JPS604977Y2 - Raw material supply equipment for manufacturing optical fiber base material - Google Patents
Raw material supply equipment for manufacturing optical fiber base materialInfo
- Publication number
- JPS604977Y2 JPS604977Y2 JP6795880U JP6795880U JPS604977Y2 JP S604977 Y2 JPS604977 Y2 JP S604977Y2 JP 6795880 U JP6795880 U JP 6795880U JP 6795880 U JP6795880 U JP 6795880U JP S604977 Y2 JPS604977 Y2 JP S604977Y2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- glass raw
- container
- optical fiber
- material container
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Landscapes
- Manufacture, Treatment Of Glass Fibers (AREA)
Description
【考案の詳細な説明】
本考案はVAD法による光フアイバ用母材の製造におい
て、母材の主原料である四塩化シリコンの自動供給装置
に関するものである。[Detailed Description of the Invention] The present invention relates to an automatic supply device for silicon tetrachloride, which is the main raw material of the base material, in the production of optical fiber base materials by the VAD method.
従来、この種の装置は、ガラスの゛原料となる四塩化け
い素およびドーピング物質、たとえば四塩化ゲルマニウ
ム、オキシ塩化りん、三臭化はう素等を、各原料容器内
に充填し、流量制御されたキャリアガス、たとえばアル
ゴンガスを各容器内の液状ガラス原料中にバブリングし
て所望の上記各原料の蒸気を得るように構成されていた
。Conventionally, this type of equipment fills silicon tetrachloride, which is the raw material for glass, and doping substances, such as germanium tetrachloride, phosphorus oxychloride, boron tribromide, etc., into each raw material container, and controls the flow rate. The apparatus was configured to bubble a carrier gas such as argon gas into the liquid glass raw material in each container to obtain the desired vapor of each of the raw materials.
第1図はこのような装置の一具体例の構成を示した概略
図であり、1はガラス製原料用容器、2はバブラ、3は
蒸気状ガラス原料の出口、4は液状ガラス原料の供給口
、5は液状ガラス原料、6はチャンバ、7は温風ヒータ
、8は液状原料収納タンク、9はバルブを表わす。FIG. 1 is a schematic diagram showing the configuration of a specific example of such an apparatus, in which 1 is a container for glass raw materials, 2 is a bubbler, 3 is an outlet for vaporized frit, and 4 is a supply for liquid glass raw material. 5 is a liquid glass raw material, 6 is a chamber, 7 is a hot air heater, 8 is a liquid raw material storage tank, and 9 is a valve.
容器1において、キャリアガスは流量制御されてバブラ
2から吹き出し液状ガラス原料5をバブリングして蒸気
状ガラス原料が得られる。In the container 1, the carrier gas is blown out from the bubbler 2 with its flow rate controlled and bubbles the liquid glass raw material 5 to obtain a vaporous glass raw material.
液状ガラス原料は時間の経過とともに減少するので、減
少量に応じて液状ガラス原料を容器内に供給しなければ
ならない。Since the liquid glass raw material decreases with the passage of time, the liquid glass raw material must be supplied into the container according to the amount of decrease.
従来、液状ガラス原料の供給方法は、液状ガラス原料収
納タンク8と供給口4を耐蝕性パイプで接続し、不活性
ガス、たとえばアルゴンガスなどによって圧力を加え、
液状ガラス原料5の液面が所定の位置、たとえば1or
lrIIL低下したところでバルブ9を開き、液状ガラ
ス原料を供給する方法が行われている。Conventionally, the method for supplying liquid glass raw materials is to connect the liquid glass raw material storage tank 8 and the supply port 4 with a corrosion-resistant pipe, apply pressure with an inert gas such as argon gas, etc.
When the liquid level of the liquid frit 5 is at a predetermined position, for example 1 or
A method is used in which the valve 9 is opened when lrIIL decreases and liquid glass raw material is supplied.
しかしこの供給方法は、圧力によって原料を供給するの
で、バルブ9を開いた瞬間に原料容器1内の圧力が高く
なり、蒸気状ガラス原料の出口3から得られる蒸気状ガ
ラス原料量は、その圧力変化に応じて増減し、ガラス原
料の供給が終るまで、これらの変動が続く。However, in this supply method, the raw material is supplied under pressure, so the pressure inside the raw material container 1 increases at the moment the valve 9 is opened, and the amount of vaporous frit obtained from the outlet 3 of the vaporous frit depends on the pressure. It increases and decreases according to changes, and these fluctuations continue until the supply of glass raw materials ends.
