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JPS5930658B2 - Method for manufacturing cylindrical glass with radially varying refractive index - Google Patents
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JPS5930658B2 - Method for manufacturing cylindrical glass with radially varying refractive index - Google Patents

Method for manufacturing cylindrical glass with radially varying refractive index

Info

Publication number
JPS5930658B2
JPS5930658B2 JP7269577A JP7269577A JPS5930658B2 JP S5930658 B2 JPS5930658 B2 JP S5930658B2 JP 7269577 A JP7269577 A JP 7269577A JP 7269577 A JP7269577 A JP 7269577A JP S5930658 B2 JPS5930658 B2 JP S5930658B2
Authority
JP
Japan
Prior art keywords
soot
nozzle
refractive index
radial direction
cylindrical glass
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP7269577A
Other languages
Japanese (ja)
Other versions
JPS547355A (en
Inventor
達夫 伊沢
豪太郎 田中
裕一 増田
武信 東本
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.)
Sumitomo Electric Industries Ltd
NTT Inc
Original Assignee
Nippon Telegraph and Telephone Corp
Sumitomo Electric Industries 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 Nippon Telegraph and Telephone Corp, Sumitomo Electric Industries Ltd filed Critical Nippon Telegraph and Telephone Corp
Priority to JP7269577A priority Critical patent/JPS5930658B2/en
Publication of JPS547355A publication Critical patent/JPS547355A/en
Publication of JPS5930658B2 publication Critical patent/JPS5930658B2/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]
    • C03B37/01413Reactant delivery systems
    • C03B37/0142Reactant deposition burners
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/60Relationship between burner and deposit, e.g. position
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/60Relationship between burner and deposit, e.g. position
    • C03B2207/66Relative motion

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】 本発明は光通信用自己集束型ファイバを作るためのガラ
ス母材の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of manufacturing a glass preform for making a self-focusing fiber for optical communications.

第1図は1本のノズルで径方向に屈折率の異なるガラス
を作る為のスート積層体を合成する様子を示した図であ
り、1はスート積層体、2はスート合成用ノズル、3は
スートを示す。図に示す様にスート合成用ノズル2は円
盤状出発部材5の径方向に等速度で往復移動させられる
。一方、ノズルにより合成されるスート3の組成及びそ
の量はノズルの往復移動に同期して周期的に変化させら
れながら回転している出発部材5上に吹さつけられ、ス
ートが積層せられる。合成されるスート量はノズルが外
周部に移動するにつれて多くされる理由は、スートの積
層厚を通常、一定の厚みに保持する為に行われる。スー
トの原料としては通常SiCl4、GeCl4、BBr
3、POCl3等のガラス形成用ハロゲン化物が使用さ
れ、これらの原料はO2、N2、Ar等のガスにより蒸
気状体にされてスート合成用ノズルに輸送される。スー
ト合成用ノズルは、ガラス形成用ハロゲン化物を高温酸
化させたり或いはHo、O。ガスにより火炎加水分解さ
せたりする事によりスートを合成する為のノズルである
。円盤状出発部材は回転され、スートの積層量に応じて
下降せられる。所定量積層されたスートは、高温炉中で
焼結され透明化ガラス化される。第2図は複数個例えば
2本のノズルを使用した例である。各々のノズルからは
異なつた組成のスートが合成されるがこの場合には、1
本のノズルより合成されるスートの組成は時間的に変化
させる必要はなく、ノズルの往復移動に同期して、各各
のノズル2−i、2−゛で合成されるスート3−i、3
−iiの相対量が変化される。ノズル2−i、2−ii
は両者とも等速度で径方向に移動せられ、円盤状出発部
材は回転され、スートの成長に従い下降せられる。
Figure 1 shows how a soot laminate is synthesized using a single nozzle to produce glasses with different refractive indexes in the radial direction. 1 is a soot laminate, 2 is a nozzle for soot synthesis, and 3 is a soot laminate nozzle. Indicates suit. As shown in the figure, the soot synthesis nozzle 2 is reciprocated in the radial direction of the disc-shaped starting member 5 at a constant speed. On the other hand, the composition and amount of the soot 3 synthesized by the nozzle are periodically changed in synchronization with the reciprocating movement of the nozzle, and the soot is sprayed onto the rotating starting member 5, thereby stacking the soot. The reason why the amount of soot to be synthesized increases as the nozzle moves toward the outer periphery is to maintain the layered soot thickness at a constant thickness. Soot raw materials are usually SiCl4, GeCl4, BBr
3. Glass-forming halides such as POCl3 are used, and these raw materials are made into a vapor state with gases such as O2, N2, Ar, etc. and transported to the soot synthesis nozzle. The soot synthesis nozzle is used to oxidize glass-forming halides at high temperatures, or to oxidize Ho, O. This is a nozzle for synthesizing soot by flame hydrolysis with gas. The disc-shaped starting member is rotated and lowered depending on the amount of soot stacked. The soot layered in a predetermined amount is sintered in a high-temperature furnace to become transparent and vitrified. FIG. 2 shows an example in which a plurality of nozzles, for example two nozzles, are used. Soots with different compositions are synthesized from each nozzle, but in this case, 1
The composition of the soot synthesized by the main nozzle does not need to be changed over time, and the soot 3-i, 3 synthesized by each nozzle 2-i, 2-゛ is synchronized with the reciprocating movement of the nozzle.
The relative amount of -ii is changed. Nozzle 2-i, 2-ii
are both moved radially at the same speed, and the disc-shaped starting member is rotated and lowered as the soot grows.

