhaust port for exhausting excess particles, pressure fluctuations in the reaction vessel, etc., but the most significant one is when the torch is removed from the torch holder to clean it.
It's time to reinstall it. Ordinary torches are made of quartz glass, so the external dimensional accuracy is not very good, so when reinstalling, the
Or even more misalignment can easily occur. However, because the flame stream and the porous glass body formed in front of the torch or the torch outlet are spatially arranged, it is very difficult to measure deviations from the initial position setting, and this makes it difficult to measure the deviation between lots. It has become clear that this is a major hindrance to eliminating deterioration in band characteristics. As a result of further studies to solve the above problem, the present inventors found that if the position of the torch or the flame stream formed in front of the torch is slightly shifted relative to the growth surface of the porous glass body, the porous glass body We found that the growth rate also changed depending on the shift. This phenomenon is the same in the production of a single-mode optical fiber base material in which a porous glass body is formed into a thin (10 mmφ to 15 mmφ), and in this case, the above-mentioned phenomenon was even more pronounced.

この現象を第2図によつて説明すると、第2図
aはグレーデツド形光フアイバ用母材となる多孔
質ガラス体製造の模式図であつて、1はトーチ、
2は火炎流、3は火炎流の中心部に形成されるガ
ラス微粒子流、4は多孔質ガラス体(直径45mmφ
〜55mmφ)、Aは多孔質ガラス体の回転中心軸、
Bはトーチの中心軸である。第2図bは多孔質ガ
ラス体中心軸Aとトーチ中心軸Bが交差する角度
θを一定にして、トーチ中心軸Bをx方向および
y方向に移動させ、移動距離と多孔質ガラス体の
成長速度の関係を調べた図である。いま第2図a
において、角度θを20゜、火炎流2を形成するH2
ガスを3/min、O2ガスを6/min、ガラス
微粒子流3を形成するSiCl4を40℃に保ちながら
キヤリア−Arガス100c.c./minでバブリングし、
またGeCl4を32℃に保ちながらキヤリア−Arガス
90c.c./minでバブリングして各ガスをトーチ1に
送り込み、約50minφの多孔質ガラス体4を製造
した。これを光フアイバ化したところ帯域特性は
1.2GHz・Kmであつた。つぎに各ガス条件および
角度θを一定にしてトーチ1の中心軸Bをx方向
に移動させた。この結果、移動距離に応じて帯域
特性は劣化し、100μmの移動で、650MHz・Km、
200μmの移動で420MHz・Km、300μmの移動で
360MHz・Kmであつた。またy方向についても同
様な結果が得られた。これらの移動距離と多孔質
ガラス体の成長速度は、第2図bに示した実線の
ような関係であつた。1.2GHz・Kmが得られた時
の成長速度が42mm/hr(図中0点)であるのに対
して、トーチ中心軸をx方向に移動させると成長
速度は上昇し、300μmの移動距離で64mm/hrの
速度となつた。また、y方向に移動させると成長
速度は下降し、300μmの移動距離で20mm/hrと
なつた。図中の点線は単一モード光フアイバ用多
孔質ガラス体を製造した場合の成長速度変化であ
つて、グレーデツト形多孔質ガラス体の速度変化
に較べて、より以上大きく変化した。これら速度
変化の絶対値はトーチの形状や寸法、トーチに送
り込む各ガス流量条件などによつて異なつてくる
が、多孔質ガラス体の成長面に対するトーチの位
置設定が多孔質ガラス体の成長速度および得られ
る光フアイバの帯域特性と密接な関係にあること
が明らかになつた。
This phenomenon will be explained with reference to FIG. 2. FIG. 2a is a schematic diagram of the production of a porous glass body to be used as a base material for graded optical fiber, in which 1 is a torch;
2 is a flame flow, 3 is a glass particle flow formed in the center of the flame flow, and 4 is a porous glass body (diameter 45 mmφ
~55mmφ), A is the rotation center axis of the porous glass body,
B is the central axis of the torch. Figure 2b shows the movement distance and the growth of the porous glass body when the torch center axis B is moved in the x and y directions while keeping the angle θ at which the porous glass body central axis A intersects with the torch central axis B constant. It is a diagram examining the relationship between speeds. Now Figure 2a
, the angle θ is 20°, and H 2 forms flame flow 2.
Gas was bubbled at 3/min, O 2 gas at 6/min, and carrier Ar gas was bubbled at 100 c.c./min while SiCl 4 forming glass particle flow 3 was maintained at 40°C.
Also, while keeping GeCl 4 at 32℃, carrier Ar gas
Each gas was sent into the torch 1 by bubbling at a rate of 90 c.c./min to produce a porous glass body 4 having a diameter of about 50 min. When this was converted into an optical fiber, the band characteristics were
It was 1.2GHz・Km. Next, the central axis B of the torch 1 was moved in the x direction while keeping each gas condition and angle θ constant. As a result, the band characteristics deteriorate depending on the moving distance, and with a movement of 100 μm, 650 MHz・Km,
420MHz Km with 200μm movement, 300μm movement
It was 360MHz/Km. Similar results were also obtained in the y direction. The relationship between these moving distances and the growth rate of the porous glass body was as shown by the solid line shown in FIG. 2b. The growth rate when 1.2GHz/Km was obtained was 42mm/hr (point 0 in the figure), but when the torch center axis was moved in the x direction, the growth rate increased, and with a moving distance of 300μm. The speed was 64mm/hr. Furthermore, when moving in the y direction, the growth rate decreased to 20 mm/hr at a moving distance of 300 μm. The dotted line in the figure shows the change in growth rate when a porous glass body for a single-mode optical fiber was manufactured, which was much larger than the change in the growth rate for a graded porous glass body. The absolute value of these speed changes varies depending on the shape and dimensions of the torch, the flow rate conditions of each gas sent to the torch, etc., but the positioning of the torch relative to the growth surface of the porous glass body changes the growth rate of the porous glass body and It has become clear that there is a close relationship with the band characteristics of the resulting optical fiber.

