JPS5954638A - Spinning of hollow glass filament and its device - Google Patents

Spinning of hollow glass filament and its device

Info

Publication number
JPS5954638A
JPS5954638A JP16443282A JP16443282A JPS5954638A JP S5954638 A JPS5954638 A JP S5954638A JP 16443282 A JP16443282 A JP 16443282A JP 16443282 A JP16443282 A JP 16443282A JP S5954638 A JPS5954638 A JP S5954638A
Authority
JP
Japan
Prior art keywords
molten glass
spinning
glass
melted glass
nozzle
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.)
Granted
Application number
JP16443282A
Other languages
Japanese (ja)
Other versions
JPH0346412B2 (en
Inventor
Norio Shimizu
紀夫 清水
Yukihiro Murakishi
村岸 幸宏
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.)
Tanaka Kikinzoku Kogyo KK
Original Assignee
Tanaka Kikinzoku Kogyo KK
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 Tanaka Kikinzoku Kogyo KK filed Critical Tanaka Kikinzoku Kogyo KK
Priority to JP16443282A priority Critical patent/JPS5954638A/en
Publication of JPS5954638A publication Critical patent/JPS5954638A/en
Publication of JPH0346412B2 publication Critical patent/JPH0346412B2/ja
Granted legal-status Critical Current

Links

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

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)
  • Manufacture, Treatment Of Glass Fibers (AREA)

Abstract

PURPOSE:To prepare easily hollow glass filaments having approximately uniform thickness on the whole circle and high dimensional accuracy, by making melted glass flow continuously and gradually to form a thin melted glass layer, entraining air in it, drawing it. CONSTITUTION:In the spinning device 16, the melted glass 5 put in the melted glass bath 10 is made to flow gradually by its own liquid pressure through the melted glass flow nozzle 11 at the bottom of the melted glass bath 10, received on the tray 12, so that the melted glass 5 is made into the fixed thin melted glass layer 18. The melted glass 5 is drawn from the thin melted glass layer 18 through the spinning nozzle 13, air in the air layer forming layer 14 is entrained in it by suction pressure of the drawing to spin the hollow glass filament 19. Air is forcedly fed from the feed pipe 15 into the air layer forming layer 14, and the pressure is preferably balanced with the liquid pressure in the melted glass bath 10.

Description

【発明の詳細な説明】 本発明は、中空ガラス繊維の紡糸方法及びその装置に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a hollow glass fiber spinning method and apparatus.

ガラス繊維は、人@無機械維として轍も生産量が多く 
、A;+1用技□術も進んでいろがζン伎近急速fで生
産量が増大してきている炭素繊3イトに比べ、密度が太
き゛い1弾性率が小さいなどの欠点がある為、これを克
服し、さらに新た庁機能を持たする為に中空ガラス繊維
が開発された。
Glass fiber has a large production volume due to human @ non-mechanical fiber production.
, A; +1 Although the technology for using it has progressed, it has disadvantages such as higher density and lower elastic modulus compared to carbon fiber 3-ite, whose production volume is increasing rapidly in the near future. Hollow glass fibers were developed to overcome this problem and provide new office functions.

中空ガラス′繊維は、ガラス繊維の紡糸中ンこ偶発的に
且つ局部的に形成されることがあるが、この場合はむし
ろ欠陥ガラス繊維として取扱わil−る。
Hollow glass fibers may be formed accidentally and locally during spinning of glass fibers, in which case they are treated rather as defective glass fibers.

