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JPS605536B2 - Method and device for preventing devitrification of molten glass - Google Patents
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JPS605536B2 - Method and device for preventing devitrification of molten glass - Google Patents

Method and device for preventing devitrification of molten glass

Info

Publication number
JPS605536B2
JPS605536B2 JP4109882A JP4109882A JPS605536B2 JP S605536 B2 JPS605536 B2 JP S605536B2 JP 4109882 A JP4109882 A JP 4109882A JP 4109882 A JP4109882 A JP 4109882A JP S605536 B2 JPS605536 B2 JP S605536B2
Authority
JP
Japan
Prior art keywords
channel
molten glass
stirrer
glass
flow path
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP4109882A
Other languages
Japanese (ja)
Other versions
JPS58161940A (en
Inventor
勝三郎 山本
政博 森
達夫 屋敷
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.)
Nitto Boseki Co Ltd
Original Assignee
Nitto Boseki Co 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 Nitto Boseki Co Ltd filed Critical Nitto Boseki Co Ltd
Priority to JP4109882A priority Critical patent/JPS605536B2/en
Publication of JPS58161940A publication Critical patent/JPS58161940A/en
Publication of JPS605536B2 publication Critical patent/JPS605536B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B7/00Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
    • C03B7/02Forehearths, i.e. feeder channels
    • C03B7/06Means for thermal conditioning or controlling the temperature of the glass
    • C03B7/07Electric means
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/18Stirring devices; Homogenisation
    • C03B5/187Stirring devices; Homogenisation with moving elements

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Manufacture, Treatment Of Glass Fibers (AREA)

Description

【発明の詳細な説明】 本発明はガラス繊維の荻糸に関し、特にガラス織総紡糸
装置における溶融ガラスの失透防止方法及び装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a glass fiber thread, and more particularly to a method and device for preventing devitrification of molten glass in a glass weaving total spinning device.

従来、溶融ガラスを受けるほぼ水平なチャンネルと、こ
のチャンネルの底壁に形成され、チャンネル内の溶融ガ
ラスが流下する流路と、この流路に整合して取り付けら
れ、流路を流下してきた溶融ガラスを織糸するプッシン
グとを有するガラス繊維紙糸装置は知られている。
Conventionally, a nearly horizontal channel that receives molten glass, a flow path formed on the bottom wall of this channel through which the molten glass flows down, and a flow path that is installed in alignment with this flow path to collect the molten glass that has flowed down the flow path. Glass fiber paper yarn devices having a pusher for weaving glass are known.

このようなガラス繊維紙糸装置において、最近、耐アル
カリ性ガラス繊維のガラス材料など失透しやすく溶融性
や級タ糸性に問題が起こりがちなガラス材料からもガラ
ス繊維を織糸する必要が生じて釆ている。例えば耐アル
カリ性ガラス繊維用のガラス材料は一般にZr02を多
量に含有しているが、このように多量のZの2を含有す
るガラス材料や他の特殊な組成のガラス材料は、ほとん
どの場合液相温度が通常のガラスより高くなり、紙糸温
度(1びポィズにおける粘度)と液相温度との差が小さ
くなり、例えばその差は3000以下になる。従って級
糸の際に結晶化し易くなり、失透発生の問題が極めて生
じ易くなる。熔融ガラスにおけるこの失透の発生はガラ
ス繊維紙糸時の切断要因となる。本発明の目的は、Zr
02成分を多量に含むか又は特殊なガラス組成のような
失透しやすし、ガラス材料からガラス繊維を紡糸する際
、溶融ガラスの失透を防止し、ガラス繊維の切断要因を
減少させることのできる溶融ガラスの失透防止方法及び
装置を提供することである。
Recently, in such glass fiber paper yarn machines, it has become necessary to weave glass fibers from glass materials that are prone to devitrification and tend to have problems with meltability and grading properties, such as alkali-resistant glass fibers. It is in operation. For example, glass materials for alkali-resistant glass fibers generally contain a large amount of ZrO2, but glass materials containing such a large amount of ZrO2 and glass materials with other special compositions are almost always in the liquid phase. The temperature is higher than that of ordinary glass, and the difference between the paper yarn temperature (viscosity at 1 poise) and the liquidus temperature is small, for example, the difference is 3000 or less. Therefore, it is easy to crystallize during cutting, and the problem of devitrification is extremely likely to occur. The occurrence of devitrification in the molten glass becomes a cause of breakage of the glass fiber paper yarn. The object of the present invention is to
When spinning glass fibers from glass materials that contain a large amount of 02 components or have a special glass composition that easily devitrifies, it can prevent devitrification of the molten glass and reduce the factors that cause glass fibers to break. An object of the present invention is to provide a method and device for preventing devitrification of molten glass.

