JPH0417538Y2 - - Google Patents

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Publication number
JPH0417538Y2
JPH0417538Y2 JP1987078700U JP7870087U JPH0417538Y2 JP H0417538 Y2 JPH0417538 Y2 JP H0417538Y2 JP 1987078700 U JP1987078700 U JP 1987078700U JP 7870087 U JP7870087 U JP 7870087U JP H0417538 Y2 JPH0417538 Y2 JP H0417538Y2
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JP
Japan
Prior art keywords
glass
melting
blow
chamber
melting tank
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
JP1987078700U
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Japanese (ja)
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JPS63192436U (en
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Priority to JP1987078700U priority Critical patent/JPH0417538Y2/ja
Publication of JPS63192436U publication Critical patent/JPS63192436U/ja
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Publication of JPH0417538Y2 publication Critical patent/JPH0417538Y2/ja
Expired legal-status Critical Current

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  • Glass Melting And Manufacturing (AREA)
  • Furnace Housings, Linings, Walls, And Ceilings (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案はガラス原料を溶融し、清澄された溶融
ガラスを成形工程へ送るサイド吹出式ガラス溶融
タンク窯の改良に関し、詳細には前記サイド吹出
式ガラス溶融タンク窯の溶融室のバツクウオール
から最終吹出部までの間において、該ガラス溶融
タンク窯の天井迫、吹出口柱部および上部側壁等
の内面に沿つて垂れ落下する本来めざしているガ
ラスとは異質の汚染した不純物組成物が溶融ガラ
ス中に浸入するのを防止する構造としたものであ
り、ことに板ガラス用サイド吹出式ガラス溶融タ
ンク窯に有用であつて、特に種々のサイド吹出式
原料溶融窯にも広く採用し得るものである。
[Detailed description of the invention] [Field of industrial application] The present invention relates to an improvement of a side-blowing type glass melting tank kiln that melts glass raw materials and sends the clarified molten glass to a forming process. During the period from the back wall of the melting chamber of the type glass melting tank kiln to the final blowing section, the glass that is originally targeted for dripping down along the inner surfaces of the ceiling abutment, blowing outlet column, upper side wall, etc. of the glass melting tank kiln. This is a structure that prevents foreign contaminated impurity compositions from entering the molten glass, and is particularly useful for side-blowing type glass melting tank kilns for flat glass. It can also be widely used in raw material melting furnaces.

〔従来の技術〕[Conventional technology]

通常サイド吹出式ガラス溶融タンク窯はガラス
原料を連続的に供給する投入口、両サイドからの
オイルバーナーの燃焼等による加熱で最高温度
1550℃前後に保持されガラス原料を溶解する溶融
室、溶融ガラス素地を清澄する清澄室、清澄ガラ
ス素地をさらに清澄しととのえる調整室およびガ
ラス素地を成形するための作業室等からなり、供
給するガラス原料と成形するために窯内から引き
出す溶融ガラス素地とをバランスさせ窯内のガラ
ス素地面の高さを実質的に一定の水準に保持して
いる。一般にはサイド吹出式ガラス溶融タンク窯
の内溶融室は天井迫が珪石レンガ、側壁、アゴ
瓦、種瓦等が電鋳ブロツクで構成されている。
Normally, a side-blowing type glass melting tank kiln has an inlet that continuously supplies glass raw materials, and reaches a maximum temperature due to heating by oil burner combustion from both sides.
It consists of a melting chamber that is maintained at around 1550℃ to melt glass raw materials, a fining chamber that refines the molten glass base, an adjustment chamber that further refines the clarified glass base, and a work room that molds the glass base. The height of the glass base surface inside the kiln is maintained at a substantially constant level by balancing the raw materials with the molten glass base material drawn from the kiln for molding. Generally, the melting chamber of a side-blowing glass melting tank kiln has a ceiling abutment made of silica brick, and side walls, jaw tiles, seed tiles, etc. made of electroformed blocks.

