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JPH0526732B2 - - Google Patents
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JPH0526732B2 - - Google Patents

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Publication number
JPH0526732B2
JPH0526732B2 JP3809885A JP3809885A JPH0526732B2 JP H0526732 B2 JPH0526732 B2 JP H0526732B2 JP 3809885 A JP3809885 A JP 3809885A JP 3809885 A JP3809885 A JP 3809885A JP H0526732 B2 JPH0526732 B2 JP H0526732B2
Authority
JP
Japan
Prior art keywords
porous glass
glass rod
reaction vessel
passage
vessel
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 - Fee Related
Application number
JP3809885A
Other languages
Japanese (ja)
Other versions
JPS61197439A (en
Inventor
Hideyo Kawazoe
Akira Iino
Katsumi Orimo
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP3809885A priority Critical patent/JPS61197439A/en
Priority to GB8611440A priority patent/GB2190078B/en
Publication of JPS61197439A publication Critical patent/JPS61197439A/en
Publication of JPH0526732B2 publication Critical patent/JPH0526732B2/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]
    • C03B37/0144Means 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)
  • Glass Melting And Manufacturing (AREA)
  • Manufacture, Treatment Of Glass Fibers (AREA)

Description

【発明の詳細な説明】 『産業上の利用分野』 本発明は光フアイバ用、ロツドレンズ用などの
光学系多孔質ガラス母材をVAD法により製造す
る際の方法と装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method and apparatus for producing a porous glass base material for optical systems such as optical fibers and rod lenses by the VAD method.

『従来の技術』 VAD法により光学系の多孔質ガラス母材を製
造するとき、その製造雰囲気を形成している反応
容器内の気流を安定させる必要があり、その安定
性が十分に確保できないと、多孔質ガラス母材の
外径変動、屈折率分布の変動が大きくなる。
``Prior art'' When manufacturing a porous glass base material for optical systems using the VAD method, it is necessary to stabilize the airflow in the reaction vessel that forms the manufacturing atmosphere, and it is necessary to stabilize the airflow in the reaction vessel that forms the manufacturing atmosphere. , the variation in the outer diameter of the porous glass base material and the variation in the refractive index distribution become large.

そのため、反応容器の排気圧をコントロールし
たり、反応容器上部からその内部へ流量制御、圧
力制御されたガスを流入させるなど、適宜の手段
が講じられており、これらに関する技術として例
えば特開昭56−69234号公報、特開昭57−135738
号公報の発明が提供されている。
For this reason, appropriate measures have been taken, such as controlling the exhaust pressure of the reaction vessel, and flowing flow-controlled and pressure-controlled gas into the interior of the reaction vessel from the upper part of the reaction vessel. -69234 publication, JP 57-135738
The invention of the publication is provided.

従来法として特開昭57−135738号公報の発明を
例示した第3図イ,ロにおいて、1は排気口2を
有する反応容器、3は反応容器1の上部からその
内部へ挿入された通路管、4は反応容器1の下部
からその内部へ先端が装着されたガラス微粒子生
成用バーナ、5はターゲツト、6は多孔質ガラス
棒である。
In FIGS. 3A and 3B, which illustrate the invention disclosed in Japanese Patent Application Laid-Open No. 57-135738 as a conventional method, 1 is a reaction vessel having an exhaust port 2, and 3 is a passage pipe inserted into the inside of the reaction vessel 1 from the upper part thereof. , 4 is a burner for producing glass fine particles whose tip is attached to the inside of the reaction vessel 1 from the lower part thereof, 5 is a target, and 6 is a porous glass rod.

第3図の方法では、多孔質ガラス棒6を形成す
るに際して通路管3内からその下方へ所定のガス
を流すが、同図イのごとく多孔質ガラス棒6の形
成初期には通路管3内のクリアランスが大きく、
多孔質ガラス棒6の成長とともにこれが通路管3
内に浸入したとき、上記クリアランスが小さくな
る。
In the method shown in FIG. 3, when forming the porous glass rod 6, a predetermined gas is caused to flow from inside the passage tube 3 downward. However, as shown in FIG. The clearance is large,
As the porous glass rod 6 grows, this becomes the passage tube 3.
When the liquid penetrates into the interior, the above-mentioned clearance becomes smaller.

