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JP2003119034A - Manufacturing method and manufacturing apparatus for glass fine particle deposit - Google Patents

Manufacturing method and manufacturing apparatus for glass fine particle deposit

Info

Publication number
JP2003119034A
JP2003119034A JP2001315279A JP2001315279A JP2003119034A JP 2003119034 A JP2003119034 A JP 2003119034A JP 2001315279 A JP2001315279 A JP 2001315279A JP 2001315279 A JP2001315279 A JP 2001315279A JP 2003119034 A JP2003119034 A JP 2003119034A
Authority
JP
Japan
Prior art keywords
glass
deposit
manufacturing
clean air
building
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.)
Pending
Application number
JP2001315279A
Other languages
Japanese (ja)
Inventor
Tomohiro Ishihara
朋浩 石原
Masaaki Nakamori
正昭 中盛
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
Original Assignee
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 Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP2001315279A priority Critical patent/JP2003119034A/en
Publication of JP2003119034A publication Critical patent/JP2003119034A/en
Pending 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]
    • C03B37/01406Deposition reactors therefor

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)

Abstract

PROBLEM TO BE SOLVED: To provide a manufacturing method which is capable of stably feeding clean air into a glass particulate deposit manufacturing apparatus, preventing the intrusion of impurity gas and decreasing the number of foreign matters intruding into a glass particulate deposit and an apparatus for the same. SOLUTION: This manufacturing method for the glass particulate deposit is a method of manufacturing the glass particulate deposit by using the glass particulate deposit manufacturing apparatus installed in a manufacturing building and depositing the glass particulates formed by a burner for synthesizing the glass particulates on a starting rod, in which the deposition of the glass particulates is performed while the clean air generated in a clean air generator for taking the air from an intake port opened outside the building into the building and cleaning the air is introduced into the apparatus.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は気相合成法によるガ
ラス微粒子堆積体の製造方法及び装置、特に製造装置内
への不純物ガスの流入を防止したガラス微粒子堆積体の
製造方法及び装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for producing a glass fine particle deposit by a vapor phase synthesis method, and more particularly to a method and an apparatus for producing a glass fine particle deposit which prevents an impurity gas from flowing into the production apparatus.

【0002】[0002]

【従来の技術】OVD法(外付け法)などの気相合成法
によるガラス微粒子堆積体の製造方法においては、ガラ
ス微粒子合成用バーナにガラス原料となるSiCl4
GeCl4 を供給し、火炎加水分解反応により生成する
SiO2 やGeO2 などのガラス微粒子を回転する出発
ロッドに堆積させてガラス微粒子堆積体を製造する。こ
のような製造方法においては、ガラス微粒子の堆積を行
う製造装置内にダストや金属を腐食する不純物ガスを含
む外気が流入すると、装置内部の金属が腐食して装置内
部雰囲気中の金属系のダスト数が増加し、このような雰
囲気下でガラス微粒子の堆積を行うと、ガラス微粒子堆
積体中に金属系異物が混入する。このようなガラス微粒
子堆積体を脱水、透明ガラス化して得られる光ファイバ
母材は前記の気泡や異物に基づく異常点が存在し、線引
き後のファイバ強度試験時に断線が多発する。
2. Description of the Related Art In a method for producing a glass fine particle deposit by a vapor phase synthesis method such as an OVD method (external method), SiCl 4 or GeCl 4 as a glass raw material is supplied to a burner for synthesizing glass fine particles to burn flame. Glass fine particles such as SiO 2 and GeO 2 produced by the decomposition reaction are deposited on a rotating starting rod to produce a glass fine particle deposit body. In such a manufacturing method, when outside air containing dust or an impurity gas that corrodes a metal flows into the manufacturing apparatus for depositing glass particles, the metal inside the apparatus is corroded and the metal-based dust in the atmosphere inside the apparatus is dusted. When the number of the glass particles increases and the glass particles are deposited in such an atmosphere, metallic foreign matters are mixed in the glass particle deposit body. The optical fiber preform obtained by dehydrating and vitrifying such a glass particle deposit has abnormal points due to the above-mentioned bubbles and foreign matters, and frequently breaks during the fiber strength test after drawing.

