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JPS5918327B2 - Manufacturing method of optical transmission line - Google Patents
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JPS5918327B2 - Manufacturing method of optical transmission line - Google Patents

Manufacturing method of optical transmission line

Info

Publication number
JPS5918327B2
JPS5918327B2 JP21313782A JP21313782A JPS5918327B2 JP S5918327 B2 JPS5918327 B2 JP S5918327B2 JP 21313782 A JP21313782 A JP 21313782A JP 21313782 A JP21313782 A JP 21313782A JP S5918327 B2 JPS5918327 B2 JP S5918327B2
Authority
JP
Japan
Prior art keywords
refractive index
glass
manufacturing
additive
optical transmission
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
JP21313782A
Other languages
Japanese (ja)
Other versions
JPS58130132A (en
Inventor
浩司 岡村
純二郎 後藤
武志 赤松
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.)
Fujitsu Ltd
Original Assignee
Fujitsu 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 Fujitsu Ltd filed Critical Fujitsu Ltd
Priority to JP21313782A priority Critical patent/JPS5918327B2/en
Publication of JPS58130132A publication Critical patent/JPS58130132A/en
Publication of JPS5918327B2 publication Critical patent/JPS5918327B2/en
Expired 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]
    • C03B37/018Manufacture 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] by glass deposition on a glass substrate, e.g. by inside-, modified-, plasma- or plasma modified- chemical vapour deposition [ICVD, MCVD, PCVD, PMCVD], i.e. by thin layer coating on the inside or outside of a glass tube or on a glass rod
    • C03B37/01861Means for changing or stabilising the diameter or form of tubes or rods
    • 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]
    • C03B37/018Manufacture 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] by glass deposition on a glass substrate, e.g. by inside-, modified-, plasma- or plasma modified- chemical vapour deposition [ICVD, MCVD, PCVD, PMCVD], i.e. by thin layer coating on the inside or outside of a glass tube or on a glass rod
    • C03B37/01807Reactant delivery systems, e.g. reactant deposition burners

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】 本発明は気相化学反応を利用する光伝送線の製造方法の
改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for manufacturing an optical transmission line using a gas phase chemical reaction.

高品位の光伝送線の製造に適する方法として、加熱した
石英ガラス管内壁に、気相化学反応により石英(SiO
2)を主成分とする芯ガラス層を析出させて被着し、し
かる後さらに加熱して中心の空所を無くした棒状の中実
母材を得、この母材を引き伸ばして光学繊維とする工程
が、例えば特開昭50−120352号公報等から周知
である。
As a method suitable for manufacturing high-quality optical transmission lines, quartz (SiO
Step 2) Precipitating and depositing a core glass layer containing 2) as the main component, then further heating to obtain a rod-shaped solid base material with no center void, and stretching this base material to form an optical fiber. is well known, for example, from Japanese Patent Laid-Open No. 120352/1983.

この方法において、芯ガラスの屈折率を制御するフ に
は、石英ガラスの屈折率を高める添加剤、例えば二酸化
ゲルマニウム(GeO2)を、石英の原料となるノ和ゲ
ン化シリコン(例えば四塩化シリコン)中に同じくハロ
ゲン化物の形で混合して同時に反応させてSiO2とと
もにガラス管内壁に析出・o させる。このようにすれ
ば、芯の屈折率プロフィールの形状を容易に所望のよう
にすることができる。ゆえに、中心から半径方向に沿つ
てなだらかに低下してゆく屈折率プロフィールを有する
集束性の光学繊維をこの方法により容易に製すること1
5ができる。しかるに、上記の方法により製した光学繊
維には、屡々中心部の屈折率に異常変化が生じ易い。
In this method, in order to control the refractive index of the core glass, an additive that increases the refractive index of quartz glass, such as germanium dioxide (GeO2), is added to silicon nitride (such as silicon tetrachloride), which is the raw material for quartz. It is also mixed in the form of a halide and reacted at the same time, causing it to precipitate on the inner wall of the glass tube along with SiO2. In this way, the shape of the refractive index profile of the core can be easily made into a desired shape. Therefore, it is possible to easily produce a focusing optical fiber having a refractive index profile that gradually decreases from the center in the radial direction by this method.
I can do 5. However, optical fibers manufactured by the above method are often prone to abnormal changes in the refractive index at the center.

