JPH07157316A - Method for promoting change of body for glass smelting furnace - Google Patents
Method for promoting change of body for glass smelting furnaceInfo
- Publication number
- JPH07157316A JPH07157316A JP5338908A JP33890893A JPH07157316A JP H07157316 A JPH07157316 A JP H07157316A JP 5338908 A JP5338908 A JP 5338908A JP 33890893 A JP33890893 A JP 33890893A JP H07157316 A JPH07157316 A JP H07157316A
- Authority
- JP
- Japan
- Prior art keywords
- glass
- section
- melting
- ton
- feeders
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B7/00—Distributors 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
- C03B7/02—Forehearths, i.e. feeder channels
-
- 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
- C03B5/02—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture in electric furnaces, e.g. by dielectric heating
- C03B5/027—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture in electric furnaces, e.g. by dielectric heating by passing an electric current between electrodes immersed in the glass bath, i.e. by direct resistance heating
- C03B5/03—Tank furnaces
-
- 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
- C03B5/04—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture in tank furnaces
-
- 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
- C03B5/173—Apparatus for changing the composition of the molten glass in glass furnaces, e.g. for colouring the molten glass
-
- 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
- C03B5/18—Stirring devices; Homogenisation
- C03B5/187—Stirring devices; Homogenisation with moving elements
-
- 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
- C03B5/235—Heating the glass
- C03B5/2353—Heating the glass by combustion with pure oxygen or oxygen-enriched air, e.g. using oxy-fuel burners or oxygen lances
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Glass Melting And Manufacturing (AREA)
- Glass Compositions (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、素地替え(組成、色)
用のガラス溶解炉において、電気ブースター、スターラ
ーを設置し、高品質を維持しながら短期間で素地替え完
了を目的とするものである。FIELD OF THE INVENTION The present invention is for changing ground (composition, color).
In the glass melting furnace for industrial use, an electric booster and a stirrer are installed, and the purpose is to complete the material replacement in a short period while maintaining high quality.
【0002】[0002]
【従来の技術】従来、ガラス溶融窯における溶融ガラス
の素地替え(組成替えあるいは色替えを含む)を行う方
法としては、ドレアンドフィル法(素地抜き法とも呼ば
れる)と呼ばれる窯のボトムから古いガラスの大部分を
抜いて新たな成形に移る方法と、トランジッションチェ
ンジ法(押し出し法とも呼ばれる)と呼ばれる溶融部へ
新たなガラス原料を投入、溶融し、古い溶融ガラス素地
を作業部、フィーダーを経て順次流出させつつ素地替え
を行う方法が行われてきた。前者は、ブラックから白へ
の色替えなど極端な変更の際に時折行われるのみで、後
者が一般的であった。後者の場合には、溶融ガラス素地
の置換促進のために溶融部、作業部、フィーダーの各部
分の温度を上げる等の手段が講じられてきた。また、ガ
ラス溶融炉において、色素地のガラス製品を生産する時
には、ボトムの温度が下り易い為に、フリントガラス炉
より比較的浅い構造(例えば、1000m/m前後)と
して更にボトム温度維持の目的で電気ブースターを設置
することが一般に行われてきた。2. Description of the Related Art Conventionally, as a method for changing the base material (including composition change or color change) of molten glass in a glass melting kiln, the old glass from the bottom of the kiln called the Dreand-fill method (also called unbleaching method) The method of pulling out most of the material and moving to a new molding, and the new glass raw material is put into the melting part called the transition change method (also called extrusion method) and melted, the old molten glass base material is sequentially passed through the working part and the feeder. There has been a method of replacing the ground while draining it. The former was only performed occasionally at the time of extreme changes such as color change from black to white, and the latter was common. In the latter case, measures such as raising the temperature of each of the melting section, working section and feeder have been taken in order to promote the replacement of the molten glass base material. In addition, when a dyed glass product is produced in a glass melting furnace, the temperature of the bottom tends to drop, so that the structure is relatively shallower than the flint glass furnace (for example, around 1000 m / m) for the purpose of further maintaining the bottom temperature. It has been common practice to install electric boosters.