年々サイド吹出式ガラス溶融タンク窯は大容量
化し、高溶融能を要求され、出来るだけ高温で出
来るだけ多くガラス原料を溶融してしかも高均質
に清澄された溶融ガラス素地で成形ガラス製品に
リーム、フシあるいはデストーシヨン等の欠陥が
ないことが要求されている。
The capacity of side-blown glass melting tank kilns has increased year by year, and high melting capacity is required, so by melting as much glass raw material as possible at as high a temperature as possible and using a molten glass base that is highly homogeneous and refined, it is reamed into molded glass products. It is required that there be no defects such as sticks or destruction.

かようななかで、溶融室、ことにバツクウオー
ルから最終吹出部までの間では、有効に燃焼加熱
するためにガラス素地面以上の比較的高い空間を
もたせているので、大きい側壁面積が露出し、高
温な燃焼フレーム等苛酷な条件にさらされること
になり、一方、連続的に供給されるガラス原料に
も熱エネルギーが有効に働くよう例えば山状にう
ねをつけ表面積を増し、燃焼フレームを広く近ず
けて行くようにすること等もなされている。この
時燃焼フレームの流れによつて微細なガラス原料
の極く一部の粒子あるいはガス揮発物が上部空間
部に舞い上がり、前記溶融室の上部構造である天
井迫および上部側壁等に付着し化学反応し異質の
ガラス状物質となり、前記構造物を侵触すること
にもなつて天井迫、上部側壁等を伝つて垂れ、溶
融ガラス素地中に滴下落下し、溶融ガラス素地を
汚染し、作業室に到つても均質化されることなく
残り、成形ガラス製品に前述したような欠陥をも
たらす原因となるものである。
Under these circumstances, the melting chamber, especially between the back wall and the final blowout section, has a relatively high space above the glass base surface in order to effectively burn and heat, so a large side wall area is exposed. On the other hand, glass raw materials that are continuously supplied are exposed to harsh conditions such as high-temperature combustion flames, and so that the heat energy can be effectively applied to the continuously supplied glass raw materials. Efforts have also been made to move closer. At this time, due to the flow of the combustion flame, a very small part of the fine glass raw material particles or gas volatiles fly up into the upper space and adhere to the upper structure of the melting chamber, such as the ceiling abutments and upper side walls, causing a chemical reaction. It becomes a foreign glass-like substance that invades the structure, drips down the ceiling abutments, upper side walls, etc., drips into the molten glass base, contaminates the molten glass base, and reaches the work room. Even if the glass is heated, it remains without being homogenized and causes the defects mentioned above in the molded glass product.

さらに操業の初期においては、前記電鋳ブロツ
クが前述のように上部側壁として苛酷な条件にさ
らされると汗かき現象、すなわちブロツク中のガ
ラス状マトリツクスが湧き出し、前記現象を増長
するものである。
Further, in the early stages of operation, when the electroformed block is exposed to severe conditions as the upper side wall as described above, the sweating phenomenon, that is, the glassy matrix in the block springs out, aggravating the phenomenon.

このような本来目標とする溶融ガラス素地とは
異質の汚染物質がガラス溶融窯内の溶融ガラス素
地に混入するのを防止するため種々の工夫がなさ
れている。例えば実公昭49−16368号公報にはガ
ラス溶融タンクが記載されており、溶融ガラス室
を構成する下部側壁と天井に向つて上方に延びた
上部側壁とを有し、上部側壁の内面直下に段部を
設けて上部側壁が下部側壁に対して外方に引込め
てあり、段部の頂面上に溶融ガラスの表面と接す
る如く設けた冷却装置とを有するガラス溶融タン
クにおいて、冷却装置と接しかつ落下する不純物
を捕捉するため上部側壁直下に配設した捕捉面を
有する取外し可能の捕捉装置を配設したものが開
示されている等が知られている。
Various measures have been taken to prevent contaminants that are different from the intended molten glass base from entering the molten glass base in the glass melting furnace. For example, Japanese Utility Model Publication No. 49-16368 describes a glass melting tank, which has a lower side wall constituting a molten glass chamber and an upper side wall extending upward toward the ceiling, with a step immediately below the inner surface of the upper side wall. In a glass melting tank, the upper side wall is recessed outwardly with respect to the lower side wall, and the cooling device is provided on the top surface of the stepped portion so as to be in contact with the surface of the molten glass. In addition, a device is disclosed in which a removable trapping device having a trapping surface is disposed directly under the upper side wall in order to trap falling impurities.

