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WO2024166883A1 - Device for producing porous optical fiber base material - Google Patents

Device for producing porous optical fiber base material Download PDF

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Publication number
WO2024166883A1
WO2024166883A1 PCT/JP2024/003785 JP2024003785W WO2024166883A1 WO 2024166883 A1 WO2024166883 A1 WO 2024166883A1 JP 2024003785 W JP2024003785 W JP 2024003785W WO 2024166883 A1 WO2024166883 A1 WO 2024166883A1
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Prior art keywords
burner
reaction chamber
holding
optical fiber
porous optical
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PCT/JP2024/003785
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French (fr)
Japanese (ja)
Inventor
佑平 浦田
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Shin Etsu Chemical Co Ltd
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Shin Etsu Chemical Co Ltd
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Publication of WO2024166883A1 publication Critical patent/WO2024166883A1/en
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    • 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

Definitions

  • the present invention relates to a porous glass preform manufacturing apparatus for manufacturing porous glass preform for optical fiber, for example, by the vapor-phase axial deposition (VAD) method.
  • VAD vapor-phase axial deposition
  • Patent Document 1 JP 2007-210837 A
  • One aspect of the present invention is a porous optical fiber preform manufacturing device that deposits glass particles generated by a flame hydrolysis reaction of a raw material gas onto a starting material that is pulled up while rotating.
  • the device includes a reaction chamber and a holder that holds a burner for depositing the glass particles, and at least one of the mounting position and mounting direction of the burner can be changed in the holder.
  • the holding part may be detachable from the reaction chamber, so that at least one of the burner holding position and holding direction may be changed.
  • the holding part may be attached below the reaction chamber to form a sub-chamber of the reaction chamber.
  • the reaction chamber may have two sub-chambers connected vertically by their openings, and the holding part may be attached to the lower sub-chamber to form part of the side wall of the lower sub-chamber.
  • the holding section may have a plurality of openings capable of holding burners, and caps for closing the openings among the plurality of openings that do not hold the burners.
  • FIG. 2 is a schematic diagram for explaining an outline of a manufacturing apparatus for a porous optical fiber preform.
  • 4 is a schematic diagram illustrating the seal structure between the burner and the flange surface of the burner insertion port.
  • FIG. FIG. 2 is a schematic diagram showing an outline of an apparatus for producing a porous optical fiber preform according to the present embodiment, the reaction chamber of which is composed of two reaction compartments.
  • FIG. 2 is a schematic diagram showing a configuration of a reaction chamber for explaining Example 1.
  • FIG. 13 is a schematic diagram showing a configuration of a reaction chamber for explaining Comparative Example 1.
  • FIG. 11 is a schematic diagram showing a configuration of a reaction chamber for explaining Example 2.
  • FIG. 11 is a schematic diagram illustrating a configuration of a reaction chamber before the manufacturing conditions are considered, for explaining Example 3.
  • FIG. 11 is an exploded perspective view of the reaction chamber of Example 3.
  • FIG. 11 is an enlarged cross-sectional view of the reaction chamber and the reaction compartment mounting portion of Example 3.
  • FIG. 11 is a schematic diagram illustrating a configuration of a reaction chamber that facilitates the examination of manufacturing conditions, for explaining Example 3.
  • FIG. 11 is a schematic diagram showing a configuration of a reaction chamber for explaining Comparative Example 2.
  • FIG. 13 is a schematic diagram showing the configuration of a reaction chamber for explaining Example 4.
  • FIG. 13 is another schematic diagram showing the configuration of the reaction chamber for explaining Example 4.
  • the reaction chamber is configured to have at least two reaction compartments, with the lower reaction compartment being removable and replaceable. This makes it easy to change the preform manufacturing conditions by replacing the lower reaction compartment with a reaction compartment in which, for example, the position of the first burner for depositing the cladding portion has been changed.
  • the reaction chamber has an opening at its bottom, and a burner insertion plate with a burner insertion port at the opening can be removed and replaced freely. This makes it easy to change the manufacturing conditions of the base material by replacing the burner insertion plate with one that changes the positioning angle of the core deposition burner, for example.
  • the manufacturing device of this embodiment is configured in this way, making it possible to consider a variety of manufacturing conditions and to do so at low cost.
  • Figure 1 is a schematic diagram of a conventional manufacturing device for a porous optical fiber preform 12, which is equipped with a core deposition burner 13 for depositing the central core portion depicted at the bottom, a first cladding deposition burner 14 for depositing the cladding portion slightly above that, and a second cladding deposition burner 15 above that, and the soot is manufactured using multiple burners as a whole.
  • the core deposition burner 13 deposits glass particles generated in an oxyhydrogen flame, which is accompanied by dopant materials such as germanium tetrachloride in addition to silicon tetrachloride, onto the starting material, and then the cladding deposition burners 14 and 15 deposit the cladding so as to cover the core from the outside.
  • dopant materials such as germanium tetrachloride in addition to silicon tetrachloride
  • Each burner is inserted through a burner insertion port provided in the reaction chamber, and each burner insertion port must be adequately sealed to prevent outside air from being drawn in.
  • FIG. 2 is a schematic diagram explaining the seal structure of the burner and the flange surface of the burner insertion port.
  • a burner insertion port 51 with a flange surface is arranged on the burner installation wall of the reaction chamber, and a flexible seal member 53 with a flange surface is inserted into the cylindrical part of the burner 52.
  • the burner 52 When the burner 52 is arranged, it is brought into contact with the flange surface of the burner insertion port 51 arranged on the reaction chamber side so that the contact area between the flange surface of the seal member 53 inserted into the burner 52 is maximized.
  • Example 1 the manufacturing conditions are examined by changing the position of only the first burner for depositing the clad portion to face the burner for depositing the core portion.
  • reaction chamber 32 is composed of reaction compartment 21 and reaction compartment 22, which are connected by connection part 19, and reaction compartment 21 is removable and replaceable.
  • the reaction chamber 21 does not have a burner insertion port for placing the first burner 14 for depositing the clad portion opposite the burner 13 for depositing the core portion.
  • another reaction chamber 23 having a first burner insertion port 14B for depositing the clad portion is prepared at a position opposite the core deposition burner 13, and is attached to the reaction chamber 22 in place of the reaction chamber 21 to create a new reaction chamber 33.
  • a holding part for holding the core deposition burner 13 and the first burner for depositing the clad portion 14 is attached below the reaction chamber 22 to form the reaction chambers 21, 23, and because the holding part is detachable from the reaction chamber 22, the holding position of the first burner for depositing the clad portion 14 can be changed.
  • the first burner 14 for depositing the clad portion can be easily moved to a position opposite the burner 13 for depositing the core portion by simply replacing reaction compartment 21 with reaction compartment 23, which reduces the cost of considering the manufacturing conditions compared to preparing an entire new reaction chamber.