従来、Zの2成分を多量に含むか又は特殊なガラス組成
のような失透しやすいガラス材料を織糸する際に発生す
る失透の問題は、ブツシング内やブッシングの底面に形
成されているチップ/ズル内における溶融ガラスの問題
として検討されてきた。
Conventionally, the problem of devitrification that occurs when weaving glass materials that are prone to devitrification, such as those containing a large amount of two components of Z or having a special glass composition, is that devitrification is formed within the bushing or on the bottom surface of the bushing. The problem of molten glass in the chip/zure has been discussed.

しかしながら種々検討した結果、溶融ガラスがファーハ
ースのチャンネルからブツシングに入る過程でより大き
な障害となる問題があることが判明した。この点を耐ア
ルカリ性ガラス繊維のガラス材料の場合を例にして説明
すると、Z「02を多量に含むガラス材料は溶融及び清
澄の過程でZの2成分が炉底部に沈む傾向があり、特に
ファーハースの長いチャンネル内をガラスがゆっくり流
れる場合には、チャンネルの底部にZの2を多量に含ん
だガラスが層状となって沈積する。
However, as a result of various studies, it has been found that there is a problem in which the molten glass becomes a bigger obstacle in the process of entering the bushing from the channel of the furnace. To explain this point using the case of alkali-resistant glass fiber glass materials as an example, glass materials containing a large amount of Z"02 tend to have two components of Z sinking to the bottom of the furnace during the melting and fining process. When glass flows slowly through a long channel of a hearth, a layer of glass containing a large amount of Z2 is deposited at the bottom of the channel.