第1図は上記異常変化を生じた一例の屈折率プロフィー
ルを示したもので、中央部に急激なスパイ20 ク状の
落ち込みaが認められる。このような異常が生じた場合
には光学繊維の光伝送性能が著しく劣化することは当然
である。図に示した例は芯ガラスの添加剤としてGe0
2を用いるものであつて、上述した異常の成因は次のよ
うに考えられる。25さきに述べたガラス管の空所を無
くする中実化工程(コラプス工程と呼ばれる)は、20
00℃程度の高温下において行なわれる。
FIG. 1 shows an example of a refractive index profile in which the above-mentioned abnormal change occurred, and a sharp spike-shaped depression a is observed in the center. Naturally, when such an abnormality occurs, the optical transmission performance of the optical fiber is significantly degraded. The example shown in the figure is Ge0 as an additive to the core glass.
2, and the cause of the above-mentioned abnormality is thought to be as follows. 25 The solidification process (called the collapse process) that eliminates the empty spaces in the glass tube described earlier is 20
It is carried out at a high temperature of about 00°C.

ゆえに該コプラス工程で一旦堆積したガラス層からSi
O2及び、GeO2双方の蒸発が起こるが、GeO2は
元来305102に比し易蒸発性であるので、蒸発した
気相中のGeO2濃度は固相中の濃度に比して高いと考
えられ、結局ガラス層表層部でGeO2がファな状態と
なる。さらに、一旦蒸発したSiO2及びGe02は、
低35温部で再び固相となつて再堆積するが、この再堆
積層のGeO2濃度は相当に低いものと推定され、結局
この蒸発−固化再堆積の過程によつて、工程中気相と接
している部分、即ち気相から析出したガラス層表面の、
ごく薄い層において屈折率を高める添加剤(この場合に
はGeO2)の濃度が減少し、結果として第1図に示し
たような屈折率プロフイールの欠陥が生ずるものと考え
られる。
Therefore, Si is removed from the glass layer once deposited in the coplus process.
Evaporation of both O2 and GeO2 occurs, but since GeO2 is inherently more easily evaporated than 305102, the GeO2 concentration in the evaporated gas phase is considered to be higher than the concentration in the solid phase, and as a result, GeO2 is in a free state at the surface layer of the glass layer. Furthermore, once evaporated SiO2 and Ge02,
GeO2 is redeposited again as a solid phase in the low temperature region, but the GeO2 concentration in this redeposited layer is estimated to be quite low, and as a result, through this evaporation-solidification redeposition process, it becomes a solid phase and is redeposited during the process. The contact area, that is, the surface of the glass layer deposited from the gas phase,
It is believed that in very thin layers the concentration of the refractive index enhancing additive (GeO2 in this case) is reduced, resulting in the defective refractive index profile shown in FIG.

本発明は前述の点に鑑みなされたもので、気相化学反応
により析出させたガラス層に、添加剤蒸気を接触せしめ
て中実化工程を行なうことにより所望の屈折率プロフイ
ールを得る、新規なる光伝送線の製造方法を提供せんと
するものである。以下本発明の一実施例につき詳細に説
明する。第2図は本発明の方法による集束性光学繊維の
製造工程の一例を示したもので、1は純粋なSiO2か
ら成る管であつて、内径は10数謂程度である。2は気
相化学反応、例えばSiCl4及びGeCl4の酸化反
応によりSiO,管1の内壁に−旦微粉状で堆積した混
合酸化物層をガラス化して形成したSiO2とGeO2
とのガラス層である。
The present invention has been made in view of the above-mentioned points, and is a novel method for obtaining a desired refractive index profile by bringing additive vapor into contact with a glass layer precipitated by a gas phase chemical reaction and carrying out a solidification process. The present invention aims to provide a method for manufacturing an optical transmission line. An embodiment of the present invention will be described in detail below. FIG. 2 shows an example of the manufacturing process of a focusing optical fiber according to the method of the present invention, in which 1 is a tube made of pure SiO2, and the inner diameter is about 10 or so. 2 is SiO2 and GeO2 formed by vitrifying a mixed oxide layer deposited in the form of fine powder on the inner wall of tube 1 through a gas phase chemical reaction, for example, an oxidation reaction of SiCl4 and GeCl4.
It is a glass layer with.

