JPH06340429A - Fused glass outflow device - Google Patents
Fused glass outflow deviceInfo
- Publication number
- JPH06340429A JPH06340429A JP5129318A JP12931893A JPH06340429A JP H06340429 A JPH06340429 A JP H06340429A JP 5129318 A JP5129318 A JP 5129318A JP 12931893 A JP12931893 A JP 12931893A JP H06340429 A JPH06340429 A JP H06340429A
- Authority
- JP
- Japan
- Prior art keywords
- nozzle
- heat insulating
- pipe
- glass
- insulating cylinder
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/26—Outlets, e.g. drains, siphons; Overflows, e.g. for supplying the float tank, tweels
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、光学素子等の硝子製品
製造工程において、溶融炉で溶融された硝子を、溶融炉
から炉外の型等に流出させるためのパイプ状の、ノズル
を備えた溶融硝子流出装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is provided with a pipe-shaped nozzle for flowing glass melted in a melting furnace from a melting furnace to a mold outside the furnace in a glass product manufacturing process such as optical elements. And a molten glass outflow device.
【0002】[0002]
【従来の技術】従来は、硝子が流出するノズル先端が外
部の大気と触れて冷却されてしまうため、ノズル先端を
バーナー等で加熱し、流出をスムースに行えるようにし
ていた。その一例として、特開昭62−270427に
は、ノズル先端をノズル加熱用ヒーターで覆い硝子の流
出を行う技術が開示されている。また特公平4−271
74には、流出用白金パイプの下側部分の電気抵抗値を
上側部分の電気抵抗値より大きくし、そのパイプに電圧
を印加することにより、パイプ先端部の温度降下を防ぐ
技術が開示されている。2. Description of the Related Art Conventionally, since the tip of a nozzle through which glass flows out is cooled by contact with the outside atmosphere, the nozzle tip has been heated by a burner or the like so that the nozzle can be smoothly discharged. As one example thereof, Japanese Patent Laid-Open No. 62-270427 discloses a technique of covering the tip of the nozzle with a heater for heating the nozzle so that the glass flows out. In addition,
No. 74 discloses a technique of increasing the electric resistance value of the lower part of the outflow platinum pipe to be larger than that of the upper part and applying a voltage to the pipe to prevent the temperature drop at the tip of the pipe. There is.
【0003】しかしながら、前記従来例のようにバーナ
ーや、ヒーターでノズル先端を加熱する方法は、間接加
熱となるため、ノズル先端に対する温度の応答性や精度
に問題が生じやすい。またノズル先端近傍にバーナーや
ヒーター等が配置されるため、ノズルの下方で行うプレ
ス等のための作業スペースの確保が困難になったり、装
置自体が複雑になるという問題があった。また、前記従
来例に開示されている流出用白金パイプの下側部分の電
気抵抗値を上側部分の電気抵抗値より大きくし、そのパ
イプに電圧を印加することによりパイプ先端の温度降下
を防ぐ方法の場合には、パイプ先端の硝子流出口の温度
に関しては、外気との接触面積の増大や、この部分に通
電用の電極が配置されるため、パイプの下側部分の温度
が、パイプ全体に比較して低くなってしまう。このた
め、パイプ先端部の硝子流出口で硝子が失透(結晶化)
を起こし、流出した硝子の品質を悪化させる。また、逆
に失透を防ぐために硝子流出口の温度を上げると、パイ
プ上部の温度が上がりすぎ、硝子中に泡を再発生させて
しまうという問題や、流出硝子の外周部と内部との温度
差が大きくなり温度分布の少ない硝子流を得にくいとい
う問題があった。通常のプレス成形のように、必要な重
量の硝子塊を得るために切断刃を用いて硝子流を切断す
る場合には、このような流出硝子の外周部と内部の温度
差は余り問題にならない。しかし、硝子を流出口より滴
下させたり、硝子流の下降速度に変化を与えて、硝子の
表面張力で硝子流を切断する場合には、流出硝子の外周
部と内部の温度差がなければ硝子の表面張力により硝子
流は切断面に何の欠陥を残すことなく切断できるが、こ
の温度差が大きいと切断の際に切断部の硝子が糸状に伸
ばされ、それが切断断面に付着したり、切断部に再度巻
き込まれたりして硝子に欠陥を残してしまうという問題
が生じる。However, since the method of heating the nozzle tip with a burner or a heater as in the above-mentioned conventional example uses indirect heating, problems in temperature response and accuracy with respect to the nozzle tip are likely to occur. Further, since a burner, a heater, etc. are arranged near the tip of the nozzle, there are problems that it is difficult to secure a working space for a press or the like performed below the nozzle, and the apparatus itself becomes complicated. Also, a method of preventing the temperature drop at the tip of the pipe by increasing the electric resistance value of the lower part of the outflow platinum pipe disclosed in the conventional example to be larger than that of the upper part and applying a voltage to the pipe. In this case, regarding the temperature of the glass outlet at the tip of the pipe, the contact area with the outside air increases and the electrode for energization is placed in this part, so the temperature of the lower part of the pipe is It will be lower than the comparison. Therefore, the glass is devitrified (crystallized) at the glass outlet at the tip of the pipe.