【0003】しかし、このような従来の方法による素地
替えでは、均質化は窯内のガラスの自然対流まかせであ
り、均質性をコントロールできていないので素地替えの
スピードアップをはかるために変更幅を大きくすると組
成の異なるガラスが混じり合い「組成ムラ」あるいは
「色ムラ」と称される製品欠点を発生させていた。ま
た、場合によっては作業部内の溶融ガラス素地の置換が
遅れ、残留ガラス素地が素地替えの後半に少しずつ流出
して上記同様の「組成ムラ」あるいは「色ムラ」が生じ
ていた。そのため、素地替えについては、製品欠点であ
る色ムラ、組成ムラ(コード)が発生しない範囲で段階
的に目的の色調(組成)まで変更している。しかし、こ
の方法では、ゆっくりと順次段階を追って変更しなけれ
ば上記欠点が発生してしまうので、非常に時間を要して
いた。However, in such a conventional method of changing the substrate, homogenization is a natural convection of the glass in the kiln, and since the homogeneity cannot be controlled, the range of change is increased in order to speed up the substrate change. When it is increased, glass having different compositions are mixed with each other to cause a product defect called "composition unevenness" or "color unevenness". Further, in some cases, the replacement of the molten glass base material in the working section was delayed, and the residual glass base material gradually flowed out in the latter half of the replacement of the base material, causing the same "composition unevenness" or "color unevenness" as described above. Therefore, in changing the substrate, the target color tone (composition) is gradually changed within a range in which the product defects such as color unevenness and composition unevenness (code) do not occur. However, in this method, the above-mentioned drawbacks would occur unless the change was made slowly and step by step. Therefore, it took a very long time.
【0004】[0004]
【発明が解決しようとする課題】本発明は、上記問題点
を解決し、高品質に保ちながら、短期間で素地替えを完
了することができるものである。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems and is capable of completing the material replacement in a short period while maintaining high quality.
【0005】[0005]
【課題を解決するための手段】本発明は、溶融部と作業
部とフィーダーを有するガラス溶融窯において(ガラス
引上げ量(トン/日)/窯ガラス保有量(トン))>1
(ここで窯ガラス保有量とは溶融部と作業部とフィーダ
ーの溶融ガラスの合計量をいう。)となるように、溶融
部に設けられた複数の電気ブースター及び/又は酸素バ
ーナーセットと、すべてのフィーダーに設けられた攪拌
装置によって強制的にガラス引上げ量及びガラスの均質
性を向上させたことを特徴とするものである。According to the present invention, a glass melting furnace having a melting part, a working part and a feeder (glass pulling amount (ton / day) / ceramic glass holding amount (ton))> 1
(Here, the amount of kiln glass held is the total amount of molten glass in the melting section, working section and feeder.) So that all of the electric boosters and / or oxygen burner sets installed in the melting section The glass pulling amount and the homogeneity of the glass are forcibly improved by the stirring device provided in the feeder.
