JPS594632B2 - aluminum melting furnace - Google Patents
aluminum melting furnaceInfo
- Publication number
- JPS594632B2 JPS594632B2 JP11567579A JP11567579A JPS594632B2 JP S594632 B2 JPS594632 B2 JP S594632B2 JP 11567579 A JP11567579 A JP 11567579A JP 11567579 A JP11567579 A JP 11567579A JP S594632 B2 JPS594632 B2 JP S594632B2
- Authority
- JP
- Japan
- Prior art keywords
- aluminum
- furnace
- exhaust gas
- heat
- tube
- 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
Links
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- Manufacture And Refinement Of Metals (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
- Furnace Details (AREA)
Description
【発明の詳細な説明】
本発明は、無酸素状態にして酸化アルミニウムの生成を
防止できると共に熱効率を顕著に高めたアルミニウム溶
融炉に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an aluminum melting furnace that can prevent the formation of aluminum oxide in an oxygen-free state and has significantly improved thermal efficiency.
従来のアルミニウム溶融炉は炉内に燃焼装置により重油
を噴射燃焼させ、その輻射熱でアルミニウム地金を溶融
し、次いで湯口からの溶融アルミニウムの取出しに伴っ
て断続的に炉内に供給されるアルミニウム地金を重油の
燃焼の輻射熱と溶融アルミニウムの伝熱とで溶融する構
造であり、燃焼火炎が溶融アルミニウムに直接接触する
こととなる為、約2.5係の酸化アルミニウムか生成さ
れることとなっており、従って例えば月産1000トン
の炉では25トンもの酸化アルミニウムが生成されてし
まいその廃棄を余儀なくされ美大な費用の損失をみすみ
す蒙っている。Conventional aluminum melting furnaces inject and burn heavy oil into the furnace using a combustion device, and use the radiant heat to melt the aluminum base metal.Then, as the molten aluminum is taken out from the sprue, the aluminum base metal is intermittently supplied into the furnace. It has a structure in which gold is melted by radiant heat from the combustion of heavy oil and heat transfer from molten aluminum, and since the combustion flame comes into direct contact with molten aluminum, aluminum oxide of approximately 2.5% is produced. Therefore, for example, in a furnace with a monthly production capacity of 1,000 tons, 25 tons of aluminum oxide are produced, which must be disposed of, resulting in a huge loss of costs.
他方、最近開発されているアルミニウム溶融炉には、炉
内に伝熱線を設け、この伝熱線の輻射熱と溶融アルミニ
ウムの伝熱とでアルミニウム地金を溶融する電気炉があ
るが、これはアルミニウム地金を炉内の当初の空気中の
酸素分だけ酸化し尽した後は無酸素状態でアルミニウム
地金を1融できるので酸化アルミニウムの生成量が非常
に少なく約0.3係に抑えられたとして業界に注目され
ているが、電力消費が非常に大きいという欠点があり、
ランニングコストの面を考えると設備することに難点が
ある。On the other hand, recently developed aluminum melting furnaces include electric furnaces that have heat transfer wires installed in the furnace and use the radiant heat of the heat transfer wires and the heat transfer of molten aluminum to melt the aluminum base metal. After the gold has been oxidized by the amount of oxygen in the initial air in the furnace, it is possible to melt one piece of aluminum in an oxygen-free state, so the amount of aluminum oxide produced is extremely small and can be suppressed to about 0.3%. Although it is attracting attention in the industry, it has the disadvantage of extremely high power consumption.
There are some difficulties in installing the equipment in terms of running costs.
また、従来のアルミニウム溶融炉は一般に排ガスを予熱
に利用する構成でないので熱効率が20係程度にしか上
らない。Further, since conventional aluminum melting furnaces are generally not configured to use exhaust gas for preheating, the thermal efficiency is only about 20 factors.
他の用途の炉においても排ガスを予熱に利用すると熱効
率を40係程度に高められ燃料消費量を半分にすること
ができる。Even in furnaces for other uses, if exhaust gas is used for preheating, the thermal efficiency can be increased to about 40 coefficients and fuel consumption can be halved.
でアルミニウム溶融炉においても予熱構造とすることが
強く要望されている。Therefore, there is a strong demand for a preheating structure in aluminum melting furnaces as well.