□中空ガラス繊維を作るIfCは、従来第1図に示す如
く溶融ガラス槽1め底に紡糸ノズル2を設け、その紡糸
ノズル°2に空気導入管3の先端部を挿入して溶融ガラ
ス相1内に垂1Hに立設して成る紡糸装置4を用いて、
□紡糸ノズル2から溶融ガラス槽1内め浴融ガラス5を
吐出すると同時にその溶融ガラス5中に空気々¥導入管
を:1Er1して空気をまき込ん・で、□中空ガラス紘
維6を作っていた。1   ′□ところで前記の紡糸装
置4でV」中空ガラス繊維6が容易に得られる反面、窄
気シ〜入管3の装着が極めて困難であり、高温運転時季
1r(な孕′A4 入管3が紡糸ノズル2と芯ずれした
り、傾いたりして装置ヶ’/l /Jが不安シーと斥り
、捷I融ガラス槽1 o’iン(/i:多数の紡糸ノズ
ル2を、設けることが困難であり、□。
□IfC for producing hollow glass fibers has conventionally been manufactured by installing a spinning nozzle 2 at the bottom of a molten glass tank 1 as shown in Fig. 1, and inserting the tip of an air introduction tube 3 into the spinning nozzle °2 to inject a molten glass phase 1. Using a spinning device 4 vertically installed inside the
□The molten glass 5 in the molten glass tank 1 is discharged from the spinning nozzle 2, and at the same time, an air introduction tube is inserted into the molten glass 5 to inject air into the molten glass 5, thereby producing □hollow glass fibers 6. was. 1'□By the way, although V'' hollow glass fibers 6 can be easily obtained using the above-mentioned spinning device 4, it is extremely difficult to attach the inlet tube 3 during the high-temperature operation period (1r). If the center of the nozzle 2 is misaligned or it is tilted, the device may be unstable and the molten glass tank 1 o'in (/i: A large number of spinning nozzles 2 may be installed. It is difficult and □.

妊らに運転保守に常時監視が必要である2、従ってIf
F:産に不向きであり、得ら)する中空ガラスに哉維6
は高価なもの、!:なり、且つ品質不良なものもあった
。。
Pregnant women require constant monitoring for operation and maintenance2, so if
F: Hollow glass that is unsuitable for production and is not suitable for production (6)
That's expensive! : There were also some with poor quality. .

そこで本発明名らは斯かる中空ガラス繊維6の紡糸装置
4K((わる装置の開発に先立って、前記紡糸装置4に
於ける紡糸ノズル2の付近の?+r l*I!ガラス5
の流用挙動を詳+VIIj K調べた結果、次のことが
判明した。
Therefore, the name of the present invention is to develop a spinning device 4K for such hollow glass fibers 6 (((Prior to the development of the spinning device 4K), the spinning device 4K (?+r l*I! glass 5 near the spinning nozzle 2 in the spinning device 4) was developed.
As a result of a detailed investigation of the appropriation behavior of +VIIjK, the following was found.

l)紡糸ノズル2の中心上部の溶融ガラス5が最も早く
流れる。
l) The molten glass 5 at the upper center of the spinning nozzle 2 flows fastest.

2)流速、II、Iンま紡糸ノズル2 rt) r4v
心部が4外に向って詰まっている、 3)紡糸ノズル2の上部のノズル径に相当する距離で、
溶融ガラス5の最も早く流iLている部分がノズル径の
1/3程区の位置である。
2) Flow rate, II, In-ma spinning nozzle 2 rt) r4v
3) the core is packed outwards 4; 3) at a distance corresponding to the nozzle diameter of the upper part of the spinning nozzle 2;
The part where the molten glass 5 is flowing fastest is a position about 1/3 of the nozzle diameter.

従って、溶融ガラス5の最も1−iL (流れる部分に
空気をまき込むととにより、中空ガラス繊#、IA 6
を□容易に作り出せることが判った。即ち、浴融ガラ≧
:5の、液深をノズル径程度に保持すると溶融ガラ、2
5を引き出すだ、けで容易VC中空ガラで繊維6を作力
出せることが判った1、但j、7、ノズル形状に−より
最:IL!i液深は変化するが、一般的にt、1:ノズ
ル径の10倍以下である。
Therefore, by injecting air into the flowing part of the molten glass 5, the hollow glass fiber #, IA 6
It was found that □ can be easily created. That is, bath melting glass ≧
:5, if the liquid depth is maintained at about the nozzle diameter, molten glass, 2
It was found that it was easy to make fiber 6 with a VC hollow glass by pulling out 5. The i-liquid depth varies, but is generally t,1: 10 times or less the nozzle diameter.