したがつて多孔質ガラス棒6の成長にともない
通路管3を介した流動性に変化が生じ、これとと
もに反応容器1内でのバーナ火炎の指向性(ガラ
ス微粒子の噴射方向)にも変化が生じる。
Therefore, as the porous glass rod 6 grows, the fluidity through the passage pipe 3 changes, and along with this, the directivity of the burner flame (the direction of injection of glass particles) inside the reaction vessel 1 also changes. .

説明を省略した特開昭56−69234号公報の発明
でも同様の現象が生じる。
A similar phenomenon occurs in the invention disclosed in Japanese Patent Application Laid-Open No. 56-69234, the explanation of which is omitted.

『発明が解決しようとする問題点』 上述したように従来法の場合は、バーナ火炎の
指向性に変化が生じるため、所望長さの多孔質ガ
ラス棒6を製造する際、そのガラス棒6の外径変
動や屈折率分布の変動を確実に防止することがで
ず、これを補償すべき通路管3内の流量制御、反
応容器1内の圧力制御も困難である。
"Problems to be Solved by the Invention" As mentioned above, in the case of the conventional method, the directivity of the burner flame changes, so when manufacturing the porous glass rod 6 of a desired length, the It is not possible to reliably prevent variations in the outer diameter or the refractive index distribution, and it is also difficult to control the flow rate in the passage pipe 3 and the pressure in the reaction vessel 1 to compensate for this.

一方、通路管3の内径を大きくして上記流動性
の変化を無視できる程度に小さくした場合、多孔
質ガラス棒6の外径は安定するようになるが、こ
の場合は反応容器上部から流動エネルギが小さく
なることにより、バーナ4からのガラス微粒子が
容器1内で乱舞し、多孔質ガラス棒6の屈折率分
布の安定性が損なわれる。
On the other hand, if the inner diameter of the passage tube 3 is increased to make the change in fluidity so small as to be negligible, the outer diameter of the porous glass rod 6 becomes stable, but in this case, the flow energy is not absorbed from the upper part of the reaction vessel. As a result, the glass particles from the burner 4 dance wildly within the container 1, and the stability of the refractive index distribution of the porous glass rod 6 is impaired.

本発明は上記の問題点に鑑み、反応容器内にお
ける流動性を安定させ、これにより長手方向にわ
たる外径、屈折率分布の安定した多孔質ガラス棒
が得られる方法および装置を提供しようとするも
のである。
In view of the above-mentioned problems, the present invention aims to provide a method and apparatus for stabilizing fluidity within a reaction vessel and thereby obtaining a porous glass rod with a stable outer diameter and refractive index distribution in the longitudinal direction. It is.

『問題点を解決するための手段』 *本発明方法の場合。"Means for solving problems" *In the case of the method of the present invention.

本発明は容器側部の排気口、容器上部からその
内部にわたる上下方向の通路部、および容器下部
からその内部に先端が装着されたガラス微粒子生
成用のバーナを有する反応容器と、上記通路部か
ら反応容器内へ下動自在かつ回転自在に挿入され
たターゲツトとを用い、反応容器内の所定位置で
回転しているターゲツトの下端には、バーナを介
して生成されたガラス微粒子を噴射かつ堆積させ
て多孔質ガラス棒を形成し、該多孔質ガラス棒の
成長速度に応じてターゲツトを引き上げる多孔質
ガラス棒の製造方法において、上記反応容器内に
はその通路部の外周に沿う下降気流を生じさせる
ことを特徴としている。
The present invention provides a reaction vessel having an exhaust port on the side of the container, a vertical passage extending from the upper part of the container to the inside thereof, and a burner for producing glass particles whose tip is installed from the lower part of the container into the inside thereof; A target is inserted into a reaction vessel so as to be freely movable and rotatable, and glass fine particles generated via a burner are injected and deposited on the lower end of the target rotating at a predetermined position within the reaction vessel. In the method for producing a porous glass rod, a porous glass rod is formed and a target is pulled up according to the growth rate of the porous glass rod, a downward air current is generated in the reaction vessel along the outer periphery of the passage. It is characterized by

*本発明装置の場合。*In the case of the device of the present invention.