And deteriorate the quality of the glass that has flowed out. Conversely, if the temperature at the glass outlet is raised to prevent devitrification, the temperature at the top of the pipe will rise too high and bubbles will be regenerated in the glass. There is a problem that the difference becomes large and it is difficult to obtain a glass flow with a small temperature distribution. When cutting the glass flow with a cutting blade to obtain a necessary mass of glass like ordinary press molding, such a temperature difference between the outer peripheral portion and the inner portion of the outflowing glass does not become a problem. . However, when the glass flow is cut by the surface tension of the glass by dropping the glass from the outlet or changing the descending speed of the glass flow, if there is no difference in temperature between the outer peripheral portion of the outflowing glass and the inside, Due to the surface tension of the glass flow, the glass flow can be cut without leaving any defects on the cut surface, but if this temperature difference is large, the glass at the cutting part will be stretched into a thread at the time of cutting, and it will adhere to the cutting cross section, There is a problem that defects are left in the glass by being caught again in the cut portion.
【0004】[0004]
【発明が解決しようとする課題】本発明は上記問題を解
決するためになされたもので、その目的とするところ
は、ノズル、特に硝子流出口近傍の温度を下げることな
く、また、簡単な装置構成で温度分布のない硝子流を得
ることができる溶融硝子の流出装置を提供することにあ
る。SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and an object of the present invention is to reduce the temperature in the vicinity of the nozzle, especially the glass outlet, and to provide a simple apparatus. An object of the present invention is to provide a molten glass outflow device capable of obtaining a glass flow having no temperature distribution with a configuration.
【0005】[0005]
【課題を解決するための手段】上記目的を達成するため
に本発明は、一端にノズル部を形成すると共に他端を硝
子溶融炉に連結して炉内の溶融硝子を取り出すパイプ状
の溶融硝子流出装置において、ノズル部先端側に内径が
ノズル部内径よりも大径の保温筒を連設すると共に、前
記ノズル部と保温筒とに通電加熱用電極を設けるもの
で、上記ノズル部の先端側及び/又はノズル部先端側と
保温筒とを連結する接続部の肉厚をノズル部の肉厚より
も小さく形成すること、ノズル部が白金又は、白金合金
からなるものであること、ノズル部と保温筒とを一つの
直接通電で加熱することを含む。In order to achieve the above object, the present invention provides a pipe-shaped molten glass in which a nozzle portion is formed at one end and the other end is connected to a glass melting furnace to take out the molten glass in the furnace. In the outflow device, a heat retaining tube having an inner diameter larger than the inner diameter of the nozzle portion is continuously provided on the tip side of the nozzle portion, and an electric heating electrode is provided on the nozzle portion and the heat retaining tube. And / or forming the wall thickness of the connecting portion connecting the tip end side of the nozzle portion and the heat insulating cylinder smaller than the wall thickness of the nozzle portion, the nozzle portion being made of platinum or a platinum alloy, and the nozzle portion. Heating the heat retaining tube with a single direct current flow.