このZ幻2のリッチなガラス層は正常なガラスよりも液
相温度が高い。他方チャンネル内の溶融ガラスが流路を
経てブッシング内に流下する過程において、流路を画成
する側壁に近接して流れる溶融ガラスの温度は流下する
に従って次第に低下する。従ってZr02のリッチなガ
ラス層が流路を函成する側壁に近接して流れる際に失透
が生じ結晶が晶出する。晶出した結晶のブッシングに流
れ込み、紙糸における繊維化に際して切断の原因となる
。本発明は上述の発見に基づいてなされたもので、本発
明によれば溶融ガラスを受けるほぼ水平なチャンネルと
、前記チャンネルの底壁に形成され、該チャンネル内の
溶融ガラスが流下する流路と、前記流路に整合して取り
付けるれ該流路を流下してきた溶融ガラスを紡糸するブ
ッシングとを有するガラス繊維紙糸装置における溶融ガ
ラスの失透防止方法において、前記流路を画成する側壁
のうち前記チャンネルの幅方向の側壁に隣接した位置で
、前記流路を流下する溶融ガラスを額拝することを特徴
とする方法が得られる。又本発明によれば、溶融ガラス
を受けるほぼ水平なチャンネルと、前記チャンネルの底
壁に形成0され、該チャンネル内の溶融ガラスが流下す
る流路と、前記流路に整合して取り付けられ、該流路を
流下してきた溶融ガラスを紡糸するプツシングとを有す
るガラス繊維線糸装置における溶融ガラスの失透防止装
置において、回転軸に羽根を取り夕付けたスターラと、
前記スターラを回転駆動するための駆動装置とからなる
櫨梓装置を前記スターラの羽根が前記流路を画成する側
壁のうち前記チャンネルの幅方向の側壁に隣接して位置
するよう設置したことを特徴とする装置が得られる。
This rich glass layer of Z-Illusion 2 has a higher liquidus temperature than normal glass. On the other hand, as the molten glass in the channel flows down into the bushing through the flow path, the temperature of the molten glass flowing close to the side walls defining the flow path gradually decreases as it flows down. Therefore, when the Zr02-rich glass layer flows close to the side wall defining the channel, devitrification occurs and crystals crystallize. The crystallized crystals flow into the bushing and cause the fibers to break in the paper yarn. The present invention has been made based on the above-mentioned discovery, and according to the present invention, a substantially horizontal channel for receiving molten glass, and a flow path formed in the bottom wall of the channel, through which the molten glass in the channel flows downward. , a method for preventing devitrification of molten glass in a glass fiber paper yarn device having a bushing that is attached in alignment with the flow path and spins molten glass flowing down the flow path; There is obtained a method characterized in that the molten glass flowing down the flow path is placed in a position adjacent to the side wall in the width direction of the channel. Further, according to the present invention, a substantially horizontal channel for receiving molten glass, a flow path formed in the bottom wall of the channel and through which the molten glass flows down, and a channel installed in alignment with the flow path, A device for preventing devitrification of molten glass in a glass fiber yarn device having a pushing device for spinning molten glass flowing down the flow path, a stirrer having blades attached to a rotating shaft;
and a drive device for rotationally driving the stirrer is installed such that the blades of the stirrer are located adjacent to a side wall in the width direction of the channel among the side walls defining the flow path. A device with characteristics is obtained.

o 燈杵装置の回転速度は5〜3仇pmとすることが好
ましい。以下本発明の実施例を図面を参照して説明する
。第1図はガラス繊維織糸装置の全体を示し、この実施
例では電気的に溶融及び清澄される霞気溶タ融炉の例を
示している。
o The rotation speed of the pestle device is preferably 5-3pm. Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows the entire glass fiber weaving apparatus, and this embodiment shows an example of a haze melting furnace which is electrically melted and refined.

図において符号1は溶解室を示し、溶解室1内にはチャ
ージャ2によってガラスバッチ3が投入され、モリブデ
ン電極4により加熱溶融されスロート5を通りラィザー
6を経て、ファーハース7のチャンネル8に至る。な0
お溶解室1の加熱はバーナの火炎による加熱、或るし、
はこの火炎と電気的加熱との併用も可能である。ファー
ハース7は全体が耐火レソガのような耐熱材料で形成さ
れ、このファーハース7は溶融ガタラス9を受ける前述
したほぼ水平なチャンネル8に加え、チャンネル8の底
壁101こ形成され、チャンネル8内の溶融ガラス9が
流下する流路11と、流路11に整合して取り付けられ
、流路11を流下してきた溶融ガラスを級糸するプッシ
ング0 12とを有する。
In the figure, reference numeral 1 indicates a melting chamber, into which a glass batch 3 is charged by a charger 2, heated and melted by a molybdenum electrode 4, passes through a throat 5, passes through a riser 6, and reaches a channel 8 of a furhearth 7. . na 0
The melting chamber 1 is heated by the flame of a burner, or
It is also possible to use this flame in combination with electrical heating. The entire fur hearth 7 is made of a heat-resistant material such as refractory resin, and in addition to the above-mentioned substantially horizontal channel 8 that receives the molten glass 9, a bottom wall 101 of the channel 8 is formed, and a bottom wall 101 of the channel 8 is formed. It has a channel 11 through which the molten glass 9 flows down, and a pusher 012 which is attached in alignment with the channel 11 and which threads the molten glass flowing down the channel 11.