本発明は容器側部の排気口、容器上部からその
内部にわたる上下方向の通路部、および容器下部
からその内部に先端が装着されたガラス微粒子生
成用のバーナを有する反応容器と、上記通路部か
ら反応容器内へ上下動自在かつ回転自在に挿入さ
れたターゲツトとを備えた多孔質ガラス棒の製造
装置において、上記通路部の上には気密性を有す
る筒体が連結され、反応容器の上部内周と通路部
外周との間には下降気流を形成するためのガス流
路が形成され、そのガス流路の上端にガス流入部
が形成されていることを特徴としている。
The present invention provides a reaction vessel having an exhaust port on the side of the container, a vertical passage extending from the upper part of the container to the inside thereof, and a burner for producing glass particles whose tip is installed from the lower part of the container into the inside thereof; In an apparatus for producing a porous glass rod, the target is vertically movable and rotatably inserted into a reaction vessel, and an airtight cylinder is connected above the passage. A gas flow path for forming a downward airflow is formed between the periphery and the outer periphery of the passage portion, and a gas inflow portion is formed at the upper end of the gas flow path.

『作用』 本発明において、反応容器内のバーナ先端より
噴射したガラス微粒子を回転状態のターゲツト下
端に堆積させて多孔質ガラス棒を形成し、該多孔
質ガラス棒の成長速度に応じてターゲツトを引き
上げる点では従来例と同じであるが、こうして多
孔質ガラス棒を形成するとき、反応容器内には通
路部の外周に沿う下降気流を生じさせる。
``Operation'' In the present invention, glass fine particles injected from the tip of a burner in a reaction vessel are deposited on the lower end of a rotating target to form a porous glass rod, and the target is pulled up according to the growth rate of the porous glass rod. Although this is the same as the conventional example, when a porous glass rod is formed in this way, a downward air current is generated in the reaction vessel along the outer periphery of the passage.

上記のようにして多孔質ガラス棒を製造すると
き、通路部内を多孔質ガラス棒はターゲツトとと
もに通路部内を通り、下降気流は通路部の外周に
沿つて排気口へと流れる。
When manufacturing a porous glass rod as described above, the porous glass rod passes along with the target inside the passage, and the downward airflow flows along the outer periphery of the passage to the exhaust port.

したがつて、はじめターゲツトが通り、つぎに
成長した多孔質ガラス棒が通ることにとより通路
部内のクリアランスが変化するとしても、その通
路部外周に沿つて下降する気流には、上記クリア
ラスの変化による影響が生ぜず、常に安定した流
動性を呈する。
Therefore, even if the clearance inside the passage changes as the target passes through it first and then the grown porous glass rod passes through it, the airflow descending along the outer periphery of the passage will have the above-mentioned change in clearance. It does not have any influence from other people and always exhibits stable fluidity.

その結果、安定状態の下降気流により多孔質ガ
ラス母材の外径がほぼ一定に仕上がり、また、堆
積面に対し一定したバーナ火炎の指向性、下降気
流によるガラス微粒子の乱舞阻止など、これらの
相乗効果により、多孔質ガラス母材の長手方向に
わたる屈折率分布も一定化し、かくて品質、特性
のよい多孔質ガラス母材が得られる。
As a result, the outer diameter of the porous glass base material is almost constant due to the stable downdraft, the directivity of the burner flame is constant with respect to the deposition surface, and the downdraft prevents the glass particles from dancing, all of which are synergistic. As a result, the refractive index distribution over the longitudinal direction of the porous glass base material is also made constant, and thus a porous glass base material with good quality and properties can be obtained.

『実施例』 以下、本発明方法および装置の具体例につき、
図面を参照して説明する。
``Example'' Hereinafter, specific examples of the method and apparatus of the present invention will be described.
This will be explained with reference to the drawings.

第1図、第2図において、11は排気口12を
有する反応容器、13は反応容器11の上部から
その内部にわたつて設けられた通路部、14は反
応容器11の下部からその内部へ先端が装着され
たガラス微粒子生成用のバーナ、15は回転かつ
上下動自在な既知のターゲツトである。
In FIGS. 1 and 2, 11 is a reaction vessel having an exhaust port 12, 13 is a passage provided from the top of the reaction vessel 11 to the inside thereof, and 14 is a tip extending from the bottom of the reaction vessel 11 to the inside thereof. The burner 15 for producing glass particles equipped with a burner 15 is a known target that is rotatable and movable up and down.

上記において、通路部13の上面には気密性を
有する筒体16が連結され、反応容器11の上部
内周と通路部13外周との間には下降気流を生じ
させるためのガス流路17が形成されているとと
もにそのガス流路17の上端にはガス導入部18
が形成されている。
In the above, an airtight cylindrical body 16 is connected to the upper surface of the passage section 13, and a gas flow path 17 is provided between the upper inner periphery of the reaction vessel 11 and the outer periphery of the passage section 13 for generating a downward airflow. A gas introduction section 18 is formed at the upper end of the gas flow path 17.
is formed.