【0006】本発明をするに至った経過について説明す
る。溶融炉の素地替え期間は窯の保有量に対してどれだ
けの溶融ガラスを流したかでほぼ決まることが分かって
いる。そこで、その短縮を行う為には、(最大ガラス流
出量(トン/日))/(窯ガラス保有量(トン))を最
大にすることが重要であると考えた。この値は一般には
0.6〜0.8程度であり1を越えること通常考えられ
ない。言い換えるなら、それ以上引き上げると、窯を傷
めて窯寿命が短くなるあるいは素地替え中の品質が著し
くおちる、電気ブースターのコストアップが避けられな
いなどの理由から行われてこなかった。しかし、本願で
は逆に1より大きくすることを前提として技術を追求し
ていった。これを行う方法として考えられるものを次に
挙げる。 (1) スピードアップ(ガラス引上げ量を増大させ、
(ガラス引上げ量(トン/日)/窯ガラス保有量(ト
ン))を増大させる。)の目的の構成変更 (1)− 色替え用の電気ブースターを設置する。 従来、電気ブースターはコストが高く、ボトム温度維持
の為に最小限使うと言う方式が一般的であったが、これ
を最大限まで使用する。 (1)− 酸素バーナー加熱によりガラス溶融能力を
上げる。 (2) 組成ムラ(色ムラ)防止の目的の構成変更 (2)− 全フィーダーに攪拌装置を設置する。 素地替えステップを大幅に変更しても色ムラ、コード等
が出ないようにすることができる。The process leading to the present invention will be described. It has been known that the period for replacing the material in the melting furnace is almost determined by how much molten glass is flown relative to the amount held in the kiln. Therefore, it was considered important to maximize the (maximum glass outflow rate (ton / day)) / (ceramic glass holding amount (ton)) in order to shorten it. This value is generally about 0.6 to 0.8, and it is usually not considered that it exceeds 1. In other words, if it is raised further, the kiln will be damaged and the life of the kiln will be shortened, or the quality of the kiln will be significantly deteriorated during the replacement of the material, and the cost of the electric booster will be unavoidably increased. However, in the present application, conversely, the technology was pursued on the premise that the value was made larger than 1. Here are some possible ways to do this: (1) Speed up (increasing the amount of glass pulled,
(Glass pulling amount (ton / day) / ceramic glass holding amount (ton)) is increased. ) Change the objective configuration (1) -Install an electric booster for color change. Conventionally, an electric booster is high in cost, and it is common to use a minimum to maintain the bottom temperature, but this is used to the maximum. (1)-Glass melting ability is increased by heating with an oxygen burner. (2) Change in composition for the purpose of preventing composition unevenness (color unevenness) (2) -Install a stirring device on all feeders. Even if the substrate replacement step is changed significantly, it is possible to prevent color unevenness and codes from appearing.
【0007】そこで、このうち(1)の方法について検
討を重ねていった。まずの電気ブースターは、本来、
溶解炉で溶融されているガラス中に電極を設置し、電流
を流して溶解能力のアップをはかる装置である。使用す
る目的としては、オイル燃焼に対して熱効率が高い、引
上げ付加変動に対し対応が容易である、温度の低い部分
に対し局部加熱が可能であるなどの特徴から引上げ量ア
ップの為に用いられている。電極材料は本願では、特に
限定するものではないが、モリブデンが多くの面で好ま
しく、白金、酸化スズ、黒鉛なども用いられることもあ
る。この電気ブースターを、本願発明では、素地替え促
進の目的で複数設けることで、非常に高い効果が生じる
ことを見いだした。設置する位置としては、効率の面か
ら考えて底から電極を挿入することが望ましいが、側面
からでも良い。ここで、電極の挿入は、煉瓦ブロックに
孔をあけ、そこから差し込めばよいので、稼働中でも可
能であり、後からでも設置することができるものであ
る。又、の酸素バーナーセットによる溶融能力アップ
による方法でも引上げ量を増大させることは可能であ
る。Therefore, the method (1) was repeatedly examined. The first electric booster was originally
This is a device that installs an electrode in glass that is melted in a melting furnace and applies an electric current to increase the melting capacity. The purpose of use is to increase the pulling amount because of its features such as high thermal efficiency for oil combustion, easy response to additional pulling fluctuations, and local heating for low temperature parts. ing. In the present application, the electrode material is not particularly limited, but molybdenum is preferable in many respects, and platinum, tin oxide, graphite, etc. may be used. In the present invention, it has been found that providing a plurality of electric boosters for the purpose of accelerating the replacement of the material produces a very high effect. Regarding the position of installation, it is desirable to insert the electrode from the bottom in terms of efficiency, but it may be from the side. Here, the electrode can be inserted by making a hole in the brick block and inserting from there, so that it can be installed even during operation and can be installed later. Also, the pulling amount can be increased by the method of increasing the melting capacity by the oxygen burner set.