【0006】[0006]
【実施例】以下、本発明の実施例を、図面を参照して具
体的に説明する。 (実施例1)図1は本発明の溶融硝子流出装置の第1の
実施例を示すもので、図1中、1は図示されていない溶
融炉に接続されている白金パイプであり、白金パイプ1
の下に硝子流出部となる流出ノズル2が接続されてい
る。4は、流出ノズル2と接続部3で接続された保温筒
で、その内径は流出ノズル2の内径よりも大径に形成さ
れており、これによってノズル2の先端から流出した硝
子21の急激な温度低下を防ぐものである。Embodiments of the present invention will be specifically described below with reference to the drawings. (Embodiment 1) FIG. 1 shows a first embodiment of the molten glass outflow apparatus of the present invention. In FIG. 1, 1 is a platinum pipe connected to a melting furnace (not shown). 1
An outflow nozzle 2 which serves as a glass outflow portion is connected to the lower part. Reference numeral 4 denotes a heat-retaining cylinder connected to the outflow nozzle 2 by the connecting portion 3, and the inner diameter thereof is formed to be larger than the inner diameter of the outflow nozzle 2, whereby the glass 21 abruptly flowed out from the tip of the nozzle 2. It prevents temperature drop.
【0007】白金パイプ1の一端と流出ノズル2の連結
部、及び保温筒4の先端には通電したときに局部的に電
流密度が増えるのを防止するための通電リング5a,6
aが設けられていて、通電リング5a,6aにはさらに
電極5,6がそれぞれ設けられている。また、11は白
金パイプ1を加熱するための電源であり、電源の一方は
導線14を介して電極5に接続されており、もう一方は
同様に導線13を介して図示されていない白金パイプ1
の他端側(上部)に設けられた電極に接続されており、
電源11の電力を調整することで白金パイプの温度を任
意にコントロールできるようになっている。12も同様
に流出ノズル2と接続部3と保温筒4を加熱するための
電源で、導線15,16を介してそれぞれ電極5,6に
接続されている。17は外乱の影響を減らし、加熱、均
熱効果を上げるための保温材であり図示のように白金パ
イプ1及び流出ノズル2を覆っている。Energizing rings 5a, 6 for preventing a local increase in the current density when electricity is energized at one end of the platinum pipe 1 and the connecting portion of the outflow nozzle 2 and at the tip of the heat insulating cylinder 4.
a is provided, and the energization rings 5a and 6a are further provided with electrodes 5 and 6, respectively. Reference numeral 11 denotes a power source for heating the platinum pipe 1, one of the power sources is connected to the electrode 5 via the lead wire 14, and the other one is similarly connected via the lead wire 13 to the platinum pipe 1 not shown.
Is connected to the electrode provided on the other end side (upper part) of
By adjusting the electric power of the power supply 11, the temperature of the platinum pipe can be arbitrarily controlled. Similarly, reference numeral 12 is a power source for heating the outflow nozzle 2, the connecting portion 3, and the heat insulating cylinder 4, and is connected to the electrodes 5 and 6 through the lead wires 15 and 16, respectively. Reference numeral 17 is a heat insulating material for reducing the influence of disturbance and enhancing heating and soaking effects, and covers the platinum pipe 1 and the outflow nozzle 2 as shown in the figure.
【0008】白金パイプ1、流出ノズル2、接続部3、
保温筒4、通電リング5a,6a、電極5,6は全て白
金又は白金合金で作られており、パイプ1、ノズル2の
内径はφ6mm、外径φ8mmに仕上げられている。保
温筒4は内径φ10mm、外径φ11.3mmに仕上げ
られており、それぞれの電流の流れ方向に対する断面積
はほぼ同じである。接続部3は0.8mmの肉厚の板で
作られており、ノズル2の肉厚より薄くなっていて、電
源12から電流を流したときにノズル2の近傍の温度が
一番高く、保温筒4に近づくにしたがい徐々に温度が低
下していく構造とした。A platinum pipe 1, an outflow nozzle 2, a connecting portion 3,
The heat insulating cylinder 4, the energizing rings 5a and 6a, and the electrodes 5 and 6 are all made of platinum or a platinum alloy, and the pipe 1 and the nozzle 2 are finished to have an inner diameter of 6 mm and an outer diameter of 8 mm. The heat insulating cylinder 4 is finished to have an inner diameter of 10 mm and an outer diameter of 11.3 mm, and the cross-sectional areas in the current flow direction are substantially the same. The connecting portion 3 is made of a 0.8 mm-thick plate and is thinner than the nozzle 2 and has a highest temperature in the vicinity of the nozzle 2 when an electric current is supplied from the power supply 12 and keeps it warm. The structure is such that the temperature gradually decreases as it approaches the cylinder 4.