なお、第1図の場合は反応容器11の上面に等
間隔で穿設された複数の円形透孔によりガス導入
部18が形成されており、第2図の場合はガス導
入口19とリング状のガス吐出口20とを有する
部材を介してガス流入部18が形成されていると
ともにガス導入口19には流量調整器21を有す
る配管系22が接続されている。
In addition, in the case of FIG. 1, the gas introduction part 18 is formed by a plurality of circular through holes bored at equal intervals on the upper surface of the reaction vessel 11, and in the case of FIG. A gas inlet 18 is formed through a member having a gas discharge port 20, and a piping system 22 having a flow rate regulator 21 is connected to the gas inlet 19.

図中、23は多孔質ガラス棒を示す。 In the figure, 23 indicates a porous glass rod.

上述した図示の装置により多孔質ガラス棒23
を製造するとき、ターゲツト15はその下端が反
応容器11内の所定位置まで挿入されて回転さ
れ、バーナ14を介した火炎加水分解反応による
生成物すなわちガラス微粒子が上記ターゲツト1
5の下端に向けて噴射かつ堆積される。
The porous glass rod 23 is formed by the illustrated apparatus described above.
When manufacturing the target 15, the lower end thereof is inserted into the reaction vessel 11 to a predetermined position and rotated, and the product of the flame hydrolysis reaction via the burner 14, that is, the glass fine particles, is transferred to the target 1.
It is injected and deposited towards the lower end of 5.

かかるガラス微粒子の堆積により、ターゲツト
15の下端には多孔質ガラス棒23が形成され、
該多孔質ガラス棒23の成長速度に応じてターゲ
ツト15は通路部13内、筒体16内を上方へ引
き上げられるが、この際、反応容器11内は排気
口12より排気されるとともにその排気にともな
う自然導入、または配管系22からの強制導入に
より所定のガスがガス導入部18からガス流路1
7へと導入され、これにより通路部13の外周に
沿う下降気流が生じる。
Due to the deposition of such glass particles, a porous glass rod 23 is formed at the lower end of the target 15.
Depending on the growth rate of the porous glass rod 23, the target 15 is pulled upward within the passage 13 and the cylindrical body 16, but at this time, the inside of the reaction vessel 11 is exhausted from the exhaust port 12, and the exhaust gas A predetermined gas is introduced from the gas introduction part 18 into the gas flow path 1 by natural introduction or forced introduction from the piping system 22.
7, thereby creating a downward airflow along the outer periphery of the passage section 13.

前述したように、通路部13の外周に沿つて排
気口12へと流れる当該下降気流は、通路部13
内のクリアランスの変化に影響されない安定した
流動性を示し、堆積面に対する一定したバーナ火
炎の指向性、ガラス微粒子の乱舞阻止などの作用
効果を奏するから、多孔質ガラス母材23の長手
方向にわたる外径および屈折率分布が一定とな
る。
As described above, the downward airflow flowing along the outer periphery of the passage section 13 toward the exhaust port 12 flows through the passage section 13.
It exhibits stable fluidity unaffected by changes in the internal clearance, has effects such as constant directivity of the burner flame to the deposition surface, and prevention of scattering of glass particles. The diameter and refractive index distribution are constant.

なお、上記において多孔質ガラス棒23を製造
するとき、反応容器11内の排気圧、下降気流の
流量等を一定に保持すべき圧力コントロール、流
量コントロールを行なうのがよく、これらの制御
は排気口12に接続された配管系の排気量調整器
(図示せず)、ガス導入口19に接続された配管系
22の流量調整器21等により調整して行なう。
In addition, when manufacturing the porous glass rod 23 in the above, it is preferable to perform pressure control and flow rate control to keep the exhaust pressure inside the reaction vessel 11 constant, the flow rate of the descending air, etc., and these controls are performed at the exhaust port. This adjustment is performed using a displacement regulator (not shown) of the piping system connected to the gas inlet 12, a flow regulator 21 of the piping system 22 connected to the gas inlet 19, and the like.

『発明の効果』 以上説明した通り、本発明方法によるときは、
VAD法により多孔質ガラス棒を製造するとき、
反応容器内の通路部外周に沿う下降気流を生じさ
せるから、通路部内のクリアランスの変化に影響
されない安定した当該下降気流により、長手方向
にわたる外径および屈折率分布の一定な多孔質ガ
ラス母材が得られる。
"Effects of the Invention" As explained above, when using the method of the present invention,
When manufacturing porous glass rods by the VAD method,
Since a downward airflow is generated along the outer periphery of the passage in the reaction vessel, this stable downward airflow is unaffected by changes in the clearance within the passage, and as a result, a porous glass base material with a constant outer diameter and refractive index distribution in the longitudinal direction is formed. can get.