【0008】さらに全フィーダーに攪拌装置を設置すれ
ば、素地替え促進には非常に効果が大きいことが分かっ
た。自然対流のみによる均質性をアップする為の手段と
して全てのフォアハースに最低2列以上のスターラー又
はパドラーをー設置して均質性(色ムラ、組成ムラ)の
コントロールを図る。これによりスピードアップによる
デメリットである均質性劣化を防止できる。更に変更幅
を大きくとっても均質性(色ムラ、組成ムラ)は保たれ
るので、色替え促進が期待できる。しかし、(1)、
(2)の方法を単独使用しても各々の効果はあるが、
(1)のみでは、スピードアップをはかる分ガラスの溶
融時間が短くなるので、均質化不足となることがわかっ
た。一方で(2)のみでは色ムラは減少するもののスピ
ードアップは少なく、(1)+(2)によって(1)の
均質化不足を(2)によって補い、スピードアップ、組
成ムラ(色ムラ)の両面が解決した。更に(1)+
(2)によって変更幅を大きくすることができるので時
間短縮が一層可能となり、(1)+(2)による相乗効
果が生まれた。そして、これらによって素地替え変更を
目的の組成(あるいは色)に置換するまでに、最初から
変更倍率を高くしていくことができ、その結果、素地替
え期間を短縮できる。例えば、色替えの時、当初着色剤
を目的色の2倍未満の量を加えて段階をおって替えてい
たものが、目的色の4倍量の着色剤を当初投入して着色
を早める事が可能となる。Further, it has been found that if a stirring device is installed in all the feeders, it is very effective in accelerating the replacement of the substrate. As a means to improve homogeneity only by natural convection, at least two rows of stirrers or padlers are installed on all forehearths to control homogeneity (color unevenness, composition unevenness). As a result, deterioration of homogeneity, which is a disadvantage due to speedup, can be prevented. Furthermore, since the uniformity (color unevenness, composition unevenness) is maintained even if the change range is made large, it is expected that color change is promoted. However, (1),
Even if the method of (2) is used alone, each effect is obtained,
It has been found that the homogenization is insufficient because only (1) shortens the melting time of the glass for speeding up. On the other hand, with (2) alone, color unevenness is reduced, but speedup is small. With (1) + (2), the lack of homogenization in (1) is supplemented by (2), resulting in speedup and compositional unevenness (color unevenness). Both sides resolved. Further (1) +
Since the change range can be increased by (2), the time can be further shortened, and the synergistic effect of (1) + (2) is created. Then, the change magnification can be increased from the beginning until the change of the material replacement is replaced with the desired composition (or color), and as a result, the material replacement period can be shortened. For example, at the time of color change, the colorant was initially added in an amount less than twice the target color and changed in stages, but the colorant should be added four times the target color to accelerate the coloring. Is possible.
【0009】[0009]
【実施例】本発明を実施例に従って、さらに詳しく説明
する。図1は、本発明の実施態様を示すものであり、1
がガラス溶融窯であり、溶融窯1は溶融部2、作業部
3、フィーダー4から構成されている。溶融部2内へ投
入されたガラス原料は図示していない加熱手段(バーナ
ー等)によって溶融され、その溶融ガラスは続いてスロ
ート5より順次作業部3内へ送り込まれるようになって
いる。ここで、溶融部2には、複数の電気ブースター6
が設置されており(図では20か所)、溶融部2の局部
加熱、ガラス対流の増大が行われることになる。また、
フィーダー4には、それぞれ4本のスターラーが2列に
わたって設置されており、素地替え期間中強制的に攪拌
されることになる。そして、通常の方法に従って、ガラ
ス製品成形機へと供給されることとなる。このように、
電気ブースター6と攪拌装置7を併用することによって
ガラス溶融窯1全体にわたってガラス素地の置換が促進
されることとなり、従来の方法に比べて残留ガラス素地
による組成ムラ、色ムラの発生を短時間で抑えることが
でき、素地替えに必要な期間を短くすることができるの
である。EXAMPLES The present invention will be described in more detail with reference to examples. FIG. 1 shows an embodiment of the present invention.