このガラス層2が完成時には芯ガラスとなることは周知
の通りである。3は管1に沿つて移動する酸水素バーナ
であつて、このバーナ3の移動により前述の混合酸化物
層を順次ガラス化させて所要量のガラス層2を形成後、
さらに加熱温度を上げてSlO2管1を軟化させると、
1aのごとく径が小さくなる。
It is well known that this glass layer 2 becomes core glass when completed. 3 is an oxyhydrogen burner that moves along the tube 1, and by the movement of this burner 3, the aforementioned mixed oxide layer is sequentially vitrified to form the required amount of glass layer 2, and then
If the heating temperature is further increased to soften the SlO2 tube 1,
The diameter becomes smaller as shown in 1a.

従来のコラプス工程においては内部の孔が無くなつて中
実のガラス棒となるまでコラプスを行なうのであるが、
本発明においては内径が1Um程度となれば止める。こ
れはコラプス中管内に添加剤としてのGeO2原料の蒸
気を通するためである。即ち、一旦所要のガラス層2を
堆積後は石英原料としてのS!Cl4の蒸気の導入を停
止し、GeCl4蒸気と、GeCl4を酸化するための
酸素ガス(02)との混合ガスのみをSiO2管1内に
通しつつコラプスを行なう。ガスの流路は、図示の如く
、加熱済みの部分即ち細径の部分から″加熱前の部分へ
と、矢印4のごとく一般のノズル等に於ける流路とは逆
の方向に流すのが良い。この理由は、コラプス時の加熱
で蒸発した混合酸化物の再堆積層がガラス化するに先立
つてGeO,を添加しておくためである。即ち、第2図
のようにすれば、上記添加剤と酸化剤の混合ガスはバー
ナ3の近傍で気相化学反応を起こしてGeO2を生成し
、このGeO2はコラプス時のバーナ3の加熱によつて
蒸発したSlO,とGeO2の混合酸化物と共に当該バ
ーナの下流側低温部のガラス層2上に2aのような形で
再堆積する。ゆえに、この再堆積層2aがバーナ3の移
動で再たびガラス化する際は、その表層(孔の内面)で
のGeO2の濃度低下が補なわれた形となる。このこと
から直ちに予想されるように、ガラス化後の再堆積層2
aの表面に於けるGeO2濃度は、第2図のコラプス工
程に於けるGeO2の添加の度合いに依存し、条件によ
つて充分補なわれない場合もあれば、過補償即ち中心部
でGeO2濃度が不当に増大する場合もある。しかし本
発明者らの実験結果によれば、管内に流す混合ガスの流
量によつて補償の度合いを大幅に調整することが可能で
、従つて調整により殆ど理想的な屈折率プロフイールを
有する光学繊維が得られることが明らかになつた。なお
、前述のようにして孔の内径が細径となつた石英管は、
さらに従来のコラプス工程と同様の工程によつて中実の
ガラス棒となし、その後延伸して繊維状の光伝送線とす
る。第3図A及びBは、従来の製造法によつて製した光
学繊維の屈折率プロフイールと、本発明の製造法によつ
た場合のそれとを比較したものであつて、材料は両者に
おいて同一である。
In the conventional collapse process, collapse is performed until the internal pores disappear and the glass rod becomes a solid glass rod.
In the present invention, it is stopped when the inner diameter reaches about 1 Um. This is to pass the vapor of the GeO2 raw material as an additive into the tube during the collapse. That is, once the required glass layer 2 is deposited, S! The introduction of Cl4 vapor is stopped, and collapse is performed while passing only a mixed gas of GeCl4 vapor and oxygen gas (02) for oxidizing GeCl4 into the SiO2 tube 1. As shown in the figure, the gas flow path is to flow in the opposite direction to the flow path in a general nozzle, etc., as shown by arrow 4, from the heated part, that is, the small diameter part, to the unheated part. Good. The reason for this is that GeO is added before the redeposited layer of mixed oxide evaporated by heating during collapse becomes vitrified. That is, if you do as shown in Figure 2, the above The mixed gas of the additive and the oxidizer causes a gas phase chemical reaction near the burner 3 to generate GeO2, and this GeO2 is evaporated by the heating of the burner 3 during the collapse, together with the mixed oxide of SlO and GeO2. It is redeposited in the form 2a on the glass layer 2 in the downstream low-temperature part of the burner.Therefore, when this redeposited layer 2a is vitrified again by the movement of the burner 3, the surface layer (the inner surface of the hole) ) in the redeposited layer 2 after vitrification.
The GeO2 concentration at the surface of a depends on the degree of GeO2 addition in the collapse process shown in Fig. 2, and depending on the conditions, it may not be sufficiently compensated, or the GeO2 concentration at the center may be overcompensated. may increase unreasonably. However, according to the experimental results of the present inventors, it is possible to greatly adjust the degree of compensation by changing the flow rate of the mixed gas flowing into the tube, and therefore, by adjusting the degree of compensation, it is possible to create an optical fiber with an almost ideal refractive index profile. It became clear that it was possible to obtain In addition, the quartz tube with the inner diameter of the hole made small as described above,
Further, it is formed into a solid glass rod through a process similar to the conventional collapse process, and then stretched to form a fibrous optical transmission line. Figures 3A and 3B compare the refractive index profile of an optical fiber manufactured by a conventional manufacturing method and that of an optical fiber manufactured by the manufacturing method of the present invention, and the materials are the same in both. be.