一方、本発明装置の場合、反応容器の排気口と
通路部、ガラス微粒子生成用のバーナ、ターゲツ
ト等を備えているだけでなく、反応容器の上部内
周と通路部外周との間にガス流路が形成され、そ
のガス流路の上端にはガス流入部が形成され、上
記通路部の上には気密性を有する筒体が連結され
ているから、所定の下降気流を容易に生じさせる
ことができ、多孔質ガラス棒の引き上げ操作も通
路部上の筒体を利用して反応容器内の雰囲気を損
なうことなく行ない得る。
On the other hand, the apparatus of the present invention is not only equipped with an exhaust port and passage of the reaction vessel, a burner for generating glass particles, a target, etc., but also has a gas flow between the inner periphery of the upper part of the reaction vessel and the outer periphery of the passage. A passage is formed, a gas inflow part is formed at the upper end of the gas flow passage, and an airtight cylinder is connected above the passage part, so that a predetermined downward airflow can be easily generated. The operation of pulling up the porous glass rod can also be carried out using the cylindrical body above the passage without damaging the atmosphere inside the reaction vessel.

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

第1図は本発明方法ならびに装置の一実施例を
略示した説明図、第2図は同上の他実施例を略示
した説明図、第3図イ,ロは従来例の説明図であ
る。 11……反応容器、12……排気口、13……
通路部、14……バーナ、15……ターゲツト、
16……筒体、17……ガス流路、18……ガス
導入部、19……ガス導入口、20……ガス吐出
口、21……流量調整器、22……配管系、23
……多孔質ガラス棒。
Fig. 1 is an explanatory diagram schematically showing one embodiment of the method and apparatus of the present invention, Fig. 2 is an explanatory diagram schematically showing another embodiment of the same, and Fig. 3 A and B are explanatory diagrams of a conventional example. . 11... Reaction container, 12... Exhaust port, 13...
Passage section, 14... burner, 15... target,
16... Cylindrical body, 17... Gas flow path, 18... Gas inlet, 19... Gas inlet, 20... Gas discharge port, 21... Flow rate regulator, 22... Piping system, 23
...Porous glass rod.

Claims (1)