本発明は、炉内に放熱管を設けてこの管内で燃焼を行わ
せて炉内に供給されたアルミニウム地金を無酸素状態で
溶融して酸化アルミニウムの生成量を従来炉の約2.5
係から電気炉の0.3係に近づけるように大幅に低減で
きるガス燃焼式とすると共に、アルミ供給筒を予熱室と
した熱効率が高いアルミニウム溶融炉を提供するもので
ある。In the present invention, a heat dissipation tube is provided in the furnace, and the aluminum ingot supplied to the furnace is melted in an oxygen-free state by combustion within the tube, and the amount of aluminum oxide produced is approximately 2.5 that of the conventional furnace.
The purpose of the present invention is to provide an aluminum melting furnace that is of a gas combustion type that can significantly reduce the heat dissipation rate to approach that of an electric furnace at 0.3, and has a high thermal efficiency using an aluminum feed tube as a preheating chamber.
以下に、本発明のアルミニウム溶融炉の実施例を図面を
参照して説明する。Embodiments of the aluminum melting furnace of the present invention will be described below with reference to the drawings.
ケーシング1に耐熱ンンガあるいはセラミックファイバ
2をライニングして炉本体3が形成されている。A furnace body 3 is formed by lining a casing 1 with heat-resistant fibers or ceramic fibers 2.
この炉本体3は、炉床4が炉後部のアルミ供給筒5側が
高く、炉前部の湯口6側が低く設けられ、また炉内7の
輻射熱をアルミ供給筒5’に逃げないように遮断する下
り壁8が設けられ、炉本体3の後壁と炉床4とが曲率半
径の大きい滑らかな曲面で結ばれており、上記湯口6に
は湯栓9が施されている。In this furnace body 3, the hearth 4 is set high on the aluminum supply cylinder 5 side at the rear of the furnace and low on the sprue 6 side at the front of the furnace, and also blocks radiant heat in the furnace 7 from escaping to the aluminum supply cylinder 5'. A descending wall 8 is provided, and the rear wall of the furnace body 3 and the hearth 4 are connected by a smooth curved surface with a large radius of curvature, and the sprue 6 is provided with a hot water tap 9.
上記アルミ供給筒5より炉床4に落し込まれるアルミニ
ウム地金を無酸素状態で溶融する為に、燃焼装置10に
より管内にガスを噴射され燃焼する輻射熱で炉内に供給
されるアルミニウム地金を溶融し得、排ガスが上記アル
ミ供給・筒5に導かれる放熱管11が設けられている。In order to melt the aluminum ingot dropped into the hearth 4 from the aluminum supply tube 5 in an oxygen-free state, the combustion device 10 injects gas into the tube and uses the radiant heat of the combustion to melt the aluminum ingot fed into the furnace. A heat dissipation pipe 11 is provided which can be melted and through which exhaust gas is guided to the aluminum feed tube 5.
この放熱管11は1000℃位でも十分耐え得る高湿耐
熱性の材料から図示の如き直管又はU字状もしくは蛇行
状等の曲管とされ必要とされる熱容量に応じて1本又は
2本以上設けられている。The heat dissipation tube 11 is made of a high-humidity and heat-resistant material that can withstand temperatures of about 1000°C, and is made of a straight tube as shown in the figure or a curved tube in a U-shape or meandering shape, and may be one or two depending on the required heat capacity. The above are provided.
上記燃焼装置10は各放熱管11の炉外の一端に取付け
られ、ガス管12A及び元栓12Bを介してボンベ13
やタンク室等のガス供給源に接続されている。The combustion device 10 is attached to one end of each heat radiation pipe 11 outside the furnace, and is connected to the cylinder 13 through a gas pipe 12A and a main plug 12B.
It is connected to a gas supply source such as a gas tank or a tank room.
また各放熱管11の他端も炉外に突出しており、この端
部が排ガスヘッダー14に接続され、この排ガスヘッダ
ー14の端部がアルミ供給筒5に接続されているから上
述の如く各放熱管11からの排ガスがアルミ供給筒5に
導かれるように成っている。The other end of each heat radiation tube 11 also protrudes outside the furnace, and this end is connected to the exhaust gas header 14, and the end of this exhaust gas header 14 is connected to the aluminum supply tube 5. The exhaust gas from the pipe 11 is guided to the aluminum supply cylinder 5.