この結果、蒸気状ガラス原料を安定に供給することがで
きず、これによって作製される光フアイバ用母材の屈折
率は、微少なゆらぎが生じることになり、光ファイバの
光学特性に悪影響を及ぼすことになる。As a result, it is not possible to stably supply the vaporized glass raw material, and the refractive index of the optical fiber base material produced by this causes slight fluctuations, which adversely affects the optical properties of the optical fiber. It turns out.
本考案はこれらの欠点を解決するためになされたもので
あり、その目的は、液状ガラス原料の供給時に生じるガ
ラス原料用容器内の圧力変動を防止し、蒸気状ガラス原
料を安定に供給し得る光フアイバ母材製造用原料供給装
置を提供することにある。The present invention was devised to solve these drawbacks, and its purpose is to prevent pressure fluctuations in the frit container that occur when liquid frit is supplied, and to stably supply vaporized frit. An object of the present invention is to provide a raw material supply device for manufacturing an optical fiber base material.
本考案について概説すれば、本考案の光フアイバ母材製
造用原料供給装置は、液状ガラス原料を収納タンクから
容器に供給し、これにキャリアガスをバブリングして、
蒸気状ガラス原料およびキャリアガスの混合物として供
給する光フアイバ母材製造用原料供給装置において、ガ
ラス原料用容器に設けた液状ガラス原料供給管路4中に
圧力調整用原料容器を設けたものである。To summarize the present invention, the raw material supply device for producing an optical fiber base material of the present invention supplies liquid glass raw material from a storage tank to a container, bubbles carrier gas into it,
In a raw material supply device for producing an optical fiber preform, which supplies a mixture of a vaporous glass raw material and a carrier gas, a raw material container for pressure adjustment is provided in a liquid glass raw material supply pipe 4 provided in a glass raw material container. .
本考案による圧力調整用原料容器を設けた原料供給系に
おいては、液状ガラス原料をガラス原料用容器に供給す
ることによって生じるガラス原料容器内の圧力変動が防
止されて、常に一定圧力の蒸気状ガラス原料が得られ、
これにより製造される光フアイバ母材の屈折率(Δn)
のゆらぎも著しく減少させることができる。In the raw material supply system equipped with the pressure-adjusting raw material container according to the present invention, pressure fluctuations in the glass raw material container caused by supplying liquid glass raw material to the glass raw material container are prevented, and the vaporized glass is always maintained at a constant pressure. raw materials are obtained,
Refractive index (Δn) of the optical fiber base material manufactured by this method
fluctuations can also be significantly reduced.
次に、本考案の実施例を図面により詳細に説明する。Next, embodiments of the present invention will be described in detail with reference to the drawings.
第2図は光フアイバ母材製造用原料供給系の一具体例の
構成を示す概略図であり、1および13は原料容器、2
はバブラ、4は原料供給口、5および14は四塩化けい
素、6はチャンバ、7は温風装置、8は四塩化シリコン
収納タンク、9.10,11および12はバルブ、15
はキリアガス、16は蒸気状ガラス原料、17は圧力調
整管、18は液面検知器を示す。FIG. 2 is a schematic diagram showing the configuration of a specific example of a raw material supply system for manufacturing optical fiber preforms, in which 1 and 13 are raw material containers, 2
is a bubbler, 4 is a raw material supply port, 5 and 14 are silicon tetrachloride, 6 is a chamber, 7 is a hot air device, 8 is a silicon tetrachloride storage tank, 9. 10, 11 and 12 are valves, 15
16 is a vaporized glass raw material, 17 is a pressure adjustment tube, and 18 is a liquid level detector.
四塩化けい素収納タンク8と圧力調整用原料容器13を
テフロン管で接続し、その管路中にバルブ11を設けた
。The silicon tetrachloride storage tank 8 and the raw material container 13 for pressure adjustment were connected with a Teflon pipe, and a valve 11 was provided in the pipe line.
圧力調整用原料容器13の上部に排気管をつけ、その管
路中にバルブ12を設けた。An exhaust pipe was attached to the upper part of the raw material container 13 for pressure adjustment, and a valve 12 was provided in the pipe line.
圧力調整用原料容器13の上部と原料容器1の上部をテ
フロン管で接接し、その管路中にバルブ10を設けた。The upper part of the raw material container 13 for pressure adjustment and the upper part of the raw material container 1 were connected to each other by a Teflon pipe, and a valve 10 was provided in the pipe line.
圧力調整用原料容器13の下部と原料容器を原料供給管
4で接続し、その管路中にバルブ9を設けた。The lower part of the pressure regulating raw material container 13 and the raw material container were connected by a raw material supply pipe 4, and a valve 9 was provided in the pipe.