【特許請求の範囲】 1 容器側部の排気口、容器上部からその内部に
わたる上下方向の通路部、および容器下部からそ
の内部に先端が装着されたガラス微粒子生成用の
バーナを有する反応容器と、上記通路部から反応
容器内へと上下動自在かつ回転自在に挿入された
ターゲツトとを用い、反応容器内の所定位置で回
転しているターゲツトの下端には、バーナを介し
て生成されたガラス微粒子を噴射かつ堆積させて
多孔質ガラス棒を形成し、該多孔質ガラス棒の成
長速度に応じてターゲツトを引き上げる多孔質ガ
ラス棒の製造方法において、上記反応容器内には
その通路部の外周に沿う下降気流を生じさせるこ
とを特徴とする多孔質ガラス棒の製造方法。 2 通路部の外周に沿う下降気流が一定となるよ
う、当該気流の流量を調整する特許請求の範囲第
1項記載の多孔質ガラス棒の製造方法。 3 反応容器内の排気圧が一定となるよう、通路
部の外周に沿う下降気流の流量を調整する特許請
求の範囲第1項記載の多孔質ガラス棒の製造方
法。 4 容器側部の排気口、容器上部からその内部に
わたる上下方向の通路部、および容器下部からそ
の内部に先端が装着されたガラス微粒子生成用の
バーナ有する反応容器と、上記通路部から反応容
器内へ上下動自在かつ回転自在に挿入されたター
ゲツトとを備えた多孔質ガラス棒の製造装置にお
いて、上記通路部の上には気密性を有する筒体が
連結され、反応容器の上部内周と通路部外周との
間には下降気流を形成するためのガス流路が形成
され、そのガス流路の上端にガス流入部が形成さ
れていることを特徴とする多孔質ガラス棒の製造
装置。 5 ガス流入部が反応容器の上面に穿設された複
数の透孔からなる特許請求の範囲第4項記載の多
孔質ガラス棒の製造装置。 6 ガス導入口とリング状のガス吐出口とを有す
る部材を介してガス流入部が形成されている特許
請求の範囲第4項記載の多孔質ガラス棒の製造装
置。 7 ガス導入口には流量調整器を有する配管系が
接続されている特許請求の範囲第6項記載の多孔
質ガラス棒の製造装置。
[Scope of Claims] 1. A reaction vessel having an exhaust port on the side of the vessel, a vertical passage extending from the top of the vessel to the inside thereof, and a burner for producing glass particles whose tip is installed inside the vessel from the bottom of the vessel; Using a target that is vertically movable and rotatably inserted into the reaction vessel from the passage section, glass fine particles generated via a burner are placed at the lower end of the target rotating at a predetermined position within the reaction vessel. In the method for producing a porous glass rod, in which a porous glass rod is formed by injecting and depositing a porous glass rod, and a target is pulled up according to the growth rate of the porous glass rod, a A method for producing a porous glass rod characterized by generating a downward air current. 2. The method for manufacturing a porous glass rod according to claim 1, wherein the flow rate of the airflow is adjusted so that the downward airflow along the outer periphery of the passage portion is constant. 3. The method for manufacturing a porous glass rod according to claim 1, wherein the flow rate of the descending air flow along the outer periphery of the passage section is adjusted so that the exhaust pressure in the reaction vessel is constant. 4. A reaction vessel having an exhaust port on the side of the container, a vertical passage extending from the top of the container to the inside thereof, and a burner for generating glass particles whose tip is installed inside the vessel from the bottom of the vessel, and a passage from the passage to the inside of the reaction vessel. In an apparatus for manufacturing a porous glass rod, the target is vertically movable and rotatably inserted into the target, and an airtight cylinder is connected above the passage, and the upper inner periphery of the reaction vessel and the passage are connected to each other. 1. An apparatus for manufacturing a porous glass rod, characterized in that a gas flow path for forming a downward airflow is formed between the rod and the outer periphery of the rod, and a gas inflow portion is formed at the upper end of the gas flow path. 5. The apparatus for manufacturing a porous glass rod according to claim 4, wherein the gas inflow portion comprises a plurality of through holes drilled in the upper surface of the reaction vessel. 6. The apparatus for manufacturing a porous glass rod according to claim 4, wherein the gas inflow portion is formed through a member having a gas inlet and a ring-shaped gas discharge port. 7. The porous glass rod manufacturing apparatus according to claim 6, wherein a piping system having a flow rate regulator is connected to the gas inlet.
JP3809885A 1985-02-27 1985-02-27 Production of porous glass rod and devices therefor Granted JPS61197439A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP3809885A JPS61197439A (en) 1985-02-27 1985-02-27 Production of porous glass rod and devices therefor
GB8611440A GB2190078B (en) 1985-02-27 1986-05-10 Method of fabricating porous glass rod and apparatus for fabricating the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3809885A JPS61197439A (en) 1985-02-27 1985-02-27 Production of porous glass rod and devices therefor

Publications (2)

Publication Number Publication Date
JPS61197439A JPS61197439A (en) 1986-09-01
JPH0526732B2 true JPH0526732B2 (en) 1993-04-19

Family

ID=12515998

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3809885A Granted JPS61197439A (en) 1985-02-27 1985-02-27 Production of porous glass rod and devices therefor

Country Status (2)

Country Link
JP (1) JPS61197439A (en)
GB (1) GB2190078B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2603472B2 (en) * 1987-05-12 1997-04-23 旭硝子株式会社 Manufacturing method of porous quartz glass base material

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54116429A (en) * 1978-03-03 1979-09-10 Hitachi Ltd Production of material for optical fiber
DE3036915C2 (en) * 1979-10-09 1987-01-22 Nippon Telegraph And Telephone Corp., Tokio/Tokyo Method and device for producing optical fiber starting shapes and their use for drawing optical fibers
JPS57100934A (en) * 1980-12-12 1982-06-23 Nippon Telegr & Teleph Corp <Ntt> Manufacturing of optical fiber preform
JPS57100933A (en) * 1980-12-12 1982-06-23 Nippon Telegr & Teleph Corp <Ntt> Preparation of base material for optical fiber
US4435199A (en) * 1982-04-26 1984-03-06 Western Electric Co., Inc. Exhaust system for a vapor deposition chamber

Also Published As

Publication number Publication date
JPS61197439A (en) 1986-09-01
GB8611440D0 (en) 1986-06-18
GB2190078A (en) 1987-11-11
GB2190078B (en) 1990-04-11

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