ファーハース7の底壁10は、ブッシング12の近傍に
おいて一般に上層のフローブロック13と下層のブツシ
ングブロック14の二重構造となっている。但しフロー
ブロック13を厚く機成し、一層構造とすることもでき
る。ブッシング12は電気抵抗加熱されており、供給さ
れる溶融ガラスを再加熱し、温度制御をしている。溶解
炉1からの溶融ガラス9は炭化ケイ素のような加熱体2
6で熱的に保持及び調整されながら、チャンネル8内を
所定の液深でゆっくりと流れ、フローブロック13、ブ
ツシングブロツク14の側壁によって画成される流路1
1を経て、ブッシング12で紙糸され繊維化される。フ
ァーハース7には又、流路11に関連して本発明の特徴
を成す鷹洋装暦15が設けられている。
In the vicinity of the bushing 12, the bottom wall 10 of the furhearth 7 generally has a double structure of an upper layer flow block 13 and a lower layer bushing block 14. However, the flow block 13 can also be made thicker and have a single layer structure. The bushing 12 is electrically resistance heated to reheat the supplied molten glass and control the temperature. The molten glass 9 from the melting furnace 1 is heated by a heating element 2 such as silicon carbide.
The fluid slowly flows at a predetermined depth in the channel 8 while being thermally maintained and regulated by the flow path 1 defined by the side walls of the flow block 13 and the bushing block 14.
1, the paper is turned into paper threads at a bushing 12 and made into fibers. The furhearth 7 is also provided with a hawk ephemeris 15 which is a feature of the present invention in connection with the flow path 11.

この実施例では各流路11に2つの蝿梓装置がある。第
2図に詳細に示されているごとく蝿梓装置15は、回転
軸16に羽根17を取り付けたスターラ18と、スター
ラ18を回転駆動するための駆動装置即ちモータ19と
から成っている。蝿梓装置15は、スターラ18の羽根
17が流路11を画成する側壁のうちチャンネル8の幅
方向の側壁201こ隣接して位置するよう設置されてい
る。スターラ18の回転軸16は、白金製のパイプの下
端を閉じたものとし、羽根17はその白金製のパイプに
溶接された複数枚の羽根とすることができる。スターラ
18の回転軸16は、ファーハースの頂壁即ち天井レン
ガ21の開□22を通ってチャンネル8の外側に延在し
ており、その位置で駆動装置19は回転軸16に接続さ
れている。駆動装置19は台枠23上に袋架されており
、台枠23は例えば鉄製のアングル材を箱状に組み、フ
ァーハース7の頂壁21をまたぐように、その下端部を
ファーハース7の側壁外面に固定された支持金具24に
取り付けることができる。
In this embodiment, there are two flywheel devices in each channel 11. As shown in detail in FIG. 2, the fly stirrer 15 consists of a stirrer 18 having blades 17 attached to a rotating shaft 16, and a drive device, ie, a motor 19, for driving the stirrer 18 in rotation. The fly stirrer device 15 is installed such that the blades 17 of the stirrer 18 are located adjacent to the side wall 201 in the width direction of the channel 8 among the side walls defining the flow path 11 . The rotating shaft 16 of the stirrer 18 is a platinum pipe with the lower end closed, and the blades 17 can be a plurality of blades welded to the platinum pipe. The axis of rotation 16 of the stirrer 18 extends outside the channel 8 through an opening 22 in the top wall or ceiling brick 21 of the furnace, at which point a drive 19 is connected to the axis of rotation 16. . The drive device 19 is mounted on an underframe 23, and the underframe 23 is made of, for example, iron angle members assembled into a box shape, and its lower end is attached to the top wall 21 of the fur hearth 7 so as to straddle the top wall 21 of the fur hearth 7. It can be attached to a support fitting 24 fixed to the outer surface of the side wall.