本発明は以上の検討結果に基づいて行なわれた
ものであり、多孔質ガラス体の製造においてロツ
ト間毎の成長速度が一定となるようにトーチを移
動させるものである。すなわち本発明は、多孔質
ガラス体の任意の成長速度を入力する成長速度設
定器と、製造される多孔質ガラス体の成長速度を
検出する成長速度検出器と、成長速度設定器から
出力される電気信号と成長速度検出器から出力さ
れる電気信号を処理する成長速度制御器および制
御器から出力される電気信号に応じて左右に移動
するトーチ移動装置を具備し、多孔質ガラス体の
成長速度を任意の速度に制御できるようにしたも
のである。したがつて、本発明によれば、良好な
帯域特性が得られる多孔質ガラス体の製造条件に
おいて常に成長速度を一定に保つことができるた
め、帯域特性のロツト間変動を極めて少なくする
ことができる。
The present invention was carried out based on the above study results, and involves moving the torch so that the growth rate from lot to lot is constant during the production of porous glass bodies. That is, the present invention provides a growth rate setter for inputting an arbitrary growth rate of the porous glass body, a growth rate detector for detecting the growth rate of the porous glass body to be manufactured, and a growth rate setter for inputting an arbitrary growth rate of the porous glass body; It is equipped with a growth rate controller that processes electric signals and electric signals output from a growth rate detector, and a torch moving device that moves left and right according to the electric signals output from the controller, and which controls the growth rate of the porous glass body. can be controlled to any speed. Therefore, according to the present invention, the growth rate can always be kept constant under the manufacturing conditions of a porous glass body that provides good band characteristics, so it is possible to extremely reduce lot-to-lot variation in band characteristics. .

第3図は、本発明方法を実施する装置の概略で
あり、5は出発材、6は反応容器、7は排気口、
8は回転装置、9は引上げ用ボールネジ、10は
成長速度(引上げ速度)検出器、11は成長速度
設定器、12は成長速度制御器、13は左右移動
装置、14はトーチ用ホルダーである。いま広帯
域特性が得られた時の多孔質ガラス体成長速度を
速度設定器11に入力して多孔質ガラス体4の製
造を開始し、この時の成長速度を速度検出器10
によつて検出する。検出された速度信号と速度設
定器11から出力された速度信号を成長速度制御
器12によつて比較し、速度設定器11の信号に
対して速度検出器10の信号が小さい(速度が遅
い)場合には、左右移動装置13に取り付けられ
たトーチ用ホルダー14がx方向に移動するよう
に制御器12から移動装置14に信号を送る。ま
た、速度設定器11の信号よりも速度検出器12
の信号が大きい(速度が速い)場合には、トーチ
用ホルダー14がy方向に移動するように移動装
置14に信号を送る。このようにして速度設定器
11から出力された信号と速度検出器10から出
力された信号が等しくなるようにトーチ用ホルダ
ーを移動させることにより、多孔質ガラス体4の
成長面とトーチ1の相対的な位置関係、すなわち
火炎流の中心軸と多孔質母材の中心軸が交わる点
および角度を常に一定にすることができ、従つ
て、従来問題であつた帯域特性のロツト間変動を
極めて少なくすることができるとともに再現性の
よい光フアイバ用母材を製造することができる。
FIG. 3 is a schematic diagram of an apparatus for carrying out the method of the present invention, in which 5 is a starting material, 6 is a reaction vessel, 7 is an exhaust port,
8 is a rotation device, 9 is a ball screw for pulling, 10 is a growth rate (pulling rate) detector, 11 is a growth rate setting device, 12 is a growth rate controller, 13 is a left-right moving device, and 14 is a torch holder. Manufacturing of the porous glass body 4 is started by inputting the growth rate of the porous glass body at which the broadband characteristics have been obtained into the speed setter 11, and the growth rate at this time is inputted to the speed detector 10.
Detected by. The detected speed signal and the speed signal output from the speed setter 11 are compared by the growth speed controller 12, and the signal from the speed detector 10 is smaller than the signal from the speed setter 11 (the speed is slow). In this case, the controller 12 sends a signal to the moving device 14 so that the torch holder 14 attached to the left-right moving device 13 moves in the x direction. In addition, the signal from the speed detector 12 is higher than the signal from the speed setter 11.
When the signal is large (speed is fast), a signal is sent to the moving device 14 so that the torch holder 14 moves in the y direction. In this way, by moving the torch holder so that the signal output from the speed setter 11 and the signal output from the speed detector 10 are equal, the relationship between the growth surface of the porous glass body 4 and the torch 1 is increased. The positional relationship, that is, the point and angle at which the central axis of the flame flow intersects with the central axis of the porous base material, can be kept constant at all times. Therefore, the variation between lots in band characteristics, which was a problem in the past, can be extremely reduced. It is possible to manufacture an optical fiber preform with good reproducibility.