〔考案が解決しようとする問題点〕[Problem that the invention attempts to solve]

前述したように従来の実公昭49−16368号公報
に記載されているものは、所謂種瓦の天端の溶融
ガラス素地面部に冷却ボツクスをセツトし、その
背後または斜め上面に取り出し可能に汚物捕捉装
置を配置したものであり、それ自体も複雑なだけ
でなく、その周囲の構造も複雑とならざるを得な
いものであり、また水冷ボツクス、汚物捕捉装置
の取り替え取り出し等の保守作業も困難性をとも
なうものであり、例えばアンダポートタイプの構
造のガラス溶融窯等には適用し難いものである。
As mentioned above, the conventional method described in Japanese Utility Model Publication No. 16368/1983 sets a cooling box on the molten glass base surface at the top of a so-called seed tile, and has a removable filth trap placed behind or diagonally above the cooling box. Not only is the equipment itself complicated, but the surrounding structure must also be complicated, and maintenance work such as replacing and removing the water cooling box and dirt trapping device is also difficult. Therefore, it is difficult to apply it to, for example, a glass melting furnace with an underport type structure.

〔問題点を解決するための手段〕[Means for solving problems]

本考案は従来のかかる欠点に鑑みてなしたもの
であつて、上部構造の最下部で上部側壁をささえ
ているアゴ瓦の上面部に溝状凹部を設け、該溝状
凹部を蓄熱室に連絡するようにする単純な構造に
より汚物を流動性のある状態を保持したまま、吹
出部床面を介して蓄熱室に極自然に流入するよう
にし、溶融室の溶融ガラス素地内に混入すること
を防止することができるサイド吹出式ガラス溶融
タンク窯を提供するものである。
The present invention was developed in view of the above drawbacks of the conventional technology, and includes providing a groove-like recess in the upper surface of the chin tile that supports the upper side wall at the lowest part of the upper structure, and connecting the groove-like recess to the heat storage chamber. The simple structure allows the waste to flow naturally into the heat storage chamber through the outlet floor while maintaining its fluidity, thereby preventing it from getting mixed into the molten glass base in the melting chamber. To provide a side-blowing type glass melting tank kiln that can prevent the above.

すなわち、本考案はサイド吹出式ガラス溶融タ
ンク窯の溶融室内のバツクウオールから最終吹出
部までの間において、該間の上部側壁ならびに各
吹出口柱部の内面直下に位置するアゴ瓦上面部分
に、溝状凹部を設け、かつ前記各吹出部床面の全
面ないし該床面の一部を、溶融室側から蓄熱室側
に向け下方に傾斜させ、前記溝状凹部と蓄熱室と
を連絡させたことを特徴とするサイド吹出式ガラ
ス溶融タンク窯を供給するものである。
That is, the present invention provides a side blow-out type glass melting tank kiln, between the back wall in the melting chamber and the final blow-out part, on the upper side wall in between and on the upper surface part of the jaw tile located directly under the inner surface of each blow-off outlet column. A groove-shaped recess is provided, and the entire or part of the floor surface of each blowout section is inclined downward from the melting chamber side toward the heat storage chamber side, so that the groove-shaped recess and the heat storage chamber are in communication with each other. The present invention provides a side-blowing type glass melting tank kiln characterized by the following.