また原料供給管4は、原料容器1に充填される四塩化け
い素5の液面より下部になるように長くした。Further, the raw material supply pipe 4 was made long so as to be located below the liquid level of the silicon tetrachloride 5 filled in the raw material container 1.
次に本考案の動作を説明する。Next, the operation of the present invention will be explained.
温風ヒータ7によってチャンバ6内の温度を40℃に昇
温した。The temperature inside the chamber 6 was raised to 40° C. by the hot air heater 7.
次にバルブ9,10.11および12を開き、四塩化け
い素収納タンク8に、アルゴンガスによって0.15に
9/C71!の圧力を加えて、四塩化けい素を原料容器
1に充填した。Next, open valves 9, 10, 11 and 12, and add 9/C71! to 0.15 with argon gas to the silicon tetrachloride storage tank 8! The raw material container 1 was filled with silicon tetrachloride by applying a pressure of .
原料容器1に四塩化けい素が充填された後、バルブ9を
閉じて圧力調整用原料容器13に四塩化けい素を充填し
、バルブ11および12を閉じた。After the raw material container 1 was filled with silicon tetrachloride, the valve 9 was closed, the pressure-adjusting raw material container 13 was filled with silicon tetrachloride, and the valves 11 and 12 were closed.
このような状態において、100cc/minに制御さ
れたアルゴンキャリアガス15をバブラ2に流して、四
塩化けい素5をバブリングして蒸気状四塩化けい素16
を得た。In such a state, argon carrier gas 15 controlled at 100 cc/min is flowed through bubbler 2 to bubble silicon tetrachloride 5 to form vaporized silicon tetrachloride 16.
I got it.
1時間経過した後、四塩化けい素5の液面が初期状態よ
り1−低下した。After 1 hour had passed, the liquid level of silicon tetrachloride 5 was lowered by 1 - from the initial state.
ここでバルブ9を開き、圧力調整用原料容器13中の四
塩化けい素14を原料容器1中に充填し、四塩化けい素
5の液面が初期状態にもどった時点でバルブ9を閉じた
。Here, the valve 9 was opened, and the silicon tetrachloride 14 in the pressure adjustment raw material container 13 was filled into the raw material container 1, and when the liquid level of the silicon tetrachloride 5 returned to the initial state, the valve 9 was closed. .
これらの作業中、蒸気状原料の出口3側の圧力変動は、
はとんど認められなかった。During these operations, the pressure fluctuation on the outlet 3 side of the vaporous raw material is as follows:
was hardly recognized.
この結果は、バルブ9を開いて原料容器1中に四塩化け
い素を充填する際、原料容器1の中の四塩化けい素液面
の上部空間の圧力は高くなるが、この圧力増加分は管路
17を経て、圧力調整用原料容器13に吸収されたと結
論できる。This result shows that when opening the valve 9 and filling silicon tetrachloride into the raw material container 1, the pressure in the space above the silicon tetrachloride liquid level in the raw material container 1 increases, but this pressure increase is It can be concluded that the liquid was absorbed into the pressure regulating raw material container 13 via the pipe line 17.
本考案者らはこの原料供給系を用いて、蒸気状ガラス原
料を得、この原料によって光フアイバ用母材を作製した
結果、母材の長尺方向の屈折率(Δn)変化は0.01
%以下であった。The present inventors used this raw material supply system to obtain a vaporized glass raw material, and as a result of producing an optical fiber base material using this raw material, the change in refractive index (Δn) in the longitudinal direction of the base material was 0.01.
% or less.
なお比較のために、圧力調整用原料容器13を設けず、
原料供給口4とバルブ11を接続しての実験を行ったが
、この場合には、原料を供給する際の圧力変動が大きく
、得られた光フアイバ母材の長尺方向の屈折率(Δn)
変化は0.2%と大きく、母材の寸法精度も悪くなった
。For comparison, the raw material container 13 for pressure adjustment was not provided.
An experiment was conducted by connecting the raw material supply port 4 and the valve 11, but in this case, the pressure fluctuation when supplying the raw material was large, and the refractive index (Δn) of the obtained optical fiber base material in the longitudinal direction was )
The change was as large as 0.2%, and the dimensional accuracy of the base material also deteriorated.
また本考案は4個のバルブの開閉を簡単なリレー回路を
用いて連動させることにより自動化することができ、こ
のため、長尺ファイバ、たとえば500〜1000km
相当量の一定な蒸気状ガラス原料を自動的に、かつ簡単
に得ることができる。Furthermore, the present invention can automate the opening and closing of four valves by interlocking them using a simple relay circuit.
