[go: up one dir, main page]

JPH033615B2 - - Google Patents

Info

Publication number
JPH033615B2
JPH033615B2 JP2753086A JP2753086A JPH033615B2 JP H033615 B2 JPH033615 B2 JP H033615B2 JP 2753086 A JP2753086 A JP 2753086A JP 2753086 A JP2753086 A JP 2753086A JP H033615 B2 JPH033615 B2 JP H033615B2
Authority
JP
Japan
Prior art keywords
gas
reaction vessel
gas pressure
manufacturing apparatus
glass manufacturing
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
Application number
JP2753086A
Other languages
Japanese (ja)
Other versions
JPS62187121A (en
Inventor
Masatoshi Mikami
Kunihiro Matsubara
Yasuro Furui
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 JP2753086A priority Critical patent/JPS62187121A/en
Publication of JPS62187121A publication Critical patent/JPS62187121A/en
Publication of JPH033615B2 publication Critical patent/JPH033615B2/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]
    • 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』 本発明は通信用、光学用の合成ガラスを製造す
るための装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an apparatus for producing synthetic glass for communications and optical applications.

『従来の技術』 高品位の合成石英からなる通信用、光学用のガ
ラスロツド、ガラスパイプ等を製造する手段の一
つにOVD方がある。
``Prior Art'' OVD is one of the methods for producing glass rods, glass pipes, etc. for communication and optical applications made of high-grade synthetic quartz.

既知の通り、OVD法では火炎加水分解反応お
よび/または熱酸化反応により生成したスート状
のガラス微粒子(SiO2、GeO2、P2O5、B2O3
ど)を、出発母材と称するガラス堆積基材の外周
に堆積させて多孔質ガラス層を形成し、その後、
多孔質ガラス層を加熱、脱泡して透明ガラス化す
る。
As is known, in the OVD method, soot-like glass particles (SiO 2 , GeO 2 , P 2 O 5 , B 2 O 3 , etc.) generated by flame hydrolysis reaction and/or thermal oxidation reaction are called the starting base material. deposited on the outer periphery of the glass deposition substrate to form a porous glass layer;
The porous glass layer is heated and defoamed to become transparent glass.

より具体的には、上記多孔質ガラス層の堆積形
成時、ガス導入系、ガス排出系を有する反応容器
内に、ガラス微粒子生成用のバーナと、回転しな
がら軸方向に往復動するガラス堆積基材とを相互
に対応させて内装しておき、バーナを介して反応
生成されたガラス微粒子をガラス堆積基材の外周
に堆積させる。
More specifically, during the deposition formation of the porous glass layer, a burner for producing glass particles and a glass deposition base that reciprocates in the axial direction while rotating are placed in a reaction vessel having a gas introduction system and a gas exhaust system. The glass particles are arranged in a manner that corresponds to each other, and the glass fine particles produced by the reaction are deposited on the outer periphery of the glass deposition base material through a burner.

かかるOVD法の場合、多孔質ガラス層を軸方
向(縦長の棒状)に成長させるVAD法と比べ、
自重による多孔質ガラス層の破壊が起こりがたい
とされている。
In the case of this OVD method, compared to the VAD method in which the porous glass layer is grown in the axial direction (in the shape of a vertically long rod),
It is said that the porous glass layer is unlikely to break due to its own weight.

『発明が解決しようとする問題点』 上述したOVD法の場合、原料ガスとして主に
SiCl4、GeCl4、POCl3、BCl3などの塩化物を使用
するため、これらの反応ガスにはCl2、HClなど
の腐蝕性ガスが多く含まれる。
``Problems to be solved by the invention'' In the case of the above-mentioned OVD method, the raw material gas is mainly
Since chlorides such as SiCl 4 , GeCl 4 , POCl 3 , and BCl 3 are used, these reaction gases contain a large amount of corrosive gases such as Cl 2 and HCl.