  • Comparative Example 1 As in Example 1, this is a case in which only the first burner for depositing the cladding portion is changed to a position facing the burner for depositing the core portion, and manufacturing conditions are examined.
  • the reaction chamber 31 does not have a burner insertion port for changing the position of the burner for depositing the clad portion to a position opposite the first burner for depositing the clad portion 14. Therefore, it is necessary to change the design of the entire reaction chamber 31 and prepare a new reaction chamber 34 in which the first burner insertion port for depositing the clad portion 14B is moved to a position opposite that in FIG. 1, as shown in FIG. 5. This change in the design of the entire reaction chamber 31 will require extremely high costs for considering the manufacturing conditions.
  • Example 2 the angle of the core deposition burner relative to the horizontal plane is changed from 60 degrees to 75 degrees, and manufacturing conditions are examined.
  • Figure 3 shows an outline of a manufacturing device that consists of a reaction chamber with two reaction compartments.
  • the core deposition burner insertion port 13A is fixed to the reaction compartment 21 so that the angle of the core deposition burner 13 is 60 degrees, and the arrangement angle cannot be changed.
  • FIG. 6 another reaction chamber 24 was replaced with the reaction chamber 21, and connected to the reaction chamber 22 via a connector 19 to form a new reaction chamber 35.
  • the core deposition burner insertion port 13C is arranged in the reaction chamber 24 so that the central axis of the core deposition burner 13, whose angle with respect to the horizontal plane has been changed from 60 degrees to 75 degrees, is perpendicular to the flange surface of the core deposition burner insertion port 13C. This allows the periphery of the burner to be sufficiently sealed as described above.
  • Example 2 the holding portion that holds the core deposition burner 13 and the first clad deposition burner 14 is attached below the reaction chamber 22 to form the reaction chambers 21 and 24, and the holding portion is detachable from the reaction chamber 22, making it possible to change the holding direction of the first clad deposition burner 14.
  • reaction chamber in this way as two separate reaction chambers, it is possible to change the angle of the core deposition burner 13 more easily than if an entire reaction chamber were to be prepared, thereby reducing the cost of considering manufacturing conditions.
  • Example 3 In this embodiment, as in the second embodiment, the angle of the core deposition burner with respect to the horizontal plane is changed from 60 degrees to 75 degrees, and manufacturing conditions are examined.
  • the reaction chamber 36 shown in FIG. 7 has an opening at the bottom of the reaction chamber 25, where a burner insertion plate 41 with a burner insertion port is installed.
  • the core deposition burner insertion port 13A is fixed to the burner insertion plate 41, and the burner angle is 75 degrees.
  • the lower part of the reaction chamber 25 forms a reaction chamber 60 connected to the upper part by an opening 27.
  • the reaction chamber 60 has a triangular prism shape with one side open, and has a flange 62 around the opening.
  • the flange 62 has a plurality of through holes 64.
  • the flange 62 is attached to the bottom surface of the upper part of the reaction chamber 25, where the opening 27 is provided, via a heat-resistant sealant 70.
  • the sealant 70 has a through hole 72 at a position corresponding to the through hole 64.
  • a bolt 74 is inserted into the corresponding through holes 64, 72, and the sealant 70 is sandwiched between the bolt 74 and the nut 76. This fixes the upper part of the reaction chamber 25 and the reaction chamber 60 while maintaining airtightness around the opening 27.
  • This fixing method may be used in other embodiments, for example, as a fixing method using the connector 19 in FIG. 6.
  • the burner insertion plate 41 is attached to the side opposite the opening in the reaction chamber 60.
  • a flange 66 is provided on this side.
  • the side of the flange 66 facing the burner insertion plate 41 is frosted.
  • the area of the burner insertion plate 41 facing the flange 66 is also frosted.
  • the burner insertion plate 41 can be removed from the reaction chamber 60 by removing the clips and peeling off the heat-resistant tape.
  • the burner insertion plate 41 is provided with a burner insertion port 13A for core deposition and a first burner insertion port 14B for clad deposition.
  • Example 3 the burner insertion plate 41 that holds the core deposition burner 13 and the first clad deposition burner 14 is attached to the reaction chamber 60 as a holding part to form part of the side wall of the reaction chamber 60, and since the holding part is detachable from the reaction chamber 60, it is an example in which the holding direction of the first clad deposition burner 14 can be changed.
  • the entire reaction chamber as a reaction chamber with an opening at the bottom and a burner insertion plate, it was possible to study the manufacturing conditions more easily and at lower cost than if an entire reaction chamber were to be prepared separately.
  • the burner insertion plate 41 with a burner insertion plate that changes the holding position of the first burner 14 for depositing the clad portion, it is possible to change the holding position of the first burner 14 for depositing the clad portion.
  • Comparative Example 2 As in the second and third embodiments, the angle of the core deposition burners with respect to the horizontal plane is changed from 60 degrees to 75 degrees, and manufacturing conditions are examined.
  • the burner cannot be positioned at 75 degrees to the horizontal plane in the core deposition burner insertion port 13A of the reaction chamber 31.
  • To change the burner angle it is necessary to change the overall design of the reaction chamber 31 in FIG. 1 and prepare a new reaction chamber 38 with a core deposition burner insertion port 13C that sets the burner position angle at 75 degrees, as shown in FIG. 11. Replacing this reaction chamber makes the cost of considering the manufacturing conditions extremely high.
  • Example 4 12 and 13 are schematic diagrams of the reaction chamber 80 in the production apparatus according to Example 4.
  • the structure above the reaction chamber 80 is the same as that of other examples, for example, Example 3, and therefore illustrations and explanations thereof are omitted.
  • the reaction chamber 80 of the manufacturing apparatus of Example 4 has two openings 81, 82 for the first burner 14 for depositing the clad portion, and one opening 83 for the burner 13 for depositing the core portion. In addition, multiple openings are provided for one first burner 14 for depositing the clad portion. In FIG. 12, the first burner 14 for depositing the clad portion is inserted into the opening 81, and the burner 13 for depositing the core portion is inserted into the opening 83.
  • a cap 84 is inserted into the opening 82 into which the first burner 14 for depositing the clad portion is not inserted, of the two openings 81, 82.
  • the portion of the cap 84 that is inserted into the opening 82 and its flange portion have an outer shape that corresponds to the outer shape of the first burner 14 for depositing the clad portion and the seal member 53, for example the same outer shape.
  • the cap 84 is formed from a heat-resistant material. This allows the opening 82 into which the burner is not inserted to be airtightly sealed.
  • the first burner 14 for depositing the clad portion is inserted into the opening 82, and a cap 84 is inserted into the opening 81. This allows the first burner 14 for depositing the clad portion to be held in a holding position different from that in FIG. 12.
  • the reaction chamber 80 has a plurality of openings 81, 82 capable of holding the first burner 14 for depositing the clad portion, and the holding position of the first burner 14 for depositing the clad portion can be changed by blocking the opening 81, 82 that is not holding the first burner 14 for depositing the clad portion with a cap 84.
  • the holding direction of the first burner 14 for depositing the clad portion may be changed by changing the orientation of the flanges between the openings 81 and 82.