【0003】ガラス微粒子堆積中に堆積体微粒子に異物
が付着するのを防止する方法は種々検討されており、ガ
ラス微粒子の堆積中に反応装置内へクリーンエアを導入
する方法も提案されている。例えば特開平5−1169
79号公報には、OVD法によるガラス微粒子堆積体の
製造時に、コア用ガラス棒の全長にわたって清浄ガス流
を吹き付けて火炎が当たっていない部分に異物が付着す
るのを防止する方法が開示されている。
Various methods have been studied for preventing foreign substances from adhering to the deposit particles during the deposition of the glass particles, and a method of introducing clean air into the reactor during the deposition of the glass particles has also been proposed. For example, Japanese Patent Laid-Open No. 5-1169
Japanese Patent Publication No. 79 discloses a method of spraying a clean gas flow over the entire length of a glass rod for a core to prevent foreign matters from adhering to a portion not hit by a flame when a glass particulate deposit is manufactured by the OVD method. There is.

【0004】[0004]

【発明が解決しようとする課題】このようなクリーエア
を使用する方法の場合、通常は高性能フィルターを有す
るクリーンエア発生器を用いてダスト数を低減した空気
が使用される。ガラス微粒子堆積体の製造装置は、通
常、後工程のガラス微粒子堆積体を高温加熱して、透明
ガラス化を行う焼結装置などの関連装置と同一建屋内に
設置されている。これらの装置では塩素系ガス、SiC
4 、GeCl4 、Cl2 、SiF4 などの金属を腐食
させるガスが多用されており、何らかのトラブルが生じ
た場合にはこれらの特殊ガスが漏れ出す場合もあり、そ
れらがクリーンエア発生器に吸気されてクリーンエア発
生器を損傷させたり、クリーンエアに含まれた形でガラ
ス微粒子堆積体製造装置内へ混入し、該装置の内部の金
属材を腐食させて異物発生の原因となる場合がある。
In the method of using such clean air, air having a reduced dust number is usually used by using a clean air generator having a high performance filter. The apparatus for producing a glass particle deposit is usually installed in the same building as a related apparatus such as a sintering device that heats a glass particle deposit in a post-process to a high temperature to form a transparent glass. In these devices, chlorine gas, SiC
l 4, GeCl 4, Cl 2 , and the gas to corrode metals such as SiF 4 is frequently used, in the case where some trouble has occurred in some cases these special gas leaks, in their clean air generator Inhalation may damage the clean air generator, or it may mix in the clean air generator into the glass particulate deposit production equipment, corrode the metal material inside the equipment, and cause foreign matter to be generated. is there.

【0005】本発明はこのような従来技術における問題
を解決し、ガラス微粒子堆積体製造装置が設置された建
屋内において金属腐食性ガスの漏洩があった場合でも、
ガラス微粒子堆積体製造装置内への不純物ガスの混入を
防ぎ、ガラス微粒子堆積体中に混入する異物数を低減す
ることができるガラス微粒子堆積体の製造方法及びその
ための装置を提供しようとするものである。
The present invention solves the above problems in the prior art, and even if there is a leak of a metal corrosive gas in the building in which the apparatus for producing glass particle deposits is installed,
An object of the present invention is to provide a method for producing a glass particle deposit body and an apparatus for the same, which can prevent the mixture of an impurity gas into the apparatus for producing a glass particle deposit body and reduce the number of foreign matters mixed in the glass particle deposit body. is there.

【0006】[0006]

【課題を解決するための手段】本発明は上記課題を解決
する手段として次の(1)及び(2)の方法及び装置を
提供するものである。 (1)建屋内に設置されたガラス微粒子堆積体製造装置
を使用し、ガラス微粒子合成用バーナにガラス原料を供
給して火炎加水分解し生成するガラス微粒子を回転する
出発ロッドに堆積させてガラス微粒子堆積体を製造する
方法において、前記建屋外に開口する吸気口から空気を
取り入れて浄化するクリーンエア発生器で発生させたク
リーンエアを前記装置内へ導入しながらガラス微粒子の
堆積を行うことを特徴とするガラス微粒子堆積体の製造
方法。
The present invention provides the following methods (1) and (2) as means for solving the above problems. (1) Glass particulates are produced by supplying glass raw material to a burner for synthesizing glass particulates by using a glass particulate deposit manufacturing apparatus installed in a building and depositing glass particulates produced by flame hydrolysis on a rotating starting rod. In the method for producing a deposit, glass particles are deposited while introducing clean air generated by a clean air generator that takes in and purifies air from an intake opening opened to the outside of the building into the apparatus. And a method for producing a glass particulate deposit.