すなわち、第3図Aの従来の製造法によつたものは第1
図の再掲であり、具体的にはSiCl4の流量を4.5
m01/Min,.O2の流量を1000CC/Min
にそれぞれ固定し、GeCl4の流量を0.68×10
−4m01/Minから3.4X10−3m01/Mi
nまで50等分した分量ずつ増加させながら内径127
nmのSiO2管内に50層のガラス層を堆積させ、こ
れを通常の方法でコラツプスして繊維とした場合の屈折
率プロフイールを示している。これに対し、上記従来例
と同様の条件で50層のガラス層を堆積した後、本発明
に従つてコラツプス時に酸素の流量(1000CC/M
in)は変えないでGeC!4を4.0X10″5m0
1/Minの流量で流した場合、従来例に見られた屈折
率プロフイール中心部の欠陥aは殆ど安全に補償されて
、第3図Bのように理想に近いフ狛フイールを得ること
ができた。GeCl4の流量がこれ以上多くなると過補
償となつて中心部での屈折率が高くなり過ぎ、流量がそ
れよりも少ないと補償が不充分となる。なお、先に参照
した特開昭50−120352号等においてコラツプス
時にも反応性の原料ガスを流すことは周知であるが、ガ
ラス堆積時と同様にSiCl4とGeCl4の両方のガ
スを流したのでは、いかにGeCl4リツチに保つても
本発明のような効果を得るのは困難である。
In other words, the conventional manufacturing method shown in Figure 3A is
This is a reprint of the figure, and specifically, the flow rate of SiCl4 is 4.5
m01/Min,. O2 flow rate 1000CC/Min
and fixed the GeCl4 flow rate to 0.68×10
-4m01/Min to 3.4X10-3m01/Mi
Inner diameter 127 while increasing the amount divided into 50 equal parts up to n
The refractive index profile is shown when 50 glass layers are deposited in a nanometer SiO2 tube and collapsed into a fiber using conventional methods. On the other hand, after depositing 50 glass layers under the same conditions as the conventional example, according to the present invention, the flow rate of oxygen (1000 CC/M
in) without changing GeC! 4 to 4.0X10″5m0
When flowing at a flow rate of 1/Min, the defect a at the center of the refractive index profile seen in the conventional example is almost safely compensated for, and it is possible to obtain a nearly ideal foil as shown in Figure 3B. Ta. If the flow rate of GeCl4 is higher than this, overcompensation will occur and the refractive index at the center will become too high, and if the flow rate is lower than this, the compensation will be insufficient. Incidentally, it is well known that reactive raw material gases are flowed during collapse in the previously referenced Japanese Patent Application Laid-open No. 50-120352, etc., but it seems that both SiCl4 and GeCl4 gases were flowed in the same way as during glass deposition. However, no matter how rich GeCl4 is kept, it is difficult to obtain the effect of the present invention.