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  • 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)

Abstract

This device for producing a porous optical fiber base material causes glass microparticles produced by flame hydrolysis of a starting gas to be deposited onto a starting material that is being taken up while being turned. The device is provided with a reaction chamber and a holding part for holding the burner used when depositing the glass microparticles. The holding position and/or the holding direction of the burner held by the holding part are variable. The burner attachment position and/or the attachment direction can also be varied as a result of the holding part being detachable with respect to the reaction chamber of this device for producing a porous optical fiber base material.

Description

多孔質光ファイバ母材の製造装置Manufacturing equipment for porous optical fiber preform

 本発明は、例えば気相軸付け法(VAD法)による光ファイバ用多孔質ガラス母材を製造する多孔質ガラス母材の製造装置に関する。 The present invention relates to a porous glass preform manufacturing apparatus for manufacturing porous glass preform for optical fiber, for example, by the vapor-phase axial deposition (VAD) method.

 「排気口5と給気口6を有する上部堆積室2と、給気口7を有する下部堆積室3と、上部堆積室2の上部にあって、堆積によって形成された多孔質母材1を引上げ格納する上室4とを有する反応容器16を備えている」多孔質母材の製造装置がある(例えば、特許文献1)。
 [特許文献1]特開2007-210837
There is a manufacturing apparatus for a porous base material which is "equipped with a reaction vessel 16 having an upper deposition chamber 2 having an exhaust port 5 and an air inlet 6, a lower deposition chamber 3 having an air inlet 7, and an upper chamber 4 located above the upper deposition chamber 2 for pulling up and storing the porous base material 1 formed by deposition" (for example, Patent Document 1).
[Patent Document 1] JP 2007-210837 A

 本発明の一形態は、回転しつつ引き上げられる出発材に、原料ガスの火炎加水分解反応により生成するガラス微粒子を堆積させる多孔質光ファイバ母材の製造装置であって、反応室と、ガラス微粒子堆積用のバーナーを保持する保持部とを備え、保持部において、バーナーの取付位置および取付方向の少なくとも一方が変えられる。 One aspect of the present invention is a porous optical fiber preform manufacturing device that deposits glass particles generated by a flame hydrolysis reaction of a raw material gas onto a starting material that is pulled up while rotating. The device includes a reaction chamber and a holder that holds a burner for depositing the glass particles, and at least one of the mounting position and mounting direction of the burner can be changed in the holder.

 上記多孔質光ファイバ母材の製造装置において、保持部が反応室に対し着脱自在であることにより、バーナーの保持位置および保持方向の前記少なくとも一方が変えられてもよい。保持部は、反応室の下方に取り付けられて反応室の分室を形成してもよい。反応室は、互いの開口で上下に連結した2つの分室を有し、保持部は、下方の分室に取り付けられて下方の分室の側壁の一部を形成してもよい。 In the above-mentioned porous optical fiber preform manufacturing apparatus, the holding part may be detachable from the reaction chamber, so that at least one of the burner holding position and holding direction may be changed. The holding part may be attached below the reaction chamber to form a sub-chamber of the reaction chamber. The reaction chamber may have two sub-chambers connected vertically by their openings, and the holding part may be attached to the lower sub-chamber to form part of the side wall of the lower sub-chamber.

 上記多孔質光ファイバ母材の製造装置において、保持部は、バーナーを保持可能な複数の開口部と、複数の開口部のうち前記バーナーを保持していない開口部を塞ぐキャップとを有してもよい。 In the above-mentioned porous optical fiber preform manufacturing apparatus, the holding section may have a plurality of openings capable of holding burners, and caps for closing the openings among the plurality of openings that do not hold the burners.