【0007】(2)建屋内に設置されたガラス微粒子堆
積体製造装置であって、ガラス微粒子合成用バーナにガ
ラス原料を供給して火炎加水分解し生成するガラス微粒
子を回転する出発ロッドに堆積させてガラス微粒子堆積
体を製造する装置において、前記建屋外に開口する吸気
口から空気を取り入れて浄化するクリーンエア発生器で
発生させたクリーンエアを導入するクリーンエア導入管
が接続されていることを特徴とするガラス微粒子堆積体
の製造装置。
(2) A glass fine particle deposit manufacturing apparatus installed in a building, wherein a glass raw material is supplied to a burner for synthesizing glass fine particles to deposit glass fine particles produced by flame hydrolysis on a rotating starting rod. In a device for producing a glass particulate deposit, a clean air introducing pipe for introducing clean air generated by a clean air generator for taking in and purifying air from an intake opening opened to the outside of the building is connected. Characteristic glass particle deposit manufacturing apparatus.

【0008】[0008]

【発明の実施の形態】以下、本発明の方法及び装置をO
VD法によりガラス微粒子堆積体を製造する場合を例に
とって、図面を参照して説明する。図1は本発明の1実
施態様に係る装置構成の概要を模式的に示す説明図であ
る。図1のガラス微粒子堆積体製造装置(以下、単に堆
積体製造装置とも記載する)1の主要部は、複数本(こ
の例では3本)のバーナ5と排気管6を有する反応容器
2と、上部にガラス微粒子堆積体15の出し入れを行う
ための上蓋を有する上煙突3と、ガラス微粒子堆積体1
5を往復運動させるための下煙突4で構成されている。
上煙突3及び下煙突4にはクリーンエア(CA)発生器
7からのクリーンエア(CA)を導入するCA導入管9
が取付けられている。CA導入管9は上煙突3又は下煙
突4のどちらか一方に取付ける形とすることもできる。
BEST MODE FOR CARRYING OUT THE INVENTION The method and apparatus of the present invention are described below.
The case of manufacturing a glass particle deposit by the VD method will be described as an example with reference to the drawings. FIG. 1 is an explanatory diagram schematically showing the outline of the apparatus configuration according to one embodiment of the present invention. The glass particulate deposit manufacturing apparatus (hereinafter, also simply referred to as a deposit manufacturing apparatus) 1 shown in FIG. An upper chimney 3 having an upper lid for loading and unloading the glass particle deposit body 15 and a glass particle deposit body 1
It is composed of a lower chimney 4 for reciprocating the movement 5.
A CA introduction pipe 9 for introducing clean air (CA) from a clean air (CA) generator 7 to the upper chimney 3 and the lower chimney 4.
Is installed. The CA introducing pipe 9 may be attached to either the upper chimney 3 or the lower chimney 4.

【0009】CA発生器7は要求されるクリーンエア中
のダスト数に応じたダスト除去能力を有する高性能フィ
ルタを備えた空気浄化装置であり、吸気口8から取り入
れた空気をろ過してダストを除去し、クリーンエアとし
て接続管10、CA導入管9を経由して装置内へ供給す
る装置であり、一般にクリーンルーム用として使用され
ているものが使用できる。この例においてCA発生器7
の吸気口8は堆積体製造装置1が設置されている建屋の
外に開口している。
The CA generator 7 is an air purifying device equipped with a high-performance filter having a dust removing capacity according to the number of dusts in the required clean air, and filters the air taken in from the intake port 8 to remove the dusts. A device that removes the clean air and supplies it as clean air into the device through the connecting pipe 10 and the CA introducing pipe 9, and a device that is generally used for clean rooms can be used. CA generator 7 in this example
The intake port 8 is open outside the building in which the deposit manufacturing apparatus 1 is installed.

