JPH0244041A - Glass fiber spinning device - Google Patents
Glass fiber spinning deviceInfo
- Publication number
- JPH0244041A JPH0244041A JP19389388A JP19389388A JPH0244041A JP H0244041 A JPH0244041 A JP H0244041A JP 19389388 A JP19389388 A JP 19389388A JP 19389388 A JP19389388 A JP 19389388A JP H0244041 A JPH0244041 A JP H0244041A
- Authority
- JP
- Japan
- Prior art keywords
- glass
- core
- clad
- pot
- molten
- 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
Links
- 239000003365 glass fiber Substances 0.000 title claims description 14
- 238000009987 spinning Methods 0.000 title claims description 14
- 239000011521 glass Substances 0.000 claims abstract description 75
- 239000006060 molten glass Substances 0.000 claims abstract description 18
- 238000003756 stirring Methods 0.000 claims description 28
- 238000005253 cladding Methods 0.000 claims description 13
- 239000000835 fiber Substances 0.000 abstract description 13
- 101100298225 Caenorhabditis elegans pot-2 gene Proteins 0.000 abstract 1
- 238000013019 agitation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 5
- 239000013307 optical fiber Substances 0.000 description 4
- 230000003287 optical effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 241001597150 Thalassodes Species 0.000 description 1
- 239000006121 base glass Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000008054 signal transmission Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/02—Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor
- C03B37/022—Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor from molten glass in which the resultant product consists of different sorts of glass or is characterised by shape, e.g. hollow fibres, undulated fibres, fibres presenting a rough surface
- C03B37/023—Fibres composed of different sorts of glass, e.g. glass optical fibres, made by the double crucible technique
Landscapes
- Engineering & Computer Science (AREA)
- 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)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はガラスファイバー紡糸装置に関し、特に光ファ
イバー等、コアガラス部とこれを囲む1層以上のクラッ
ドガラス部とを有するガラスファイバーを成形する場合
に、ファイバー断面内の各ガラス部の形状・寸法、及び
ファイバー外径を高精度に制御する技術に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a glass fiber spinning device, and particularly for forming a glass fiber such as an optical fiber, which has a core glass portion and one or more clad glass layers surrounding it. The present invention relates to a technology for highly accurately controlling the shape and dimensions of each glass portion within a fiber cross section and the outer diameter of the fiber.
コアガラスとこれよりも低屈折率のクラッドガラス層と
を有する光ファイバーを、溶融ガラス状態から直接連続
的に成形する方法としてポット法が知られている。A pot method is known as a method for directly and continuously forming an optical fiber having a core glass and a cladding glass layer having a lower refractive index from a molten glass state.
また光フアイバー以外にも、例えば屈折率分布型ロンド
レンズの母材となるガラスファイバーを成形する工程に
おいて、熱成形性があまり良好でないガラス組成でレン
ズを構成する場合に、レンズ母材ガラスの外周に熱成形
性の良好なガラスから成るクラッドガラス層を設けて一
体に紡糸成形した後、屈折率分布付けのためのイオン交
換処理を行なう方法(特願昭62−231848)があ
り、該方法の実施にもポット法が用いられる。In addition to optical fibers, for example, in the process of molding the glass fiber that is the base material of a gradient index Ronde lens, when the lens is constructed with a glass composition that does not have very good thermoformability, the outer periphery of the lens base glass is used. There is a method (Japanese Patent Application No. 62-231848) in which a clad glass layer made of glass with good thermoformability is provided and integrally formed by spinning, and then an ion exchange treatment is performed to create a refractive index distribution. The pot method is also used for implementation.
ポット法で使用する紡糸装置の基本的な構造を第5図に
示す。The basic structure of the spinning device used in the pot method is shown in FIG.
図示のように紡糸装置lは、中心に配置した断面円形の
コアポット部2と、このコアポット部2の外周を囲むよ
うに同心円環状に配置されたクラッドポット部3から成
り、これら両ポット部2゜3の下底には溶融ガラス流出
ノズル2A、 3Aがそれぞれ設けてあって、これら両
ノズル2A、 34も同心状に配置されている。As shown in the figure, the spinning apparatus 1 consists of a core pot part 2 with a circular cross section arranged at the center, and a clad pot part 3 arranged in a concentric ring shape so as to surround the outer periphery of this core pot part 2. Both of these pot parts 2° Molten glass outflow nozzles 2A and 3A are provided at the bottom of the nozzle 3, respectively, and these nozzles 2A and 34 are also arranged concentrically.
そして、これらポット部2.3及びノズル部2八。And these pot part 2.3 and nozzle part 28.