多孔質光ファイバ母材の製造装置の概略を説明する模式図である。FIG. 2 is a schematic diagram for explaining an outline of a manufacturing apparatus for a porous optical fiber preform. バーナとバーナ挿入口のフランジ面のシール構造を説明する概略模式図である。4 is a schematic diagram illustrating the seal structure between the burner and the flange surface of the burner insertion port. FIG. 本実施形態の、反応室が2つの反応分室からなる多孔質光ファイバ母材の製造装置の概略を示す模式図である。FIG. 2 is a schematic diagram showing an outline of an apparatus for producing a porous optical fiber preform according to the present embodiment, the reaction chamber of which is composed of two reaction compartments. 実施例1を説明するための反応室の構成を示した模式図である。FIG. 2 is a schematic diagram showing a configuration of a reaction chamber for explaining Example 1. 比較例1を説明するための反応室の構成を示した模式図である。FIG. 13 is a schematic diagram showing a configuration of a reaction chamber for explaining Comparative Example 1. 実施例2を説明するための反応室の構成を示した模式図である。FIG. 11 is a schematic diagram showing a configuration of a reaction chamber for explaining Example 2. 実施例3を説明するための、製造条件検討前の反応室の構成を示した模式図である。FIG. 11 is a schematic diagram illustrating a configuration of a reaction chamber before the manufacturing conditions are considered, for explaining Example 3. 実施例3の反応分室の分解斜視図である。FIG. 11 is an exploded perspective view of the reaction chamber of Example 3. 実施例3の反応室と反応分室の取り付け部分の拡大断面図である。FIG. 11 is an enlarged cross-sectional view of the reaction chamber and the reaction compartment mounting portion of Example 3. 実施例3を説明するための、製造条件の検討を容易にした反応室の構成を示した模式図である。FIG. 11 is a schematic diagram illustrating a configuration of a reaction chamber that facilitates the examination of manufacturing conditions, for explaining Example 3. 比較例2を説明するための反応室の構成を示した模式図である。FIG. 11 is a schematic diagram showing a configuration of a reaction chamber for explaining Comparative Example 2. 実施例4を説明するための反応分室の構成を示した模式図である。FIG. 13 is a schematic diagram showing the configuration of a reaction chamber for explaining Example 4. 実施例4を説明するための反応分室の構成を示した他の模式図である。FIG. 13 is another schematic diagram showing the configuration of the reaction chamber for explaining Example 4.

 以下、実施の形態について説明するが、下記のこれらに限定されるものではなく、様々な態様が可能である。 The following describes embodiments, but is not limited to these, and various other configurations are possible.

 一実施形態の多孔質光ファイバ母材の製造装置は、反応室を少なくとも2つの反応分室からなる構成とし、下方側の反応分室が取り外し交換自在となっている。これにより、下方側の反応分室を、例えば、クラッド部堆積用第1バーナの位置を変更した反応分室と交換することで、母材の製造条件を容易に変更することができる。 In one embodiment of the porous optical fiber preform manufacturing apparatus, the reaction chamber is configured to have at least two reaction compartments, with the lower reaction compartment being removable and replaceable. This makes it easy to change the preform manufacturing conditions by replacing the lower reaction compartment with a reaction compartment in which, for example, the position of the first burner for depositing the cladding portion has been changed.

 さらに別の実施形態は、反応室がその下部に開口部を有する構造とし、該開口部にバーナ挿入口を備えたバーナ挿入板が取り外し交換自在となっている。これにより、バーナ挿入板を、例えば、コア部堆積用バーナの配置角度を変更したバーナ挿入板と交換することで、母材の製造条件を容易に変更することができる。 In yet another embodiment, the reaction chamber has an opening at its bottom, and a burner insertion plate with a burner insertion port at the opening can be removed and replaced freely. This makes it easy to change the manufacturing conditions of the base material by replacing the burner insertion plate with one that changes the positioning angle of the core deposition burner, for example.

 本実施形態の製造装置は、このような構成としたことにより多様な製造条件の検討が可能であり、かつ低コストで行うことができる。 The manufacturing device of this embodiment is configured in this way, making it possible to consider a variety of manufacturing conditions and to do so at low cost.

 図1は、従来使用されている多孔質光ファイバ母材12の製造装置の概略図であり、最下方に描かれた中心のコア部を堆積するためのコア部堆積用バーナ13と、そのやや上方にクラッド部を堆積するためのクラッド部堆積用第1バーナ14、さらにその上方にクラッド部堆積用第2バーナ15を備えており、スートは全体として複数のバーナを用いて製造される。 Figure 1 is a schematic diagram of a conventional manufacturing device for a porous optical fiber preform 12, which is equipped with a core deposition burner 13 for depositing the central core portion depicted at the bottom, a first cladding deposition burner 14 for depositing the cladding portion slightly above that, and a second cladding deposition burner 15 above that, and the soot is manufactured using multiple burners as a whole.

 コア部堆積用バーナ13には、四塩化ケイ素の他に四塩化ゲルマニウムなどのドーパント原料を同伴させて酸水素火炎中で生成したガラス微粒子を出発材上に堆積させたのち、クラッド部堆積用バーナ14,15でコア部を外側から覆うようにクラッド部を堆積させている。 The core deposition burner 13 deposits glass particles generated in an oxyhydrogen flame, which is accompanied by dopant materials such as germanium tetrachloride in addition to silicon tetrachloride, onto the starting material, and then the cladding deposition burners 14 and 15 deposit the cladding so as to cover the core from the outside.

 多孔質光ファイバ母材中への不純物の混入を極力減らしたり、ガラス原料の火炎加水分解反応で生じる塩化水素による設備の腐食を防ぎ、外乱なく安定して堆積を行うため、上述の各バーナによる堆積は、外気から遮断された反応室内で行われる。 In order to minimize the intrusion of impurities into the porous optical fiber base material, to prevent corrosion of the equipment caused by hydrogen chloride produced in the flame hydrolysis reaction of the glass raw materials, and to ensure stable deposition without disturbance, deposition using the above-mentioned burners is carried out in a reaction chamber that is isolated from the outside air.

 各バーナは、反応室に設けたバーナ挿入口から挿入され、外気を取り込まないように、各バーナのバーナ挿入口は十分にシールすることが求められる。 Each burner is inserted through a burner insertion port provided in the reaction chamber, and each burner insertion port must be adequately sealed to prevent outside air from being drawn in.