反応容器内の反応ガスは、廃ガスとしてガス排
出系からその容器外へ排出され、有害成分を除去
するための処理を受けるが、ガス排出系に不測の
異常事態が発生し、排気能力が低下した場合、反
応容器内には廃ガスが充満する。
The reaction gas in the reaction vessel is discharged as waste gas from the gas exhaust system to the outside of the vessel and undergoes treatment to remove harmful components, but an unexpected abnormality occurs in the gas exhaust system and the exhaust capacity decreases. In this case, the reaction vessel is filled with waste gas.

ガス排出系に特に異常がない場合でも、反応容
器内外の圧力変動により、廃ガスがガス排出系か
ら反応容器内へ逆拡散することがある。
Even if there is no particular abnormality in the gas exhaust system, waste gas may back-diffuse from the gas exhaust system into the reaction vessel due to pressure fluctuations inside and outside the reaction vessel.

そのため、反応容器の内部が廃ガスにより汚染
され、殊に反応容器の気密正が不充分な場合には
反応容器から漏洩した廃ガスにより周囲の環境が
悪化する。
Therefore, the inside of the reaction vessel is contaminated by the waste gas, and especially when the reaction vessel is not sufficiently airtight, the surrounding environment is deteriorated by the waste gas leaking from the reaction vessel.

もちろん、廃ガスは上述した腐蝕成分を含むの
で、設備装置の金属部分を錆化させたり、人体に
も悪影響を及ぼす。
Of course, since the waste gas contains the above-mentioned corrosive components, it can rust the metal parts of equipment and have an adverse effect on the human body.

一方、反応容器内は高品質の合成石英を得るた
め高クリーン度が要求されるが、上記ガス排出系
を介して吸引されている当該反応容器内は定常的
に負圧傾向となり、したがつて、反応容器の気密
性が不充分な場合、外部の塵埃等が不純物として
混入し、反応容器内のクリーン度低下させるので
上記品質維持が困難となる。
On the other hand, a high level of cleanliness is required inside the reaction vessel in order to obtain high-quality synthetic quartz, but the inside of the reaction vessel, which is sucked in through the gas exhaust system, constantly tends to have a negative pressure. If the airtightness of the reaction vessel is insufficient, external dust and the like will enter as impurities and reduce the cleanliness inside the reaction vessel, making it difficult to maintain the above-mentioned quality.

本発明は上記の問題点に鑑み、反応容器からそ
の外部へのガス漏れ、および外部から反応容器内
への不純物混入等が防止できる。しかも、高品質
の合成ガラス製造できる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 can prevent gas leakage from a reaction vessel to the outside thereof, and contamination of impurities from the outside into the reaction vessel. Furthermore, the present invention aims to provide an apparatus capable of producing high quality synthetic glass.

『問題点を解決するための手段』 本発明は上記の目的を達成するため、ガス導入
系、ガス排出系を有する反応容器内に、ガラス微
粒子生成用のバーナと、ガラス堆積基材とが相互
に対応して内装された合成ガラス製造装置におい
て、上記反応容器の一部または全部が内部空間を
有する二重壁体により構成され、当該反応容器に
は、反応容器外部のガス圧に対して反応容器内部
のガス圧、二重壁体の内部空間のガス圧が相対的
に調整可能なガス調整機構が設けられていること
を特徴とする。
"Means for Solving the Problems" In order to achieve the above object, the present invention provides a system in which a burner for producing glass fine particles and a glass deposition substrate are mutually connected in a reaction vessel having a gas introduction system and a gas exhaust system. In a synthetic glass manufacturing apparatus equipped with an interior corresponding to It is characterized by being provided with a gas adjustment mechanism that can relatively adjust the gas pressure inside the container and the gas pressure in the internal space of the double-walled body.

『作用』 本発明装置の場合、反応容器内で回転しながら
所定方向へ往復動するガラス堆積基材の外周に、
バーナを介して反応生成したガラス微粒子を堆積
させ、これにより多孔質ガラス層を形成する。
``Operation'' In the case of the device of the present invention, on the outer periphery of the glass deposition substrate that reciprocates in a predetermined direction while rotating within the reaction vessel,
Glass particles produced by the reaction are deposited through a burner, thereby forming a porous glass layer.

この際、ガス排出系を介して反応容器内を排気
し、これとともにガス導入系からクリーンな気体
を反応容器内に導入する。
At this time, the inside of the reaction vessel is evacuated via the gas exhaust system, and at the same time, clean gas is introduced into the reaction vessel from the gas introduction system.