3Aは図外の加熱装置で高温に保持される。コアポット
部2内には、コアガラス4が溶融状態で保持されており
、タラッドボソト部3内には、コアガラス4とは異質の
クラッドガラス5が溶融状態で保持されている。3A is maintained at a high temperature by a heating device not shown. A core glass 4 is held in a molten state in the core pot part 2, and a clad glass 5, which is different from the core glass 4, is held in a molten state in the turret part 3.
両ポット部2,3内の溶融ガラス4.5はノズル2A、
3A内を流下し、合流点6で合流した後さらにノズル
内を流下して徐々に冷却され、下端開口から引き出され
て、連続する一定外径のガラスファイバー10が成形さ
れる。The molten glass 4.5 in both pot parts 2, 3 is supplied to the nozzle 2A,
3A, merge at the confluence point 6, further flow down the inside of the nozzle, be gradually cooled, and be pulled out from the lower end opening to form a continuous glass fiber 10 with a constant outer diameter.
得られるガラスファイバー10は、第6図に断面図で示
すように、コアガラス部10Aとこれの外周を囲むタラ
ソドガラス層10Bとで構成される二重構造となってい
る。The obtained glass fiber 10 has a double structure consisting of a core glass part 10A and a thalassod glass layer 10B surrounding the outer periphery of the core glass part 10A, as shown in the cross-sectional view in FIG.
上記のようなポット紡糸装置では一般に、主体となるコ
アガラスを高品質化するために、コアポット部z内の溶
融ガラスを撹拌する回転羽根から成る撹拌装置7を設け
ている。In the pot spinning apparatus as described above, generally, in order to improve the quality of the main core glass, a stirring device 7 made of rotating blades is provided to stir the molten glass in the core pot part z.
なお図には、クラッドポット部3を一層だけ設けた二重
ポットを示しているが、必要に応じて上記クラッドポッ
ト部を同心円環状に二重以上の多重に設けてもよく、本
願発明はかかる多重ポットをも包含するが、便宜上二重
ポットを例にとり説明する。Although the figure shows a double pot in which only one layer of clad pot portions 3 is provided, the clad pot portions may be provided in a concentric ring shape in two or more layers as necessary, and the present invention does not apply to such a method. Although multiple pots are also included, for convenience, a double pot will be explained as an example.
、上述のようにコアポット部に撹拌装置を設ける利点は
、ガラス溶解時に生じる不均質を防止し、光信号伝送あ
るいは画像伝送の主体となるコアガラスを高均質化でき
る点にあるが、伝送主体とならないクラッドガラス部に
ついては従来あまり配慮されていなかった。As mentioned above, the advantage of providing a stirring device in the core pot part is that it can prevent non-uniformity that occurs during glass melting and make the core glass, which is the main body of optical signal transmission or image transmission, highly homogeneous. Conventionally, little consideration has been given to the clad glass portion that cannot be used.
しかしながら、本発明者らの研究、実験によれば、コア
ークラッドガラスファイバーの断面内におけるコアガラ
スの偏心、及びファイバーの外径のバラツキは、クラッ
ドガラスの不均質に大きく起因していることが解った。However, according to the research and experiments conducted by the present inventors, it has been found that the eccentricity of the core glass within the cross section of the core-clad glass fiber and the variation in the outer diameter of the fiber are largely caused by the non-uniformity of the clad glass. Ta.
クラッドガラスが溶融状態で不均質であると、一定の温
度条件下でファイバーを紡糸成形する際、クラッドガラ
ス自身の粘性が不連続に変化するため、紡糸速度の制御
だけでは一定の紡糸線径に抑えることができず、この結
果成形されるファイバーの外径が長さ方向に大きくばら
つくことになり、また例えできたとしても、それは外径
の制御であるため、光学性能を決めるコアガラスの径ま
で制御できない。この結果、ファイバー断面内でコアガ
ラスが偏心(クラッドガラスの厚みが不均一になる)し
たり、またファイバー外径が一定であっても長さ方向で
コア径のバラツキを生じることになる。If the clad glass is heterogeneous in its molten state, the viscosity of the clad glass itself changes discontinuously when spinning fibers under constant temperature conditions, so it is difficult to maintain a constant spun wire diameter by controlling the spinning speed alone. As a result, the outer diameter of the formed fiber will vary greatly in the length direction, and even if it were possible to control the outer diameter, the diameter of the core glass, which determines the optical performance. I can't control it. As a result, the core glass becomes eccentric within the fiber cross section (the thickness of the cladding glass becomes non-uniform), and even if the fiber outer diameter is constant, the core diameter varies in the length direction.