上記排ガスヘッダー14は本発明の必須の構成要件では
ない。The exhaust gas header 14 is not an essential component of the present invention.
例えば、燃焼装置10が図示の湯口6と同じ側に来るよ
うに各放熱管11を方向を変えて配設すると共に、炉本
体3の下り壁8に孔を設けた変形した構成とすれば、こ
の孔を通して各放熱管11からの排ガスを直接にアルミ
供給筒5に導くことができるから排ガスヘッダー14は
必要的でない。For example, if the heat dissipation pipes 11 are arranged in different directions so that the combustion device 10 is on the same side as the illustrated sprue 6, and a hole is provided in the descending wall 8 of the furnace body 3, a modified configuration is adopted. The exhaust gas header 14 is not necessary because the exhaust gas from each heat dissipation tube 11 can be directly guided to the aluminum supply cylinder 5 through this hole.
炉外の排ガスヘッダー14等には放熱防止の為断熱材1
5が被覆されている。Insulating material 1 is installed on the exhaust gas header 14 etc. outside the furnace to prevent heat radiation.
5 is coated.
上記燃焼装置10は放熱管11をアルミニウムの融点6
60℃より高い700℃から1000℃位の範囲で調整
可能に加熱し得る容量とされている。The combustion device 10 has a heat dissipation tube 11 made of aluminum with a melting point of 6
It has a capacity that can adjustably heat the temperature in the range of 700°C to 1000°C, which is higher than 60°C.
こうして炉内7に放熱管11を設け、この管内でガスを
噴射燃焼させるようにすると炉内7は無酸素状態となる
。In this way, the heat dissipation tube 11 is provided in the furnace 7, and when gas is injected and burned within this tube, the furnace interior 7 becomes anoxic.
なぜなら、炉内7に初期に存在する空気中の酸素分は酸
化アルミニウムの生成によって間もなく消尽し、アルミ
供給筒5の排ガス中の酸素分は炉内7が高圧側となって
いるから炉内Iへの拡散が行われ難いからである。This is because the oxygen content in the air that initially exists in the furnace 7 is soon exhausted by the formation of aluminum oxide, and the oxygen content in the exhaust gas from the aluminum supply tube 5 is reduced because the furnace interior 7 is on the high pressure side. This is because it is difficult to diffuse into.
放熱管11からの排ガスをアルミ供給筒5に導いて、ア
ルミ供給筒5を予熱室とする為には排ガスヘッダー14
からの排ガスが、アルミニウムの融点660℃よりもは
るかに高く、そのままでは予熱に利用できないから排ガ
スを550℃位に冷却し得る排ガス冷却装置16が設け
られている。An exhaust gas header 14 is used to guide the exhaust gas from the heat dissipation pipe 11 to the aluminum supply tube 5 and use the aluminum supply tube 5 as a preheating chamber.
Since the exhaust gas from the exhaust gas is much higher than the melting point of aluminum, 660°C, and cannot be used for preheating as it is, an exhaust gas cooling device 16 is provided that can cool the exhaust gas to about 550°C.
この装置16はアルミニウム地金及び溶融アルミニウム
に悪影響を及ぼさない限りいかなる構成でも良いが、図
示の如く冷風を送風するブロワ−を採用するのが簡便で
ある。This device 16 may have any configuration as long as it does not adversely affect the aluminum base metal and molten aluminum, but it is convenient to use a blower that blows cold air as shown in the figure.
このブロワ−16は冷風を排ガスと十分に混合できる限
りいかなる位置から排ガスに混合させるように設けても
良く、例えばアルミ供給筒5に送風しても良いが、図示
の如く排ガスヘッダー14のベンド部より騒音の発生防
止を確保しつつ設けられた冷風送風口16Aより送風す
る構成とすることで冷風と排ガスとの十分な混合を図っ
ている。The blower 16 may be installed at any position as long as the cold air can be sufficiently mixed with the exhaust gas. For example, the blower 16 may be blown into the aluminum supply cylinder 5, but as shown in the figure, the blower 16 may be installed at a bend portion of the exhaust gas header 14. Sufficient mixing of the cold air and the exhaust gas is achieved by blowing air from the provided cold air outlet 16A while ensuring prevention of noise generation.