又スターラ18は頂壁21の開口22より駆動装置19
ごと取り出して交換する必要があるので、関口22の直
径は羽根17が抜けることができるほど十分に大きく、
例えば直径8仇肋もあるので、関口22よりの熱放散を
極力少なくするため開□22の上側を断熱材26で覆う
ことが好ましい。断熱材25は例えば保温レンガ或るし
、はアルミナフアィバーやセラミックファイバーのボー
ドで構成することができる。断熱材25は第3図に示さ
れるごとく二つ割りの構成とすることが好ましく、この
実施例では断熱材25の厚さは5仇舷である。スターラ
18の羽根17の形状は第4図及び第5図に示すごとく
、回転によって溶融ガラスを下方に押し下げるような効
果が得られるように羽根の先端が下向きにねじれた形状
にすることが好ましい。
,鷹梓装置15の作用について説明すると、溶融ガラ
ス9は加熱体26で熱的に保持及び調整されながらチャ
ンネル8内を流れるが、その過程でZrQ成分がチャン
ネル8の底部に沈む傾向を示し、実施例によれば底部の
耐火物との境界に約0.7柳にわたり1割程度Zの2濃
度が高いガラス層Aが生じていた。
Further, the stirrer 18 is connected to the driving device 19 through the opening 22 of the top wall 21.
Since it is necessary to take out the entire blade and replace it, the diameter of the Sekiguchi 22 is large enough to allow the blade 17 to come out.
For example, since there are eight ribs in diameter, it is preferable to cover the upper side of the opening 22 with a heat insulating material 26 in order to minimize heat dissipation from the entrance 22. The heat insulating material 25 can be made of, for example, heat-retaining bricks, alumina fibers, or ceramic fiber boards. It is preferable that the heat insulating material 25 is divided into two parts as shown in FIG. 3, and in this embodiment, the thickness of the heat insulating material 25 is 5 mm. The shape of the blades 17 of the stirrer 18 is preferably such that the tips of the blades are twisted downward, as shown in FIGS. 4 and 5, so that the effect of pushing the molten glass downward by rotation can be obtained.
To explain the operation of the Takaazusa apparatus 15, the molten glass 9 flows through the channel 8 while being thermally held and adjusted by the heating element 26, but in the process, the ZrQ component tends to sink to the bottom of the channel 8. According to the example, a glass layer A having a high concentration of Z2 of about 10% was formed over about 0.7 willow at the boundary with the bottom refractory.

このことは例えばZr02を15%含有するZの2−S
i02−R′○−Na20系の耐アルカリ性ガラス材料
の場合、ガラス層AのZの2の含有量は1割増の16.
5%となり、液相温度は正常なガラス組成の1200q
oから1260q0に上昇することを意味する。又チャ
ンネル8の底壁10において、フローブロック13の上
面はそれに接して流れる高温の溶融ガラスによって比較
的高温にあるが、フローブロック13からブツシングブ
ロツク14の底面に向かってそれらの断面方向に温度降
下がある。従って流路11を画成するチャンネル8の幅
方向の側壁20に近接して流れる溶融ガラスの温度は、
溶融ガラスが流下するに従って次第に低下する。従って
上述したように液相温度が上昇し結晶化しやすくなった
ガラス層Aの溶融ガラスが側壁201こ沿って流下する
と、その過程で結晶化を起こし失透する危険性がある。
この危険性は上述したように側壁2川こ隣接した位置に
スターラ18の羽根17を有する燈梓装置15を設け、
溶融ガラスを縄拝することによってほぼ完全に解消させ
ることができる。この効果を実施例で見てみると、櫨梓
装置を取り付ける以前の繊維化歩蟹りは65%であり、
繊維化の際の切断原因の約90%がZの2系結晶のスト
ーンであった。
This means that, for example, 2-S of Z containing 15% Zr02
In the case of i02-R'○-Na20-based alkali-resistant glass material, the content of 2 in Z in glass layer A is 16.
5%, and the liquidus temperature is 1200q of normal glass composition.
It means rising from o to 1260q0. In addition, in the bottom wall 10 of the channel 8, the top surface of the flow block 13 is at a relatively high temperature due to the high temperature molten glass flowing in contact with it, but the temperature increases in the cross-sectional direction from the flow block 13 to the bottom surface of the bushing block 14. There is a descent. Therefore, the temperature of the molten glass flowing close to the side wall 20 in the width direction of the channel 8 defining the flow path 11 is
It gradually decreases as the molten glass flows down. Therefore, when the molten glass of the glass layer A, whose liquidus temperature has increased and is more likely to crystallize as described above, flows down along the side wall 201, there is a risk of crystallization and devitrification in the process.
This danger can be avoided by installing the lamp device 15 having the blades 17 of the stirrer 18 at two adjacent sides of the side wall, as described above.
The problem can be almost completely eliminated by using molten glass as a rope. Looking at this effect in an example, the fiberization rate before installing the Azusa device was 65%,
Approximately 90% of the causes of cutting during fiberization were Z-2 crystal stones.