第4図は、先に述べた従来法で50層のガラス堆積層を
形成した後、SiCl4のガス流量は最終層形成時と同
じ4.5X10−3m01/Minに保ち、GeCl4
の流量を1.3×10−2m01/Minに増加してコ
ラツスしたものの屈折率プロフイールを示している。こ
の第4図から明らかなように、いかにGeCl4リツチ
であつてもSiCl4を含んだガスを用いる限り、中心
部周辺b部で再堆積層により屈折率が増大するものの、
該再堆積層のガラス化時には表層部からGeO2が多く
蒸発してSlO2が優先的に残存し、結局屈折率の落ち
込み部aを補償することができないわけである。以上説
明した実施例は芯がなだらかな屈折率プロフイールを有
する光学繊維に本発明の製造方法を適用した場合である
が、芯の屈折率が全体に亘り一様な光学繊維を製造する
場合にも、芯材の添加剤として易蒸発性物質を用いる限
り中心部に於ける添加剤濃度の低下、従つて屈折率プロ
フイールの落ち込みが生ずることは当然で、この場合に
も本発明の方法を用いれば好結果を得られる。
Figure 4 shows that after forming 50 glass deposited layers using the conventional method described above, the SiCl4 gas flow rate was kept at 4.5 x 10-3 m01/Min, the same as when forming the final layer, and the GeCl4
The figure shows a refractive index profile obtained by increasing the flow rate to 1.3 x 10-2 m01/Min and collapsing it. As is clear from FIG. 4, no matter how rich GeCl4 is, as long as a gas containing SiCl4 is used, the refractive index will increase due to the redeposited layer in part b around the center.
When the redeposited layer is vitrified, a large amount of GeO2 evaporates from the surface layer, and SlO2 preferentially remains, and as a result, it is not possible to compensate for the depressed portion a of the refractive index. The embodiments described above are cases where the manufacturing method of the present invention is applied to an optical fiber whose core has a gentle refractive index profile, but it can also be applied to the case where the manufacturing method of the present invention is applied to an optical fiber whose core has a uniform refractive index throughout. As long as an easily evaporable substance is used as an additive in the core material, it is natural that the concentration of the additive in the center will decrease, and therefore the refractive index profile will drop.If the method of the present invention is used in this case as well, Good results can be obtained.

本発明の製造方法によれば、光伝送線の芯ガラスとして
易蒸発性の添加剤を含むSlO2等を用い、気相化学反
応法により該芯ガラスを形成する際の添加剤濃度変化に
起因する屈折率プロフイールの異常を防止することがで
き、理想的な屈折率プロフイール、従つて理想的な光伝
送特性を有する光伝送線を製造し得る優れた利点がある
。それゆえとくに集束性光伝送線の製造に適用して甚だ
有利である。
According to the manufacturing method of the present invention, SlO2 or the like containing an easily evaporable additive is used as the core glass of the optical transmission line, and the change in the additive concentration occurs when the core glass is formed by a vapor phase chemical reaction method. There is an excellent advantage that abnormalities in the refractive index profile can be prevented and that an optical transmission line having an ideal refractive index profile and therefore ideal optical transmission characteristics can be manufactured. It is therefore particularly advantageous to apply it to the production of convergent optical transmission lines.

