JPH1111954A - Glass melting method - Google Patents
Glass melting methodInfo
- Publication number
- JPH1111954A JPH1111954A JP9159619A JP15961997A JPH1111954A JP H1111954 A JPH1111954 A JP H1111954A JP 9159619 A JP9159619 A JP 9159619A JP 15961997 A JP15961997 A JP 15961997A JP H1111954 A JPH1111954 A JP H1111954A
- Authority
- JP
- Japan
- Prior art keywords
- melting
- glass
- oxygen
- combustion flame
- raw material
- 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
- 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
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B3/00—Charging the melting furnaces
- C03B3/02—Charging the melting furnaces combined with preheating, premelting or pretreating the glass-making ingredients, pellets or cullet
- C03B3/026—Charging the melting furnaces combined with preheating, premelting or pretreating the glass-making ingredients, pellets or cullet by charging the ingredients into a flame, through a burner or equivalent heating means used to heat the melting furnace
-
- 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
-
- 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
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
(57)【要約】
【課題】 ガラスやセラミックスを加熱溶解するための
バーナーの燃焼火炎が有するエネルギーを積極的に利用
してガラスの溶解効率の向上を図る。
【解決手段】 ガラス原料からなる粉粒体を酸素バーナ
ーの燃焼火炎中に供給し、燃焼火炎からの輻射伝熱と対
流伝熱とにより加熱して溶解しながら炉内に供給する。
(57) [Summary] [PROBLEMS] To improve the melting efficiency of glass by positively utilizing the energy of the combustion flame of a burner for heating and melting glass and ceramics. SOLUTION: Granules made of a glass raw material are supplied into a combustion flame of an oxygen burner, and supplied into a furnace while being heated and melted by radiant heat transfer and convective heat transfer from the combustion flame.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ガラスの溶解方法
に関し、詳しくは、バーナーの燃焼火炎を熱源としてガ
ラスやセラミックスを加熱溶解するための溶解炉におけ
る溶解効率を向上させる方法に関する。The present invention relates to a method for melting glass, and more particularly to a method for improving melting efficiency in a melting furnace for heating and melting glass and ceramics using a combustion flame of a burner as a heat source.
【0002】[0002]
【従来の技術】従来から、ガラス製造業界では、ガラス
溶解炉の省エネルギー化の達成に向けて各種の対策を実
施し、一応の成果を収めてきている。例えば、溶解炉の
保温・断熱性の向上や侵入空気の低減、排熱回収率を高
めるための蓄熱室の大型化やチェッカー煉瓦の材質・形
状の改善、原料へのカレット添加率の増加等が行われ、
これらによってエネルギー原単位を従来に比べて約20
%低減させている。さらに、現在では、排ガスでガラス
原料を予熱することによって熱回収効率を更に向上させ
ようとしており、また、バーナーとして従来の空気バー
ナーに代えて酸素バーナーを使用することにより、排ガ
ス熱損の低減,窒素酸化物(NOX)の低減,火炎温度
の上昇による溶解効率の向上等を図ることも実用化され
つつある。2. Description of the Related Art Conventionally, in the glass manufacturing industry, various measures have been taken to achieve energy saving in glass melting furnaces, and tentative results have been obtained. For example, improving the heat retention and heat insulation of the melting furnace, reducing the amount of invading air, increasing the size of the heat storage chamber, improving the material and shape of the checker brick, and increasing the cullet addition rate to the raw materials, etc. Done,
As a result, the energy intensity can be reduced by about 20
%. Furthermore, at present, heat recovery efficiency is being further improved by preheating glass raw materials with exhaust gas, and by using an oxygen burner instead of a conventional air burner as a burner, the heat loss of the exhaust gas can be reduced. Attempts are being made to reduce nitrogen oxides (NOX) and improve the melting efficiency by raising the flame temperature.