アルミ供給筒5を予熱室とする為に地金をストックし得
、かつ地金を所望時に炉床4に落し込み得る棚装置18
が設げられている。A shelf device 18 capable of stocking metal in order to use the aluminum supply cylinder 5 as a preheating chamber and dropping the metal into the hearth 4 when desired.
is provided.
この棚装置18はアルミ供給筒5内の排ガス人口11よ
りも上方に設けられ、例えばシャフト19に棚板20を
取付けこの棚板20をシャフト19の炉外の端部に固定
した開閉ンバー21をストッパ22の係止から解除して
半転させることにより地金AAを載置した実線位置から
矢印23の如く開けて地金を落し込める構成とされてい
る。This shelf device 18 is provided above the exhaust gas population 11 in the aluminum supply cylinder 5, and includes, for example, an opening/closing bar 21 in which a shelf board 20 is attached to the shaft 19 and the shelf board 20 is fixed to the end of the shaft 19 outside the furnace. By releasing the lock of the stopper 22 and turning it half way, it is possible to open the base metal AA from the solid line position where it is placed as shown by the arrow 23 and drop the base metal into it.
またこの棚装置18は棚板20に載置された地金の回り
に550°C位の排ガスを十分に流通させる為に、棚板
20の格子状、網状、あるいは多孔状等の排ガスを流通
し得る形状に形成されている。In addition, this shelf device 18 distributes the exhaust gas in a lattice, net, or porous shape on the shelf 20 in order to sufficiently circulate the exhaust gas at about 550°C around the metal placed on the shelf 20. It is formed into a shape that can be used.
棚板20による通気抵抗が余りに大きいと排ガスが筒内
を極めて上昇し難くなり炉内が異常高圧となってガス燃
J焼が不完全に行われるので、この点からも棚板20は
地金を載置し得る役目を持たせて最大限に隙間のある格
子状等にすることが好ましい。If the ventilation resistance caused by the shelf board 20 is too large, it will be extremely difficult for the exhaust gas to rise inside the cylinder, resulting in abnormally high pressure inside the furnace and incomplete gas combustion. It is preferable to use a lattice shape or the like with as many gaps as possible so that it can be placed thereon.
棚装置18は熱効率を高める点から見て1段でも差支え
ないがアルミ供給筒5における排ガスの予熱としての利
用をより高効率とする為に上記の棚装置18を図示の如
く通気抵抗を考慮しつつできるだけ多段に設ける。From the point of view of increasing thermal efficiency, there is no problem with the shelf device 18 having one stage, but in order to make the use of the exhaust gas for preheating in the aluminum supply pipe 5 more efficient, the above-mentioned shelf device 18 is designed as shown in the figure, taking into account ventilation resistance. Provide as many tiers as possible.
また、最上段の棚装置18に所要量毎の地金を供給する
為にパケットコンベアが設置されているものとする。It is also assumed that a packet conveyor is installed to supply the required amount of metal to the top shelf device 18.
次に上述のように構成されたアルミニウム溶融炉の作用
を説明する。Next, the operation of the aluminum melting furnace configured as described above will be explained.
先ず、炉内7に所定量のアルミニウム地金その他アルミ
ニウム屑(以下、アルミニウム地金という。First, a predetermined amount of aluminum ingots and other aluminum scraps (hereinafter referred to as aluminum ingots) are placed in the furnace 7.
)を供給する。この供給は、図示しないパケットコンベ
アで最上段の棚装置18に地金を供給し、次々に下段側
の棚装置に落し込んでいくことにより行う。). This supply is performed by supplying the metal to the uppermost shelf device 18 using a packet conveyor (not shown) and dropping the metal into the lower shelf devices one after another.
炉内7への最初の地金の供給が終える時には各段の棚装
置18にも地金をストックする。When the initial supply of metal into the furnace 7 is completed, metal is also stocked in the shelf devices 18 of each stage.
次いで、又はこれに先行して燃焼装置」0により放熱管
11の管内でガスを噴射燃焼する。Next, or prior to this, gas is injected and burned within the heat dissipation tube 11 by the combustion device ``0''.
すると、炉内7は放熱管11が700℃か、ら1000
℃位の範囲で調整加熱され、その放熱により地金が溶融
される。Then, inside the furnace 7, the temperature of the heat dissipation tube 11 changes from 700°C to 1000°C.