Is a glass melting furnace, and the melting furnace 1 is composed of a melting section 2, a working section 3, and a feeder 4. The glass raw material charged into the melting part 2 is melted by a heating means (burner or the like) not shown, and the molten glass is successively fed into the working part 3 from the throat 5. Here, in the melting part 2, a plurality of electric boosters 6 are provided.
Are installed (at 20 places in the figure), and local heating of the melting part 2 and increase of glass convection will be performed. Also,
Four stirrers are installed in each of the feeders 4 in two rows, and they are forcibly agitated during the material replacement period. Then, it is supplied to the glass product molding machine according to a usual method. in this way,
By using the electric booster 6 and the stirrer 7 together, the replacement of the glass base material is promoted throughout the glass melting furnace 1, and the composition unevenness and the color unevenness due to the residual glass base material are generated in a shorter time than the conventional method. Therefore, it is possible to reduce the time required for changing the substrate.
【0010】以下に本願発明の実施例を記載する。 (実施例1)容量235トンのガラス保有量を有するガ
ラス溶融窯において、電気ブースターを20用意し、そ
れぞれ上記の図1の配置にて側面から電極(いずれもモ
リブデン電極)を挿入し、2000kwの電力で加熱を
行った。また、同時に3つのフィーダーにてそれぞれ4
本2列に配置されたスターラーによる攪拌を行った。な
お、比較例として電気ブースター及びスターラーを用い
ずに同じ保有量のガラス溶融窯で素地替えを行った。Examples of the present invention will be described below. (Example 1) In a glass melting furnace having a glass holding capacity of 235 tons, 20 electric boosters were prepared, and electrodes (both molybdenum electrodes) were inserted from the side faces in the arrangement shown in FIG. Heating was performed with electric power. At the same time, 4 in each of 3 feeders
Stirring was performed with a stirrer arranged in two rows. As a comparative example, the material was replaced with the same amount of glass melting furnace without using the electric booster and the stirrer.
【0011】その結果、1日のガラス引上げ量はそれぞ
れ180トン/日、240トン/日となり、素地替えが
完了した。即ち、(最大ガラス引上げ量(トン/日))
/(窯ガラス保有量(トン))の値は、比較例が0.7
7であるのに対して、実施例は1.02と大きく値が上
がった。素地替えのスピードとしては33%アップする
ことができた。As a result, the daily glass pulling amounts were 180 tons / day and 240 tons / day, respectively, and the replacement of the substrate was completed. That is, (maximum glass pulling amount (ton / day))
The value of / (ceramic glass possession amount (ton)) is 0.7 in the comparative example.
7, the value was significantly increased to 1.02 in the example. We were able to increase the speed of changing the substrate by 33%.
【0012】(実施例2)上記と同じ窯、方法にてフリ
ントガラスからグリーンガラスへ色替えを行った。比較
例では、着色剤倍率を標準に対して1.4倍〜1.3〜
1.2〜1.1〜1.0の5段階のステップで変化させ
ていたものが、実施例では標準に対して4.0〜2.0
〜1.5〜1.0の4段階のステップで完了し、着色時
間の短縮化をはかることができた。実際の色替え時間
は、比較例が32時間かかったのに対して、実施例で
は、15時間で色替えを終えることができた。また、色
ムラによる製品欠点が実施例では発生せずに、良品が生
産できるようになったことも確認された。(Example 2) The color was changed from flint glass to green glass by the same kiln and method as above. In the comparative example, the colorant magnification is 1.4 times to 1.3 times the standard.
What was changed in 5 steps of 1.2 to 1.1 to 1.0 is 4.0 to 2.0 with respect to the standard in the embodiment.
It was completed in four steps of ~ 1.5 to 1.0, and the coloring time could be shortened. The actual color change time was 32 hours in the comparative example, whereas in the example, the color change was completed in 15 hours. It was also confirmed that product defects due to color unevenness did not occur in the examples and good products could be produced.