かかる多孔質ガラス層の形成、ガス排出、ガス
導入等は従来例と同じである。
Formation of the porous glass layer, gas discharge, gas introduction, etc. are the same as in the conventional example.

本発明装置では、上記のようにして多孔質ガラ
ス層を形成する際の反応容器(一部または全部)
が、内部空間を有する二重壁体により構成され、
しかも反応容器には、反応容器外部のガス圧P1
に対して反応容器内部のガス圧P3、二重壁体の
内部空間のガス圧P2が相対的に調整可能なガス
調整機構が設けられている。
In the apparatus of the present invention, the reaction vessel (part or all) used when forming the porous glass layer as described above is
is composed of a double-walled body with an internal space,
Moreover, the gas pressure outside the reaction vessel P 1
A gas adjustment mechanism is provided which can relatively adjust the gas pressure P 3 inside the reaction vessel and the gas pressure P 2 inside the double-walled body.

したがつて、仮に反応容器の気密性が不充分で
あるとしても、ガス調整機構を介してP1<P3
P2を満足させ、あるいはP2<P1とP2<P3とを満
足させることにより、反応容器内からその外部へ
のガス漏れ、外部から反応容器内への不純物混
入、ガス排出系から反応容器内への廃ガスの逆拡
散等が防止でき、高品質の多孔質ガラス層が安定
して製造できる。
Therefore, even if the airtightness of the reaction vessel is insufficient, P 1 < P 3 <
By satisfying P 2 or satisfying P 2 < P 1 and P 2 < P 3 , gas leakage from inside the reaction vessel to the outside, impurity contamination from the outside into the reaction vessel, and gas exhaust system can be prevented. Back diffusion of waste gas into the reaction vessel can be prevented, and a high-quality porous glass layer can be stably produced.

『実施例』 以下本発明装置の実施例につき、図面を参照し
て説明する。
``Embodiments'' Examples of the apparatus of the present invention will be described below with reference to the drawings.

図において、石英ガラスまたはセラミツクスか
らなる反応容器1はガス導入系2a,2bとガス
排出系3とを有する。
In the figure, a reaction vessel 1 made of quartz glass or ceramics has gas introduction systems 2a, 2b and a gas exhaust system 3.

場合により、反応容器1を構成する材料は、樹
脂コーテイングされた石英ガラス、セラミツクス
等からなり、その樹脂コーテイング材としてフツ
素樹脂またはシリコーン樹脂等が採用される。
In some cases, the material constituting the reaction vessel 1 may be resin-coated quartz glass, ceramics, or the like, and the resin coating material may be fluorine resin, silicone resin, or the like.

ガス導入系2a,2bはフイルタ4a,4bを
備え、かかるフイルタ4a,4bは外気をクリー
ン度0〜100クラス程度に濾過する機能を有する。
The gas introduction systems 2a and 2b are equipped with filters 4a and 4b, and these filters 4a and 4b have a function of filtering outside air to a cleanliness level of about 0 to 100 class.

ガス導入系2a,2bには、反応容器1内への
ガス導入用として図示しない不活性ガスボンベ、
あるいはクリーンエア(クリーン度0〜100クラ
ス)のボンベが配管接続されることがあるが、こ
の場合、上記フイルタ4a,4bは省略されても
よい。
The gas introduction systems 2a and 2b include inert gas cylinders (not shown) for introducing gas into the reaction vessel 1;
Alternatively, a cylinder of clean air (cleanliness class 0 to 100) may be connected via piping, but in this case, the filters 4a and 4b may be omitted.

ガス排出系3は廃ガスの有害成分除去槽5、吸
引型の排気フアン6を備え、有害成分除去槽5は
水、アルカリ液等の洗浄液を廃ガスに対して向流
させる機能を有する。
The gas exhaust system 3 includes a waste gas harmful component removal tank 5 and a suction type exhaust fan 6, and the harmful component removal tank 5 has a function of causing a cleaning liquid such as water or alkaline solution to flow countercurrently to the waste gas.