一方本発明の方法によって蝿洋装贋を取りつけ、スター
ラを2比pmで澄拝させると、繊維化歩留りは91%と
著しく改善され、Zr02系の結晶ストーンの発生は皆
無となった。なお、側壁20に隣接して取り付ける羽根
17の高さは高すぎても低すぎても好ましくない。スタ
ーラ18の羽根17があまり低い位置にあり、例えばプ
ッシングブロック14の底面よりも下がるような位置に
あると、ブッシングのチップのノズルに到る溶融ガラス
の層流を乱し好ましくない。又フローブロック13の比
較的高い位置は高温にあるので、結晶化の危険性が少な
い。又スターラ18の羽根17の側壁2川こ対する距離
Bは、それがあまり小さすぎるとブツシングフロツク1
4又はフローブロック13のレンガが浸食されてブッと
なり、織糸時の切断原因となり、又スターラ18の回転
軸16のわん曲に対する余裕も必要であるため、一般に
その距離Bは15側から25側とするのが好ましい。
On the other hand, by the method of the present invention, when a fly cloth was attached and the stirrer was stirred at a ratio of 2 pm, the fiberization yield was significantly improved to 91%, and there was no generation of Zr02-based crystal stones. Note that it is not preferable that the height of the blade 17 attached adjacent to the side wall 20 is too high or too low. If the blades 17 of the stirrer 18 are located too low, for example below the bottom surface of the pushing block 14, this is undesirable as it disturbs the laminar flow of the molten glass that reaches the nozzle of the bushing tip. Furthermore, since the relatively high position of the flow block 13 is at a high temperature, there is little risk of crystallization. Also, if the distance B between the two side walls of the blades 17 of the stirrer 18 is too small, the butching flock 1
4 or the bricks of the flow block 13 are eroded and become lumpy, which can cause breakage during weaving.Also, allowance for the bending of the rotating shaft 16 of the stirrer 18 is required, so generally the distance B is from the 15 side to the 25 side. It is preferable that

ブツシングブロック14及びフローフロツク13は白金
でカバーすることができその場合は距離Bは幾分狭くす
ることができる。又損洋装層15において、スターラ1
8の回転速度は5〜3仇pmが好ましく、&pmより遅
いと効果がなく、一方3比pmより高速になると耐火物
の浸食が激しい上、巻き込み泡を生じたりして繊維化効
率の障害となることが判明した。
Bushing block 14 and flow block 13 can be covered with platinum, in which case distance B can be made somewhat narrower. In addition, in the clothing layer 15, the starrer 1
The rotation speed of No. 8 is preferably 5 to 3 pm; if it is slower than &pm, there is no effect; on the other hand, if it is faster than 3 pm, the refractory will be severely eroded and bubbles will be formed, which will impede the fiberization efficiency. It turned out to be.