The metal is heated in a controlled manner within a range of approximately ℃, and the metal is melted by the heat radiation.
炉内7は当初は空気中の酸素分があって酸化アルミニウ
ムを生成するが、酸素分が酸化し尽′した後は炉内7が
高圧側となるので排ガス中の酸素分、すなわちCOやC
O2の炉内7への拡散流入が極めて行われ難く、従って
炉内7が無酸素状態となって酸化アルミニウムの生成が
従来炉の量の2.5係よりも大幅に低減する。Initially, the furnace interior 7 contains oxygen in the air and produces aluminum oxide, but after the oxygen content is oxidized, the furnace interior 7 becomes the high pressure side, so the oxygen content in the exhaust gas, that is, CO and C
It is extremely difficult for O2 to diffuse into the furnace interior 7, so that the furnace interior 7 becomes anoxic and the production of aluminum oxide is significantly reduced by 2.5 times the amount of conventional furnaces.
無酸素状態では0.3係程度に抑えられることは伝熱線
の輻射熱で加熱する電気炉において実証されている。It has been demonstrated in an electric furnace that heats with radiant heat from heat transfer wires that the coefficient can be suppressed to about 0.3 in an oxygen-free state.
放熱管11からの排ガスは排ガスヘッダー14を介して
アルミ供給筒5に導かれる多段の棚装置18にストック
されている地金を予熱して熱効率を予熱しない時の倍近
くに高めて図示しない煙突より低温となって排出される
。Exhaust gas from the heat dissipation pipe 11 is led to the aluminum supply pipe 5 via the exhaust gas header 14. The metal stocked in the multi-stage shelf device 18 is preheated, and the thermal efficiency is increased to nearly twice that of the case without preheating. It is discharged at a lower temperature.
排ガス中の酸素分はCO2CO2となっており、排ガス
温度j都50℃位であるからアルミ供給筒5内にストッ
クされている地金に対して酸化アルミニウムの生成の関
与にそれほど活発でなく予熱を行う。The oxygen content in the exhaust gas is CO2CO2, and the exhaust gas temperature is about 50°C, so the metal stocked in the aluminum supply tube 5 is not very active in producing aluminum oxide, so preheating is necessary. conduct.
こうして炉内7に最初に供給される地金は放熱管11の
輻射熱で無酸素状態で溶融される。In this way, the metal that is initially supplied into the furnace 7 is melted in an oxygen-free state by the radiant heat of the heat radiation tube 11.
放熱管11の輻射熱は下り壁8によりアルミ供給筒5に
逃げずに地金の溶融に寄与する。The radiant heat of the heat dissipation pipe 11 is prevented from escaping into the aluminum supply cylinder 5 by the descending wall 8 and contributes to melting of the metal.
図示しない覗き窓等により炉内7のアルミニウムの全量
が溶融状態になったことを検知したら、湯栓9を外して
湯口6より溶融アルミニウムをトリベ等によって所要量
だけ取出す。When it is detected through a viewing window (not shown) that the entire amount of aluminum in the furnace 7 is in a molten state, the hot water tap 9 is removed and the required amount of molten aluminum is taken out from the sprue 6 using a ladle or the like.
しがる後:予熱ストックされている最下段の棚装置18
の地金を炉床4に落し込み、最下段の棚装置18を復帰
したらその上の棚装置にストックされている地金を落し
込み、こうして次々に上段にストックされている地金を
下段に落し込む。After wrapping: Lowermost shelf device 18 with preheated stock
of bullion is dropped into the hearth 4, and when the lowest shelf device 18 is restored, the bullion stocked on the shelf device above it is dropped, and in this way, the bullion stocked on the upper shelf is transferred to the lower shelf one after another. fall into it.
炉床4に落し込まれた地金は放熱管11の輻射熱と溶融
アルミニウムの伝熱により溶融されるが、その地金は5
50℃位に予熱されているから融点の660℃にまで迅
速に高められ溶融されることになり、溶融能力は予熱効
率の分だけ高まることになる。The ingot dropped into the hearth 4 is melted by the radiant heat of the heat radiation pipe 11 and the heat transfer of the molten aluminum, but the ingot falls into the hearth 4.
Since it is preheated to about 50°C, it is quickly raised to the melting point of 660°C and melted, and the melting ability is increased by the preheating efficiency.