上記のような形状、寸法の不均一は、光ファイバーある
いはレンズの光学性能の不均一を引き起す。The above-described non-uniformity in shape and size causes non-uniformity in the optical performance of the optical fiber or lens.
コアポット部とクラッドポット部の双方に、これらポッ
ト部内の溶融ガラスを強制撹拌する手段を設ける。Both the core pot section and the cladding pot section are provided with means for forcibly stirring the molten glass in these pot sections.
この撹拌手段は一般的には、溶融ガラス中に浸漬され外
部駆動機構によって回転される撹拌羽根で構成され、コ
ア部とクラッド部の各撹拌羽根は、後述の好適実施例に
示すように、共通の回転軸に設けて同時回転させてもよ
いし、あるいは別体としてそれぞれ独立に回転させるよ
うにしてもよい。This stirring means generally consists of stirring blades immersed in the molten glass and rotated by an external drive mechanism, and the stirring blades in the core section and the cladding section are common, as shown in the preferred embodiment below. They may be provided on the rotation shafts of the two and rotated at the same time, or they may be made as separate bodies and rotated independently.
ただし、クラッドポット部は上方開口が円環状を成して
いるとともに間隙が狭いため、タラソドポット部内の特
定箇所に羽根を浸漬配置するよりも前者構造として、ク
ラッドポット部の円周に沿って溶融ガラス撹拌羽根が回
転運動するようにした方がより高い均質化効果が得られ
るので望ましい。However, since the upper opening of the clad pot part is annular and the gap is narrow, the former structure is used instead of immersing the blades in a specific location within the thalasso pot part. It is preferable that the stirring blade rotates because a higher homogenization effect can be obtained.
〔作用〕
上記構造の紡糸装置を用いることにより、コアガラスの
みならずクラッドガラスも充分に高均質化し、したがっ
て溶融ガラスの粘性がコア、クララドともに均一となる
ため、クラッドガラスの不均質に起因するファイバー中
のコアガラス偏心、コアガラス径バラツキあるいはファ
イバー外径のバラツキが従来に比べて大幅に減少する。[Function] By using the spinning device with the above structure, not only the core glass but also the cladding glass can be made sufficiently homogeneous, and therefore the viscosity of the molten glass becomes uniform in both the core and the cladding glass, so that the viscosity of the molten glass becomes uniform in both the core and the cladding glass. Core glass eccentricity in the fiber, core glass diameter variation, and fiber outer diameter variation are significantly reduced compared to conventional methods.
以下本発明を図面に示した実施例について詳細に説明す
る。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to embodiments shown in the drawings.
第1図は本発明に係る紡糸装置の断面図であり、コアポ
ット部2内の溶融コアガラス4と、クラッドボット3内
の溶融クラッドガラス5とを共通の撹拌装置20で回転
撹拌する構造となっている。FIG. 1 is a cross-sectional view of the spinning device according to the present invention, which has a structure in which the molten core glass 4 in the core pot section 2 and the molten clad glass 5 in the clad bot 3 are rotationally stirred by a common stirring device 20. ing.
撹拌装置20は、図外の駆動装置によって回転駆動され
る回転軸21に、コアガラス4中に浸漬される撹拌羽根
22を設けるとともに、これよりも上方において回転軸
21に固着された円筒状のクラッドガラススクーラー3
0を設けて構成されている。クラッドガラススクーラー
30の平面図、側面図、斜視図をそれぞれ第2図、第3
図、第4図に示す。The stirring device 20 includes stirring blades 22 immersed in the core glass 4 on a rotating shaft 21 that is rotationally driven by a drive device (not shown), and a cylindrical stirring blade 22 fixed to the rotating shaft 21 above this. clad glass cooler 3
It is configured with 0. A plan view, a side view, and a perspective view of the clad glass cooler 30 are shown in FIGS. 2 and 3, respectively.
It is shown in Fig. 4.
クラッドガラススクーラー30は、下方が開放された略
円筒状を成しており、上壁31中心孔に回転軸21を通
し、放射状に延びるリブ32で回転軸21に一体的に固
着されており、上壁面には溶融ガラスからの発生ガスを
逃がすためのガス抜き開口33を設けである。The clad glass cooler 30 has a substantially cylindrical shape with an open bottom, and the rotating shaft 21 is passed through the center hole of the upper wall 31, and is integrally fixed to the rotating shaft 21 with radially extending ribs 32. A gas vent opening 33 is provided on the upper wall surface to release gas generated from the molten glass.