 図2は、バーナとバーナ挿入口のフランジ面のシール構造を説明する概略模式図である。反応室のバーナ設置壁には、フランジ面を有するバーナ挿入口51を配置し、バーナ52の円筒部には可撓性でフランジ面を有するシール部材53を挿通しておき、バーナ52を配置する際には、反応室側に配置されたバーナ挿入口51のフランジ面と、バーナ52に挿通させたシール部材53のフランジ面との接触面積が最大となるように接触させる。すなわち、バーナ52の中心軸とバーナ挿入口51のフランジ面が直交するように配置することがシールする上で重要である。 Figure 2 is a schematic diagram explaining the seal structure of the burner and the flange surface of the burner insertion port. A burner insertion port 51 with a flange surface is arranged on the burner installation wall of the reaction chamber, and a flexible seal member 53 with a flange surface is inserted into the cylindrical part of the burner 52. When the burner 52 is arranged, it is brought into contact with the flange surface of the burner insertion port 51 arranged on the reaction chamber side so that the contact area between the flange surface of the seal member 53 inserted into the burner 52 is maximized. In other words, it is important for sealing that the central axis of the burner 52 and the flange surface of the burner insertion port 51 are arranged so as to be perpendicular to each other.

 以下、本発明の製造装置について、実施例に基づき具体的に説明する。 The manufacturing device of the present invention will be specifically explained below based on examples.

 実施例1;
 クラッド部堆積用第1バーナのみをコア部堆積用バーナと対向する位置に変更して製造条件を検討するケースである。
Example 1
In this case, the manufacturing conditions are examined by changing the position of only the first burner for depositing the clad portion to face the burner for depositing the core portion.

 図3において、反応室32は、反応分室21と反応分室22とから構成され、接続部19で接続され、反応分室21が取り外し交換可能な構造となっている。 In FIG. 3, reaction chamber 32 is composed of reaction compartment 21 and reaction compartment 22, which are connected by connection part 19, and reaction compartment 21 is removable and replaceable.

 反応分室21には、コア部堆積用バーナ13と対向する位置にクラッド部堆積用第1バーナ14を対向配置するためのバーナ挿入口がない。 The reaction chamber 21 does not have a burner insertion port for placing the first burner 14 for depositing the clad portion opposite the burner 13 for depositing the core portion.

 そこで図4に示すように、コア部堆積用バーナ13と対向する位置にクラッド部堆積用第1バーナ挿入口14Bを有する別の反応分室23を用意し、反応分室21と交換して反応分室22に取り付け、新たな反応室33とした。よって、実施例1は、コア部堆積用バーナ13およびクラッド部堆積用第1バーナ14を保持する保持部が、反応分室22の下方に取り付けられて反応分室21,23を形成しており、保持部が反応分室22に対し着脱自在であることにより、クラッド部堆積用第1バーナ14の保持位置を変えることができる例となっている。 As shown in FIG. 4, another reaction chamber 23 having a first burner insertion port 14B for depositing the clad portion is prepared at a position opposite the core deposition burner 13, and is attached to the reaction chamber 22 in place of the reaction chamber 21 to create a new reaction chamber 33. Thus, in Example 1, a holding part for holding the core deposition burner 13 and the first burner for depositing the clad portion 14 is attached below the reaction chamber 22 to form the reaction chambers 21, 23, and because the holding part is detachable from the reaction chamber 22, the holding position of the first burner for depositing the clad portion 14 can be changed.

 このように反応室を2つの反応分室からなる構成にしておけば、反応分室21を反応分室23に交換するだけで、クラッド部堆積用第1バーナ14をコア部堆積用バーナ13と対向する位置に容易に変更することができ、反応室全体を新たに用意するよりも製造条件の検討コストを下げることができた。 By configuring the reaction chamber in this way with two reaction compartments, the first burner 14 for depositing the clad portion can be easily moved to a position opposite the burner 13 for depositing the core portion by simply replacing reaction compartment 21 with reaction compartment 23, which reduces the cost of considering the manufacturing conditions compared to preparing an entire new reaction chamber.

 比較例1;
 実施例1と同様に、クラッド部堆積用第1バーナのみをコア部堆積用バーナと対向する位置に変更して製造条件を検討するケースである。
Comparative Example 1
As in Example 1, this is a case in which only the first burner for depositing the cladding portion is changed to a position facing the burner for depositing the core portion, and manufacturing conditions are examined.

 図1において、反応室31にはクラッド部堆積用第1バーナ14と対向する位置にクラッド部堆積用バーナを配置変更するためのバーナ挿入口がない。そのため、反応室31全体の設計を変更して、図5に示すように、クラッド部堆積用第1バーナ挿入口14Bを図1とは対向する位置に移動させた新たな反応室34を用意する必要がある。この反応室31全体の設計変更は、製造条件の検討コストが極めて高いものとなる。 In FIG. 1, the reaction chamber 31 does not have a burner insertion port for changing the position of the burner for depositing the clad portion to a position opposite the first burner for depositing the clad portion 14. Therefore, it is necessary to change the design of the entire reaction chamber 31 and prepare a new reaction chamber 34 in which the first burner insertion port for depositing the clad portion 14B is moved to a position opposite that in FIG. 1, as shown in FIG. 5. This change in the design of the entire reaction chamber 31 will require extremely high costs for considering the manufacturing conditions.

 実施例2;
 本実施例では、コア部堆積用バーナの配置角度を水平面に対して60度から75度に変更して製造条件を検討するケースである。
Example 2
In this embodiment, the angle of the core deposition burner relative to the horizontal plane is changed from 60 degrees to 75 degrees, and manufacturing conditions are examined.

 図3に、反応室を2つの反応分室からなる製造装置の概略を示したが、この装置ではコア部堆積用バーナ13の角度が60度となるようにコア部堆積用バーナ挿入口13Aが反応分室21に固定されており、配置角度を変更することはできない。 Figure 3 shows an outline of a manufacturing device that consists of a reaction chamber with two reaction compartments. In this device, the core deposition burner insertion port 13A is fixed to the reaction compartment 21 so that the angle of the core deposition burner 13 is 60 degrees, and the arrangement angle cannot be changed.