以上の如くして連続的にアルミニウムの溶融が行われる
。As described above, aluminum is continuously melted.
以上説明したように、本発明のアルミニウム溶融炉は、
アルミニウム地金を無酸素状態で溶融する為に炉内に火
炎と溶融アルミニウムとが接触することがない燃焼室と
して放熱管を設け、また供給筒を予熱室と、(熱効率を
高める為に排ガス冷却装置及び棚装置を設けた構成であ
るから炉内に供給された地金を無酸素状態で放熱管の輻
射熱と溶融アルミニウムの伝熱で連続的に溶融でき、従
来の如く重油の火炎が直接アルミニウムと接触するアル
ミニウム溶融炉における酸化アルミニウムの生成量的2
.5係を大幅に低減でき、美大な損失を廻避できると共
に熱効率を予熱しない時の倍近くまで引上げて燃料費を
半分近くに節減でき、従来炉よりも大幅に小形化できる
。As explained above, the aluminum melting furnace of the present invention has
In order to melt the aluminum ingot in an oxygen-free state, a heat dissipation tube is installed in the furnace as a combustion chamber where the flame and molten aluminum do not come into contact. Because the structure is equipped with a device and a shelf device, the metal supplied to the furnace can be continuously melted in an oxygen-free state using the radiant heat from the heat sink and the heat transfer from the molten aluminum, and unlike conventional methods, the heavy oil flame directly melts the aluminum Amount of aluminum oxide produced in an aluminum melting furnace in contact with
.. 5 ratio can be significantly reduced, a large amount of loss can be avoided, and the thermal efficiency can be increased to nearly double that without preheating, fuel costs can be cut by nearly half, and the furnace can be made much smaller than conventional furnaces.
図面は本発明のアルミニウム溶融炉の実施例に係り、第
1図は縦断側面図、第2図は第1図における■−■断面
図、第3図は第1図における■−■断面図である。
4・・・・・・アルミ供給筒、7・・・・・・炉内、1
0・・・・・・燃焼装置、11・・・・・・放熱管、1
6・・・・・・排ガス冷却装置、18・・・・・・棚装
置。The drawings relate to an embodiment of the aluminum melting furnace of the present invention, and FIG. 1 is a vertical side view, FIG. 2 is a cross-sectional view taken along ■-■ in FIG. 1, and FIG. 3 is a cross-sectional view taken along ■-■ in FIG. be. 4...Aluminum supply cylinder, 7...Furnace interior, 1
0... Combustion device, 11... Heat radiation pipe, 1
6...Exhaust gas cooling device, 18...Shelf device.
Claims (1)
熱で炉内に供給されるアルミニウム地金を溶融し得、排
ガスがアルミ供給筒に導かれる1本又は2本以上の放熱
管を設け、アルミ供給筒に導かれる上記排ガスをアルミ
ニウムの融点より低い温度に冷却し得る排ガス冷却装置
を設けると共に、この冷却された排ガスを流通し得アル
ミニウム地金を載置し得落し込み得る棚装置を設けたこ
とを特徴とするアルミニウム溶融炉。1. Gas is injected into the pipe by the combustion device and the radiant heat of combustion can melt the aluminum ingot supplied into the furnace, and one or more heat dissipation pipes are provided to guide the exhaust gas to the aluminum supply pipe, and the aluminum supply pipe is An exhaust gas cooling device capable of cooling the exhaust gas introduced into the cylinder to a temperature lower than the melting point of aluminum is provided, and a shelf device is provided through which the cooled exhaust gas can flow and on which aluminum ingots can be placed and dropped. An aluminum melting furnace featuring:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11567579A JPS594632B2 (en) | 1979-09-11 | 1979-09-11 | aluminum melting furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11567579A JPS594632B2 (en) | 1979-09-11 | 1979-09-11 | aluminum melting furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5640072A JPS5640072A (en) | 1981-04-16 |
| JPS594632B2 true JPS594632B2 (en) | 1984-01-31 |
Family
ID=14668498
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11567579A Expired JPS594632B2 (en) | 1979-09-11 | 1979-09-11 | aluminum melting furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS594632B2 (en) |
-
1979
- 1979-09-11 JP JP11567579A patent/JPS594632B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5640072A (en) | 1981-04-16 |
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