例1 SiO2−GeO22成分系ガラスで径方向に屈折率変
化をもたせたガラスを合成する為に、原料としてSlC
l4及びGeCl4を用い、キヤリアガスとして02を
用い、第3図に示す様に周期的に両ハブ(ラ一に送るキ
ヤリアガスの比率α 及びSiCl4用キヤリアガス量V,を変化させ、1本
のスート合成用ノズル(酸水素バーナ)に送り込んだ。
Example 1 In order to synthesize a SiO2-GeO2 binary glass with a refractive index change in the radial direction, SlC was used as a raw material.
Using SiCl4 and GeCl4, and using 02 as a carrier gas, the ratio α of carrier gas sent to both hubs (Ra1) and the carrier gas amount V for SiCl4 were changed periodically as shown in Fig. It was fed into the nozzle (oxygen hydrogen burner).

SiCl4,GeCl4のバブラ一温度はそれぞれ20
℃、及び40℃である。
The bubbler temperature of SiCl4 and GeCl4 is 20
℃, and 40℃.

αとしては0より0.4まで変化させ、V,としてはO
より200sccmまで変化させた。
α is varied from 0 to 0.4, and V is O.
The speed was changed to 200 sccm.

一方ノズルを直径10(1771の石英ガラス製出発部
材の半径方向に5CTIL/分の速度で往復移動させノ
ズルが中心位置にある時にはV1−0,α−0.4とな
るように同期させた。バーナの炎中で加水分解され、合
成されたSiO2−GeO2微粉末は、このようにして
出発部材上に吹きつけられた。出発部材は等速で回転さ
せ、スートの積層量に応じて下降させた。このようにし
て大きさが直径約10CT!L1長さが約30?の円柱
状スート体を作り、これを約1550℃、N2雰囲気下
の焼結炉へ、下降速度2mm/分で下降され透明化した
所、断面屈折率分布が第3図のキヤリアガス比率に類似
した直径約6へ長さ約20?の透明ガラスが得られた。
例2 Si02−GeO22成分系ガラスで径方向に屈折率変
化をもたせたガラスを合成する為に、原料としてSlC
l4及びGeCl4を用い、キヤリアガスとしてはAr
を用い、それぞれの原料をそれぞれのスート合成用ノズ
ルに導き、高温酸化反応を起し、得られるSiO2及び
GeO2の微粒子状ガラス(スート)を円盤状出発部材
に吹きつけた。
On the other hand, the nozzle was reciprocated in the radial direction of a starting member made of quartz glass with a diameter of 10 (1771) at a speed of 5 CTIL/min, and synchronized so that when the nozzle was at the center position, V1-0, α-0.4. The synthesized SiO2-GeO2 fine powder was hydrolyzed in the flame of the burner and sprayed onto the starting member in this way.The starting member was rotated at a constant speed and lowered according to the amount of soot stacked. In this way, a cylindrical soot body with a diameter of about 10 CT!L1 length of about 30 cm was made, and this was lowered into a sintering furnace at about 1550°C and under a N2 atmosphere at a descending speed of 2 mm/min. When the glass was made transparent, a transparent glass having a cross-sectional refractive index distribution similar to the carrier gas ratio shown in FIG. 3 and having a diameter of about 6 and a length of about 20 was obtained.
Example 2 In order to synthesize a Si02-GeO2 binary glass with a refractive index change in the radial direction, we used SlC as a raw material.
14 and GeCl4, and Ar as the carrier gas.
Each raw material was guided to the respective soot synthesis nozzle using a soot, a high-temperature oxidation reaction was caused, and the resulting fine particulate glass (soot) of SiO2 and GeO2 was blown onto a disc-shaped starting member.