つぎに本発明の具体例について述べると、第2
図の実験で帯域特性1.2GHz・Kmが得られた製造
条件(H2流量、O2流量、SiCl4流量、GeCl4流量)
に各流量を設定し、速度設定器11に42mm/hrの
速度信号を入力して多孔質ガラス体を10本製造し
た。この際、トーチ1をトーチ用ホルダー14か
ら4回取りはずして洗浄した。この結果、多孔質
ガラス体10本の成長速度はいずれも42mm/hrであ
り、また10本の母材をフアイバ化して帯域特性を
測定したところ1.05GHz・Km〜1.2GHz・Kmの範囲
内であつた。比較のため、本発明を実施しなかつ
た場合の10本の帯域特性は460MHz・Km〜1.2G
Hz・Kmの範囲で変動していた。
Next, a specific example of the present invention will be described.
Manufacturing conditions (H 2 flow rate, O 2 flow rate, SiCl 4 flow rate, GeCl 4 flow rate) under which a band characteristic of 1.2 GHz/Km was obtained in the experiment shown in the figure.
Each flow rate was set to , and a speed signal of 42 mm/hr was input to the speed setting device 11 to manufacture 10 porous glass bodies. At this time, the torch 1 was removed from the torch holder 14 four times and washed. As a result, the growth rate of all 10 porous glass bodies was 42 mm/hr, and when the 10 base materials were made into fibers and the band characteristics were measured, they were within the range of 1.05 GHz・Km to 1.2 GHz・Km. It was hot. For comparison, the band characteristics of 10 lines without implementing the present invention are 460MHz・Km ~ 1.2G
It fluctuated in the range of Hz/Km.

なお、本発明によれば、ロツト間変動のみなら
ず長尺多孔質ガラス体の長手方向の特性変動も少
なくすることができる。従来法では、長尺多孔質
ガラス体を製造する際、反応容器内の圧力が時間
経過とともに減少し、従つて多孔質ガラス体成長
面と火炎流の相対的な位置(火炎流の位置がずれ
ることはトーチの中心軸がずれることと同じ現象
である。)がずれて成長速度が変化し、帯域特性
が長手方向に変動する場合があつた。しかし、本
発明の実施例により長尺多孔質ガラス体でも一定
速度で製造することができ、帯域特性の長手方向
の変動を少なくすることができた。
According to the present invention, it is possible to reduce not only the variation between lots but also the variation in the properties of the long porous glass body in the longitudinal direction. In the conventional method, when producing a long porous glass body, the pressure inside the reaction vessel decreases over time, and the relative position of the porous glass body growth surface and the flame flow (the position of the flame flow shifts). This is the same phenomenon as when the center axis of a torch shifts.) This shift causes the growth rate to change and the band characteristics to fluctuate in the longitudinal direction. However, according to the embodiments of the present invention, even a long porous glass body could be manufactured at a constant speed, and fluctuations in the band characteristics in the longitudinal direction could be reduced.