ここで、サイド吹出式ガラス溶融タンク窯の溶
融室内のバツクウオールから最終吹出部までの間
としたのは、該間がサイド吹出式ガラス溶融タン
ク窯でも最高温度約1550℃前後と温度が高く、ガ
ラス原料が溶融するまでに粒子の飛散または揮発
物の発生が起りやすく、燃焼ガスがある等で耐火
物の浸触をはじめ汚物の発生がしやすいためであ
り、ガラス原料投入口内壁のバツクウオールから
最終吹出部までの範囲をいうものとするものであ
る。
Here, the reason for the distance from the back wall in the melting chamber of the side blowing type glass melting tank kiln to the final blowing part is that even in the side blowing type glass melting tank kiln, the maximum temperature is around 1550℃, which is high. This is because particles tend to scatter or volatile substances are generated before the glass raw material is melted, and the presence of combustion gas tends to cause dirt to come into contact with the refractory, and the back wall on the inner wall of the glass raw material inlet This refers to the range from the end to the final blowout section.

また例えば吹出部においては、前記溝状凹部を
吹出口柱部に沿つて設け、蓄熱室との連絡道であ
る吹出部床面全面ないしその床面の一部を溶融室
側から蓄熱室側に向け下方に傾斜させ流下した汚
物等の不純物を、極く自然に蓄熱室へ常時流入せ
しめて排除させるようにするものであり、前記傾
斜角度は3°以下とすることが好ましいものであ
る。
Further, for example, in the blowout section, the groove-like recess is provided along the blowout port column, and the entire floor surface or a part of the floor surface of the blowout section, which is a communication path with the heat storage chamber, is moved from the melting chamber side to the heat storage chamber side. Impurities such as filth flowing downward are allowed to flow into the heat storage chamber very naturally at all times and are removed, and it is preferable that the angle of inclination is 3° or less.

以下、本考案の実施例を図面に基づいて説明す
る。
Hereinafter, embodiments of the present invention will be described based on the drawings.

第1図は、サイド吹出式ガラス溶融タンク窯の
両サイドにある吹出部の斜視図であり、該ガラ
ス溶融タンク窯は通常、敷瓦2の端縁部に種瓦3
を立設して溶融ガラス素地がほぼ満量となるよう
その天端よりやや下げて溶融ガラス素地面(第2
図で示すメタルライン13)を一定に保持するよ
うにしている。該種瓦3の上にはアゴ瓦4があ
り、該アゴ瓦4に直接やや後方に引いて上部側壁
5が構築され、該上部側壁5と面一に吹出口柱6
および吹出口迫7を形成しており、該燃焼用加熱
空気を供給する吹出口部のアゴ瓦にはバーナータ
イル8が設けてあり、例えばオイルバーナー(図
示せず)によりオイルを噴霧し燃焼フレームによ
つて加熱するようになつており、前記上部側壁5
の上には溶融室全体を覆う天井迫9があり、これ
らの構成はそれぞれ外部を金物(図示せず)で支
持しているものである。またこの吹出部はサイ
ド吹出式ガラス溶融タンク窯によつて必ずしも個
数は一定ではないが板ガラスの窯では大体4〜8
個程度両サイドにそれぞれ配設しているのが一般
的である。またさらに図示していないが吹出部
の溶融室の外側には両サイドに蓄熱室があり、こ
の吹出部と連絡道で連絡されていて、その吹出
部床面10がある。
FIG. 1 is a perspective view of the blow-off parts 1 on both sides of a side blow-out type glass melting tank kiln.
The molten glass base surface (the second
The metal line 13) shown in the figure is kept constant. There is a chin tile 4 on top of the seed tile 3, and an upper side wall 5 is constructed extending directly slightly backward from the chin tile 4, and an air outlet pillar 6 is installed flush with the upper side wall 5.
A burner tile 8 is provided on the chin tile of the outlet part that supplies heated air for combustion, and for example, oil is sprayed by an oil burner (not shown) to form a combustion flame. The upper side wall 5
Above is a ceiling abutment 9 that covers the entire melting chamber, and each of these structures is supported externally by metal fittings (not shown). In addition, the number of blowing sections 1 is not necessarily constant depending on the side blowing type glass melting tank kiln, but in a plate glass kiln, there are approximately 4 to 8.
It is common to have about 1,000 pieces each on both sides. Furthermore, although not shown, the blowing section 1
There are heat storage chambers on both sides outside the melting chamber, which are connected to the blow-off section 1 through a communication path, and there is a floor surface 10 of the blow-off section.