一方、溶融ガラス5の液深を浅くすると、?TkJ:I
三が小さく分り、溶融ガラス5の流出力が小さくなり、
連続的に中空ガラス繊維6を紡糸することが困難になる
。
On the other hand, if the liquid depth of the molten glass 5 is made shallow, ? TkJ:I
3 becomes smaller, the outflow force of the molten glass 5 becomes smaller,
It becomes difficult to continuously spin the hollow glass fibers 6.

本発明は上記の点□にM目してなさ)1.たものであり
、溶融ガラスを1身の液圧或やは外15μよりの圧力調
整により連続的5徐々に流下させてi4い溶融ガラス層
を形成し、この薄い溶tFガラス層から浴融ガラスを引
き出すと共に空気1」込んで中空ガラス繊維を紡糸する
方法とその装j1tを提供″すること全目的とするもの
である。
The present invention focuses on the above points □) 1. The molten glass is made to flow down continuously and gradually by adjusting the pressure from 15 μm or more to form a thin molten glass layer, and from this thin molten tF glass layer, the bath molten glass is The overall object of the present invention is to provide a method and equipment for spinning hollow glass fibers by drawing out and introducing air.

以下本発明による中空ガラス2fR維の紡糸方法及びそ
の装置を図面に基いて説明する。先ず、Ab糸方法を実
施する為の紡糸装置の一例を第2図a、bによって説明
すると、10は多量の溶融ガラス5を保持゛″J″る溶
融ガラス槽で、この溶融ガラス槽10の底に複数個本例
では4個の溶融ガラス流下ノズル11が前後左右に等間
隔に設けられている。
The method and apparatus for spinning hollow glass 2fR fibers according to the present invention will be explained below with reference to the drawings. First, an example of a spinning apparatus for carrying out the Ab yarn method will be explained with reference to FIGS. A plurality of molten glass flowing down nozzles 11 (four in this example) are provided on the bottom at equal intervals in the front, rear, left and right directions.

この溶融ガラス流下ノズル11の下方、には薄い溶融ガ
ラス層を形成するトレイ1275に設けられ、このトレ
イ12は前記溶融ガラス槽10と同一平面積になされて
いて、底面に複数本例では9個の紡糸ノズルエ3が前記
溶融ガラス流下ノズル・11の投影位置の周囲斜め方向
位置に等間隔に設けられている。前記溶融ガラス流下ノ
ズル11の周囲は溶融ガラス4!!10とトレイ12.
を連結した周壁により空気層形成槽14が形成され、こ
の空気層形成槽】4には空気導入管15が連通されてい
る。
A tray 1275 for forming a thin molten glass layer is provided below the molten glass flowing down nozzle 11, and this tray 12 has the same planar area as the molten glass tank 10, and has a plurality of 9 in this example on the bottom surface. The spinning nozzles 3 are provided at equal intervals at diagonal positions around the projected position of the molten glass flowing down nozzle 11. The area around the molten glass flowing down nozzle 11 is molten glass 4! ! 10 and tray 12.
An air layer forming tank 14 is formed by the peripheral wall connecting the two, and an air introduction pipe 15 is communicated with this air layer forming tank 4.

次円かがる構造の紡糸装置16を用いる本発明の紡糸方
法について説明する。溶融ガラス槽10に保持された溶
融ガラス5を自身の液圧により溶融ガラスや1υ】0の
底の溶融ガラス流下ノズノtzllより連続的に徐々に
?1ffl下させてトレイ12上に受。
Next, the spinning method of the present invention using the spinning device 16 having a rounded structure will be explained. The molten glass 5 held in the molten glass tank 10 is continuously and gradually converted into molten glass by its own hydraulic pressure from the molten glass flowing down nozzle tzll at the bottom of 1υ]0? Lower it by 1ffl and place it on tray 12.