反応容器1内には縦型下向のガラス微粒子生成
用バーナ7と、横型(水平)のガラス堆積基材8
とが相互に対応して内装されている。
Inside the reaction vessel 1 are a vertical downward glass particle generation burner 7 and a horizontal (horizontal) glass deposition substrate 8.
and are decorated in correspondence with each other.

バーナ7は、例えば同心状に並んだ複数のガス
流路を有する多重管構造からなり、これらガス流
路には所定のガス管がそれぞれ接続されている。
The burner 7 has, for example, a multi-tube structure having a plurality of gas passages arranged concentrically, and predetermined gas pipes are respectively connected to these gas passages.

図示しない回転手段、往復動手段を介して回転
かつ軸方向に往復動自在なガラス堆積基材8は石
英棒または石英管からなり、当該堆積基材8の両
端は反応容器1外へ突出され、チヤツク9a,9
bを介して支持されている。
The glass deposition substrate 8, which can be rotated and reciprocated in the axial direction via a rotation means and a reciprocating means (not shown), is made of a quartz rod or a quartz tube, and both ends of the deposition substrate 8 are protruded outside the reaction vessel 1. Chuck 9a, 9
It is supported through b.

なお、ガラス堆積基材8については、チヤツク
9a,9b、その回転手段、往復動手段等を含め
た全体が反応容器1内へ内装されることがある。
The glass deposition substrate 8, including the chucks 9a, 9b, their rotation means, reciprocating means, etc., may be housed in the reaction vessel 1 in its entirety.

また、図示のごとくガス排出系3の基端、バー
ナ7へのガス供給管、ガラス堆積基材8の両端等
が反応容器1の壁面を貫通しているとき、これら
の貫通部分にはシール手段が講じられる。
Further, as shown in the figure, when the base end of the gas exhaust system 3, the gas supply pipe to the burner 7, both ends of the glass deposition substrate 8, etc. penetrate the wall surface of the reaction vessel 1, sealing means is provided at these penetrating portions. will be taken.

本発明では、かかる構成の合成ガラス製造装置
において、反応容器1の全部(または一部でもよ
い)が内部空間10を有する二重壁体11により
構成されている。
In the present invention, in the synthetic glass manufacturing apparatus having such a structure, the entire reaction vessel 1 (or even a part thereof) is constituted by a double-walled body 11 having an internal space 10.

二重壁体11には、その内部空間10に連通す
る給気系12と、圧力調整弁13を有する排気系
14とがそれぞれ連結される。
An air supply system 12 communicating with the internal space 10 and an exhaust system 14 having a pressure regulating valve 13 are connected to the double wall body 11, respectively.

給気系12は前記ガス導入系2a,2bの場合
と同じくフイルタ(濾過機能:クリーン度0〜
100クラス)を有するとか、あるいは不活性ガス
ボンベ、あるいはクリーンエア(クリーン度0〜
100クラス)のボンベが配管接続される。
The air supply system 12 is equipped with a filter (filtration function: cleanliness level 0 to
100 class), or an inert gas cylinder, or clean air (cleanliness level 0~
100 class) cylinders are connected by piping.

さらに本発明装置には、前記の通り、反応容器
1外のガス圧に対して反応容器1内のガス圧、二
重壁体11の内部空間10のガス圧が相対的に調
整可能なガス調整機構が装備される。
Furthermore, as described above, the apparatus of the present invention has a gas adjustment system that allows the gas pressure inside the reaction container 1 and the gas pressure in the internal space 10 of the double-walled body 11 to be adjusted relative to the gas pressure outside the reaction container 1. Equipped with a mechanism.

そのガス調整機構の一部は、前述したガス導入
系2a,2b、ガス排出系3、給気系12、排気
系14からなる。
Part of the gas adjustment mechanism includes the gas introduction systems 2a and 2b, the gas exhaust system 3, the air supply system 12, and the exhaust system 14 described above.