【0013】(実施例3)SiO2 73%、CaO12
%、Na2 O13%のガラスからSiO2 73%、Ca
O11%、Na2 O14%のガラスへの組成変更を上記
と同様の窯にて従来のものと比較を行った。結果は、C
aO→Na2 O置換1%を実施するのに従来、組成ムラ
(コード)の危険がある為、3ステップに分け各々4日
間安定させてから次のステップへ進み合計12日間かけ
て変更していたものが、本実施例では、1回の変更で完
了することができた。(Example 3) SiO 2 73%, CaO 12
%, Na 2 O 13% glass to SiO 2 73%, Ca
The composition was changed to a glass containing 11% of O and 14% of Na 2 O in the same kiln as above to compare with the conventional one. The result is C
Since there is a risk of composition unevenness (code) in carrying out aO → Na 2 O substitution of 1%, it is divided into 3 steps and stabilized for 4 days each, then proceed to the next step and change over a total of 12 days. However, in the present embodiment, it could be completed with one change.
【0014】[0014]
【発明の効果】本発明によれば、素地替えステップを大
幅に変更しても色ムラ、コード等が発生せず、高品質を
維持したままで短期間で素地替えが可能となったもので
ある。また、付帯的な効果として、通常時の品質アップ
も十分に期待できる。よって、本願発明は、従来の欠点
を解消し、上記効果を有するものであるので、産業にお
いて十分に寄与することができるものである。EFFECTS OF THE INVENTION According to the present invention, even if the substrate replacement step is significantly changed, color unevenness, codes, etc. do not occur, and it is possible to replace the substrate in a short period while maintaining high quality. is there. In addition, as an additional effect, quality improvement in normal times can be expected sufficiently. Therefore, the present invention solves the conventional drawbacks and has the above-mentioned effects, and thus can sufficiently contribute to the industry.
【図1】本発明の実施態様を表す断面図である。FIG. 1 is a cross-sectional view showing an embodiment of the present invention.
1 ガラス溶融窯 6 電気ブース
ター 2 溶融部 7 攪拌装置 3 作業部 4 フィーダー1 Glass Melting Kiln 6 Electric Booster 2 Melting Section 7 Stirrer 3 Working Section 4 Feeder
Claims (1)
ラス溶融窯において(ガラス引上げ量(トン/日)/窯
ガラス保有量(トン))>1(ここで窯ガラス保有量と
は溶融部と作業部とフィーダーの溶融ガラスの合計量を
いう。)となるように、溶融部に設けられた複数の電気
ブースター及び/又は酸素バーナーセットと、すべての
フィーダーに設けられた攪拌装置によって強制的にガラ
ス引上げ量及びガラスの均質性を向上させたことを特徴
とするガラス溶融窯の素地替え促進方法。1. A glass melting furnace having a melting section, a working section and a feeder (glass pulling amount (ton / day) / ceramic glass holding amount (ton))> 1 (where, the kiln glass holding amount is the melting portion). The total amount of molten glass in the working part and the feeder) is forced by the plurality of electric boosters and / or oxygen burner sets provided in the melting part and the stirring devices provided in all the feeders. A method for accelerating replacement of a material in a glass melting kiln, characterized in that the amount of glass pulled and the homogeneity of the glass are improved.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5338908A JPH07157316A (en) | 1993-12-02 | 1993-12-02 | Method for promoting change of body for glass smelting furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5338908A JPH07157316A (en) | 1993-12-02 | 1993-12-02 | Method for promoting change of body for glass smelting furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07157316A true JPH07157316A (en) | 1995-06-20 |
Family
ID=18322479
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5338908A Pending JPH07157316A (en) | 1993-12-02 | 1993-12-02 | Method for promoting change of body for glass smelting furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07157316A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100358542B1 (en) * | 1996-01-26 | 2002-12-18 | 아사히 가라스 가부시키가이샤 | Plunger for gob feeder |
KR100355550B1 (en) * | 1998-12-09 | 2003-01-29 | 한국전기초자 주식회사 | Glass Melting Furnace |
JP2020522455A (en) * | 2017-06-06 | 2020-07-30 | コーニング インコーポレイテッド | Readjustment method for glass manufacturing system |