容させて溶融ガラス5iKニ一定の薄い溶融ガラス層1
8と成し、然る後この薄い溶融ガラス層18から溶融ガ
ラス5を紡糸ノズル13f通し、て引き出スメ共にその
引き出(〜による吸引圧により空気層形成槽14中の空
気、をまき込んで中空ガラス繊維19を紡糸する。
A certain thin layer of molten glass 1
After that, the molten glass 5 is passed through the spinning nozzle 13f from this thin molten glass layer 18, and the air in the air layer forming tank 14 is drawn in by the suction pressure caused by . A hollow glass fiber 19 is spun.

尚、空気層形成槽14中には積獣的に空気を供給して溶
融ガラス槽10の液圧しバランスさせるのが好ましい。
It is preferable to supply air into the air layer forming tank 14 in a cumulative manner to balance the liquid pressure in the molten glass tank 10.

但し、空気層を保持する部分は閉された空間でなくとも
、大気に開放された空間でも良い。閉された空気層を作
りだせけ溶融ガラスの液圧を直接ノズルかち流出する溶
融ガラスに伝えられるため紡糸は容易になる。しかし、
溶融ガラスの液圧で充分制御された薄い溶融ガラス層が
確保でき紡糸できれば、空気層は大気に開放されていて
もさしつかえない。
However, the part that holds the air layer does not have to be a closed space, but may be a space that is open to the atmosphere. By creating a closed air space, the liquid pressure of the molten glass can be directly transmitted to the molten glass flowing out through the nozzle, making spinning easier. but,
As long as a thin molten glass layer that is sufficiently controlled by the liquid pressure of the molten glass can be spun, the air layer may be open to the atmosphere.

以上の如く紡糸された中空ガラス繊維]、 9 ti、
肉厚が全周略均−で内外周面に芯ずれが殆んど無く、ま
た全長に亘って全周の肉厚が略均=で局部的に肉厚の薄
い個所は殆んど無く、寸法at IfFの高い品質良好
な・ものである。
Hollow glass fiber spun as described above], 9 ti,
The wall thickness is approximately uniform all around, with almost no misalignment on the inner and outer peripheral surfaces, and the wall thickness is approximately uniform throughout the entire length, with almost no locally thinner areas. It is of good quality with high dimensions at IfF.

そこで本発明の中空ガラス繊維の紡糸方法の効果を明ら
かに−する為に、その具体的な実h1u例と従来1fl
l [ついて説明する。
Therefore, in order to clarify the effects of the hollow glass fiber spinning method of the present invention, we will introduce a concrete example of the hollow glass fiber spinning method and a conventional 1 fl
l [I will explain about it.

〔実施+nl 1〕 第2図3.[)に示す構造の白、金製の紡糸装置16に
於いて溶融ガラス槽10の寸法が縦100m、横1Fl
omat  のbノミ面方形で高さ150 u、、溶融
ガラス流ドノズル11の直径4.0間、長さ7.0yJ
R,)レイ] 2 tDt4i を]、 OTIjI、
 紡糸ノズル13 (D 1(q径2. l) y。
[Implementation+nl 1] Figure 2 3. In the spinning device 16 made of white and gold having the structure shown in [), the dimensions of the molten glass tank 10 are 100 m in length and 1 Fl in width.
omat b chisel plane square, height 150 u, molten glass flow nozzle 11 diameter 4.0, length 7.0 yJ
R,) Ray]2 tDt4i], OTIjI,
Spinning nozzle 13 (D 1 (q diameter 2. l) y.

長さ0.511+J、空気層形成1v!I 14の高さ
7.01+1J 、空気供給管J5の内径4.0鮪とな
した紡糸装置16を用いて下記の紡糸条件にてBタイプ
ガラスより成る溶酸1(ガラス5を紡糸して中空ガラス
繊維19をイ!lだ。
Length 0.511+J, air layer formation 1v! Using a spinning device 16 with a height of 7.01 + 1 J for I 14 and an inner diameter of 4.0 J for air supply pipe J5, the molten acid 1 (glass 5) made of B type glass was spun into a hollow fiber under the following spinning conditions. I love glass fiber 19!