以上、図面に示した実施例にもとずいて詳細に
説明したように、成長速度設定器と成長速度検出
器および前後左右に移動機能をそなえたトーチ用
ホルダーにより任意に設定した成長速度と同じ速
度となるようにトーチ用ホルダーを移動させ、火
炎流の中心軸と多孔質母材の中心軸が交わる点お
よび角度を一定となるように制御して多孔質ガラ
ス体を製造する本発明によれば、従来の問題であ
つた帯域特性のロツト間変動を極めて少なくする
ことができるとともに長尺光フアイバ用母材の長
手方向の特性変動も少なくすることができる利点
がある。
As explained above in detail based on the embodiment shown in the drawings, the growth rate is the same as the growth rate arbitrarily set by the growth rate setting device, the growth rate detector, and the torch holder equipped with the ability to move forward, backward, left, and right. According to the present invention, a porous glass body is manufactured by moving a torch holder so that the speed of the torch holder becomes constant, and controlling the point and angle at which the central axis of the flame flow intersects with the central axis of the porous base material to be constant. For example, there are advantages in that it is possible to extremely reduce inter-lot variation in band characteristics, which has been a problem in the past, and also in that variation in longitudinal characteristics of the base material for a long optical fiber can be reduced.

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

第1図は屈折率分布係数と帯域の関係を示すグ
ラフ、第2図aはグレーデツド形光フアイバ用母
材となる多孔質ガラス体製造の模式図、第2図b
は多孔質ガラス体の成長面に対するトーチの位置
と多孔質ガラス体成長速度の関係を表わしたグラ
フ、第3図は本発明方法を実施する装置の概略図
である。 図面中、1はガラス微粒子合成トーチ、2は火
炎流、3はガラス微粒子流、4は多孔質ガラス
体、5は出発材、6は反応容器、7は排気口、8
は回転装置、9は引上げ用ボールネジ、10は成
長速度検出器、11は成長速度設定器、12は制
御器、13は移動装置、14はトーチ用ホルダー
である。
Figure 1 is a graph showing the relationship between the refractive index distribution coefficient and the band, Figure 2a is a schematic diagram of the production of a porous glass body that will be the base material for graded optical fibers, Figure 2b
3 is a graph showing the relationship between the position of the torch with respect to the growth surface of the porous glass body and the growth rate of the porous glass body, and FIG. 3 is a schematic diagram of an apparatus for carrying out the method of the present invention. In the drawing, 1 is a glass particle synthesis torch, 2 is a flame stream, 3 is a glass particle stream, 4 is a porous glass body, 5 is a starting material, 6 is a reaction vessel, 7 is an exhaust port, 8
10 is a rotation device, 9 is a pulling ball screw, 10 is a growth rate detector, 11 is a growth rate setter, 12 is a controller, 13 is a moving device, and 14 is a torch holder.

Claims (1)

【特許請求の範囲】[Claims] 1 ガラス形成原料をガラス微粒子合成トーチに
よつて酸化反応せしめ合成されたガラス微粒子を
回転する出発材の先端に吹き付けて成長させ丸棒
状の多孔質ガラス母材を形成した後、透明ガラス
化して光フアイバ用母材を得る気相軸付け法にお
いて、多孔質ガラス母材の成長速度設定部と多孔
質ガラス体の成長速度検出部および前後左右に移
動する機能をそなえたガラス微粒子合成トーチ用
ホルダーにより前記成長速度設定部に入力した信
号と前記成長速度検出部から出力された信号が一
致するように前記ガラス微粒子合成トーチ用ホル
ダーの位置を保持し、火炎流の中心軸と多孔質母
材の中心軸が交わる点および角度を一定となるよ
うに制御することを特徴とする光フアイバ用母材
の製造方法。
1. Glass forming raw materials are subjected to an oxidation reaction using a glass particle synthesis torch, and the synthesized glass particles are sprayed onto the tip of a rotating starting material to grow and form a round bar-shaped porous glass base material, which is then turned into transparent glass and exposed to light. In the vapor phase axis method for obtaining a fiber base material, a holder for a glass fine particle synthesis torch is equipped with a growth rate setting section for the porous glass base material, a growth rate detection section for the porous glass body, and a function to move back and forth and left and right. The position of the glass particle synthesis torch holder is held so that the signal input to the growth rate setting section and the signal output from the growth rate detection section match, and the central axis of the flame flow and the center of the porous base material are maintained. 1. A method for manufacturing an optical fiber base material, which comprises controlling the point and angle at which the axes intersect to be constant.
JP4245483A 1983-03-16 1983-03-16 Preparation of parent material for optical fiber Granted JPS59169950A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4245483A JPS59169950A (en) 1983-03-16 1983-03-16 Preparation of parent material for optical fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4245483A JPS59169950A (en) 1983-03-16 1983-03-16 Preparation of parent material for optical fiber

Publications (2)

Publication Number Publication Date
JPS59169950A JPS59169950A (en) 1984-09-26
JPH033617B2 true JPH033617B2 (en) 1991-01-21

Family

ID=12636507

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4245483A Granted JPS59169950A (en) 1983-03-16 1983-03-16 Preparation of parent material for optical fiber

Country Status (1)

Country Link
JP (1) JPS59169950A (en)

Also Published As

Publication number Publication date
JPS59169950A (en) 1984-09-26

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