そのガス調整機構の他部は、反応容器1外のガ
ス圧を測定するための圧力計15と、内部空間1
0のガス圧を測定するための圧力計16と、反応
容器1内のガス圧を測定するための圧力計17
と、反応容器1内のガス圧および内部空間10の
ガス圧を制御するための制御機器18とからな
り、圧力計15は反応容器1外に配置され、圧力
計16のセンサ19は内部空間10内に配置さ
れ、圧力計17のセンサ20は反応容器1内に配
置される。
The other parts of the gas adjustment mechanism include a pressure gauge 15 for measuring the gas pressure outside the reaction vessel 1, and an internal space 1.
A pressure gauge 16 for measuring the gas pressure at 0, and a pressure gauge 17 for measuring the gas pressure inside the reaction vessel 1.
and a control device 18 for controlling the gas pressure in the reaction vessel 1 and the gas pressure in the internal space 10, the pressure gauge 15 is disposed outside the reaction vessel 1, and the sensor 19 of the pressure gauge 16 is located in the interior space 10. The sensor 20 of the pressure gauge 17 is placed inside the reaction vessel 1 .

制御機器18は各圧力計15〜17からの測定
値入力に基づき、反応容器1内のガス圧、内部空
間10のガス圧を所定値に調整するが、そのた
め、ガス導入系2a,2b、ガス排出系3、給気
系12、排気系14の一部または全部を制御する
機能を有する。
The control device 18 adjusts the gas pressure in the reaction vessel 1 and the gas pressure in the internal space 10 to predetermined values based on the measured value input from each pressure gauge 15 to 17. It has a function of controlling part or all of the exhaust system 3, air supply system 12, and exhaust system 14.

より具体的には、制御機器18は、少なくとも
ガス排出系3の排気フアン6と排気系14の圧力
調整弁13とを制御する機能を有する。
More specifically, the control device 18 has a function of controlling at least the exhaust fan 6 of the gas exhaust system 3 and the pressure regulating valve 13 of the exhaust system 14.

上述した本発明装置の場合、従来例と同様、反
応容器1内においてガラス堆積基材8を回転なら
びにその軸方向へ往復動させ、多重管構造のバー
ナ7には例えばSiCl4、Ar、O2、H2等を供給し、
これら各ガスの所定反応に生成したガラス微粒子
を上記ガラス堆積基材8の外周に堆積させて石英
系の多孔質ガラス層21を形成する。
In the case of the apparatus of the present invention described above, the glass deposition substrate 8 is rotated and reciprocated in the axial direction within the reaction vessel 1, as in the conventional example, and the burner 7 having a multi-tubular structure is filled with, for example, SiCl 4 , Ar, O 2 . , H2 etc.,
Glass particles generated by a predetermined reaction of each of these gases are deposited on the outer periphery of the glass deposition substrate 8 to form a quartz-based porous glass layer 21.

こうして合成ガラスを製造するとき、ガス導入
系2a,2bとガス排出系3とを稼動させるだけ
でなく、給気系12、排気系14をも稼働させ、
しかもこの際、反応容器1外のガス圧P1、内部
空間10のガス圧P2、反応容器1内のガス圧P3
等を圧力計15〜17を介して測定して、これら
の測定結果を制御機器18へ入力し、当該制御機
器18にてガス排出系3の排気フアン6と排気系
14の圧力調整弁13とを制御することにより、
上記各圧力を『P1<P3<P2』としたり、あるい
は『P2<P1、P2<P3』とする。
When manufacturing synthetic glass in this way, not only the gas introduction systems 2a and 2b and the gas exhaust system 3 are operated, but also the air supply system 12 and the exhaust system 14 are operated,
Moreover, at this time, the gas pressure P 1 outside the reaction vessel 1, the gas pressure P 2 in the internal space 10, and the gas pressure P 3 inside the reaction vessel 1.
etc. are measured via the pressure gauges 15 to 17, and these measurement results are input to the control device 18, and the control device 18 controls the exhaust fan 6 of the gas exhaust system 3 and the pressure regulating valve 13 of the exhaust system 14. By controlling the
The above pressures may be set to "P 1 < P 3 < P 2 ", or "P 2 < P 1 , P 2 < P 3 ".