紡糸条件 溶M゛1[ガラス温度    1260℃紡糸ノズル温
度    1050℃ 溶融ガラス液深      40關 薄い溶融ガラス層     3肪 、紡 糸 速 度    500rrt/宵i得られた
中空ガラス繊維、。
Spinning conditions Melt M1 [Glass temperature 1260°C Spinning nozzle temperature 1050°C Molten glass liquid depth 40% thin molten glass layer 3, spinning speed 500rrt/night The hollow glass fiber obtained.

繊  維  径          工 4 μm 。Fiber diameter: 4 μm.

中・ 空 $         25チ肉    厚 
       最大5/1m最小3μin 〔実施例2〕 実施例1と同一の紡糸装置16を用いて下記の鞘糸、条
件にてE、夕、イブガラスより成るm融ガラス5″f、
紡糸して中空ガラス繊維19を得た。
Medium/Empty $25 thick
Maximum 5/1 m Minimum 3 μin [Example 2] Using the same spinning device 16 as in Example 1 and using the following sheath threads and conditions, m fused glass 5″f consisting of E, Yu, Eve glass,
A hollow glass fiber 19 was obtained by spinning.

紡糸多作 溶融ガラス温度    1260℃ 紡糸ノズ、ル温度     105 Q℃溶融ガラス液
深    40j+J 薄い溶融ガラス層    30     。
Spinning molten glass temperature 1260℃ Spinning nozzle temperature 105 Q℃ Molten glass liquid depth 40J+J Thin molten glass layer 30.

紡  糸  速 度      800…/i得られた
中空ガラス繊維 繊維径 12itm 中  空  率     30 チ 肉    厚    最大4μm、最小2 μm〔実施
例3〕 薄い溶融ガラス層18の液深を変える為に、溶融ガラス
流下ノズル11の長さのみ5.0鮎と変更し、その他t
ま実施例1と同じ寸法の紡糸装置16を用いて下記の紡
糸条件にてEタイプガラスよシ成る溶融ガラス5を紡糸
して中空ガラス繊維19不ヒイリだ1、 紡糸条件 溶融ガラス温度   1250℃ 紡糸ノズル温度   1050℃ 溶融ガラス液深    100龍 薄い溶融ガラス層    5閃 紡糸速度  8 o1’o m7M− 得られた中空ガラス繊維   1.、。
Spinning speed 800.../i Obtained hollow glass fiber diameter 12 itm Hollowness ratio 30 Thickness Maximum 4 μm, minimum 2 μm [Example 3] In order to change the liquid depth of the thin molten glass layer 18, the molten glass was Only the length of the downstream nozzle 11 was changed to 5.0 Ayu, and other
Using a spinning device 16 with the same dimensions as in Example 1, the molten glass 5 made of E type glass was spun under the following spinning conditions to obtain hollow glass fibers 19. Spinning conditions: Molten glass temperature: 1250°C Spinning Nozzle temperature: 1050°C Molten glass liquid depth: 100 mm Thin molten glass layer 5 Spinning speed: 8 o1'o m7M- Obtained hollow glass fiber 1. ,.

繊維径  13μm 中  空  率         20qb肉    
厚       最大4 It m 、最小3μm、ヶ
や71.′□ 第1図に示す構造の白金製の紡糸装置4に於いて、溶融
ガラス槽lの寸法が縦50關、横50關の断面方形で高
さ100m、紡糸ノズル2の直径4、 Owax 、長
さ5.0 間、開口径2.0pun、空気導入管3の直
径1.0uとなした紡糸装置4を用いて下記の紡糸条件
にてEタイプガラスより成る溶融ガラス5を紡糸して中
空ガラ堺繊維6を得た。
Fiber diameter 13μm Hollow rate 20qb flesh
Thickness: Maximum 4 It m, minimum 3 μm, thickness 71. '□ In the spinning device 4 made of platinum having the structure shown in Fig. 1, the molten glass tank l has a rectangular cross section of 50 mm in length and 50 mm in width, and a height of 100 m, and the diameter of the spinning nozzle 2 is 4. Using a spinning device 4 having a length of 5.0mm, an opening diameter of 2.0pun, and an air introduction tube 3 diameter of 1.0u, molten glass 5 made of E type glass is spun into a hollow fiber under the following spinning conditions. Gala Sakai fiber 6 was obtained.