【0010】この装置においてガラスロッド13の上下
にそれぞれダミーロッド14を溶着して作製した出発ロ
ッドを、支持棒11で保持して昇降装置12により回転
させつつ上下に往復運動させながら、周囲にバーナ5で
合成されるガラス微粒子を堆積させてガラス微粒子堆積
体15を製造する。バーナ5としてはSiCl4 などの
ガラス原料噴出ポート、H2 などの可燃性ガス噴出ポー
ト、O2 などの助燃性ガス噴出ポート及びArなどの不
活性ガス噴出ポートを備えたガラス微粒子合成用バーナ
が好適に使用できる。
In this apparatus, starting rods prepared by welding dummy rods 14 to the upper and lower sides of a glass rod 13 respectively are held by a supporting rod 11 and are rotated by an elevating and lowering device 12 while reciprocating up and down, while surrounding burners. The glass fine particles synthesized in 5 are deposited to manufacture the glass fine particle deposit body 15. The burner 5 is a burner for synthesizing glass particles, which has a glass raw material ejection port such as SiCl 4 , a flammable gas ejection port such as H 2 , an auxiliary combustion gas ejection port such as O 2 and an inert gas ejection port such as Ar. It can be preferably used.

【0011】ガラス微粒子が堆積している期間を通し
て、CA発生器7から堆積体製造装置1が設置されてい
る建屋外から吸気した空気をろ過したクリーンエアを堆
積体製造装置1内へ供給するようにする。これにより何
らかのトラブルにより堆積体製造装置1が設置されてい
る建屋内にガラス原料ガスやガラス微粒子堆積体の脱
水、透明ガラス化などの際に発生する腐食性ガスなどが
漏洩した場合でも、これらのガスがCA発生器7に吸気
され、CA発生器7自体あるいは堆積体製造装置1の内
部を腐食させることがなく、クリーンな環境下でガラス
微粒子の堆積を行うことができる。
Through the period in which the glass particles are deposited, clean air obtained by filtering the air sucked from the CA generator 7 from the building outside where the deposit manufacturing apparatus 1 is installed is supplied into the deposit manufacturing apparatus 1. To As a result, even if a corrosive gas generated during dehydration of glass raw material deposits or transparent glass vitrification leaks into the building where the deposit manufacturing apparatus 1 is installed due to some trouble, The gas is sucked into the CA generator 7 and does not corrode the CA generator 7 itself or the inside of the deposit body manufacturing apparatus 1, and the glass fine particles can be deposited in a clean environment.

【0012】[0012]

【実施例】以下、実施例により本発明をさらに具体的に
説明するが、本発明はこれらの例に限定されるものでは
ない。 (実施例1)図1に示す構成のガラス微粒子堆積体製造
装置1を使用してガラス微粒子堆積体の製造を行った。
コア/クラッド部を有する直径30mm、長さ500m
mのコアロッド(ガラスロッド13)を用い、両側に石
英ガラス製のダミーロッド14を溶着して出発ロッドを
作製した。該出発ロッドを40rpmで回転させながら
鉛直に設置し、200mm/分の速度で上下に1100
mmトラバース運動させながらガラス微粒子合成用のバ
ーナ5から生成するガラス微粒子を順次堆積させてガラ
ス微粒子堆積体15を作製した。ガラス微粒子の堆積の
間、吸気口8が建屋外に開口するCA発生器7から大き
さ0.3μm以上ののダスト数が100個/CF(約
0.0035個/cm3 )のクリーンエア(ダスト数は
レーザパーティクルカウンタを用いて粒子からの散乱光
強度により測定)を導入し、反応容器2内を−20Pa
の負圧に保持した。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples. (Example 1) A glass particulate deposit body was manufactured using the glass particulate deposit manufacturing apparatus 1 having the configuration shown in FIG.
Diameter 30mm with core / cladding, length 500m
A starting rod was manufactured by using a core rod (glass rod 13) of m and welding dummy rods 14 made of quartz glass on both sides. The starting rod was installed vertically while rotating at 40 rpm, and it was moved up and down at a speed of 200 mm / min.
A glass particle deposit 15 was prepared by sequentially depositing glass particles generated from the burner 5 for synthesizing glass particles while performing a traverse motion of mm. During the deposition of the glass particles, a clean air of 100 pieces / CF (about 0.0035 pieces / cm 3 ) of dust having a size of 0.3 μm or more from the CA generator 7 whose intake port 8 opens outside the building ( The number of dust is measured by the intensity of scattered light from particles using a laser particle counter), and the inside of the reaction vessel 2 is set to −20 Pa.
The negative pressure was maintained.