本考案の溝状凹部11、ならびに該溝状凹部1
1を蓄熱室へ連絡する下方傾斜は、各吹出部
間の上部側壁5と吹出口柱6の一部の内面直下に
位置するアゴ瓦4の上面部に配設し、天井迫ある
いは上部側壁の汗かき現象およびガス原料のキヤ
リオーバー、揮発物の蒸気の凝縮反応物等より生
じる異質の汚物ガラス状溶融物が垂れ落下してく
るのを捕捉し、捕捉物を蓄熱室に極く自然に流入
させることによつて、溶融室内の溶融ガラス素地
中に流出しないようにすることができるものであ
る。
Groove-shaped recess 11 of the present invention and the groove-shaped recess 1
1 to the heat storage chamber is arranged on the upper surface of the chin tile 4 located directly under the inner surface of a part of the upper side wall 5 and the outlet pillar 6 between each outlet part 1 , and It captures the dripping of glass-like molten material, which is a foreign waste generated from sweating on the side walls, carryover of gas raw materials, condensation of volatile vapor, etc., and stores the captured material in a heat storage chamber very naturally. By allowing the molten glass to flow into the melting chamber, it is possible to prevent the molten glass from flowing into the molten glass base in the melting chamber.

第2図は第1図に示すA−A′箇所の部分断面
図であり、種瓦3、アゴ瓦4、上部側壁5と溶融
ガラス素地12、そのメタルライン13および溝
状凹部11の位置関係をより明確にしたものであ
る。
FIG. 2 is a partial cross-sectional view taken along the line A-A′ shown in FIG. is made clearer.

第3図は第1図に示すB−B′箇所の部分断面
図であり、吹出口柱6の前部に一部溝状凹部11
をまわり込んで設け、その奥側の端より溜つた異
質の汚物ガラス状溶融物を蓄熱室側へ常時極く自
然に流すためにα角度、好ましくは3°以下、最適
には1°程度吹出部床面10を傾斜させるようにし
たものである。なお前記吹出部床面10の傾斜は
一部もしくは全面のどちらでもよいが、あくまで
溝状凹部11につながつていることがかんじんで
ある。また前記吹出部床面10の傾斜角度を3°以
下としたのは3°を超えると燃焼時の吹き出し加熱
空気が上方に向つて流れるため、燃焼フレームが
スムーズに流れず、溶融能を悪化し、微細ガラス
原料のキヤリーオーバーを増長させる等の悪影響
をもたらす傾向となるからである。
FIG. 3 is a partial sectional view taken along the line B-B′ shown in FIG.
In order to constantly and naturally flow foreign waste and glass-like molten material that has accumulated from the back end of the The floor surface 10 is inclined. Incidentally, the slope of the blow-off section floor surface 10 may be either a partial slope or a full slope, but it is essential that the slope is connected to the groove-shaped recess 11. In addition, the inclination angle of the outlet floor 10 is set to 3 degrees or less because if it exceeds 3 degrees, the heated air blown out during combustion will flow upward, which will prevent the combustion flame from flowing smoothly and deteriorate the melting performance. This is because it tends to have an adverse effect such as increasing the carry over of fine glass raw materials.