かくて、反応容器1内のガスがその外部に漏れ
たり、あるいは外部から反応容器1内へ不純物が
混入することがなくなり、各系がきわめて安定し
た稼働状態を呈するようになる。
In this way, the gas inside the reaction vessel 1 will not leak to the outside, or impurities will not be mixed into the reaction vessel 1 from the outside, and each system will exhibit an extremely stable operating condition.

その結果、反応容器1内のクリーン度が良好に
保持されて高品質の多孔質ガラス層21が得ら
れ、周囲の作業循環も汚染されなくなる。
As a result, the cleanliness inside the reaction vessel 1 is maintained well, a high quality porous glass layer 21 is obtained, and the surrounding working circulation is not contaminated.

『発明の効果』 以上説明した通り、本発明によるときは、所定
の合成ガラス製造装置における反応容器の一部ま
たは全部が内部空間を有する二重壁体により構成
され、その反応容器に、反応容器外部のガス圧に
対する反応容器内部のガス圧、二重壁体の内部空
間のガス圧が相対調整可能なガス調整機構が設け
られているから、当該ガス調整機構を介して反応
容器内部のガス圧、二重壁体の内部空間のガス圧
を適切な状態に調整することにより、反応容器か
らその外部へのガス漏れ、および外部から反応容
器内への不純物混入等が防止でき、したがつて高
品質の合成ガラスが、作業環境を汚染することな
く安定して製造できる。
``Effects of the Invention'' As explained above, according to the present invention, part or all of the reaction vessel in a predetermined synthetic glass manufacturing apparatus is constituted by a double-walled body having an internal space, and the reaction vessel is Since a gas adjustment mechanism is provided that allows relative adjustment of the gas pressure inside the reaction vessel and the gas pressure in the internal space of the double-walled body with respect to the external gas pressure, the gas pressure inside the reaction vessel is adjusted via the gas adjustment mechanism. By adjusting the gas pressure in the internal space of the double-walled body to an appropriate state, it is possible to prevent gas leakage from the reaction vessel to the outside, and to prevent impurities from entering the reaction vessel from the outside. High-quality synthetic glass can be manufactured stably without contaminating the working environment.

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

図面は本発明に係るガラス合成装置の一実施例
を略示した断面図である。 1……反応容器、2a,2b……ガス導入系、
3……ガス排出系、6……排気フアン、7……ガ
ラス微粒子生成用のバーナ、8……ガラス堆積基
材、10……二重壁体の内部空間、11……二重
壁体、12……給気系、13……排気系の圧力調
整弁、14……排気系、15〜17……圧力計、
18……制御機器、19,20……圧力計のセン
サ、21……多孔質ガラス層、P1……反応容器
外部のガス圧、P2……内部空間のガス圧、P3
…反応容器内部のガス圧。
The drawing is a sectional view schematically showing an embodiment of a glass synthesis apparatus according to the present invention. 1... Reaction container, 2a, 2b... Gas introduction system,
3... Gas exhaust system, 6... Exhaust fan, 7... Burner for generating glass particles, 8... Glass deposition base material, 10... Internal space of double wall body, 11... Double wall body, 12...Air supply system, 13...Exhaust system pressure regulating valve, 14...Exhaust system, 15-17...Pressure gauge,
18...Control equipment, 19, 20...Pressure gauge sensor, 21...Porous glass layer, P1 ...Gas pressure outside the reaction vessel, P2 ...Gas pressure in the internal space, P3 ...
...Gas pressure inside the reaction vessel.

Claims (1)