以上明らかなように本発明によれば、ガラス繊維級糸装
置においてチャンネルからプッシングに到る流路を画成
する側壁のうちチャンネルの幅方向の側壁に隣接してス
ターラの羽根を位置せしめ、その側壁に近接して流下す
る結晶化の起こりやすい熔融ガラスを鷹拝するようにし
たので、溶融ガラスの結晶化則ち失透を防止することが
でき、従釆の無アルカリガラス(Eガラス)の紙糸に使
用されているガラス繊維薮糸装置を実質的に変更するこ
とないこ、失透しやすし、ガラスの紡糸を容易に行なう
ことができる。
As is clear from the above, according to the present invention, the blades of the stirrer are positioned adjacent to the side wall in the width direction of the channel among the side walls defining the flow path from the channel to the pushing in a glass fiber grade yarn device. Since the molten glass, which is prone to crystallization, flows down close to the side wall, it can be prevented from crystallizing or devitrifying the molten glass. Without substantially changing the glass fiber yarn device used for paper yarn, devitrification is more likely to occur and glass can be easily spun.

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

第1図は本発明の溶融ガラスの失透防止方法及び装置が
適応されるガラス繊維紙糸装置の全体概略断面図を示し
、第2図は第1図のガラス繊維紙糸装置の流路及びプツ
シング部分の拡大断面図であって、本発明の失透防止装
置を構成する蝿梓装置の詳細を示す図であり、第3図は
第2図に示された断熱材の横断面図を示し、第4図は、
第2図に示した鷹洋装層のスターラの羽根の詳細を示す
スターラの側面図であり、第5図は第4図に示したスタ
ーラの底面図である。 図中、符号8・・・・・・チャンネル、9・・・・・・
溶融ガラス、10・・・・・・チャンネルの底壁、11
・・・・・・流路、12・・・・・・ブツシング、1,
5・・・・・・燈梓装置、16・・・…回転軸、17…
・・・羽根、18・・・・・・スターラ、19・・・・
・・駆動装置、20・・・・・・側壁、21・・・・・
・頂壁。 第1図第2図 第3図 第4図 第5図
FIG. 1 shows an overall schematic sectional view of a glass fiber paper thread device to which the method and device for preventing devitrification of molten glass of the present invention are applied, and FIG. 2 shows the flow path and the glass fiber paper thread device of FIG. FIG. 3 is an enlarged cross-sectional view of the pushing portion, showing details of the devitrification prevention device of the present invention; FIG. 3 is a cross-sectional view of the heat insulating material shown in FIG. 2; , Figure 4 is
FIG. 5 is a side view of the stirrer showing details of the blades of the stirrer of the hawk layer shown in FIG. 2, and FIG. 5 is a bottom view of the stirrer shown in FIG. 4. In the figure, code 8...channel, 9...
Molten glass, 10...Bottom wall of channel, 11
...Flow path, 12...Butssing, 1,
5...Tonazusa device, 16... Rotating shaft, 17...
...Feather, 18...Starla, 19...
...Drive device, 20...Side wall, 21...
・Top wall. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5

Claims (1)