 そこで図6のように、別の反応分室24を反応分室21と交換し、接続具19を介して反応分室22に接続し新たな反応室35とした。反応分室24には、配置角度を水平面に対して60度から75度に変更したコア部堆積用バーナ13の中心軸とコア部堆積用バーナ挿入口13Cのフランジ面とが直交するように、コア部堆積用バーナ挿入口13Cが配置されている。これによりバーナの周囲を前述したように十分にシールすることができる。よって、実施例2は、コア部堆積用バーナ13およびクラッド部堆積用第1バーナ14を保持する保持部が、反応分室22の下方に取り付けられて反応分室21、24を形成しており、保持部が反応分室22に対し着脱自在であることにより、クラッド部堆積用第1バーナ14の保持方向を変えることができる例となっている。 As shown in FIG. 6, another reaction chamber 24 was replaced with the reaction chamber 21, and connected to the reaction chamber 22 via a connector 19 to form a new reaction chamber 35. The core deposition burner insertion port 13C is arranged in the reaction chamber 24 so that the central axis of the core deposition burner 13, whose angle with respect to the horizontal plane has been changed from 60 degrees to 75 degrees, is perpendicular to the flange surface of the core deposition burner insertion port 13C. This allows the periphery of the burner to be sufficiently sealed as described above. Therefore, in Example 2, the holding portion that holds the core deposition burner 13 and the first clad deposition burner 14 is attached below the reaction chamber 22 to form the reaction chambers 21 and 24, and the holding portion is detachable from the reaction chamber 22, making it possible to change the holding direction of the first clad deposition burner 14.

 このように反応室を2つの反応分室からなる構成にしたことで、反応室全体を新たに用意するよりも容易にコア部堆積用バーナ13の角度を変更することができ、製造条件の検討コストを下げることができた。 By configuring the reaction chamber in this way as two separate reaction chambers, it is possible to change the angle of the core deposition burner 13 more easily than if an entire reaction chamber were to be prepared, thereby reducing the cost of considering manufacturing conditions.

 実施例3;
 本実施例では、実施例2と同様にコア部堆積用バーナの配置角度を水平面に対して60度から75度に変更して製造条件を検討するケースである。
Example 3
In this embodiment, as in the second embodiment, the angle of the core deposition burner with respect to the horizontal plane is changed from 60 degrees to 75 degrees, and manufacturing conditions are examined.

 図7に示す反応室36は、その反応室25の下部に開口部を有し、そこにはバーナ挿入口を備えたバーナ挿入板41が設置されている。コア部堆積用バーナ挿入口13Aはバーナ挿入板41に固定されており、バーナの角度は75度である。 The reaction chamber 36 shown in FIG. 7 has an opening at the bottom of the reaction chamber 25, where a burner insertion plate 41 with a burner insertion port is installed. The core deposition burner insertion port 13A is fixed to the burner insertion plate 41, and the burner angle is 75 degrees.

 図8に示すように、反応室25の下部は、開口27で上部と連結された反応分室60を構成している。反応分室60は三角柱の一側面が開口した形状を有しており、当該開口の周りにフランジ62を有する。フランジ62には複数の貫通孔64が設けられている。フランジ62は耐熱性のシール材70を介して反応室25の上部において開口27が設けられた底面に取り付けられる。シール材70には貫通孔64に対応した位置に貫通孔72が設けられている。図9に示すように、対応する貫通孔64、72にボルト74が挿入されて、ナット76との間でシール材70を挟み込む。これにより、反応室25の上部と反応分室60との間が開口27の周りで気密を保って固定される。なお、この固定方法は他の実施例、例えば図6の接続具19による固定方法として用いられてよい。 As shown in FIG. 8, the lower part of the reaction chamber 25 forms a reaction chamber 60 connected to the upper part by an opening 27. The reaction chamber 60 has a triangular prism shape with one side open, and has a flange 62 around the opening. The flange 62 has a plurality of through holes 64. The flange 62 is attached to the bottom surface of the upper part of the reaction chamber 25, where the opening 27 is provided, via a heat-resistant sealant 70. The sealant 70 has a through hole 72 at a position corresponding to the through hole 64. As shown in FIG. 9, a bolt 74 is inserted into the corresponding through holes 64, 72, and the sealant 70 is sandwiched between the bolt 74 and the nut 76. This fixes the upper part of the reaction chamber 25 and the reaction chamber 60 while maintaining airtightness around the opening 27. This fixing method may be used in other embodiments, for example, as a fixing method using the connector 19 in FIG. 6.

 反応分室60における開口とは別の側面にバーナ挿入板41が取り付けられる。当該側面にはフランジ66が設けられている。フランジ66におけるバーナ挿入板41と対向する側は摺りガラス処理がされている。同様に、バーナ挿入板41におけるフランジ66に対向する領域も摺りガラス処理がされている。バーナ挿入板41がフランジ66に当接された状態でそれらが耐熱テープで貼り付けられ、かつ、金属製のクリップでクリップ止めされる。これにより、バーナ挿入板41がフランジ66に対して気密を保って固定される。 The burner insertion plate 41 is attached to the side opposite the opening in the reaction chamber 60. A flange 66 is provided on this side. The side of the flange 66 facing the burner insertion plate 41 is frosted. Similarly, the area of the burner insertion plate 41 facing the flange 66 is also frosted. With the burner insertion plate 41 in contact with the flange 66, they are attached with heat-resistant tape and clipped in place with a metal clip. This fixes the burner insertion plate 41 to the flange 66 while maintaining an airtight seal.

 当該クリップを外して耐熱テープを剥がすことでバーナ挿入板41を反応分室60から取り外すことができる。なお、バーナ挿入板41にはコア堆積用バーナ挿入口13Aおよびクラッド部堆積用第1バーナ挿入口14Bが設けられている。 The burner insertion plate 41 can be removed from the reaction chamber 60 by removing the clips and peeling off the heat-resistant tape. The burner insertion plate 41 is provided with a burner insertion port 13A for core deposition and a first burner insertion port 14B for clad deposition.