【0009】上記構成の流出装置を用いて、まず電源1
1をコントロールし、パイプ1を1050℃に設定し、
さらに電源12を調整しノズル2を1040℃に設定し
た。この状態で950℃のときに30Pa・s、104
0℃のときに10Pa・s、1135℃のとき5Pa・
sの粘度特性を示す硝子を流出させたところ、ノズル2
の下端の流出口から15mm下の所で、中心部の温度が
1045℃、外周部の温度が1035℃の安定した硝子
流21を得られた。またそのときの接続部3のノズル2
に近い所の温度は1045℃、保温筒4は950℃であ
った。 (実施例2)第2の実施例を図2を用いて説明する。こ
の実施例においては、ノズル2の先端側の外周に沿って
切り欠いた溝状の流出加熱部2aを形成した以外は実施
例1と同一構成のものとした。First, by using the outflow device having the above structure, the power source 1
Control 1 and set pipe 1 to 1050 ° C,
Furthermore, the power supply 12 was adjusted and the nozzle 2 was set to 1040 degreeC. In this state, at 950 ° C, 30 Pa · s, 104
10Pa ・ s at 0 ℃, 5Pa ・ at 1135 ℃
When the glass showing the viscosity characteristic of s was discharged, the nozzle 2
A stable glass flow 21 having a central temperature of 1045 ° C. and an outer peripheral temperature of 1035 ° C. was obtained 15 mm below the outlet at the lower end of the. Further, the nozzle 2 of the connecting portion 3 at that time
The temperature near 10 ° C. was 1045 ° C., and the temperature of the heat insulating cylinder 4 was 950 ° C. (Second Embodiment) A second embodiment will be described with reference to FIG. This embodiment has the same configuration as that of the first embodiment except that a groove-shaped outflow heating portion 2a is formed by cutting out along the outer periphery of the nozzle 2 on the tip side.
【0010】実施例1と同様に白金パイプ1、流出ノズ
ル2、流出加熱部2a、接続部3、保温筒4、通電リン
グ5a,6a、電極5,6は全て白金又は白金合金で作
られており、パイプ1、ノズル2は内径はφ6mm、外
径φ8mmに仕上げられている。保温筒4は内径φ10
mm、外径φ10.8mmに仕上げ、ノズル2に比較し
て電流密度が2割ほど大きくなるようにした。加熱部2
aは内径φ6mm、外径φ7.6mmとし、ノズル2に
比較して電流密度が3割弱大きくなるようにし、さらに
接続部3は加熱部2aと同じ0.8mmの肉厚の板で作
った。Similar to the first embodiment, the platinum pipe 1, the outflow nozzle 2, the outflow heating part 2a, the connecting part 3, the heat retaining tube 4, the energizing rings 5a and 6a, and the electrodes 5 and 6 are all made of platinum or a platinum alloy. The pipe 1 and the nozzle 2 have an inner diameter of 6 mm and an outer diameter of 8 mm. Inner diameter φ10
mm, the outer diameter φ10.8 mm, and the current density was increased by about 20% as compared with the nozzle 2. Heating part 2
a has an inner diameter of 6 mm and an outer diameter of 7.6 mm so that the current density is slightly less than 30% larger than that of the nozzle 2, and the connecting portion 3 is made of the same 0.8 mm thick plate as the heating portion 2a. .
【0011】実施例1と同様に、電源11をコントロー
ルしパイプ1を1050℃に設定した。さらに電源12
を調整しノズル2を1040℃に設定して、実施例1に
用いたのと同じ硝子を流出させたところ、流出口から1
5mm下の所で、中心部と外周部の温度が同じ1045
℃の安定した硝子流21が得られた。またそのときの加
熱部2aの温度は1055℃、接続部3のノズル2に近
い所の温度も1050℃、保温筒4は1000℃であっ
た。 (実施例3)第3の実施例を図3を用いて説明する。In the same manner as in Example 1, the power source 11 was controlled and the pipe 1 was set at 1050 ° C. Further power 12
Was adjusted to set the nozzle 2 to 1040 ° C. and the same glass as that used in Example 1 was allowed to flow out.
The temperature of the central part and the outer part is the same at 5mm below 1045
A stable glass flow of 21 ° C. was obtained. At that time, the temperature of the heating part 2a was 1055 ° C., the temperature of the connection part 3 near the nozzle 2 was 1050 ° C., and the temperature of the heat retaining cylinder 4 was 1000 ° C. (Third Embodiment) A third embodiment will be described with reference to FIG.
【0012】装置構成は接続部3を廃止し、図示のごと
く一旦上方に折り返した折り返し部7を介してノズル2
の先端側と保温筒4とをつないだ他は、実施例1と同じ
構成とした。The apparatus is constructed so that the connecting portion 3 is eliminated and the nozzle 2 is folded through the folded portion 7 which is once folded upward as shown in the figure.
The configuration was the same as that of Example 1 except that the tip end side and the heat insulating cylinder 4 were connected.
【0013】実施例1と同様に、白金パイプ1、流出ノ
ズル2、折り返し部7、保温筒4、通電リング5a,6
a、電極5,6は全て白金又は白金合金で作られてお
り、パイプ1、ノズル2は内径はφ6mm、外径φ8m
mに仕上げられている。保温筒4は内径φ12mm、外
径φ13.1mmに仕上げられており、それぞれの電流
の流れ方向に対する断面積はほぼ同じとした。折り返し
部7は内径φ9.5mm、外径10.7mmとしノズル
2に比較して電流密度が2割弱大きくなるようにした。Similar to the first embodiment, the platinum pipe 1, the outflow nozzle 2, the folded portion 7, the heat retaining cylinder 4, the current-carrying rings 5a and 6 are used.
a, the electrodes 5 and 6 are all made of platinum or a platinum alloy, and the pipe 1 and the nozzle 2 have an inner diameter of 6 mm and an outer diameter of 8 m.
It is finished in m. The heat-retaining cylinder 4 is finished to have an inner diameter of 12 mm and an outer diameter of 13.1 mm, and the cross-sectional areas in the current flow direction are substantially the same. The folded-back portion 7 had an inner diameter of 9.5 mm and an outer diameter of 10.7 mm so that the current density was slightly less than 20% larger than that of the nozzle 2.
【0014】実施例1と同様に、電源11をコントロー
ルし、パイプ1を1050℃に設定し、さらに電源12
を調整し、ノズル2を1040℃に設定した。実施例1
に用いたものと同じ硝子を流出させたところ、流出口か
ら15mm下の所で、中心部の温度が1045℃、外周
部の温度が1040℃の安定した硝子流21が得られ
た。またそのときの折り返し部7の温度は1060℃、
保温筒4は950℃であった。 (実施例4)第4の実施例を図4を用いて説明する。Similar to the first embodiment, the power source 11 is controlled, the pipe 1 is set to 1050 ° C., and the power source 12 is used.
Was adjusted and the nozzle 2 was set to 1040 ° C. Example 1
When the same glass as that used in Example 1 was allowed to flow out, a stable glass flow 21 having a central temperature of 1045 ° C. and an outer peripheral temperature of 1040 ° C. was obtained at a position 15 mm below the outlet. At that time, the temperature of the folded portion 7 is 1060 ° C,
The temperature of the heat insulating cylinder 4 was 950 ° C. (Fourth Embodiment) A fourth embodiment will be described with reference to FIG.
【0015】装置構成はノズル2の先端にノズル2の上
部より外径の小さな流出加熱部2aを設けた他は実施例
3と同じ構成とした。The apparatus configuration is the same as that of the third embodiment except that an outflow heating section 2a having a smaller outer diameter than the upper portion of the nozzle 2 is provided at the tip of the nozzle 2.
【0016】実施例3と同様に、白金パイプ1、流出ノ
ズル2、流出加熱部2a、折り返し部7、保温筒4、通
電リング5a,6a、電極5,6は全て白金又は白金合
金で作られている。パイプ1、ノズル2は内径はφ6m
m、外径φ8mmに仕上げられていて、保温筒4は内径
φ12mm、外径φ12.9mmに仕上げ、ノズル2に
比較して電流密度が2.5割ほど大きくなるようにし
た。折り返し部7も同様に内径φ9.5mm、外径1
0.7mmとし、ノズル2に比較して電流密度が2割弱
大きくなるようにした。さらに、加熱部2aは内径φ6
mm、外径φ7.7mmとし、ノズル2に比較して電流
密度が2割大きくなるようにした。As in the third embodiment, the platinum pipe 1, the outflow nozzle 2, the outflow heating section 2a, the folded section 7, the heat retaining tube 4, the energizing rings 5a and 6a, and the electrodes 5 and 6 are all made of platinum or a platinum alloy. ing. Inner diameter of pipe 1 and nozzle 2 is φ6m
m, the outer diameter was φ8 mm, and the heat insulating cylinder 4 was finished to have an inner diameter of φ12 mm and an outer diameter of φ12.9 mm so that the current density was about 2.5% larger than that of the nozzle 2. Similarly, the folded-back portion 7 has an inner diameter of 9.5 mm and an outer diameter of 1
It was set to 0.7 mm so that the current density was slightly less than 20% larger than that of the nozzle 2. Further, the heating portion 2a has an inner diameter of φ6.
mm and outer diameter φ7.7 mm so that the current density is 20% larger than that of the nozzle 2.
【0017】実施例3と同様に、電源11をコントロー
ルし、パイプ1を1050℃に設定し、さらに電源12
を調整し、ノズル2を1040℃に設定した。実施例1
に用いたものと同じ硝子を流出させたところ、流出口か
ら15mm下の所で、中心部と外周部の温度が1045
℃の安定した硝子流21が得られた。またそのときの加
熱部2aの温度は1055℃、折り返し部7の温度は1
065℃、保温筒4は950℃であった。Similar to the third embodiment, the power source 11 is controlled, the pipe 1 is set to 1050 ° C., and the power source 12
Was adjusted and the nozzle 2 was set to 1040 ° C. Example 1
When the same glass as that used for was flowed out, the temperature of the central part and the outer peripheral part was 1045 at 15 mm below the outlet.
A stable glass flow of 21 ° C. was obtained. At that time, the temperature of the heating part 2a is 1055 ° C., and the temperature of the folding part 7 is 1
The temperature was 065 ° C., and the temperature of the heat insulating cylinder 4 was 950 ° C.
【0018】[0018]
【発明の効果】本発明は、以上説明したように、硝子流
出口の先にさらに保温部を設け、流出口や、保温部と流
出口の間の温度を流出ノズル全体の温度よりも上げ、保
温と、加熱を行うことにより、不要な加熱、冷却による
失透、泡の再発生を防ぎ、切断刃を用いない硝子流の切
断に、非常に有効な温度バランスのよい流出硝子流を得
ることができる。As described above, according to the present invention, a heat retaining portion is further provided at the tip of the glass outlet, and the temperature of the outlet or between the heat retaining portion and the outlet is raised above the temperature of the entire outflow nozzle. By keeping heat and heating, unnecessary heating, devitrification due to cooling, re-generation of bubbles can be prevented, and a very effective temperature-balanced outflow glass flow can be obtained for cutting a glass flow without using a cutting blade. You can
【図1】本発明の第一の実施例を示す部分省略図であ
る。FIG. 1 is a partially omitted view showing a first embodiment of the present invention.
【図2】本発明の第二の実施例を示す部分省略図であ
る。FIG. 2 is a partially omitted view showing a second embodiment of the present invention.
【図3】本発明の第三の実施例を示す部分省略図であ
る。FIG. 3 is a partially omitted view showing a third embodiment of the present invention.
【図4】本発明の第四の実施例を示す部分省略図であ
る。FIG. 4 is a partially omitted view showing a fourth embodiment of the present invention.
1 白金パイプ 2 流出ノズル 2a 流出加熱部 3 接続部 4 保温筒 5,6 電極 5a,6a 通電リング 7 折り返し部 17 保温材 21 流出硝子 DESCRIPTION OF SYMBOLS 1 Platinum pipe 2 Outflow nozzle 2a Outflow heating part 3 Connection part 4 Insulating cylinder 5,6 Electrode 5a, 6a Energizing ring 7 Folding part 17 Insulating material 21 Outflow glass
───────────────────────────────────────────────────── フロントページの続き (72)発明者 余語 瑞和 東京都大田区下丸子3丁目30番2号 キヤ ノン株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Mizukazu 3-30-2 Shimomaruko, Ota-ku, Tokyo Canon Inc.