【0013】バーナ5としては直径30mmのバーナを
150mmの間隔で3本設置し、それぞれのバーナ5に
は原料となるSiCl4 :4SLM(スタンダードリッ
トル/分)、火炎を形成するためのH2 :80SLM及
びO2 :40SLM、さらにシールガスとしてAr:2
SLMを供給し、目標の堆積重量(6.0kg)のガラ
ス微粒子堆積体15を製造する操作を繰り返し行った。
連続製造の途中で建屋内の堆積体製造装置1でSiCl
4 ガスの漏れが発生したが、CA導入管9などの各種装
置部品が腐食することはなく、操業を続行することがで
きた。製造したガラス微粒子堆積体15を高温加熱して
透明ガラス化させた後、ファイバ化を順次行ったが、ガ
ス漏れ前後のプリフォームで、スクリーニング試験(フ
ァイバ長手方向で約2%の引き伸び率となる荷重を負荷
(1.9kgで1秒間)して低強度部を除去するための
ファイバ強度試験)の断線頻度は変化せず、平均で10
0kmで1回という頻度であった。
As the burners 5, three burners having a diameter of 30 mm are installed at intervals of 150 mm, and SiCl 4 : 4 SLM (standard liter / min) as a raw material and H 2 for forming a flame are provided in each burner 5. 80 SLM and O 2 : 40 SLM, and Ar: 2 as a seal gas
The operation of supplying the SLM and manufacturing the glass particulate deposit 15 of the target deposition weight (6.0 kg) was repeated.
During the continuous production, SiCl was used in the deposit production equipment 1 inside the building.
Although 4 gas leaked, various equipment parts such as the CA introduction pipe 9 did not corrode, and the operation could be continued. The produced glass fine particle deposit 15 was heated at a high temperature to be transparent vitrified, and then fiberized in order, but a screening test (a stretch rate of about 2% in the fiber longitudinal direction was performed on the preform before and after gas leakage. The frequency of disconnection in the fiber strength test for removing the low-strength portion by applying a load (1.9 kg for 1 second) does not change, and is 10 on average.
The frequency was once at 0 km.

【0014】(比較例1)CA発生器7の設置位置を、
吸気口8が堆積体製造装置1と同じ建屋内で、該装置上
蓋より1m上方に開口するようにした他は実施例1と同
様にして、ガラス微粒子堆積体15の製造を繰り返し行
った。連続製造の途中で建屋内の堆積体製造装置1でS
iCl4 ガスの漏れが発生した結果、CA導入管9等の
各種装置部品に腐食が発生した。製造したガラス微粒子
堆積体15を高温加熱して透明ガラス化させた後、ファ
イバ化を順次行ったところ、ガス漏れ前後のプリフォー
ムでスクリーニング試験時の断線頻度が変化し、ガス漏
れ前で100kmで1回、ガス漏れ後では100kmで
10回という結果となった。
(Comparative Example 1) The installation position of the CA generator 7 is
The glass fine particle deposit 15 was repeatedly manufactured in the same manner as in Example 1 except that the intake port 8 was opened in the same building as the deposit manufacturing apparatus 1 1 m above the lid of the apparatus. During the continuous production, S
As a result of the leakage of iCl 4 gas, corrosion occurred in various equipment parts such as the CA introduction pipe 9. When the manufactured glass particle deposit 15 was heated at a high temperature to be transparent vitrified, and then fiberized, the preform before and after the gas leakage changed the disconnection frequency during the screening test, and the pre-gas leakage was 100 km before the gas leakage. The result was once, and 10 times at 100 km after gas leakage.

【0015】[0015]

【発明の効果】本発明によれば、ガラス微粒子堆積体製
造装置内への不純物ガスの混入を防ぎ、ガラス微粒子堆
積体中に混入する異物数を低減することができ、ガラス
微粒子堆積体製造装置が設置されている建屋内におい
て、何らかのトラブルにより塩素系ガス、SiCl4
GeCl4 、Cl2 、SiF4 などの腐食性ガスが漏洩
が生じた場合でもガラス微粒子堆積体中に混入する異物
数が増加することがないガラス微粒子堆積体の製造方法
及びそのための装置が提供される。
EFFECTS OF THE INVENTION According to the present invention, it is possible to prevent the impurity gas from being mixed into the apparatus for producing glass particle deposits, and to reduce the number of foreign substances mixed in the object for glass particulate deposits. In the building where is installed, due to some trouble, chlorine gas, SiCl 4 ,
Provided is a method for manufacturing a glass particle deposit body and an apparatus for the same, which does not increase the number of foreign substances mixed in the glass particle deposit body even when a corrosive gas such as GeCl 4 , Cl 2 , SiF 4 leaks. It