 さらに、図10のように、反応室25の下部の開口部に、バーナの角度75度に対応したコア部堆積用バーナ挿入口13Cを備えた別のバーナ挿入板42をバーナ挿入板41に換えて接続し、新たな反応室37とした。よって、実施例3は、コア堆積用バーナ13およびクラッド部堆積用第1バーナ14を保持するバーナ挿入板41が保持部として、反応分室60に取り付けられて反応分室60の側壁の一部を形成しており、保持部が反応分室60に対し着脱自在であることにより、クラッド部堆積用第1バーナ14の保持方向を変えることができる例となっている。 Furthermore, as shown in FIG. 10, another burner insertion plate 42 equipped with a core deposition burner insertion port 13C corresponding to a burner angle of 75 degrees was connected to the opening at the bottom of the reaction chamber 25 in place of the burner insertion plate 41 to form a new reaction chamber 37. Thus, in Example 3, the burner insertion plate 41 that holds the core deposition burner 13 and the first clad deposition burner 14 is attached to the reaction chamber 60 as a holding part to form part of the side wall of the reaction chamber 60, and since the holding part is detachable from the reaction chamber 60, it is an example in which the holding direction of the first clad deposition burner 14 can be changed.

 このように反応室全体を、下部に開口部を持つ反応室とバーナ挿入板からなる構成とすることで、反応室全体を別に新たに用意するよりも容易かつ低コストで製造条件を検討することができた。なお、バーナ挿入板41に対してクラッド部堆積用第1バーナ14の保持位置を変えたバーナ挿入板に取り換えることにより、クラッド部堆積用第1バーナ14の保持位置を変えることができる。 In this way, by configuring the entire reaction chamber as a reaction chamber with an opening at the bottom and a burner insertion plate, it was possible to study the manufacturing conditions more easily and at lower cost than if an entire reaction chamber were to be prepared separately. In addition, by replacing the burner insertion plate 41 with a burner insertion plate that changes the holding position of the first burner 14 for depositing the clad portion, it is possible to change the holding position of the first burner 14 for depositing the clad portion.

 比較例2;
 実施例2,3と同様に、コア部堆積用バーナの配置角度を水平面に対して60度から75度に変更して製造条件を検討するケースである。
Comparative Example 2
As in the second and third embodiments, the angle of the core deposition burners with respect to the horizontal plane is changed from 60 degrees to 75 degrees, and manufacturing conditions are examined.

 図1の従来の製造装置では、反応室31のコア部堆積用バーナ挿入口13Aには水平面に対して75度でのバーナ配置はできない。バーナ角度を変更するには、図1の反応室31全体の設計を変更して、図11に示したように、バーナの配置角度を75度とするコア部堆積用バーナ挿入口13Cを有する新たな反応室38を用意する必要がある。この反応室の交換は、製造条件の検討コストを極めて高いものとする。 In the conventional manufacturing equipment of FIG. 1, the burner cannot be positioned at 75 degrees to the horizontal plane in the core deposition burner insertion port 13A of the reaction chamber 31. To change the burner angle, it is necessary to change the overall design of the reaction chamber 31 in FIG. 1 and prepare a new reaction chamber 38 with a core deposition burner insertion port 13C that sets the burner position angle at 75 degrees, as shown in FIG. 11. Replacing this reaction chamber makes the cost of considering the manufacturing conditions extremely high.

 実施例4;
 図12および図13は、実施例4に係る製造装置における反応分室80の模式図である。実施例4の製造装置において、反応分室80より上の構造は他の実施例、例えば、実施例3と同じであるので図示及び説明を省略する。
Example 4
12 and 13 are schematic diagrams of the reaction chamber 80 in the production apparatus according to Example 4. In the production apparatus of Example 4, the structure above the reaction chamber 80 is the same as that of other examples, for example, Example 3, and therefore illustrations and explanations thereof are omitted.

 実施例4の製造装置の反応分室80は、クラッド部堆積用第1バーナ14用の2つの開口部81,82と、コア部堆積用バーナ13用の1つの開口部83を有する。付言すれば、ひとつのクラッド部堆積用第1バーナ14に対して複数の開口が設けられている。図12において、クラッド部堆積用第1バーナ14は開口部81に挿入されており、コア堆積用バーナ13は開口部83に挿入されている。 The reaction chamber 80 of the manufacturing apparatus of Example 4 has two openings 81, 82 for the first burner 14 for depositing the clad portion, and one opening 83 for the burner 13 for depositing the core portion. In addition, multiple openings are provided for one first burner 14 for depositing the clad portion. In FIG. 12, the first burner 14 for depositing the clad portion is inserted into the opening 81, and the burner 13 for depositing the core portion is inserted into the opening 83.

 2つの開口部81,82のうち、クラッド部堆積用第1バーナ14が挿入されていない方の開口部82にはキャップ84が挿入されている。キャップ84は開口部82に挿入される部分およびそのフランジ部がクラッド部堆積用第1バーナ14およびシール部材53の外形に対応する外形、例えば同じ外形を有する。キャップ84は耐熱性の材料から形成される。これにより、バーナが挿入されていない開口部82を気密に塞ぐことができる。 A cap 84 is inserted into the opening 82 into which the first burner 14 for depositing the clad portion is not inserted, of the two openings 81, 82. The portion of the cap 84 that is inserted into the opening 82 and its flange portion have an outer shape that corresponds to the outer shape of the first burner 14 for depositing the clad portion and the seal member 53, for example the same outer shape. The cap 84 is formed from a heat-resistant material. This allows the opening 82 into which the burner is not inserted to be airtightly sealed.

 図13は、図12に代えて、開口部82にクラッド部堆積用第1バーナ14が挿入されており、開口部81にキャップ84が挿入されている。これにより、図12とは異なる保持位置でクラッド部堆積用第1バーナ14を保持することができる。 In FIG. 13, instead of FIG. 12, the first burner 14 for depositing the clad portion is inserted into the opening 82, and a cap 84 is inserted into the opening 81. This allows the first burner 14 for depositing the clad portion to be held in a holding position different from that in FIG. 12.

 実施例4の製造装置によれば、反応分室80はクラッド部堆積用第1バーナ14を保持可能な複数の開口部81、82を有し、開口部81、82のうちクラッド部堆積用第1バーナ14を保持していない方をキャップ84で塞ぐことにより、クラッド部堆積用第1バーナ14の保持位置を変えることができる。また、開口部81と開口部82とでフランジの向きを変えることで、クラッド部堆積用第1バーナ14の保持方向が変えられるようにしてもよい。 According to the manufacturing apparatus of Example 4, the reaction chamber 80 has a plurality of openings 81, 82 capable of holding the first burner 14 for depositing the clad portion, and the holding position of the first burner 14 for depositing the clad portion can be changed by blocking the opening 81, 82 that is not holding the first burner 14 for depositing the clad portion with a cap 84. In addition, the holding direction of the first burner 14 for depositing the clad portion may be changed by changing the orientation of the flanges between the openings 81 and 82.