また円筒側壁34の下端は、一定間隔をおいて切欠き3
5を入れることにより、隣接切欠き間に小幅の突出する
撹拌羽根部36を均等間隔で形成している。さらに撹拌
効果を増すため、撹拌羽根部36は、他の側壁部分より
も板厚を大にするとともに、平面視で回転方向前端の厚
みを後端よりも薄(してくさび形状にしである。つまり
スターク−30が矢符37方向に回転したとき、撹拌羽
根部36のくさび形により溶融ガラスを外周寄りに押し
出して、ポット半径方向での撹拌混合効果を増すように
している。さらに、撹拌羽根部36は側面視においても
くさび形状となし、溶融ガラスの深さ方向での撹拌混合
効果を増すようにしている。Further, the lower end of the cylindrical side wall 34 has notches 3 at regular intervals.
5, narrow protruding stirring blade portions 36 are formed at equal intervals between adjacent notches. In order to further increase the stirring effect, the stirring blade part 36 is made thicker than the other side wall parts, and is wedge-shaped so that the front end in the rotation direction is thinner than the rear end in plan view. In other words, when the Stark-30 rotates in the direction of arrow 37, the wedge-shaped stirring blade portion 36 pushes the molten glass toward the outer periphery, increasing the stirring and mixing effect in the radial direction of the pot. The portion 36 also has a wedge shape when viewed from the side, so as to increase the effect of stirring and mixing the molten glass in the depth direction.
上記構造をもつスターク−30の撹拌羽根部36は、ク
ラッドポット3内の溶融クラッドガラス5中に浸漬され
る。The stirring blade part 36 of the Stark-30 having the above structure is immersed in the molten clad glass 5 in the clad pot 3.
なおコアガラス撹拌羽根22は従来と同じであってよく
、図示例では、回転軸21の長さ方向に多段の羽根群を
設け、隣接する段の間で羽根の傾斜が互いに逆向となる
よう羽根に傾斜を設けである。Note that the core glass stirring blade 22 may be the same as the conventional one, and in the illustrated example, a multistage group of blades is provided in the length direction of the rotating shaft 21, and the blades are arranged so that the slopes of the blades are opposite to each other between adjacent stages. A slope is provided.
上記装置において、回転軸21を外部駆動装置によって
回転させると、撹拌羽根22がコアガラス4を撹拌する
と同時に、クラッドガラススクーラー30の撹拌羽根部
36が、円環状のタラッドポソト3内溶融ガラス中をポ
ットの形状に沿って円運動し、溶融クラッドガラス5を
撹拌する。In the above device, when the rotating shaft 21 is rotated by an external drive device, the stirring blade 22 stirs the core glass 4, and at the same time, the stirring blade part 36 of the clad glass cooler 30 moves the molten glass inside the annular TARAD POSOTO 3. The molten clad glass 5 is stirred by circular motion along the shape of the pot.
また撹拌と同時に、ガラスが高温で静置された場合生じ
るガラス中特定成分の揮発が原因の不均質、いわゆる表
面皮も取り除かれる。In addition, at the same time as stirring, non-uniformity, so-called surface skin, caused by volatilization of specific components in the glass, which occurs when the glass is left at high temperatures, is also removed.
実験の結果では、第5図に示した従来の紡糸装置で直径
1龍のガラスファイバーを成形したところ、ファイバー
外径のバラツキは±15μmあり、またクラッドガラス
厚みのバラツキは±20μmあったが、第1図ないし第
4図に示したようなりラッドガラススクーラー30を付
設して上記と同一線径のガラスファイバーを紡糸したと
ころ、ファイバーの外径及びクラッド厚みのバラツキは
いずれも±5μmと著しく改善された。According to the experimental results, when glass fibers with a diameter of 1 mm were formed using the conventional spinning device shown in Fig. 5, the variation in the outer diameter of the fibers was ±15 μm, and the variation in the thickness of the cladding glass was ±20 μm. When glass fibers with the same wire diameter as above were spun using the rad glass cooler 30 as shown in Figures 1 to 4, the variation in the outer diameter of the fibers and the cladding thickness was as large as ±5 μm. Improved.
本発明によれば、コア及びクラッド層から成るガラスフ
ァイバーを成形するに当り、溶融ガラス保持ポット内で
、コアガラスのみならずクラッドガラスも撹拌されるた
め、ガラスの不均質がクラッドガラスにおいても取り除
かれ、均一粘性のコア、クラッドガラスとなり、したが
って従来クラッドガラスの不均質に起因して発生してい
たコアガラスの偏心、径バラツキ、及びファイバーの外
径バラツキが大幅に減少する。According to the present invention, when forming a glass fiber consisting of a core and a cladding layer, not only the core glass but also the cladding glass is stirred in the molten glass holding pot, so that non-uniformities in the glass are removed even in the cladding glass. This results in a core and clad glass of uniform viscosity, and therefore, the eccentricity and diameter variations of the core glass and the variations in the outer diameter of the fibers, which conventionally occur due to the non-uniformity of the clad glass, are significantly reduced.