A considerable amount of constant vaporized glass raw material can be obtained automatically and easily.
さらに本考案によれば、液面検知器18を原料用容器1
に取り付け、液面検知器18とバルブ9を連動させるこ
とにより、液面の低下を任意に設定でき、その設定値ま
で液面が低下すると、原料の自動供給が行われるように
することもできる。Furthermore, according to the present invention, the liquid level detector 18 is connected to the raw material container 1.
By connecting the liquid level detector 18 and the valve 9, it is possible to arbitrarily set the drop in the liquid level, and when the liquid level falls to the set value, the raw material can be automatically supplied. .
以上説明したように、本考案によれば、圧力調整用原料
容器を設けたことにより、原料を供給することによって
生じる原料容器内の圧力変化による影響が改善され、常
に一定圧力の蒸気状ガラス原料を、長時間にわたり供給
することができ、この原料によって製造された光フアイ
バ用母材の長尺方向の屈折率(Δn)変動も最少限度に
抑えることができる。As explained above, according to the present invention, by providing the raw material container for pressure adjustment, the influence of pressure changes in the raw material container caused by supplying raw materials is improved, and the vaporized glass raw material is kept at a constant pressure. can be supplied over a long period of time, and fluctuations in the refractive index (Δn) in the longitudinal direction of the optical fiber base material manufactured from this raw material can also be suppressed to a minimum.
第1図は従来の原料供給装置の構成を示す概略図、第2
図は本考案による原料供給装置の構成を示す概略図であ
る。
1.13・・・・・・原料用容器、2・・・・・・バブ
ラ、3・・・・・・蒸気状ガラス原料の出口、4・・・
・・・液状ガラス原料の供給口、5,14・・・・・・
液状ガラス原料、6・・・・・・チャンバ、7・・・・
・・温風ヒータ、訃・曲設状原料収納タンク、9.1G
、11,12・・曲バルブ、15・・・・・・キャリア
ガス、16・・・・・・蒸気状ガラス原料、17・・・
・・・圧力調整管、18・・・・・・液面検知器。Figure 1 is a schematic diagram showing the configuration of a conventional raw material supply device;
The figure is a schematic diagram showing the configuration of a raw material supply device according to the present invention. 1.13... Container for raw material, 2... Bubbler, 3... Outlet for vaporized glass raw material, 4...
...Liquid glass raw material supply port, 5, 14...
Liquid glass raw material, 6...chamber, 7...
・・Hot air heater, curved raw material storage tank, 9.1G
, 11, 12...Bent valve, 15...Carrier gas, 16...Vaporous glass raw material, 17...
...Pressure adjustment pipe, 18...Liquid level detector.
Claims (1)
原料をガラス原料容器に充填し、これにキャリアガスを
バブリングして蒸気状ガラス原料を供給する光フアイバ
母材製造用原料供給装置において、前記液状ガラス収納
タンクと前記ガラス原料用容器を結ぶ原料供給管路中に
、液状ガラス原料を一時的に収納する原料用容器を設け
、この原料用容器の上部空間と、前記ガラス原料用容器
の上部空間とを連結することを特徴とする光フアイバ母
材製造用原料供給装置。In the raw material supply device for producing an optical fiber preform, the liquid glass raw material storage tank is filled with liquid glass raw material into a glass raw material container under pressure from the liquid glass raw material storage tank, and the vaporized glass raw material is supplied by bubbling carrier gas into the glass raw material container. A raw material container for temporarily storing the liquid glass raw material is provided in a raw material supply pipe connecting the glass raw material container and the glass raw material container, and the upper space of the raw glass raw material container is connected to the upper space of the glass raw material container. A raw material supply device for manufacturing an optical fiber base material, characterized in that:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6795880U JPS604977Y2 (en) | 1980-05-16 | 1980-05-16 | Raw material supply equipment for manufacturing optical fiber base material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6795880U JPS604977Y2 (en) | 1980-05-16 | 1980-05-16 | Raw material supply equipment for manufacturing optical fiber base material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56170233U JPS56170233U (en) | 1981-12-16 |
JPS604977Y2 true JPS604977Y2 (en) | 1985-02-15 |
Family
ID=29661929
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6795880U Expired JPS604977Y2 (en) | 1980-05-16 | 1980-05-16 | Raw material supply equipment for manufacturing optical fiber base material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS604977Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6031777B2 (en) * | 1982-11-19 | 1985-07-24 | 住友電気工業株式会社 | Raw material gas supply device |
-
1980
- 1980-05-16 JP JP6795880U patent/JPS604977Y2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS56170233U (en) | 1981-12-16 |
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