【特許請求の範囲】 1 ガス導入系、ガス排出系を有する反応容器内
に、ガラス微粒子生成用のバーナと、ガラス堆積
基材とが相互に対応して内装された合成ガラス製
造装置において、上記反応容器の一部または全部
が内部空間を有する二重壁体により構成され、当
該反応容器には、反応容器外部のガス圧に対して
反応容器内部のガス圧、二重壁体の内部空間のガ
ス圧が相対的に調整可能なガス調整機構が設けら
れていることを特徴とする合成ガラス製造装置。 2 ガス調整機構が、反応容器に設けられたガス
導入系およびガス排出系と、二重壁体の内部空間
に連通して設けられた給気系および排気系と、反
応容器内外のガス圧および二重壁体の内部空間の
ガス圧を測定するための圧力計と、反応容器内部
のガス圧および二重壁体の内部空間のガス圧を制
御するための制御機器とからなる特許請求の範囲
第1項記載の合成ガラス製造装置。 3 反応容器外部のガス圧をP1、二重壁体の内
部空間のガス圧をP2、反応容器内部のガス圧を
P3とした場合、これらガス圧がP1<P3<P2の関
係を満足している特許請求の範囲第1項記載の合
成ガラス製造装置。 4 反応容器外部のガス圧をP1、二重壁体の内
部空間のガス圧をP2、反応容器内部のガス圧を
P3とした場合、これらガス圧がP2<P1、P2<P3
の関係を満足している特許請求の範囲第1項記載
の合成ガラス製造装置。 5 二重壁体の内部空間のガス圧が正圧である特
許請求の範囲第1項ないし第4項いずれかに記載
の合成ガラス製造装置。 6 反応容器内へ導入するガスが、不活性ガスま
たはクリーンエアまたはこれらの混合ガスからな
る特許請求の範囲第1項ないし第4項いずれかに
記載の合成ガラス製造装置。 7 二重壁体の内部空間へ導入するガスが、不活
性ガスまたはクリーンエアまたはこれらの混合ガ
スからなる特許請求の範囲第1項ないし第5項い
ずれかに記載の合成ガラス製造装置。 8 クリーンエアのクリーン度が0〜100クラス
である特許請求の範囲第6項または第7項記載の
合成ガラス製造装置。 9 反応容器が石英ガラス、セラミツクスのうち
から選択された任意材料からなる特許請求の範囲
第1項ないし第4項または第6項いずれかに記載
の合成ガラス製造装置。 10 反応容器用の材料が樹脂コーテイングされ
ている特許請求の範囲第1項ないし第4項または
第6項または第9項いずれかに記載の合成ガラス
製造装置。 11 樹脂コーテイング材料がフツ素樹脂または
シリコーン樹脂のいずれかからなる特許請求の範
囲第9項記載の合成ガラス製造装置。
[Scope of Claims] 1. A synthetic glass manufacturing apparatus in which a burner for producing glass fine particles and a glass deposition substrate are installed in a reaction vessel having a gas introduction system and a gas exhaust system in correspondence with each other, Part or all of the reaction vessel is composed of a double-walled body having an internal space, and the reaction vessel has a gas pressure inside the reaction vessel with respect to a gas pressure outside the reaction vessel, and a pressure inside the double-walled body. A synthetic glass manufacturing apparatus characterized by being provided with a gas adjustment mechanism capable of relatively adjusting gas pressure. 2. The gas adjustment mechanism controls the gas introduction system and gas exhaust system provided in the reaction vessel, the air supply system and exhaust system provided in communication with the internal space of the double-walled body, and the gas pressure inside and outside the reaction vessel. Claims consisting of a pressure gauge for measuring the gas pressure in the internal space of the double-walled body, and a control device for controlling the gas pressure inside the reaction vessel and the gas pressure in the internal space of the double-walled body The synthetic glass manufacturing apparatus according to item 1. 3 The gas pressure outside the reaction vessel is P 1 , the gas pressure inside the double-walled body is P 2 , and the gas pressure inside the reaction vessel is P 1 .
The synthetic glass manufacturing apparatus according to claim 1, wherein these gas pressures satisfy the relationship P 1 < P 3 < P 2 when P 3 . 4 The gas pressure outside the reaction vessel is P 1 , the gas pressure inside the double-walled body is P 2 , and the gas pressure inside the reaction vessel is P 1 .
When P 3 , these gas pressures are P 2 < P 1 , P 2 < P 3
A synthetic glass manufacturing apparatus according to claim 1, which satisfies the following relationship. 5. The synthetic glass manufacturing apparatus according to any one of claims 1 to 4, wherein the gas pressure in the internal space of the double-walled body is positive pressure. 6. The synthetic glass manufacturing apparatus according to any one of claims 1 to 4, wherein the gas introduced into the reaction vessel is an inert gas, clean air, or a mixed gas thereof. 7. The synthetic glass manufacturing apparatus according to any one of claims 1 to 5, wherein the gas introduced into the internal space of the double-walled body is an inert gas, clean air, or a mixed gas thereof. 8. The synthetic glass manufacturing apparatus according to claim 6 or 7, wherein the clean air has a cleanliness level of 0 to 100 class. 9. The synthetic glass manufacturing apparatus according to any one of claims 1 to 4 or 6, wherein the reaction vessel is made of an arbitrary material selected from quartz glass and ceramics. 10. The synthetic glass manufacturing apparatus according to any one of claims 1 to 4, 6, or 9, wherein the material for the reaction vessel is coated with a resin. 11. The synthetic glass manufacturing apparatus according to claim 9, wherein the resin coating material is made of either fluororesin or silicone resin.
JP2753086A 1986-02-10 1986-02-10 Synthetic glass manufacturing equipment Granted JPS62187121A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2753086A JPS62187121A (en) 1986-02-10 1986-02-10 Synthetic glass manufacturing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2753086A JPS62187121A (en) 1986-02-10 1986-02-10 Synthetic glass manufacturing equipment