第1図は本発明の一実施例を示す縦断面図、第2図は第
1図の装置のタラッドガラススターラー部分を示す平面
図、第3図は同側面図、第4図は第1図の装置における
撹拌装置全体を示す斜視図、第5図は従来のポット法紡
糸装置を示す縦断面図、第6図は成形されるガラスファ
イバーの構造を示す断面図である。
2・・・コアポット部、3・・・クラッドポット部、2
A。
3A・・・ノズル、4・・・溶融コアガラス、5・・・
溶融クラッドガラス、10・・・ガラスファイバー 2
0・・・撹拌装置、21・・・回転軸、22・・・コア
ガラス撹拌羽根、30・・・クランドガラススターラー
、32・・・リブ、33・・・ガス抜き開口、34・・
・側壁、35・・・切欠き、36・・・クラッドガラス
撹拌羽根、37・・・回転方向。
第
図
第
図FIG. 1 is a longitudinal cross-sectional view showing one embodiment of the present invention, FIG. 2 is a plan view showing the Tallad glass stirrer portion of the apparatus shown in FIG. 1, FIG. 3 is a side view of the same, and FIG. FIG. 5 is a longitudinal sectional view showing a conventional pot method spinning device, and FIG. 6 is a sectional view showing the structure of the glass fiber to be formed. 2...Core pot part, 3...Clad pot part, 2
A. 3A... Nozzle, 4... Molten core glass, 5...
Fused clad glass, 10...Glass fiber 2
0... Stirring device, 21... Rotating shaft, 22... Core glass stirring blade, 30... Cland glass stirrer, 32... Rib, 33... Gas vent opening, 34...
- Side wall, 35... Notch, 36... Clad glass stirring blade, 37... Rotation direction. Figure Figure
Claims (1)
ポット部外周に同心環状に設けられ、前記ガラスとは異
質の溶融ガラスを保持する少なくとも1つのクラッドポ
ット部とを具え、両ポット部下底に設けられたノズル部
から溶融ガラスを連続的に引き出すことにより、コアガ
ラスとこれを囲む少なくとも1層のクラッドガラスとを
有するガラスファイバーを成形する紡糸装置において、
前記コアポット部及びクラッドポット部の双方に溶融ガ
ラス撹拌手段を設けたことを特徴とするガラスファイバ
ー紡糸装置。A core pot section that holds a first molten glass, and at least one clad pot section that is provided in a concentric ring shape around the outer periphery of the core pot section and that holds a molten glass that is different from the glass, and is provided at the bottom bottom of both pots. In a spinning device that forms a glass fiber having a core glass and at least one layer of cladding glass surrounding the core glass by continuously drawing out molten glass from a nozzle portion,
A glass fiber spinning apparatus characterized in that both the core pot section and the clad pot section are provided with molten glass stirring means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19389388A JPH0244041A (en) | 1988-08-03 | 1988-08-03 | Glass fiber spinning device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19389388A JPH0244041A (en) | 1988-08-03 | 1988-08-03 | Glass fiber spinning device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0244041A true JPH0244041A (en) | 1990-02-14 |
Family
ID=16315494
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19389388A Pending JPH0244041A (en) | 1988-08-03 | 1988-08-03 | Glass fiber spinning device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0244041A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145317A (en) * | 2013-03-28 | 2013-06-12 | 湖北新华光信息材料有限公司 | Platinum device for optical glass feed preparation |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6191036A (en) * | 1984-10-09 | 1986-05-09 | Tanaka Kikinzoku Kogyo Kk | Method and apparatus for producing composite glass fiber |
-
1988
- 1988-08-03 JP JP19389388A patent/JPH0244041A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6191036A (en) * | 1984-10-09 | 1986-05-09 | Tanaka Kikinzoku Kogyo Kk | Method and apparatus for producing composite glass fiber |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145317A (en) * | 2013-03-28 | 2013-06-12 | 湖北新华光信息材料有限公司 | Platinum device for optical glass feed preparation |
| CN103145317B (en) * | 2013-03-28 | 2015-01-14 | 湖北新华光信息材料有限公司 | Platinum device for optical glass feed preparation |
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