11…出発材,
12…多孔質光ファイバ母材,
13…コア堆積用バーナ,
14…クラッド部堆積用第1バーナ,
15…クラッド部堆積用第2バーナ,
13A~C…コア部堆積用バーナ挿入口,
14A,B…クラッド部堆積用第1バーナ挿入口, 
15A…クラッド部堆積用第2バーナ挿入口,
19…接続具,
21~24…反応分室,
25…開口部を有する反応室,
27…開口部,
31~38…反応室,
41,42…バーナ挿入板
51…バーナ挿入口,
52…バーナ,
53…シール部材,
60…反応分室,
62…フランジ,
64…貫通孔,
66…フランジ,
70…シール材,
72…貫通孔,
74…ボルト,
76…ナット,
80…反応分室,
81…開口部,
82…開口部,
83…開口部,
84…キャップ。
11... starting material,
12...Porous optical fiber preform,
13...Core deposition burner,
14: First burner for depositing clad portion,
15: Second burner for depositing clad portion,
13A-C: Core deposition burner insertion port,
14A, B: first burner insertion port for deposition of clad portion,
15A: second burner insertion port for deposition of clad portion,
19...connector,
21-24: Reaction chambers,
25...reaction chamber having an opening,
27...Opening,
31 to 38: reaction chamber,
41, 42 ... burner insertion plate 51 ... burner insertion port,
52...Burner,
53...sealing member,
60... reaction compartment,
62... flange,
64...through hole,
66...flange,
70...sealing material,
72 ... through hole,
74...volts,
76...Nut,
80...Reaction chamber,
81...Opening,
82...Opening,
83...Opening,
84...Cap.

Claims (5)

 回転しつつ引き上げられる出発材に、原料ガスの火炎加水分解反応により生成するガラス微粒子を堆積させる多孔質光ファイバ母材の製造装置であって、
 反応室と、
 ガラス微粒子堆積用のバーナーを保持する保持部と
を備え、
 前記保持部において、前記バーナーの保持位置および保持方向の少なくとも一方が変えられる多孔質光ファイバ母材の製造装置。
1. An apparatus for manufacturing a porous optical fiber preform, comprising: a starting material which is rotated and pulled up, and on which glass particles generated by a flame hydrolysis reaction of a raw material gas are deposited;
A reaction chamber;
a holder for holding a burner for depositing glass particles;
The apparatus for manufacturing a porous optical fiber preform is capable of changing at least one of the holding position and the holding direction of the burner in the holding section.
 前記保持部が前記反応室に対し着脱自在であることにより、前記バーナーの保持位置および保持方向の前記少なくとも一方が変えられる請求項1に記載の多孔質光ファイバ母材の製造装置。 The porous optical fiber preform manufacturing apparatus according to claim 1, wherein the holding part is detachable from the reaction chamber, so that at least one of the holding position and holding direction of the burner can be changed.  前記保持部は、前記反応室の下方に取り付けられて前記反応室の分室を形成する請求項2に記載の多孔質光ファイバ母材の製造装置。 The porous optical fiber preform manufacturing apparatus according to claim 2, wherein the holding section is attached below the reaction chamber to form a sub-chamber of the reaction chamber.  前記反応室は、互いの開口で上下に連結した2つの分室を有し、
 前記保持部は、下方の前記分室に取り付けられて前記下方の分室の側壁の一部を形成する請求項2に記載の多孔質光ファイバ母材の製造装置。
The reaction chamber has two separate chambers connected vertically by openings,
3. The apparatus for manufacturing a porous optical fiber preform according to claim 2, wherein the holding portion is attached to the lower compartment and forms a part of a side wall of the lower compartment.
 前記保持部は、
 前記バーナーを保持可能な複数の開口部と、
 前記複数の開口部のうち前記バーナーを保持していない開口部を塞ぐキャップと
を有する請求項1に記載の多孔質光ファイバ母材の製造装置。
The holding portion is
A plurality of openings capable of holding the burners;
2. The apparatus for manufacturing a porous optical fiber preform according to claim 1, further comprising a cap for closing an opening that does not hold the burner among the plurality of openings.
PCT/JP2024/003785 2023-02-06 2024-02-05 Device for producing porous optical fiber base material Ceased WO2024166883A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2023-016097 2023-02-06
JP2023016097 2023-02-06

Publications (1)

Publication Number Publication Date
WO2024166883A1 true WO2024166883A1 (en) 2024-08-15

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PCT/JP2024/003785 Ceased WO2024166883A1 (en) 2023-02-06 2024-02-05 Device for producing porous optical fiber base material

Country Status (1)

Country Link
WO (1) WO2024166883A1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5688838A (en) * 1979-12-20 1981-07-18 Nippon Telegr & Teleph Corp <Ntt> Apparatus for preparation of optical fiber stock by vapor-phase axial deposition method
JPH04114526U (en) * 1991-03-21 1992-10-08 藤倉電線株式会社 Glass particle deposition device
JPH10245242A (en) * 1997-03-06 1998-09-14 Furukawa Electric Co Ltd:The Equipment for manufacturing porous glass preform for optical fiber
JP2020083675A (en) * 2018-11-20 2020-06-04 信越化学工業株式会社 Method for manufacturing porous glass preform for optical fiber

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5688838A (en) * 1979-12-20 1981-07-18 Nippon Telegr & Teleph Corp <Ntt> Apparatus for preparation of optical fiber stock by vapor-phase axial deposition method
JPH04114526U (en) * 1991-03-21 1992-10-08 藤倉電線株式会社 Glass particle deposition device
JPH10245242A (en) * 1997-03-06 1998-09-14 Furukawa Electric Co Ltd:The Equipment for manufacturing porous glass preform for optical fiber
JP2020083675A (en) * 2018-11-20 2020-06-04 信越化学工業株式会社 Method for manufacturing porous glass preform for optical fiber

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