JP2021535058A (en) * | 2018-08-22 | 2021-12-16 | コーニング インコーポレイテッド | Manufacturing method of glass articles |
WO2022255040A1 (en) * | 2021-05-31 | 2022-12-08 | 日本電気硝子株式会社 | Method for producing glass article |
WO2022255295A1 (en) * | 2021-06-01 | 2022-12-08 | 日本電気硝子株式会社 | Method for producing glass article |
CN116395937A (en) * | 2023-04-04 | 2023-07-07 | 蚌埠凯盛玻璃有限公司 | Quick color changing process for glass |
-
1993
- 1993-12-02 JP JP5338908A patent/JPH07157316A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100358542B1 (en) * | 1996-01-26 | 2002-12-18 | 아사히 가라스 가부시키가이샤 | Plunger for gob feeder |
KR100355550B1 (en) * | 1998-12-09 | 2003-01-29 | 한국전기초자 주식회사 | Glass Melting Furnace |
JP2020522455A (en) * | 2017-06-06 | 2020-07-30 | コーニング インコーポレイテッド | Readjustment method for glass manufacturing system |
JP2021535058A (en) * | 2018-08-22 | 2021-12-16 | コーニング インコーポレイテッド | Manufacturing method of glass articles |
WO2022255040A1 (en) * | 2021-05-31 | 2022-12-08 | 日本電気硝子株式会社 | Method for producing glass article |
WO2022255295A1 (en) * | 2021-06-01 | 2022-12-08 | 日本電気硝子株式会社 | Method for producing glass article |
CN116395937A (en) * | 2023-04-04 | 2023-07-07 | 蚌埠凯盛玻璃有限公司 | Quick color changing process for glass |
CN116395937B (en) * | 2023-04-04 | 2023-09-01 | 蚌埠凯盛玻璃有限公司 | Quick color changing process for glass |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1953023A (en) | Method and apparatus for making glass | |
US8196432B2 (en) | Furnace with series-arranged baths for producing glass compounds having a low degree of unmelted material | |
JP2006312584A (en) | Glass-fiber forming composition | |
JPH07157316A (en) | Method for promoting change of body for glass smelting furnace | |
CN1040569A (en) | Make the method and apparatus of mineral wool | |
EA015723B1 (en) | A process for manufacturing objects from red copper glass | |
KR20020029415A (en) | An apparatus and method for producing colored glass | |
CN108409107A (en) | A kind of manufacturing method and device of the high consistency optical glass of high uniformity | |
DE3206588C2 (en) | ||
US4427429A (en) | Method for the opalization of glass | |
CN109761478B (en) | Method for changing color of float glass | |
CN209619170U (en) | A kind of U-shaped glass producing system of mass colouring | |
PL163149B1 (en) | Method of melting glass and furnace therefor | |
CN109231816A (en) | A kind of glass substrate and preparation method thereof can be used for LTPS | |
CN115124219B (en) | Method for eliminating glass defects | |
DE2917433A1 (en) | METHOD FOR ELECTROMELTING GLASS AND DEVICE FOR CARRYING OUT THE METHOD | |
JP4447327B2 (en) | Selective glass batch formation method that improves melting efficiency and reduces gross segregation of glass batch components | |
CN108395075A (en) | Molding expects pipe for inhibiting glass ingredient to volatilize and forming method | |
DE2846496C2 (en) | ||
CN103113016B (en) | Quartz crucible for founding lanthanide series optical glass and method for founding lanthanide series optical glass slag clinker | |
DE1596754B2 (en) | METHOD OF MANUFACTURING AN AMBER-COLORED GLASS WITH PREDESTINED COLOR TYPE USING A BURN FURNACE SLACK | |
RU2250198C2 (en) | Glass melting in bath furnace | |
KR101342137B1 (en) | Alumina cement using molten blast furnace slag and high temperature ladle slag and method for manufacturing the same | |
SU1666549A1 (en) | Method of producing low-phosphorus manganese slag | |
CN102153286A (en) | Smelting method for blending rare mineral into crystal, colored glaze or glass |