〔考案の効果〕[Effect of idea]

前述したように、本考案によれば、サイド吹出
式ガラス溶融タンク窯の溶融室のバツクウオール
から最終吹出部までの間における上部側壁の内面
直下に沿つてアゴ瓦上面部に溝状凹部を配設し、
該溝状凹部と蓄熱室とを巧みに連絡したことによ
り、上部側壁等から伝わつて垂れ落下する異質汚
染ガラス状溶融物等が窯内の溶融ガラス素地に混
入することがなく自浄効果を有するので、成形ガ
ラス製品におけるフシ、リーム等の欠陥の発生が
極端に減少し、しかも窯の構築も複雑でなく、水
冷ボツクスを設ける必要もなく熱効率の低下ある
いはやつかいな加熱による汚物ガラスの流し出し
作業等もなくて目的を達成できるものである。
As described above, according to the present invention, a groove-like recess is arranged in the upper surface of the jaw tile along the inner surface of the upper side wall between the back wall and the final blowing part of the melting chamber of the side blowing type glass melting tank kiln. established,
By skillfully connecting the groove-shaped recess and the heat storage chamber, foreign contaminated glass-like molten material that drips down from the upper side wall, etc., does not mix into the molten glass base in the kiln, and has a self-cleaning effect. , the occurrence of defects such as rims and reams in molded glass products is extremely reduced, and the construction of the kiln is not complicated, and there is no need to install a water-cooled box, reducing thermal efficiency or pouring out waste glass due to difficult heating. You can achieve your purpose without it.

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

図面は本考案の一実施例を示すもので、第1図
はサイド吹出式ガラス溶融タンク窯の溶融室の吹
出部における斜視図、第2図は第1図に示すA−
A′部の部分断面図、第3図は同様に第1図に示
すB−B′部の部分断面図である。 ……吹出部、4……アゴ瓦、5……上部側
壁、6……吹出口柱、10……吹出部床面、11
……溝状凹部。
The drawings show an embodiment of the present invention, in which Fig. 1 is a perspective view of the blowing section of the melting chamber of a side-blowing type glass melting tank kiln, and Fig. 2 is a perspective view of the blow-off section of the melting chamber of a side-blowing type glass melting tank kiln.
FIG. 3 is a partial sectional view of section A', and FIG. 3 is a partial sectional view of section BB' shown in FIG. 1 ... Outlet part, 4... Chin tile, 5... Upper side wall, 6... Outlet pillar, 10... Outlet part floor surface, 11
...Groove-like recess.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] サイド吹出式ガラス溶融タンク窯の溶融室内の
バツクウオールから最終吹出部までの間におい
て、該間の上部側壁ならびに各吹出口柱部の内面
直下に位置するアゴ瓦上面部分に、溝状凹部を設
け、かつ前記各吹出部床面の全面ないし該床面の
一部を、溶融室側から蓄熱室側に向け下方に傾斜
させ、前記溝状凹部と蓄熱室とを連絡させたこと
を特徴とするサイド吹出式ガラス溶融タンク窯。
Between the back wall in the melting chamber of a side-blowing type glass melting tank kiln and the final blow-off section, a groove-like recess is provided in the upper side wall between the back wall and the top surface of the jaw tile located directly below the inner surface of each blow-out port column. , and the entire surface or a part of the floor surface of each of the blow-off parts is inclined downward from the melting chamber side toward the heat storage chamber side, and the groove-shaped recesses and the heat storage chamber are connected. Side-blown glass melting tank kiln.
JP1987078700U 1987-05-27 1987-05-27 Expired JPH0417538Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987078700U JPH0417538Y2 (en) 1987-05-27 1987-05-27

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987078700U JPH0417538Y2 (en) 1987-05-27 1987-05-27

Publications (2)

Publication Number Publication Date
JPS63192436U JPS63192436U (en) 1988-12-12
JPH0417538Y2 true JPH0417538Y2 (en) 1992-04-20

Family

ID=30927882

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987078700U Expired JPH0417538Y2 (en) 1987-05-27 1987-05-27

Country Status (1)

Country Link
JP (1) JPH0417538Y2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4648252B2 (en) * 2006-06-21 2011-03-09 Hoya株式会社 Glass melting apparatus, glass manufacturing method, and glass product manufacturing method
JP6576193B2 (en) * 2015-09-30 2019-09-18 Agcセラミックス株式会社 Electrocast refractory tax tone and melting kiln

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH031456Y2 (en) * 1986-01-29 1991-01-17

Also Published As

Publication number Publication date
JPS63192436U (en) 1988-12-12

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