紡糸条件 溶融ガラス温度   i、2c;o℃ 紡糸ノズル温度   1050℃ 紡  糸  速 度     500m/顛得られた中
空ガラス稗維 繊維径  20μア 中空率  13チ 肉    厚       最大9μ川、最小511m
上記の如〈実施例1.2・、3の中受ガラス繊組は、従
来例の中空ガラス−維に比べ繊維径が細く、中空率が高
く、肉厚のばら・つきが極めて少なく略均−な肉厚で、
寸法精度嬢高く、品質良好であることが判る。
Spinning conditions Molten glass temperature i, 2c; o℃ Spinning nozzle temperature 1050℃ Spinning speed 500m/resulting hollow glass fiber Fiber diameter 20μ Hollow ratio 13mm Thickness Maximum 9μ, minimum 511m
As described above, the intermediate receiving glass fiber assembly of Examples 1, 2, and 3 has a thinner fiber diameter and a higher hollowness ratio than the conventional hollow glass fiber, and has very little variation and unevenness in wall thickness and is approximately uniform. - thick wall,
It can be seen that the dimensional accuracy is high and the quality is good.

尚、前記実施例の紡糸装置16の溶融ガラス流下ノズル
11及びトレイ12は、溶融ガラス(曹10と同一平面
上にあるが、第3図に示゛f如く溶融ガラス槽10の底
部側方に案内部20を設け、この案内部20の底に溶融
ガラス流下ノズ・ル「1を設け、その下方にトレイ12
を設け、溶融ガラス流下ノズル11の周囲に空気層形成
槽14を・設けても良いものである。
The molten glass flow down nozzle 11 and the tray 12 of the spinning device 16 of the above embodiment are on the same plane as the molten glass (bottom 10), but are placed on the bottom side of the molten glass tank 10 as shown in FIG. A guide part 20 is provided, and a molten glass falling nozzle "1" is provided at the bottom of this guide part 20, and a tray 12 is provided below it.
It is also possible to provide an air layer forming tank 14 around the molten glass flowing down nozzle 11.

以上の説明で判るように本発明の中空ガラス繊維の紡糸
方法罠よれば、繊維径が細く、中空率が晶<、肉Jツが
全周、全長共に略均−な寸法精度の高い品質良好な中空
ガラス繊維全容易に得ることができるという優れた効果
がある。
As can be seen from the above explanation, according to the hollow glass fiber spinning method of the present invention, the fiber diameter is small, the hollowness ratio is small, the thickness is approximately uniform throughout the circumference and the entire length, and the quality is high with high dimensional accuracy. It has the excellent effect that hollow glass fibers can be easily obtained.

また本発明の中空ガラス繊維の紡糸装置は、構造がシン
プルで製作が容易且つ安価であり□、メインテナンスも
容易である。しかも紡糸ノズルの増設が容易で量産化に
適し、運転制御も至って容易である等の利点がある。
Furthermore, the hollow glass fiber spinning apparatus of the present invention has a simple structure, is easy to manufacture, is inexpensive, and is easy to maintain. Moreover, it has advantages such as easy addition of spinning nozzles, suitable for mass production, and extremely easy operation control.