【0003】[0003]
【発明が解決しようとする課題】しかし、ガラス溶解炉
では、主に、バーナーの燃焼火炎からの輻射伝熱及び燃
焼火炎によって加熱された炉内壁からの輻射伝熱によっ
てガラス原料を加熱溶解しているため、他の工業炉に比
較して熱効率が低いという問題があった。However, in the glass melting furnace, the glass material is heated and melted mainly by radiant heat transfer from the combustion flame of the burner and radiant heat transfer from the furnace inner wall heated by the combustion flame. Therefore, there is a problem that the thermal efficiency is lower than other industrial furnaces.
【0004】そこで本発明は、酸素バーナーの燃焼火炎
が有するエネルギーを積極的に利用して熱効率を高め、
ガラスの溶解効率を向上させることができるガラスの溶
解方法を提供することを目的としている。Accordingly, the present invention is to improve the thermal efficiency by positively utilizing the energy of the combustion flame of the oxygen burner,
It is an object of the present invention to provide a glass melting method capable of improving the glass melting efficiency.
【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、本発明のガラスの溶解方法は、支燃性ガスとして酸
素あるいは酸素富化空気を用いる酸素バーナーの燃焼火
炎を熱源としてガラス原料を加熱溶解するガラスの溶解
方法において、ガラス原料又はカレット又はこれらの混
合原料の少なくとも一部を含む粉粒体を前記酸素バーナ
ーの燃焼火炎中に供給し、該燃焼火炎中で加熱溶解させ
てガラス溶解炉内に供給することを特徴としている。In order to achieve the above object, a method for melting glass according to the present invention comprises heating a glass raw material by using a combustion flame of an oxygen burner that uses oxygen or oxygen-enriched air as a combustion supporting gas as a heat source. In a method for melting glass to be melted, a glass material or a cullet or a powder containing at least a part of a mixed material thereof is supplied into a combustion flame of the oxygen burner, and is heated and melted in the combustion flame to form a glass melting furnace. It is characterized by being supplied inside.
【0006】また、本発明のガラスの溶解方法の他の構
成は、溶解室の前後に、原料投入部と清澄室とをそれぞ
れ連設するとともに、前記溶解室に、ガラス原料を加熱
溶解するための燃焼火炎を生成する複数本の酸素バーナ
ーを備えたガラス溶解炉でガラスを溶解する方法におい
て、前記溶解室の原料投入部側に設置した少なくとも一
つの酸素バーナーの燃焼火炎中に、ガラス原料又はカレ
ット又はこれらの混合原料の少なくとも一部を含む粉粒
体を供給し、該粉粒体を燃焼火炎中で加熱溶解させて前
記溶解室内に供給することを特徴としている。Further, another configuration of the glass melting method of the present invention is such that a raw material charging section and a fining chamber are respectively connected before and after the melting chamber, and the glass raw material is heated and melted in the melting chamber. In the method of melting glass in a glass melting furnace having a plurality of oxygen burners for generating a combustion flame, during the combustion flame of at least one oxygen burner installed on the raw material charging section side of the melting chamber, the glass raw material or A cullet or a powder containing at least a part of a mixed material thereof is supplied, and the powder is heated and melted in a combustion flame and supplied into the melting chamber.
【0007】さらに、本発明は、前記支燃性ガスの酸素
濃度が50%以上であること、前記粉粒体を、キャリア
ガスによって前記酸素バーナーに供給することを特徴と
している。Furthermore, the present invention is characterized in that the oxygen concentration of the combustion supporting gas is 50% or more, and the powder is supplied to the oxygen burner by a carrier gas.
【0008】[0008]
【発明の実施の形態】図1及び図2は、本発明方法を適
用したガラス溶解炉の一形態例を示すもので、図1はガ
ラス溶解炉の横断面図、図2は同じく縦断面図である。
このガラス溶解炉は、6本の酸素バーナー1a〜1fを
備えた溶解室2と、該溶解室2の前後に連設した原料投
入部3と清澄室4とからなるもので、原料投入部3から
投入されたガラス原料やカレットは、溶解室2において
酸素バーナー1a〜1fの燃焼火炎からの輻射伝熱及び
燃焼火炎によって加熱された炉内壁からの輻射伝熱によ
って加熱溶解された後、清澄室4で均質化されて取出さ
れる。1 and 2 show an embodiment of a glass melting furnace to which the method of the present invention is applied. FIG. 1 is a cross-sectional view of the glass melting furnace, and FIG. It is.
This glass melting furnace comprises a melting chamber 2 provided with six oxygen burners 1a to 1f, a raw material charging section 3 and a refining chamber 4 connected to the front and rear of the melting chamber 2, and a raw material charging section 3 is provided. Is heated and melted by the radiant heat transfer from the combustion flame of the oxygen burners 1a to 1f and the radiant heat transfer from the furnace inner wall heated by the combustion flame in the melting chamber 2, and then the refining chamber. 4. Homogenized and removed.
【0009】前記6本の酸素バーナー1a〜1fの内、
原料投入部3に近い側に設置されている2本の酸素バー
ナー1a,1bには、プロパンガスや重油等を供給する
燃料供給路5と、酸素や酸素富化空気を供給する支燃性
ガス供給路6と、ガラス原料又はカレット又はこれらの
混合原料の少なくとも一部を含む粉粒体を供給する原料
粉粒体供給路7とが設けられており、清澄室4側の4本
のバーナー1c〜1fには、燃料供給路5と支燃性ガス
供給路6とが設けられている。Of the six oxygen burners 1a to 1f,
The two oxygen burners 1a and 1b installed on the side close to the raw material charging section 3 have a fuel supply passage 5 for supplying propane gas, heavy oil, and the like, and a combustion supporting gas for supplying oxygen and oxygen-enriched air. A supply path 6 and a raw material powder supply path 7 for supplying a powder material containing at least a part of a glass raw material or cullet or a mixed material thereof are provided, and four burners 1 c on the refining chamber 4 side are provided. 1 to 1f, a fuel supply path 5 and a supporting gas supply path 6 are provided.
【0010】すなわち、原料投入部側の酸素バーナー1
a,1bには、燃料供給路5からの燃料と支燃性ガス供
給路6からの支燃性ガスとの燃焼により生成する火炎中
に、ガラス原料からなる粉粒体を供給するガラス原料供
給手段である原料粉粒体供給路7が設けられており、原
料粉粒体供給路7から燃焼火炎中に供給した粉粒体を、
燃焼火炎からの輻射伝熱と対流伝熱とにより加熱して溶
解するように形成している。That is, the oxygen burner 1 on the raw material charging section side
Reference numerals a and 1b denote glass material supply for supplying powdery granules made of glass material into a flame generated by the combustion of the fuel from the fuel supply passage 5 and the supporting gas from the supporting gas supply passage 6. A raw material powder supply path 7 as a means is provided, and the powder supplied into the combustion flame from the raw material powder supply path 7 is
It is formed so as to be heated and melted by radiant heat transfer from the combustion flame and convective heat transfer.
【0011】このように、ガラス原料からなる粉粒体を
燃焼火炎中に供給して加熱溶解することにより、酸素バ
ーナー1a,1bの燃焼火炎のエネルギーを、従来の酸
素バーナーと同様の輻射伝熱等によってガラス原料や炉
内壁を加熱するためだけでなく、ガラス原料を直接的に
加熱溶解することに利用できる。これにより、ガラスの
溶解効率を大幅に向上させることができ、溶解炉単位受
熱面積当たりのガラス溶解量が向上し、生産性の向上が
図れる。また、純酸素を支燃性ガスとして用いた場合
は、従来に比べて窒素酸化物(NOX)の発生量の低減
も図れる。As described above, by supplying the powdery granules made of the glass raw material into the combustion flame and melting them by heating, the energy of the combustion flame of the oxygen burners 1a and 1b can be reduced by the same radiant heat transfer as the conventional oxygen burner. It can be used not only for heating the glass raw material and the inner wall of the furnace, but also for directly heating and melting the glass raw material. Thereby, the melting efficiency of glass can be greatly improved, the amount of glass melt per unit heat receiving area of the melting furnace is improved, and productivity can be improved. In addition, when pure oxygen is used as the combustion supporting gas, the amount of generated nitrogen oxides (NOX) can be reduced as compared with the related art.
【0012】さらに、抜熱量が大きい原料投入部側の酸
素バーナー1a,1bに原料粉粒体を供給して溶解する
ことにより、溶解効率の向上効果を大きくすることがで
き、ガラスが溶解した状態の清澄室側には、原料粉粒体
供給路7を持たない通常の酸素バーナー1c〜1fを設
けたことにより、ガラスの清澄効果に悪影響を及ぼすこ
とがなくなる。Further, by supplying and melting the raw material particles to the oxygen burners 1a and 1b on the side of the raw material input section having a large heat removal amount, the effect of improving the melting efficiency can be increased, and the state in which the glass is melted can be obtained. By providing ordinary oxygen burners 1c to 1f without the raw material powder supply path 7 on the fining chamber side, the fining effect of the glass is not adversely affected.
【0013】なお、原料粉粒体供給路7を設けた酸素バ
ーナー1a,1bは、周知の粉体処理用の酸素バーナー
を用いることが可能であり、例えば、中心に粉粒体流
路、その外側に燃料流路、最も外側に支燃性ガス流路を
備えた三重管構造の酸素バーナーを用いることができ
る。また、原料粉粒体供給路を持たない通常のバーナー
ノズルの近傍に、酸素バーナーとは別に原料粉粒体を噴
出するノズルを設け、該ノズルから燃焼火炎中に原料粉
粒体を供給するようにしてもよい。原料粉粒体の搬送
は、機械的な手段で行ってもよいが、適宜なキャリアガ
ス、例えば酸素ガスや空気によって原料粉粒体を搬送す
ることにより容易に行うことができる。As the oxygen burners 1a and 1b provided with the raw material powder supply passage 7, a known oxygen burner for powder processing can be used. An oxygen burner having a triple pipe structure having a fuel flow path on the outside and a combustion supporting gas flow path on the outermost side can be used. In addition, in the vicinity of a normal burner nozzle having no raw material powder supply path, a nozzle for ejecting the raw material powder separately from the oxygen burner is provided, and the raw material powder is supplied from the nozzle into the combustion flame. It may be. The transfer of the raw material particles may be performed by mechanical means, but can be easily performed by transferring the raw material particles with an appropriate carrier gas, for example, oxygen gas or air.
【0014】原料粉粒体としては、ガラス原料又はカレ
ット又はこれらの混合原料を破砕機等で数mm以下、好
ましくは、平均粒径10μm〜1mm程度に破砕したも
のを用いることができる。このとき、粉粒体が大き過ぎ
ると、燃焼火炎中への供給が困難となるだけでなく、重
力による落下で燃焼火炎中での滞留時間が短くなって十
分な温度まで加熱できないことがある。逆に粉粒体が小
さ過ぎると、飛散してしまうおそれがある。また、酸素
バーナーに粉粒体として供給するガラス原料の量は、溶
解量の全量であってもよく、一部であってもよい。As the raw material powder, a glass raw material, a cullet or a mixture of these materials obtained by crushing with a crusher or the like to several mm or less, preferably about 10 μm to 1 mm in average particle size can be used. At this time, if the powder is too large, not only the supply into the combustion flame becomes difficult, but also the residence time in the combustion flame becomes short due to the drop due to gravity, so that the powder may not be heated to a sufficient temperature. Conversely, if the powder is too small, it may be scattered. Further, the amount of the glass raw material to be supplied to the oxygen burner as powders may be the whole amount of the dissolved amount or a part thereof.
【0015】前記酸素バーナーに供給する燃料は、気
体,液体,固体のいずれでもよく、支燃性ガスとして
は、大気の酸素濃度以上に酸素を含むガスを用いること
ができるが、いずれにしても、生成する燃焼火炎中でガ
ラス原料からなる粉粒体の全量乃至その大半を溶解させ
ることができる温度や速度,火炎長を有する燃焼火炎を
形成させることが必要である。支燃性ガス中の酸素濃度
は、酸素供給設備の状況や窒素酸化物の発生状況等を考
慮して設定すればよいが、酸素濃度50%以上のガスを
用いることが好ましい。例えば、図3は、燃料としてプ
ロパンを用いたときの支燃性ガス中の酸素濃度に対する
溶解歩留と断熱理論最高火炎温度との関係を示すもの
で、図から明らかなように、大気の酸素濃度から50%
程度までは、酸素濃度の上昇に伴う溶解歩留及び火炎温
度の向上率が大きく、酸素濃度が50%以上になると、
両者の向上効果が小さくなることがわかる。特に、溶解
歩留は、酸素濃度50%から先はほとんど上昇していな
い。したがって、酸素濃度50%以上のガス(酸素富化
空気,低純酸素,純酸素)を支燃性ガスとして用いるこ
とにより、高い溶解歩留でガラスの溶解操作を行うこと
ができる。The fuel supplied to the oxygen burner may be any of gas, liquid, and solid. As the supporting gas, a gas containing oxygen at a concentration higher than the oxygen concentration of the atmosphere can be used. It is necessary to form a combustion flame having a temperature, a speed, and a flame length capable of dissolving the whole or most of the powdery granules made of the glass raw material in the generated combustion flame. The oxygen concentration in the supporting gas may be set in consideration of the state of the oxygen supply equipment, the state of generation of nitrogen oxides, and the like, and it is preferable to use a gas having an oxygen concentration of 50% or more. For example, FIG. 3 shows the relationship between the dissolution yield and the adiabatic theoretical maximum flame temperature with respect to the oxygen concentration in the combustion supporting gas when propane is used as the fuel. 50% from concentration
Up to the extent, the rate of improvement in the melting yield and flame temperature with the increase in oxygen concentration is large, and when the oxygen concentration becomes 50% or more,
It turns out that the improvement effect of both becomes small. In particular, the dissolution yield hardly increased beyond the oxygen concentration of 50%. Therefore, by using a gas having an oxygen concentration of 50% or more (oxygen-enriched air, low-pure oxygen, pure oxygen) as the supporting gas, the glass can be melted at a high melting yield.
【0016】[0016]
【発明の効果】以上説明したように、本発明は、酸素バ
ーナーの燃焼火炎の強制対流熱伝達を積極的に利用して
ガラス原料を溶解しながら溶解炉中に供給するので、ガ
ラスの溶解効率を大幅に向上させることが可能となり、
溶解炉単位受熱面積当たりのガラス溶解量が向上し、生
産性の向上が図れる。As described above, according to the present invention, the glass raw material is fed into the melting furnace while melting the glass raw material by positively utilizing the forced convection heat transfer of the combustion flame of the oxygen burner. Can be greatly improved,
The amount of glass melting per unit heat receiving area of the melting furnace is improved, and the productivity can be improved.
【図1】 本発明の一形態例を示すガラス溶解炉の横断
面図である。FIG. 1 is a cross-sectional view of a glass melting furnace showing one embodiment of the present invention.
【図2】 同じく縦断面図である。FIG. 2 is a longitudinal sectional view of the same.
【図3】 酸素濃度に対する溶解歩留と火炎温度との関
係を示す図である。FIG. 3 is a graph showing a relationship between a melting yield and a flame temperature with respect to an oxygen concentration.
1a〜1f…酸素バーナー、2…溶解室、3…原料投入
部、4…清澄室、5…燃料供給路、6…支燃性ガス供給
路、7…原料粉粒体供給路1a to 1f: oxygen burner, 2: melting chamber, 3: raw material charging section, 4: fining chamber, 5: fuel supply path, 6: flammable gas supply path, 7: raw material powder supply path
───────────────────────────────────────────────────── フロントページの続き (72)発明者 萩原 義之 東京都港区西新橋1−16−7 日本酸素株 式会社内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Yoshiyuki Hagiwara Nippon Sanso Co., Ltd. 1-16-7 Nishi-Shimbashi, Minato-ku, Tokyo
Claims (4)
空気を用いる酸素バーナーの燃焼火炎を熱源としてガラ
ス原料を加熱溶解するガラスの溶解方法において、ガラ
ス原料又はカレット又はこれらの混合原料の少なくとも
一部を含む粉粒体を前記酸素バーナーの燃焼火炎中に供
給し、該燃焼火炎中で加熱溶解させてガラス溶解炉内に
供給することを特徴とするガラスの溶解方法。1. A glass melting method in which a glass material is heated and melted by using a combustion flame of an oxygen burner which uses oxygen or oxygen-enriched air as a combustion supporting gas, wherein at least one of a glass material, a cullet, and a mixed material thereof is used. A method for melting glass, comprising: supplying a particulate material containing a portion to a combustion flame of the oxygen burner; heating and melting the combustion particle in the combustion flame;
をそれぞれ連設するとともに、前記溶解室に、ガラス原
料を加熱溶解するための燃焼火炎を生成する複数本の酸
素バーナーを備えたガラス溶解炉でガラスを溶解する方
法において、前記溶解室の原料投入部側に設置した少な
くとも一つの酸素バーナーの燃焼火炎中に、ガラス原料
又はカレット又はこれらの混合原料の少なくとも一部を
含む粉粒体を供給し、該粉粒体を燃焼火炎中で加熱溶解
させて前記溶解室内に供給することを特徴とするガラス
の溶解方法。2. A raw material charging section and a refining chamber are respectively connected before and after the melting chamber, and a plurality of oxygen burners for generating a combustion flame for heating and melting the glass raw material are provided in the melting chamber. In a method of melting glass in a glass melting furnace, a powder containing at least a part of a glass material or a cullet or a mixed material thereof in a combustion flame of at least one oxygen burner installed on a material charging portion side of the melting chamber. A method for melting glass, comprising supplying granules, heating and melting the granules in a combustion flame, and supplying the melted particles into the melting chamber.
上であることを特徴とする請求項1又は2記載のガラス
の溶解方法。3. The method for melting glass according to claim 1, wherein the combustion supporting gas has an oxygen concentration of 50% or more.
記酸素バーナーに供給することを特徴とする請求項1又
は2記載のガラスの溶解方法。4. The method for melting glass according to claim 1, wherein the powder is supplied to the oxygen burner by a carrier gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9159619A JPH1111954A (en) | 1997-06-17 | 1997-06-17 | Glass melting method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9159619A JPH1111954A (en) | 1997-06-17 | 1997-06-17 | Glass melting method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH1111954A true JPH1111954A (en) | 1999-01-19 |
Family
ID=15697683
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9159619A Pending JPH1111954A (en) | 1997-06-17 | 1997-06-17 | Glass melting method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH1111954A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004520490A (en) * | 2001-04-27 | 2004-07-08 | ジュピター オキシジェン コーポレーション | Furnace and oxygen-supplying combustion system using the furnace, combustion method, aluminum recovery method, aluminum separation method, aluminum recovery furnace or waste incinerator, waste incineration method, and method of controlling the furnace |
| JP2006199549A (en) * | 2005-01-21 | 2006-08-03 | Tokyo Institute Of Technology | Glass raw material melting method and melting apparatus, and glass manufacturing apparatus |
| JP2007153676A (en) * | 2005-12-06 | 2007-06-21 | Daido Steel Co Ltd | Pre-melting method for glass raw materials |
| JP2007297239A (en) * | 2006-04-28 | 2007-11-15 | Tokyo Institute Of Technology | Glass raw material melting method, melting apparatus, and glass manufacturing apparatus |
| WO2011001902A1 (en) * | 2009-07-01 | 2011-01-06 | 旭硝子株式会社 | Glass melting furnace, process for producing molten glass, apparatus for manufacturing glass products, and process for manufacturing glass products |
| WO2011004851A1 (en) * | 2009-07-08 | 2011-01-13 | 旭硝子株式会社 | Glass melting furnace, molten glass manufacturing method, glass product manufacturing device, and glass product manufacturing method |
| JP2013170740A (en) * | 2012-02-20 | 2013-09-02 | Osaka Gas Co Ltd | Combustion device for glass melting furnace |
-
1997
- 1997-06-17 JP JP9159619A patent/JPH1111954A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004520490A (en) * | 2001-04-27 | 2004-07-08 | ジュピター オキシジェン コーポレーション | Furnace and oxygen-supplying combustion system using the furnace, combustion method, aluminum recovery method, aluminum separation method, aluminum recovery furnace or waste incinerator, waste incineration method, and method of controlling the furnace |
| JP2006199549A (en) * | 2005-01-21 | 2006-08-03 | Tokyo Institute Of Technology | Glass raw material melting method and melting apparatus, and glass manufacturing apparatus |
| JP2007153676A (en) * | 2005-12-06 | 2007-06-21 | Daido Steel Co Ltd | Pre-melting method for glass raw materials |
| JP2007297239A (en) * | 2006-04-28 | 2007-11-15 | Tokyo Institute Of Technology | Glass raw material melting method, melting apparatus, and glass manufacturing apparatus |
| WO2011001902A1 (en) * | 2009-07-01 | 2011-01-06 | 旭硝子株式会社 | Glass melting furnace, process for producing molten glass, apparatus for manufacturing glass products, and process for manufacturing glass products |
| JP5585581B2 (en) * | 2009-07-01 | 2014-09-10 | 旭硝子株式会社 | Glass melting furnace, molten glass manufacturing method, glass product manufacturing apparatus, and glass product manufacturing method |
| WO2011004851A1 (en) * | 2009-07-08 | 2011-01-13 | 旭硝子株式会社 | Glass melting furnace, molten glass manufacturing method, glass product manufacturing device, and glass product manufacturing method |
| JP5717054B2 (en) * | 2009-07-08 | 2015-05-13 | 旭硝子株式会社 | Glass melting furnace, molten glass manufacturing method, glass product manufacturing apparatus, and glass product manufacturing method |
| JP2013170740A (en) * | 2012-02-20 | 2013-09-02 | Osaka Gas Co Ltd | Combustion device for glass melting furnace |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1206180C (en) | Method for manufacturing molten glass and glass melting furnace | |
| JP4922735B2 (en) | Method for improving the performance of a glass melting furnace using a ceiling-mounted oxygen burner | |
| KR100595339B1 (en) | Method for melting glass | |
| JP3280884B2 (en) | Method for producing glass with reduced emissions and refractory corrosion | |
| JPH05116952A (en) | Glass melting apparatus having oxygen combustion burner in front wall | |
| JPH0597444A (en) | Technique of using auxiliary oxygen burner in cross flame type regenerative furnace for melting glass | |
| JPH05139753A (en) | Ceiling mounting type auxiliary oxygen burner | |
| JP4565185B2 (en) | Glass raw material melting method and melting apparatus, and glass manufacturing apparatus | |
| MX2008012608A (en) | Method and apparatus for preheating glassmaking materials. | |
| TW201114701A (en) | Glass melting furnace, process for producing molten glass, apparatus for manufacturing glass products, and process for manufacturing glass products | |
| KR101479603B1 (en) | Dilution combustion | |
| US6354110B1 (en) | Enhanced heat transfer through controlled interaction of separate fuel-rich and fuel-lean flames in glass furnaces | |
| JPH1111953A (en) | Glass melting method and apparatus | |
| CN100467987C (en) | Combustion method in a furnace with porous walls | |
| JP4112650B2 (en) | A method for glass furnace conversion utilizing combustion with oxygen. | |
| CN213060636U (en) | Combustion system for glass kiln and glass kiln | |
| PL196002B1 (en) | Exhaust positioned at the downstream end of a glass melting furnace | |
| CN208566698U (en) | Fixed-end forces device | |
| CN106746501A (en) | Glass furnace | |
| JPS58500854A (en) | Method of manufacturing molten glass | |
| CN103596887B (en) | Glass melting furnace | |
| JPH0820183B2 (en) | Refractory molding method and lance for spraying granular exothermic oxide material | |
| JP2000281356A (en) | Operation method of glass melting furnace | |
| Hueber et al. | Selective Oxygen Enrichment Used to Reduce Fuel Consumption in an Endport Regenerative Glass Furnace–A Case History | |
| JPS62275030A (en) | Melting furnace for class |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20040601 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20061115 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20061121 |
|
| A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20070403 |