Publications (2)

Publication Number Publication Date
JPS62187121A JPS62187121A (en) 1987-08-15
JPH033615B2 true JPH033615B2 (en) 1991-01-21

Family

ID=12223667

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2753086A Granted JPS62187121A (en) 1986-02-10 1986-02-10 Synthetic glass manufacturing equipment

Country Status (1)

Country Link
JP (1) JPS62187121A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2557651B2 (en) * 1987-07-02 1996-11-27 株式会社フジクラ Optical fiber base material manufacturing method
JP2604454B2 (en) * 1988-12-23 1997-04-30 信越化学工業株式会社 Manufacturing method of single mode optical fiber preform
JPH02243521A (en) * 1989-03-16 1990-09-27 Nippon Telegr & Teleph Corp <Ntt> Fluoride glass rod lens, its production and apparatus therefor
JP5050969B2 (en) * 1998-08-24 2012-10-17 旭硝子株式会社 Synthetic quartz glass optical member and manufacturing method thereof
JP5678711B2 (en) * 2011-02-16 2015-03-04 住友電気工業株式会社 Method for producing glass particulate deposit

Also Published As

Publication number Publication date
JPS62187121A (en) 1987-08-15

Similar Documents

Publication Publication Date Title
EP1405833A1 (en) Device and method for producing stack of fine glass particles
US4414164A (en) Process and apparatus for producing preforms for optical fibers
JP4379554B2 (en) Dehydration sintering method for optical fiber preform
JPH06345469A (en) Production of high-purity transparent glass
EP0231022B1 (en) Apparatus for the production of porous preform of optical fiber
JPH033615B2 (en)
EP1468971A1 (en) Method of manufacturing glass particulate sedimentary body, and method of manufacturing glass base material
US20040055339A1 (en) Method for producing glass-particle deposited body
US4592924A (en) Method of manufacturing a reaction vessel for crystal growth purposes
JP2808857B2 (en) Heating furnace and manufacturing method of glass preform for optical fiber
JP4375333B2 (en) Manufacturing method of glass material
JPH09188523A (en) Silica glass manufacturing method and manufacturing apparatus
JPS62176936A (en) Method and device for producing optical fiber preform
JP3290612B2 (en) Method of detecting core tube crack in sintering process of optical fiber preform and method of manufacturing optical fiber preform
JP2003212561A (en) Glass base material manufacturing method and manufacturing apparatus
EP3153478B1 (en) Apparatus for producing porous glass preform
JP2514689B2 (en) Manufacturing method for optical fiber preform
JPS605030A (en) High purity glass powder and apparatus and method for manufacturing glass products thereby
JP2002104830A (en) Manufacturing method of glass base material
JPH0222137A (en) Production of synthetic quartz preform
JPS62162646A (en) Production of glass fine particle deposit
JP2003192357A (en) Heat treatment method and apparatus for porous glass base material
JPS6283325A (en) Production of quartz glass having high purity
JP3788073B2 (en) Manufacturing method of optical fiber preform
JPH0971430A (en) Method and apparatus for manufacturing optical fiber preform

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees