Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP2615966B2 - Glass melting furnace - Google Patents
[go: Go Back, main page]

JP2615966B2 - Glass melting furnace - Google Patents

Glass melting furnace

Info

Publication number
JP2615966B2
JP2615966B2 JP1020321A JP2032189A JP2615966B2 JP 2615966 B2 JP2615966 B2 JP 2615966B2 JP 1020321 A JP1020321 A JP 1020321A JP 2032189 A JP2032189 A JP 2032189A JP 2615966 B2 JP2615966 B2 JP 2615966B2
Authority
JP
Japan
Prior art keywords
glass
furnace
heating element
melting furnace
opening
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 - Lifetime
Application number
JP1020321A
Other languages
Japanese (ja)
Other versions
JPH02199029A (en
Inventor
貴 砂田
兼仁 長嶋
茂樹 中垣
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.)
Nippon Sheet Glass Co Ltd
Original Assignee
Nippon Sheet Glass 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 Nippon Sheet Glass Co Ltd filed Critical Nippon Sheet Glass Co Ltd
Priority to JP1020321A priority Critical patent/JP2615966B2/en
Publication of JPH02199029A publication Critical patent/JPH02199029A/en
Application granted granted Critical
Publication of JP2615966B2 publication Critical patent/JP2615966B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • C03B5/02Melting in furnaces; Furnaces so far as specially adapted for glass manufacture in electric furnaces, e.g. by dielectric heating
    • C03B5/033Melting in furnaces; Furnaces so far as specially adapted for glass manufacture in electric furnaces, e.g. by dielectric heating by using resistance heaters above or in the glass bath, i.e. by indirect resistance heating
    • C03B5/0336Shaft furnaces

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Glass Melting And Manufacturing (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明はガラス溶融炉に係り、特に高品質のガラスを
効率的に安定生産することができる竪型電気溶融炉に関
する。
Description: TECHNICAL FIELD The present invention relates to a glass melting furnace, and more particularly to a vertical electric melting furnace capable of efficiently and stably producing high-quality glass.

[従来の技術及び先行技術] 従来、ガラスの竪型電気溶融炉としては、第3図に示
すように炉の最上部に原料投入口1を有し、炉内の溶融
ガラス4に浸漬した電極5よりガラスに直接通電し、発
生するジュール熱によってガラスを加熱して、ガラス素
地表面に供給したガラス原料(バッチ)3を溶融、清澄
した後、炉の底部に設けたガラス出口2よりガラスを作
業部に搬送する構造のものが一般的である。電極5の配
置としては、第3図の如く、棒状電極5を炉の側壁から
水平に挿入するもの、その他、炉の底部から垂直に挿入
するもの、あるいはガラス原料の層を貫通して炉の上部
から挿入するもの等が知られている。
[Prior Art and Prior Art] Conventionally, as a vertical electric melting furnace for glass, as shown in FIG. 3, an electrode immersed in a molten glass 4 in the furnace has a raw material inlet 1 at the top of the furnace. The glass raw material (batch) 3 supplied to the surface of the glass substrate is melted and clarified by directly supplying electricity to the glass from 5 and generating the Joule heat, and then the glass is discharged from the glass outlet 2 provided at the bottom of the furnace. In general, it is configured to be transported to a work unit. As shown in FIG. 3, the electrodes 5 may be arranged such that the rod-shaped electrodes 5 are inserted horizontally from the side wall of the furnace, other electrodes are inserted vertically from the bottom of the furnace, or through the glass material layer. A device inserted from above is known.

このような電気溶融炉では、熱エネルギーの有効利用
のために、溶融ガラス4の表面をガラス原料(バッチ)
3の層で覆う。(いわゆる「コールドトップ」を形成す
る。)しかして、ガラスの溶融、清澄は炉の深さ方向に
進行する。
In such an electric melting furnace, the surface of the molten glass 4 is made of a glass raw material (batch) for effective use of heat energy.
Cover with 3 layers. (The so-called “cold top” is formed.) However, melting and fining of the glass proceeds in the depth direction of the furnace.

このような電気溶融炉により高品質のガラスを得るに
は、炉の底部の出口2を通って作業部に供給されるガラ
スが十分な熱履歴をもった。泡や未溶融物のない素地と
なるようにする必要がある。出口2に到達するガラスの
熱履歴は、炉内のガラスの温度とガラス素地の流れによ
って決まるが、炉内のガラス素地の流れは主として炉内
のガラスの温度分布に起因する熱対流に支配されるの
で、品質の優れたガラスを製造するためには炉内を常に
安定した熱平衡下に置くことが操炉の最大のポイントと
なる。
To obtain high quality glass with such an electric melting furnace, the glass supplied to the working section through outlet 2 at the bottom of the furnace had a sufficient thermal history. It is necessary to make the substrate free of bubbles and unmelted material. The heat history of the glass reaching the outlet 2 is determined by the temperature of the glass in the furnace and the flow of the glass substrate, but the flow of the glass substrate in the furnace is mainly governed by the thermal convection caused by the temperature distribution of the glass in the furnace. Therefore, in order to produce high quality glass, the most important point of the furnace operation is to always keep the furnace in a stable thermal equilibrium.

しかしながら、棒状電極を用い、ガラスのジュール熱
による加熱を利用する従来の竪型電気溶融炉において
は、炉の平面内の電力分布を均一にすることは困難であ
り、特に電極の先端部近傍における電流密度が高くな
り、電極先端間のガラスの温度が高くなり易い。ガラス
の電気抵抗は、温度が高いほど小さくなるので、高温部
にはますます電流が流れるようになり、局所加熱は更に
助長されることとなる。このような温度分布の不均一は
炉内のガラス素地に熱対流を起こさせ、その結果、熱履
歴の短いガラス素地、つまり加熱が不十分で泡や未溶融
物を含んだガラス素地が出口から流出することとなり、
これが作業部に供給され製品に欠点を生じさせる原因と
なる。
However, in a conventional vertical electric melting furnace that uses a rod-shaped electrode and utilizes heating by Joule heat of glass, it is difficult to make the power distribution uniform in the plane of the furnace, particularly in the vicinity of the tip of the electrode. The current density increases, and the temperature of the glass between the electrode tips tends to increase. Since the electric resistance of the glass decreases as the temperature increases, an electric current flows more and more in a high-temperature portion, and local heating is further promoted. Such non-uniform temperature distribution causes thermal convection in the glass substrate in the furnace, and as a result, a glass substrate with a short heat history, that is, a glass substrate that is insufficiently heated and contains bubbles and unmelted material, is discharged from the outlet. Will be leaked,
This causes a defect in the product supplied to the working unit.

更に、不均一な温度分布及びそれによって生じるガラ
ス素地の熱対流は、ガラス素地表面のバッチの不均一な
溶解をひき起こし、素地に局所的にバッチ層で覆われな
い部分が生じて、熱損失が大きくなるとともに、ガラス
温度の低下を招く。ガラスのジュール熱を利用した加熱
の溶融炉では、前述の理由によって、ガラス素地の温度
の制御が極めて困難であることから、このようにして起
こるガラス素地の不均一な温度分布は、これを改善する
ことは殆ど不可能である。
Furthermore, the non-uniform temperature distribution and the resulting thermal convection of the glass substrate cause non-uniform melting of the batch on the surface of the glass substrate, resulting in local uncovered portions of the substrate with the batch layer, resulting in heat loss. And the temperature of the glass decreases. In the melting furnace that uses the Joule heat of glass, it is extremely difficult to control the temperature of the glass substrate for the reasons described above. It is almost impossible to do.

このような問題は、アルカリ成分を含まない電気抵抗
の大きいガラスを溶融する場合において顕著になる。即
ち、かかる無アルカリガラスは電気抵抗が大きいので、
溶融に必要な電力をガラスに与えるためには、電極間の
距離を小さくする必要があることから、上記の不均一な
温度分布が顕著となるのである。
Such a problem becomes conspicuous when melting glass having a high electric resistance containing no alkali component. That is, since such alkali-free glass has a large electric resistance,
In order to supply the glass with the power required for melting, it is necessary to reduce the distance between the electrodes, so that the above-mentioned non-uniform temperature distribution becomes remarkable.

このような問題を解決するものとして、本出願人は、
最上部に原料投入部を有し、最下部にガラス素地出口を
備えた竪型のガラス溶融炉において、ガラス素地に浸漬
する少くとも1つのレベルに、当該レベルにおける炉の
水平断面のほぼ全領域にわたって抵抗発熱体を設けたこ
とを特徴とするガラス溶融炉を開発し、先に特許出願を
行なった(特願昭62−327892号。以下「先願」とい
う。)。
In order to solve such a problem, the present applicant has
In a vertical glass melting furnace having a raw material charging section at the top and a glass base outlet at the bottom, at least one level of immersion in the glass base, substantially the entire horizontal cross section of the furnace at that level A glass melting furnace characterized by providing a resistance heating element over a long period of time was developed and a patent application was filed earlier (Japanese Patent Application No. 62-327892; hereinafter referred to as "prior application").

上記先願のガラス溶融炉によれば、従来の電極を用い
た加熱方法に比べ、温度分布が均一で熱対流が小さくな
り、熱履歴の短いガラス素地が流出し難くなるため、高
品質のガラスを効率的に製造することが可能とされる。
According to the glass melting furnace of the prior application, compared with the conventional heating method using electrodes, the temperature distribution is uniform, the heat convection is small, and it is difficult for the glass material having a short heat history to flow out, so that high-quality glass is used. Can be manufactured efficiently.

[発明が解決しようとする課題] しかしながら、上記先願のガラス溶融炉であっても、
抵抗発熱体の形状によっては温度分布の均一性があまり
良好でないものや、比較的熱履歴の短い素地が流出し易
い場合があった。
[Problems to be Solved by the Invention] However, even in the glass melting furnace of the prior application,
Depending on the shape of the resistance heating element, the uniformity of the temperature distribution may not be very good, or a substrate having a relatively short heat history may easily flow out.

本発明は上記先願を更に改善し、ガラス素地の温度分
布をより均一なものとすると共に、熱対流をより確実に
防止し、著しく高品質なガラスを安定かつ効率的に製造
することができるガラス溶融炉を提供することを目的と
する。
The present invention further improves the above-mentioned prior application, makes the temperature distribution of the glass base material more uniform, more reliably prevents thermal convection, and makes it possible to stably and efficiently produce extremely high quality glass. It is an object to provide a glass melting furnace.

[課題を解決するための手段] 本発明のガラス溶融炉は、最上部に原料投入部を有
し、最下部にガラス素地出口を備え、ガラス素地に浸漬
する少くとも1つのレベルに、当該レベルにおける炉の
水平断面のほぼ全領域にわたって抵抗発熱体を設けた竪
型のガラス溶融炉において、前記発熱体は、複数の開口
が均一に分散して設けられた板状の発熱体であり、該開
口の直径をD、隣接する開口同芯の中心間距離をP、板
状発熱体の最も長い対角線の長さをLとしたとき、 D>1mm D/L<0.5 及び、 D/P>0.1 の関係を満足することを特徴とする。
Means for Solving the Problems The glass melting furnace of the present invention has a raw material charging section at the top, a glass base outlet at the bottom, and at least one level immersed in the glass base. In a vertical glass melting furnace provided with a resistance heating element over substantially the entire horizontal cross section of the furnace, the heating element is a plate-shaped heating element provided with a plurality of openings uniformly distributed, When the diameter of the opening is D, the distance between the centers of adjacent concentric openings is P, and the length of the longest diagonal line of the plate-shaped heating element is L, D> 1 mm D / L <0.5 and D / P> 0.1 Is satisfied.

即ち、本発明者らは、前記先願のガラス溶融炉を改善
すべく鋭意検討を行なった結果、抵抗発熱体として、複
数の開口を有する板状体を用い、この開口の直径及び間
隔を特定することにより、優れた効果が得られることを
見出し、本発明を完成させた。
That is, the present inventors have conducted intensive studies to improve the glass melting furnace of the prior application, and as a result, used a plate-like body having a plurality of openings as a resistance heating element, and specified the diameter and interval of the openings. By doing so, it was found that excellent effects were obtained, and the present invention was completed.

[作 用] 本発明のガラス溶融炉では、均一に分布した複数の開
口を有する板状の抵抗発熱体(発熱板)によってガラス
素地を加熱するので、発熱量の制御が容易である。
[Operation] In the glass melting furnace of the present invention, since the glass substrate is heated by a plate-like resistance heating element (heating plate) having a plurality of openings uniformly distributed, the calorific value can be easily controlled.

従来の電極を用いた直接通電方式では電力を小さくし
過ぎると、ガラス素地が電極間を速く流れ落ち、十分に
清澄の行なわれてない素地が出口から流出し易いのに対
し、本発明に係る発熱板を用いるものでは、このような
ショートパスは起こり難い。
If the power is too small in the conventional direct energization method using electrodes, the glass substrate quickly flows down between the electrodes, and the substrate that has not been sufficiently clarified easily flows out of the outlet, whereas the heat generation according to the present invention occurs. In the case of using a plate, such a short path is unlikely to occur.

この発熱板はガラス素地内の炉の水平断面のほぼ全領
域にわたって設置されるため、ガラス素地の平面内の温
度分布は著しく均一になる。また、発熱板は、対流の流
れの障害物として機能するので、対流が抑制されるとと
もに、発熱板の表面部が最高温度となるので、発熱板よ
りも下側の領域では下方ほど温度が低い温度分布とな
り、熱対流が防止される。
Since the heating plate is installed over almost the entire horizontal cross section of the furnace in the glass substrate, the temperature distribution in the plane of the glass substrate becomes extremely uniform. In addition, since the heating plate functions as an obstacle to the flow of convection, the convection is suppressed, and the surface of the heating plate has the highest temperature. It becomes a temperature distribution and thermal convection is prevented.

ところで、発熱板の開口が発熱板に対して大き過ぎる
と温度分布の均一性が悪くなり、熱対流が促進される。
逆に、開口が小さ過ぎるとガラス素地により開口が目詰
りしたり、開口の形成加工が困難となる。また、開口の
大きさに対して、隣接する開口間隔が長過ぎると開口部
付近のガラス素地が抜け落ち易く、開口部から離れたガ
ラス素地は抜け落ち難いことから、この差が大きくな
り、ガラス素地の熱履歴が不均質なものとなる。
By the way, if the opening of the heating plate is too large with respect to the heating plate, the uniformity of the temperature distribution deteriorates, and the heat convection is promoted.
On the other hand, if the opening is too small, the opening is clogged by the glass substrate, and it is difficult to form the opening. Also, with respect to the size of the opening, if the interval between adjacent openings is too long, the glass base near the opening is easy to fall off, and the glass base far from the opening is difficult to fall off. The heat history becomes heterogeneous.

しかしながら、 D>1mm D/L<0.5 D/P>0.1 となるように、開口の直径D、発熱板の最長対角線長さ
L及び開口間隔Pを設定することにより、上記の問題は
解決され、良好な加熱溶融を行なうことが可能とされ
る。
However, the above problem is solved by setting the diameter D of the opening, the longest diagonal length L of the heating plate and the opening interval P so that D> 1 mm D / L <0.5 D / P> 0.1, Good heat melting can be performed.

[実施例] 以下、図面を参照して本発明の実施例について詳細に
説明する。
[Example] Hereinafter, an example of the present invention will be described in detail with reference to the drawings.

第1図は本発明の一実施例を示すガラス溶融炉の縦断
面図、第2図は第1図のII−II線に沿う断面図である。
FIG. 1 is a longitudinal sectional view of a glass melting furnace showing one embodiment of the present invention, and FIG. 2 is a sectional view taken along the line II-II of FIG.

第1図及び第2図に示すガラス溶融炉においては、種
瓦よりなる炉本体10は平面視で四角形をなし、上部に原
料投入部1、底部にガラス出口(本例では側方へ突出す
るスロート)2が設けられ、内部には溶融したガラス素
地4が保持されている。このガラス素地4の表面にはガ
ラス原料(バッチ)3が均等に供給されている。しかし
て、炉内のガラス素地4に浸漬されるレベルに、当該レ
ベルにおける炉の水平断面のほぼ全領域にわたって板状
の抵抗発熱体6が設置されている。この抵抗発熱体6
は、均一に分布した多数の開口7を有する板状の発熱板
6aと、その両端から上方に立ち上るターミナル部6bを備
えてなり、抵抗発熱体6の炉外の端部は電源Vに接続さ
れている。
In the glass melting furnace shown in FIGS. 1 and 2, a furnace main body 10 made of a seed tile has a rectangular shape in plan view, a raw material charging section 1 at an upper portion, and a glass outlet at a bottom portion (projects sideways in this example). A throat 2 is provided inside which a molten glass base 4 is held. The glass raw material (batch) 3 is uniformly supplied to the surface of the glass substrate 4. Thus, at the level immersed in the glass substrate 4 in the furnace, a plate-shaped resistance heating element 6 is installed over almost the entire area of the horizontal section of the furnace at that level. This resistance heating element 6
Is a plate-like heating plate having a large number of openings 7 distributed uniformly.
6a and a terminal portion 6b rising upward from both ends thereof. An end of the resistance heating element 6 outside the furnace is connected to a power supply V.

本発明において、開口7の直径(開口形状が多角形の
場合はその最も長い対角線の長さ)D、隣り合う開口
7、7′の中心間距離P、発熱板の最も長い対角線の長
さ(円形の場合はその直径)Lを、D>1mm、D/L<0.5
及び、D/P>0.1と設定する。
In the present invention, the diameter D of the opening 7 (the length of the longest diagonal line when the opening shape is a polygon), the distance P between the centers of the adjacent openings 7, 7 ', and the length of the longest diagonal line of the heating plate ( In the case of a circle, its diameter) L is D> 1 mm, D / L <0.5
And set D / P> 0.1.

開口7の直径Dが小さ過ぎると、未溶融物による目詰
りが生じ易く、また、発熱板6aの開口形成のための加工
が行ないにくい。従って、D>1mmとする。
If the diameter D of the opening 7 is too small, clogging is likely to occur due to unmelted material, and it is difficult to perform processing for forming the opening of the heating plate 6a. Therefore, D> 1 mm.

また、発熱板6aの大きさに対して開口7の大きさが大
き過ぎるとガラス素材の平面内温度分布の均一性が損な
われ、熱対流が促進される。従って、D/L<0.5とする。
If the size of the opening 7 is too large with respect to the size of the heating plate 6a, the uniformity of the in-plane temperature distribution of the glass material is impaired, and heat convection is promoted. Therefore, D / L <0.5.

更に、開口7の大きさに対してその形成間隔が大き過
ぎる場合には、ガラス素地4の熱履歴が不均質となる。
即ち、開口部付近の素地は速く抜け落ちるのに対し、開
口部から離れた素地は抜け落ち難いことから、開口部か
ら離れた素地に比べ、開口部近くの素地の熱履歴が短く
なり、加熱が不十分となり易い。
Furthermore, if the formation interval is too large with respect to the size of the opening 7, the heat history of the glass substrate 4 becomes uneven.
That is, the substrate near the opening falls off quickly, whereas the substrate away from the opening is hard to fall off, so the heat history of the substrate near the opening is shorter than that of the substrate away from the opening, and heating is difficult. It is easy to be enough.

従って、D/P>0.1とする。 Therefore, D / P> 0.1.

本発明においては、特に 0.2>D/L 0.7>D/P>0.3 と設定するのが好ましい。 In the present invention, it is particularly preferable to set 0.2> D / L 0.7> D / P> 0.3.

なお、本発明において、抵抗発熱体6の材料として
は、白金、白金−ロジウム合金、モリブデン、モリブデ
ンの表面に白金を被覆したものなどが用いられるが、特
に白金又は白金−ロジウム合金が望ましい。これらの材
料の電気抵抗の温度係数はガラスのそれに比べるとはる
かに小さいことから、温度制御が非常に容易となるとい
う利点がある。
In the present invention, as the material of the resistance heating element 6, platinum, platinum-rhodium alloy, molybdenum, molybdenum whose surface is coated with platinum, or the like is used, and platinum or platinum-rhodium alloy is particularly desirable. Since the temperature coefficient of electric resistance of these materials is much smaller than that of glass, there is an advantage that temperature control becomes very easy.

本実施例のガラス溶融炉において、発熱板6aが一辺10
0cmの正方形の板状であって、90%Pt−10%Rh製の抵抗
発熱体6を設置した。開口7は直径10mmの円形とし、隣
り合う開口の間隔は20mmと設定した。
In the glass melting furnace of this embodiment, the heating plate 6a
A resistance heating element 6 having a square plate shape of 0 cm and made of 90% Pt-10% Rh was installed. The opening 7 was a circle having a diameter of 10 mm, and the interval between adjacent openings was set to 20 mm.

かかる構成のガラス溶融炉において、抵抗発熱体6に
通電することによりガラスの加熱がなされる。この際、
抵抗発熱体6の抵抗値は温度に応じて一義的に定まるも
のであり、所定の電力を供給することにより正確に所定
量の熱を発生させることができる。また、この抵抗発熱
体6は、その発熱板6aが炉の水平断面の全領域にわたっ
て均等に設けられているからガラス素地が該水平断面の
全領域で均等に加熱されるようになり、当該水平断面に
おけるガラス素地の温度分布は著しく均一になる。
In the glass melting furnace having such a configuration, the glass is heated by energizing the resistance heating element 6. On this occasion,
The resistance value of the resistance heating element 6 is uniquely determined according to the temperature, and a predetermined amount of heat can be generated accurately by supplying a predetermined power. In addition, since the heating plate 6a of the resistance heating element 6 is provided uniformly over the entire area of the horizontal section of the furnace, the glass substrate is uniformly heated over the entire area of the horizontal section. The temperature distribution of the glass body in the cross section becomes extremely uniform.

このようなことから、水平面内の温度ムラに起因する
ガラス素地の対流が防止される。また、このガラス溶融
炉内のガラス素地4は、発熱板6aの表面と接触する部分
が最高温度になり、該発熱板6aより深くなるに従って温
度が低くなる。従って、この発熱板6aよりも下側ではガ
ラス素地4に熱対流が殆ど生じない。
For this reason, convection of the glass substrate due to temperature unevenness in the horizontal plane is prevented. Further, the temperature of the glass substrate 4 in the glass melting furnace at the portion in contact with the surface of the heating plate 6a has the highest temperature, and the temperature becomes lower as the depth becomes deeper than the heating plate 6a. Therefore, heat convection hardly occurs in the glass substrate 4 below the heating plate 6a.

発熱板6aよりも上側では、上方ほど低温になることに
起因してガラス素地4に熱対流が生じる。しかしなが
ら、この発熱板6aは、それよりも上側と下側とを離隔す
るように設けられているから、発熱板6aよりも上側にお
けるガラス素地の熱対流は発熱板6aよりも下側へは殆ど
伝達されない。
Above the heat generating plate 6a, the lower the temperature becomes, the higher the temperature becomes. However, since the heating plate 6a is provided so as to separate the upper side and the lower side, the heat convection of the glass substrate above the heating plate 6a is almost lower than the heating plate 6a. Not transmitted.

なお、発熱板6aよりも上側における熱対流も、該上側
の部分が発熱板6aによって浅く区切られていること、及
び水平方向の温度分布が均一であることから、極めて微
弱なものであり、ガラスバッチ3の不均一な溶解やガラ
ス素地の露出等の事態はひき起こすことはない。
The heat convection above the heating plate 6a is also extremely weak because the upper portion is shallowly separated by the heating plate 6a and the temperature distribution in the horizontal direction is uniform. The situation such as uneven melting of the batch 3 and exposure of the glass substrate does not occur.

このようなことから、このガラス溶融炉によればガラ
スバッチを均質に溶解し、泡や未溶解物を含まない清澄
なガラス素地を確実に製造することが可能となるのであ
る。
For this reason, according to this glass melting furnace, the glass batch can be uniformly melted, and a clear glass base material free of bubbles and undissolved substances can be reliably produced.

第1図及び第2図に示す実施例では、板状の発熱板6a
の開口7が円形の例を示したが、開口7の形状等は特に
制限されず、発熱体の発熱板6aの全面にわたって、発熱
量が均一となり、かつガラス素地4の流下が妨げられな
いものであれば、開口の形状,個数,配置等において、
他の様々な態様を採ることができる。また、発熱板は1
枚に限らず、2枚以上を多段に設けることもできる。
In the embodiment shown in FIGS. 1 and 2, the plate-like heating plate 6a
An example in which the opening 7 is circular is shown, but the shape of the opening 7 is not particularly limited, and the amount of heat generated is uniform over the entire surface of the heating plate 6a of the heating element and the flow of the glass substrate 4 is not hindered. Then, in the shape, number, arrangement, etc. of the openings,
Various other aspects can be taken. The heating plate is 1
Not limited to two sheets, two or more sheets can be provided in multiple stages.

なお、抵抗発熱体を設置する位置は、ガラス素地4内
のできるだけ上方でバッチ層3に近いことが好ましい
が、あまりにバッチ層3に近い場合には、未溶融ガラス
及び/又は未清澄のガラスが発熱体の開口を通り抜けて
炉の底部に流下する。従って、発熱体の位置(発熱体を
複数段設ける場合には最下段の発熱体の位置)は、その
位置においてガラスは完全に溶解され、未溶融物及び泡
を含まないガラスとなるような位置にするのが好まし
い。
The position where the resistance heating element is installed is preferably as close to the batch layer 3 as possible as high as possible in the glass substrate 4, but if it is too close to the batch layer 3, unmelted glass and / or unfinished glass may be It flows down through the opening of the heating element to the bottom of the furnace. Therefore, the position of the heating element (the position of the lowermost heating element in the case where a plurality of heating elements are provided) is such that the glass is completely melted at that position and the glass is free from unmelted matter and bubbles. It is preferred that

通常の場合、発熱体は、バッチ層の下方3〜40cm程度
の位置に設置するのが好ましい。
In a normal case, the heating element is preferably installed at a position of about 3 to 40 cm below the batch layer.

[発明の効果] 以上の通り、本発明のガラス溶融炉によれば、高品質
のガラスを効率的に確実かつ安定に製造することができ
る。
[Effects of the Invention] As described above, according to the glass melting furnace of the present invention, high-quality glass can be produced efficiently, reliably and stably.

また、本発明のガラス溶融炉は、どのような種類のガ
ラスに対してもほぼ同じ条件で適用することが可能であ
る。即ち、前述のように、ガラスのジュール熱を用いる
従来の電気溶融炉では、ガラスの電気抵抗値に応じて、
つまり溶融するガラスの種類によって、電極間の距離
や、電極の配置又は印加する電圧等を変えることが必要
であるが、本発明のガラス溶融炉は、どのような種類ガ
ラスに対しても汎用的に用いることができる。
Further, the glass melting furnace of the present invention can be applied to almost any kind of glass under almost the same conditions. That is, as described above, in a conventional electric melting furnace using Joule heat of glass, according to the electric resistance value of glass,
In other words, it is necessary to change the distance between the electrodes, the arrangement of the electrodes, the applied voltage, and the like, depending on the type of glass to be melted. Can be used.

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

第1図は本発明の一実施例を示すガラス溶融炉の縦断面
図、第2図は第1図のII−II線に沿う断面図、第3図は
従来の竪型ガラス溶融炉の縦断面図である。 1……原料投入口、 2……ガラス素地出口(スロート)、 3……バッチ層、4……ガラス素地、 5……電極棒、6……発熱体、 6a……発熱板。
1 is a longitudinal sectional view of a glass melting furnace showing one embodiment of the present invention, FIG. 2 is a sectional view taken along the line II-II of FIG. 1, and FIG. 3 is a longitudinal section of a conventional vertical glass melting furnace. FIG. 1. Material input port 2. Glass base outlet (throat) 3. Batch layer 4. Glass base 5. Electrode 6. Heating element 6a Heating plate.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】最上部に原料投入部を有し、最下部にガラ
ス素地出口を備え、ガラス素地に浸漬する少くとも1つ
のレベルに、当該レベルにおける炉の水平断面のほぼ全
領域にわたって抵抗発熱体を設けた竪型のガラス溶融炉
において、前記発熱体は、複数の開口が均一に分散して
設けられた板状の発熱体であり、該開口の直径をD、隣
接する開口同芯の中心間距離をP、板状発熱体の最も長
い対角線の長さをLとしたとき、 D>1mm D/L<0.5 及び、 D/P>0.1 の関係を満足することを特徴とするガラス溶融炉。
An apparatus having a raw material charging section at the top, a glass base outlet at the bottom, and at least one level of immersion in the glass base, at least one level of resistance heating over substantially the entire horizontal cross section of the furnace at that level. In a vertical glass melting furnace provided with a body, the heating element is a plate-shaped heating element provided with a plurality of openings uniformly distributed, the diameter of the openings is D, and the adjacent openings are concentric. Glass melting characterized by satisfying the following relations: D> 1 mm D / L <0.5 and D / P> 0.1, where P is the center-to-center distance and L is the longest diagonal of the plate-shaped heating element. Furnace.
JP1020321A 1989-01-30 1989-01-30 Glass melting furnace Expired - Lifetime JP2615966B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1020321A JP2615966B2 (en) 1989-01-30 1989-01-30 Glass melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1020321A JP2615966B2 (en) 1989-01-30 1989-01-30 Glass melting furnace

Publications (2)

Publication Number Publication Date
JPH02199029A JPH02199029A (en) 1990-08-07
JP2615966B2 true JP2615966B2 (en) 1997-06-04

Family

ID=12023865

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1020321A Expired - Lifetime JP2615966B2 (en) 1989-01-30 1989-01-30 Glass melting furnace

Country Status (1)

Country Link
JP (1) JP2615966B2 (en)

Also Published As

Publication number Publication date
JPH02199029A (en) 1990-08-07

Similar Documents

Publication Publication Date Title
TW200925127A (en) Method and apparatus for controlling the level of a molten material in a glass manufacturing system
WO2012132473A1 (en) Glass substrate production method
JP3116400B2 (en) Glass base homogenization method
JP2570350B2 (en) Glass melting furnace
US3305340A (en) Method and apparatus for generating currents in molten glass
KR20190078631A (en) Apparatus and method for forming a glass article
JPS63500937A (en) Forefurnace for transporting molten glass
KR102759901B1 (en) Apparatus and method for producing glass ribbons
JP7058641B2 (en) Glass article forming device and method
JP4673275B2 (en) Method for producing sheet glass by fusion downdraw method
US4906272A (en) Furnace for fining molten glass
CN111032584B (en) Method for producing glass article and melting furnace
US4227909A (en) Electric forehearth and method of melting therein
US3492107A (en) Method and apparatus for producing float glass utilizing electrically resistive refractory confining walls
JP2615966B2 (en) Glass melting furnace
RU2382739C1 (en) Method and device for tapping molten glass from discharge channels
JP5075395B2 (en) Method for producing flat glass, especially float glass, which tends to become glass ceramic
CN101921051A (en) Glass electric melting furnace
US4246432A (en) Method and apparatus for melting frits for inorganic oxidic surface coatings by electric resistance heating
US4737966A (en) Electric melter for high electrical resistivity glass materials
JP5192100B2 (en) Manufacturing method of glass substrate
JPH0891848A (en) Vertical glass fusing furnace
US3997316A (en) Use of crossed electrode pairs in a glassmaking furnace
US3806396A (en) Control of flow of glass to a glass ribbon being drawn
TWI530464B (en) Molten glass guide