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

第1図は従来の製造方法によつて製した集束性光伝送線
の屈折率プロフイールを示す線図、第2図は本発明に係
る製造方法の一実施態様を説明するための断面図、第3
図Aは従来の製造方法により製した光伝送線の屈折率プ
ロフイールを示す線図、同じくBは本発明の製造方法に
よつた光伝送線の屈折率プロフイールを示す線図、第4
図はコラツプス時にSiCl4とGeCl4との混合ガ
スを流した場合の屈折率プロフイールを示す線図である
。 a:屈折率の落ち込み、1:石英管、2:ガラス層、2
a:再堆積層、3:バーナ、4:添加剤蒸気の流通方向
FIG. 1 is a diagram showing the refractive index profile of a convergent optical transmission line manufactured by a conventional manufacturing method, FIG. 2 is a cross-sectional view for explaining one embodiment of the manufacturing method according to the present invention, 3
Figure A is a diagram showing the refractive index profile of an optical transmission line manufactured by the conventional manufacturing method, and Figure B is a diagram showing the refractive index profile of the optical transmission line manufactured by the manufacturing method of the present invention.
The figure is a diagram showing the refractive index profile when a mixed gas of SiCl4 and GeCl4 is flowed during collapse. a: drop in refractive index, 1: quartz tube, 2: glass layer, 2
a: redeposition layer, 3: burner, 4: flow direction of additive vapor.

Claims (1)

【特許請求の範囲】[Claims] 1 ガラス管内に、石英の原料および石英に対する屈折
率制御用添加剤の原料を含むガスを導入して当該ガラス
管内壁に気相化学反応により所要量のガラス層を被着形
成した後、上記石英の原料の導入を停止して、上記添加
剤の原料と、該原料を所要の添加剤に変える反応剤とを
ガス状態で流しつつ上記ガラス管を加熱して管内空所の
径を充分小さくし、しかる後中実化し、かつ線状ガラス
体となすことを特徴とする光伝送線の製造方法。
1. A gas containing a raw material for quartz and a raw material for an additive for controlling the refractive index for quartz is introduced into a glass tube, and a required amount of glass layer is deposited on the inner wall of the glass tube by a vapor phase chemical reaction. The introduction of the raw material is stopped, and the glass tube is heated while the raw material for the additive and the reactant for converting the raw material into the required additive are flowed in a gaseous state to sufficiently reduce the diameter of the cavity inside the tube. , and then solidifying it into a linear glass body.
JP21313782A 1982-12-03 1982-12-03 Manufacturing method of optical transmission line Expired JPS5918327B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21313782A JPS5918327B2 (en) 1982-12-03 1982-12-03 Manufacturing method of optical transmission line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21313782A JPS5918327B2 (en) 1982-12-03 1982-12-03 Manufacturing method of optical transmission line

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP7176476A Division JPS52153750A (en) 1976-06-17 1976-06-17 Production of optical transmission wire

Publications (2)

Publication Number Publication Date
JPS58130132A JPS58130132A (en) 1983-08-03
JPS5918327B2 true JPS5918327B2 (en) 1984-04-26

Family

ID=16634184

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21313782A Expired JPS5918327B2 (en) 1982-12-03 1982-12-03 Manufacturing method of optical transmission line

Country Status (1)

Country Link
JP (1) JPS5918327B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3929604A1 (en) * 1988-09-12 1990-03-15 Schott Glaswerke INTERNAL COATING OF A TUBE

Also Published As

Publication number Publication date
JPS58130132A (en) 1983-08-03

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