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

【図1】本発明の1実施態様に係る装置構成の概要を模
式的に示す説明図。
FIG. 1 is an explanatory view schematically showing an outline of a device configuration according to one embodiment of the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 建屋内に設置されたガラス微粒子堆積体
製造装置を使用し、ガラス微粒子合成用バーナにガラス
原料を供給して火炎加水分解し生成するガラス微粒子を
回転する出発ロッドに堆積させてガラス微粒子堆積体を
製造する方法において、前記建屋外に開口する吸気口か
ら空気を取り入れて浄化するクリーンエア発生器で発生
させたクリーンエアを前記装置内へ導入しながらガラス
微粒子の堆積を行うことを特徴とするガラス微粒子堆積
体の製造方法。
1. A glass fine particle deposit manufacturing apparatus installed in a building is used to supply a glass raw material to a burner for synthesizing glass fine particles to deposit glass fine particles produced by flame hydrolysis on a rotating starting rod. In the method for producing a glass particle deposit, the glass particles are deposited while introducing clean air generated by a clean air generator that takes in and purifies air from an intake opening opened outside the building into the apparatus. A method for producing a glass particulate deposit, comprising:
【請求項2】 建屋内に設置されたガラス微粒子堆積体
製造装置であって、ガラス微粒子合成用バーナにガラス
原料を供給して火炎加水分解し生成するガラス微粒子を
回転する出発ロッドに堆積させてガラス微粒子堆積体を
製造する装置において、前記建屋外に開口する吸気口か
ら空気を取り入れて浄化するクリーンエア発生器で発生
させたクリーンエアを導入するクリーンエア導入管が接
続されていることを特徴とするガラス微粒子堆積体の製
造装置。
2. An apparatus for producing a glass particle deposit body installed in a building, wherein a glass raw material is supplied to a burner for synthesizing glass particles, and glass particles produced by flame hydrolysis are deposited on a rotating starting rod. In an apparatus for producing a glass particulate deposit, a clean air introducing pipe for introducing clean air generated by a clean air generator for taking in and purifying air from an intake opening opened to the outside of the building is connected An apparatus for manufacturing glass particulate deposits.
JP2001315279A 2001-10-12 2001-10-12 Manufacturing method and manufacturing apparatus for glass fine particle deposit Pending JP2003119034A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001315279A JP2003119034A (en) 2001-10-12 2001-10-12 Manufacturing method and manufacturing apparatus for glass fine particle deposit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001315279A JP2003119034A (en) 2001-10-12 2001-10-12 Manufacturing method and manufacturing apparatus for glass fine particle deposit

Publications (1)

Publication Number Publication Date
JP2003119034A true JP2003119034A (en) 2003-04-23

Family

ID=19133471

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001315279A Pending JP2003119034A (en) 2001-10-12 2001-10-12 Manufacturing method and manufacturing apparatus for glass fine particle deposit

Country Status (1)

Country Link
JP (1) JP2003119034A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20170040740A (en) * 2015-10-05 2017-04-13 신에쓰 가가꾸 고교 가부시끼가이샤 Fabrication apparatus of porous glass preform
US10308541B2 (en) 2014-11-13 2019-06-04 Gerresheimer Glas Gmbh Glass forming machine particle filter, a plunger unit, a blow head, a blow head support and a glass forming machine adapted to or comprising said filter

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10308541B2 (en) 2014-11-13 2019-06-04 Gerresheimer Glas Gmbh Glass forming machine particle filter, a plunger unit, a blow head, a blow head support and a glass forming machine adapted to or comprising said filter
KR20170040740A (en) * 2015-10-05 2017-04-13 신에쓰 가가꾸 고교 가부시끼가이샤 Fabrication apparatus of porous glass preform
JP2017071513A (en) * 2015-10-05 2017-04-13 信越化学工業株式会社 Porous glass base material manufacturing equipment
CN106986534A (en) * 2015-10-05 2017-07-28 信越化学工业株式会社 The manufacturing equipment of porous glass preform
CN106986534B (en) * 2015-10-05 2021-06-08 信越化学工业株式会社 Apparatus for manufacturing porous glass preform
KR102545708B1 (en) 2015-10-05 2023-06-19 신에쓰 가가꾸 고교 가부시끼가이샤 Fabrication apparatus of porous glass preform

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