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

第1図は従来の中空ガラス繊維の紡糸装置を示す縦断面
図、第2図aは本発明の中空ガラス繊維の紡糸装置の一
例を示す縦断面図、仝図すは3図のA−4線横断矢視図
、第3図は・本発明の中空ガラス繊維の紡糸装置の他の
例を示す縦断面図であ、 る。 5、・・・溶融ガラス、10・・・溶融ガラス槽、11
・−・溶融ガラス流下ノズル、12・・・トレイ、13
・・・紡糸ノズル、14・・・空気層形成槽、15・・
・空気供給管、16・・・紡糸装置、17・・・空気層
、18・・・薄い溶融ガラス層、19・・・、中空ガラ
ス繊維。 ・  出願人  83中貴金属工業株式会社清  水 
 紀  夫 第1図 第2図(b) 第3図
FIG. 1 is a longitudinal cross-sectional view showing a conventional hollow glass fiber spinning apparatus, FIG. 3 is a longitudinal cross-sectional view showing another example of the hollow glass fiber spinning apparatus of the present invention. 5,... Molten glass, 10... Molten glass tank, 11
... Molten glass flowing down nozzle, 12... Tray, 13
... Spinning nozzle, 14... Air layer forming tank, 15...
- Air supply pipe, 16... Spinning device, 17... Air layer, 18... Thin molten glass layer, 19... Hollow glass fiber.・Applicant: 83 Naka Kikinzoku Kogyo Co., Ltd. Shimizu
Norio Figure 1 Figure 2 (b) Figure 3

Claims (1)

【特許請求の範囲】 l)溶+A!1+ガラスを自身の液圧或いは外部よりの
圧力調整に」:す:、!I!続的に徐々Ic 1)Ij
下褪せて薄い溶融ガラス層を形成し、然る後この薄い溶
融ガラス層から溶融ガラスを引き出すと共に空気をまき
込んで中空ガラス繊、i4f、’を紡糸することを特徴
とする中空ガラス繊維の紡糸方法。 2)多量の溶融ガラスを保持する高融ガラス槽と、この
溶融ガラス槽の底K d数個設けられた溶融ガラス流、
Fノズルと、該溶融ガラス流下ノズルのF方に設けられ
た薄い溶融ガラス層を形成するトレイと、該トレイの底
に81数詞に設けらh−た紡糸ノズルとより成る中空ガ
ラス繊維の紡糸装置。
[Claims] l) Solu+A! 1+Glass to adjust own hydraulic pressure or pressure from outside”:S:,! I! Continuously gradually Ic 1) Ij
Spinning of hollow glass fibers characterized by fading to form a thin molten glass layer, and then drawing out the molten glass from this thin molten glass layer and injecting air to spin hollow glass fibers, i4f,'. Method. 2) A molten glass tank that holds a large amount of molten glass, and several molten glass flows provided at the bottom of this molten glass tank,
A hollow glass fiber spinning device comprising an F nozzle, a tray for forming a thin molten glass layer provided on the F side of the molten glass flowing down nozzle, and a spinning nozzle provided at the bottom of the tray in an 81-number position. .
JP16443282A 1982-09-21 1982-09-21 Spinning of hollow glass filament and its device Granted JPS5954638A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16443282A JPS5954638A (en) 1982-09-21 1982-09-21 Spinning of hollow glass filament and its device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16443282A JPS5954638A (en) 1982-09-21 1982-09-21 Spinning of hollow glass filament and its device

Publications (2)

Publication Number Publication Date
JPS5954638A true JPS5954638A (en) 1984-03-29
JPH0346412B2 JPH0346412B2 (en) 1991-07-16

Family

ID=15793042

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16443282A Granted JPS5954638A (en) 1982-09-21 1982-09-21 Spinning of hollow glass filament and its device

Country Status (1)

Country Link
JP (1) JPS5954638A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6183643A (en) * 1984-09-27 1986-04-28 Tanaka Kikinzoku Kogyo Kk Production of hollow glass fiber and device
CN112981563A (en) * 2021-02-03 2021-06-18 北京航空航天大学 Hollow basalt fiber manufacturing device and manufacturing method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56134532A (en) * 1980-03-24 1981-10-21 Agency Of Ind Science & Technol Preparation of hollow glass fiber

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56134532A (en) * 1980-03-24 1981-10-21 Agency Of Ind Science & Technol Preparation of hollow glass fiber

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6183643A (en) * 1984-09-27 1986-04-28 Tanaka Kikinzoku Kogyo Kk Production of hollow glass fiber and device
CN112981563A (en) * 2021-02-03 2021-06-18 北京航空航天大学 Hollow basalt fiber manufacturing device and manufacturing method

Also Published As

Publication number Publication date
JPH0346412B2 (en) 1991-07-16

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