この時SiCl4,GeCl4のバブラ一温度はそれぞ
れ20℃、40℃とした。
At this time, the bubbler temperatures of SiCl4 and GeCl4 were set to 20°C and 40°C, respectively.

ノズルに導く原料ガス量としてはそれぞれをVl,V2
とすると第4図に示す様に周期的に変化させた。一方、
2本のノズルは半径方向に5cTrL/分の速度で往復
移動させ、ノズルが中心位置に来る時にはV1=0,2
=40sccmとなるように同期させた出発部材は例1
と同様のものを用い、同様の操作をした。
The amount of raw material gas introduced to the nozzle is Vl and V2, respectively.
Then, it was changed periodically as shown in FIG. on the other hand,
The two nozzles are moved back and forth in the radial direction at a speed of 5 cTrL/min, and when the nozzles reach the center position, V1 = 0, 2.
Example 1 is the starting member synchronized so that = 40 sccm
I used the same thing and did the same operation.

得られるスート体を例1と同様の操作で透明化した所、
断面屈折率分布が径方向に変化しているガラス円柱が得
られた。
The obtained soot body was made transparent by the same operation as in Example 1.
A glass cylinder with a cross-sectional refractive index distribution varying in the radial direction was obtained.

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

第1図、第2図は本発明によるガラススート積層体を合
成する説明図であり、第3図、第4図はノズルの位置と
ガス量の関係を示す。 1:ガラススート積層体、2−1,2−11:ノズル、
3−[,3−[1:スート、4−1,4−11:ノズル
の移動方向を示す。 5:出発部材を示す。
FIGS. 1 and 2 are explanatory diagrams for synthesizing a glass soot laminate according to the present invention, and FIGS. 3 and 4 show the relationship between the nozzle position and the gas amount. 1: Glass soot laminate, 2-1, 2-11: Nozzle,
3-[, 3-[1: Soot, 4-1, 4-11: Indicates the moving direction of the nozzle. 5: Indicates starting member.

Claims (1)

【特許請求の範囲】[Claims] 1 原料の気相反応によりスートを合成するノズルをタ
ーゲットの径方向に等速度で周期的に平行移動させター
ゲットの回転軸方向に積層成長させるに際し、スートの
組成又はスートの吹きつけ量のうち少くとも1つをノズ
ルの往復移動に同期して周期的に変化させ径方向に組成
の変化したスートを円筒状に積層し、これを透明化する
ことを特徴とする径方向に屈折率の変化した円筒状ガラ
スの製造方法。
1 When the nozzle for synthesizing soot through a gas-phase reaction of raw materials is periodically moved in parallel in the radial direction of the target at a constant velocity to produce layered growth in the direction of the rotational axis of the target, the smaller of the soot composition or the amount of soot sprayed is The refractive index changes in the radial direction, which is characterized by laminating soot in a cylindrical shape whose composition changes in the radial direction by periodically changing one of the soots in synchronization with the reciprocating movement of the nozzle, and making this transparent. Method for manufacturing cylindrical glass.
JP7269577A 1977-06-17 1977-06-17 Method for manufacturing cylindrical glass with radially varying refractive index Expired JPS5930658B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7269577A JPS5930658B2 (en) 1977-06-17 1977-06-17 Method for manufacturing cylindrical glass with radially varying refractive index

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7269577A JPS5930658B2 (en) 1977-06-17 1977-06-17 Method for manufacturing cylindrical glass with radially varying refractive index

Publications (2)

Publication Number Publication Date
JPS547355A JPS547355A (en) 1979-01-20
JPS5930658B2 true JPS5930658B2 (en) 1984-07-28

Family

ID=13496752

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7269577A Expired JPS5930658B2 (en) 1977-06-17 1977-06-17 Method for manufacturing cylindrical glass with radially varying refractive index

Country Status (1)

Country Link
JP (1) JPS5930658B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1574115A (en) * 1978-05-18 1980-09-03 Standard Telephones Cables Ltd Optical fibre manufacture
US4378985A (en) * 1981-06-04 1983-04-05 Corning Glass Works Method and apparatus for forming an optical waveguide fiber
DE3240355C1 (en) * 1982-11-02 1983-11-17 Heraeus Quarzschmelze Gmbh, 6450 Hanau Process for the production of an elongated glass body with an inhomogeneous refractive index distribution
DE3521623A1 (en) * 1985-06-15 1986-12-18 Heraeus Quarzschmelze Gmbh, 6450 Hanau METHOD FOR CONTINUOUSLY ESTABLISHING AN INNER CARRIER-FREE, HOLLOW CYLINDRICAL SOOTBODY

Also Published As

Publication number Publication date
JPS547355A (en) 1979-01-20

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