【特許請求の範囲】 1 溶融ガラスを受けるほぼ水平なチヤンネルと、前記
チヤンネルの底壁に形成され、該チヤンネル内の溶融ガ
ラスが流下する流路と、前記流路に整合して取り付けら
れ、該流路を流下してきた溶融ガラスを紡糸するブツシ
ングとを有するガラス繊維紡糸装置における溶融ガラス
の失透防止方法において、前記流路を画成する側壁のう
ち前記チヤンネルの幅方向の側壁に隣接した位置で、前
記流路を流下する溶融ガラスを撹拌することを特徴とす
る方法。 2 特許請求の範囲第1項記載の溶融ガラスの失透防止
方法において、前記溶融ガラスの撹拌を回転撹拌装置に
よって行なう方法。 3 特許請求の範囲第2項記載の溶融ガラスの失透防止
方法において、前記回転撹拌装置を5〜30rpmの回
転速度で回転して前記溶融ガラスを撹拌する方法。 4 溶融ガラスを受けるほぼ水平なチヤンネルと、前記
チヤンネルの底壁に形成され、該チヤンネル内の溶融ガ
ラスが流下する流路と、前記流路に整合して取り付けら
れ、該流路を流下してきた溶融ガラスを紡糸するブツシ
ングとを有するガラス繊維紡糸装置における溶融ガラス
の失透防止装置において、回転軸に羽根を取り付けたス
ターラと、前記スターラを回転駆動するための駆動装置
とからなる撹拌装置を、前記スターラの羽根が、前記流
路を画成する側壁のうち前記チヤンネルの幅方向の側壁
に隣接して位置するよう設置したことを特徴とする装置
。 5 特許請求の範囲第4項記載の溶融ガラスの失透防止
方法において、前記スターラの回転軸は前記チヤンネル
の頂壁を貫通して延在し、前記駆動装置は前記チヤンネ
ルの外側で前記回転軸に接続されている装置。 6 特許請求の範囲第4項又は第5項記載の溶融ガラス
の失透防止装置において、前記スターラの羽根は溶融ガ
ラスを下方に押し下げるような形状にされている装置。
[Scope of Claims] 1. A substantially horizontal channel for receiving molten glass, a flow path formed on the bottom wall of the channel and through which the molten glass in the channel flows, and a channel installed in alignment with the flow path, In a method for preventing devitrification of molten glass in a glass fiber spinning apparatus having a bushing for spinning molten glass flowing down a channel, a position adjacent to a side wall in the width direction of the channel among the side walls defining the channel. A method characterized in that the molten glass flowing down the flow path is stirred. 2. A method for preventing devitrification of molten glass according to claim 1, wherein the molten glass is stirred by a rotary stirring device. 3. The method for preventing devitrification of molten glass according to claim 2, in which the molten glass is stirred by rotating the rotary stirring device at a rotation speed of 5 to 30 rpm. 4. A substantially horizontal channel for receiving molten glass, a channel formed on the bottom wall of the channel and through which the molten glass in the channel flows, and a channel installed in alignment with the channel and flowing down the channel. In a device for preventing devitrification of molten glass in a glass fiber spinning device having a bushing for spinning molten glass, a stirring device comprising a stirrer with blades attached to a rotating shaft and a drive device for rotationally driving the stirrer, An apparatus characterized in that the blades of the stirrer are installed so as to be located adjacent to a side wall in the width direction of the channel among the side walls defining the flow path. 5. In the method for preventing devitrification of molten glass according to claim 4, the rotating shaft of the stirrer extends through the top wall of the channel, and the driving device connects the rotating shaft to the outside of the channel. devices connected to. 6. The device for preventing devitrification of molten glass according to claim 4 or 5, wherein the blades of the stirrer are shaped to push down the molten glass.
JP4109882A 1982-03-16 1982-03-16 Method and device for preventing devitrification of molten glass Expired JPS605536B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4109882A JPS605536B2 (en) 1982-03-16 1982-03-16 Method and device for preventing devitrification of molten glass

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4109882A JPS605536B2 (en) 1982-03-16 1982-03-16 Method and device for preventing devitrification of molten glass

Publications (2)

Publication Number Publication Date
JPS58161940A JPS58161940A (en) 1983-09-26
JPS605536B2 true JPS605536B2 (en) 1985-02-12

Family

ID=12598999

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4109882A Expired JPS605536B2 (en) 1982-03-16 1982-03-16 Method and device for preventing devitrification of molten glass

Country Status (1)

Country Link
JP (1) JPS605536B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63184842A (en) * 1987-01-27 1988-07-30 Fujitsu Ltd High speed operating system for computer system

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8113018B2 (en) * 2006-12-14 2012-02-14 Ocv Intellectual Capital, Llc Apparatuses for controlling the temperature of glass forming materials in forehearths
CN104326652B (en) * 2014-07-22 2016-08-17 宝钢矿棉科技(宁波)有限公司 A kind of skull melting furnace processing blast furnace hot molten slag

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63184842A (en) * 1987-01-27 1988-07-30 Fujitsu Ltd High speed operating system for computer system

Also Published As

Publication number Publication date
JPS58161940A (en) 1983-09-26

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