Claims (4)
硝子溶融炉に連結して炉内の溶融硝子を取り出すパイプ
状の溶融硝子流出装置において、ノズル部先端側に内径
がノズル部内径よりも大径の保温筒を連設すると共に、
前記ノズル部と保温筒とに通電加熱用電極を設けてなる
ことを特徴とする溶融硝子流出装置。1. A pipe-shaped molten glass outflow device having a nozzle portion formed at one end and the other end connected to a glass melting furnace to take out molten glass in the furnace, wherein the inner diameter is closer to the tip end side of the nozzle portion than the inner diameter of the nozzle portion. In addition to connecting a large-diameter heat insulation tube,
A molten glass outflow device, characterized in that an electric heating electrode is provided on the nozzle portion and the heat retaining cylinder.
端側と保温筒とを連結する接続部の肉厚をノズル部の肉
厚よりも小さく形成してなる請求項1記載の流出装置。2. The outflow device according to claim 1, wherein a thickness of a tip end side of the nozzle portion and / or a connecting portion connecting the tip end side of the nozzle portion and the heat insulating cylinder is smaller than a thickness of the nozzle portion.
請求項1記載の流出装置。3. The outflow device according to claim 1, wherein the nozzle portion is made of platinum or a platinum alloy.
加熱する請求項1記載の流出装置。4. The outflow device according to claim 1, wherein the nozzle portion and the heat insulating cylinder are heated by a single direct energization.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5129318A JP3046694B2 (en) | 1993-05-31 | 1993-05-31 | Molten glass outflow equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5129318A JP3046694B2 (en) | 1993-05-31 | 1993-05-31 | Molten glass outflow equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06340429A true JPH06340429A (en) | 1994-12-13 |
JP3046694B2 JP3046694B2 (en) | 2000-05-29 |
Family
ID=15006617
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5129318A Expired - Lifetime JP3046694B2 (en) | 1993-05-31 | 1993-05-31 | Molten glass outflow equipment |
Country Status (1)
Country | Link |
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JP (1) | JP3046694B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1857420A1 (en) * | 2005-03-08 | 2007-11-21 | Asahi Glass Company, Limited | Platinum or platinum alloy structure and glass puroduction apparatus making use of the same |
JP5018476B2 (en) * | 2005-06-06 | 2012-09-05 | 旭硝子株式会社 | GLASS MANUFACTURING APPARATUS, ITS COMPONENTS, AND METHOD FOR ELECTRIC HEATING THE COMPONENTS |
CN105293871A (en) * | 2015-12-04 | 2016-02-03 | 四川航天拓鑫玄武岩实业有限公司 | Platinum channel device for producing basalt fibers |
JP2017014056A (en) * | 2015-06-30 | 2017-01-19 | AvanStrate株式会社 | Production method of glass plate and production device of glass plate |
-
1993
- 1993-05-31 JP JP5129318A patent/JP3046694B2/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1857420A1 (en) * | 2005-03-08 | 2007-11-21 | Asahi Glass Company, Limited | Platinum or platinum alloy structure and glass puroduction apparatus making use of the same |
EP1857420A4 (en) * | 2005-03-08 | 2010-10-27 | Asahi Glass Co Ltd | Platinum or platinum alloy structure and glass puroduction apparatus making use of the same |
JP5018476B2 (en) * | 2005-06-06 | 2012-09-05 | 旭硝子株式会社 | GLASS MANUFACTURING APPARATUS, ITS COMPONENTS, AND METHOD FOR ELECTRIC HEATING THE COMPONENTS |
JP2017014056A (en) * | 2015-06-30 | 2017-01-19 | AvanStrate株式会社 | Production method of glass plate and production device of glass plate |
CN105293871A (en) * | 2015-12-04 | 2016-02-03 | 四川航天拓鑫玄武岩实业有限公司 | Platinum channel device for producing basalt fibers |
CN105293871B (en) * | 2015-12-04 | 2019-04-23 | 四川航天拓鑫玄武岩实业有限公司 | Platinum channel device for basalt fibre production |
Also Published As
Publication number | Publication date |
---|---|
JP3046694B2 (en) | 2000-05-29 |
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