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JPS631366B2 - - Google Patents
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JPS631366B2 - - Google Patents

Info

Publication number
JPS631366B2
JPS631366B2 JP57111196A JP11119682A JPS631366B2 JP S631366 B2 JPS631366 B2 JP S631366B2 JP 57111196 A JP57111196 A JP 57111196A JP 11119682 A JP11119682 A JP 11119682A JP S631366 B2 JPS631366 B2 JP S631366B2
Authority
JP
Japan
Prior art keywords
furnace
melted
furnace body
melting
gas
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
JP57111196A
Other languages
Japanese (ja)
Other versions
JPS591982A (en
Inventor
Senji Fujita
Kenji Kaneda
Tetsuo Okamoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP57111196A priority Critical patent/JPS591982A/en
Publication of JPS591982A publication Critical patent/JPS591982A/en
Publication of JPS631366B2 publication Critical patent/JPS631366B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Furnace Details (AREA)

Description

【発明の詳細な説明】 本発明は、アーク炉の溶解方法に関し、特に、
高い熱効率が得られる溶解方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a melting method for an arc furnace, and in particular,
The present invention relates to a melting method that provides high thermal efficiency.

アーク炉から排出される排ガス中に含まれる熱
を利用して、アーク炉中に装入されるスクラツプ
等の被溶解材料をできるだけ高い温度に予熱する
ことによつて、高い熱効率を得る方法が知られて
いる。しかしながら、従来、被溶解材料の予熱は
アーク炉の炉体外に於いて行われるのが一般的で
あり、その様な場合には、被溶解材料にダライ粉
等の低級スクラツプが含まれると、予熱の際に低
級スクラツプに含まれる油が燃焼して、被溶解材
料がアーク炉外に於いて溶解してしまう不都合が
あつた。
A method of obtaining high thermal efficiency is known by using the heat contained in the exhaust gas discharged from the arc furnace to preheat the material to be melted, such as scrap, which is charged into the arc furnace to the highest possible temperature. It is being However, in the past, preheating of the material to be melted was generally carried out outside the furnace body of the arc furnace, and in such cases, if the material to be melted contained low-grade scrap such as dull powder, the preheating There was a problem in that the oil contained in the low-grade scrap was burned and the material to be melted was melted outside the arc furnace.

他方、その様な不都合を避けるため、逆に被溶
解材料の予熱温度を抑制すると、低級スクラツプ
に含まれる油の不完全燃焼によつて悪臭を含む白
煙が発生し、設備環境を悪化させるとともに、高
い熱効率が十分に得られないのである。
On the other hand, if the preheating temperature of the material to be melted is suppressed in order to avoid such inconveniences, the incomplete combustion of the oil contained in the low-grade scrap will generate white smoke with a foul odor, which will worsen the facility environment and , high thermal efficiency cannot be obtained sufficiently.

本発明は、以上の事情を背景として為されたも
のであり、その目的とするところは、低級スクラ
ツプを含む被溶解材料であつても、環境を悪化さ
せることなく高温にてその被溶解材料を予熱し、
高い熱効率が得られるアーク炉溶解方法を提供す
ることにある。
The present invention has been made against the background of the above circumstances, and its purpose is to melt materials to be melted at high temperatures without deteriorating the environment, even if the materials to be melted include low-grade scrap. Preheat,
An object of the present invention is to provide an arc furnace melting method that provides high thermal efficiency.

斯る目的を達成するため、本発明は、一対のア
ーク炉用炉体を交互に用いて被溶解材料を溶解す
るアーク炉溶解方法であつて、 (1) 溶解中の一方の炉体中に炭素、および酸素含
有気体を吹込み、該炭素を燃焼させてCOガス
を生成せしめるとともに、該COガスを他方の
炉体内へ導く工程と、 (2) 酸素含有気体を吹込むことによつて前記CO
ガスを更に燃焼させて、前記他方の炉体内での
溶解のために該炉体内に予め装入された被溶解
材料を予熱する工程と を、含むことを特徴とする。
In order to achieve such an object, the present invention provides an arc furnace melting method for melting a material to be melted by alternately using a pair of arc furnace bodies, comprising: (2) a step of blowing carbon and oxygen-containing gas, burning the carbon to generate CO gas, and guiding the CO gas into the other furnace; (2) blowing the oxygen-containing gas to C.O.
The present invention is characterized in that it further includes the step of combusting the gas to preheat the material to be melted that has been previously charged into the other furnace body for melting in the other furnace body.

この様にすれば、溶解前の被溶解材料が他方の
炉体内にて予熱されるので、被溶解材料の予熱温
度を高くできるとともに、一方の炉体内に於いて
発生させられたCOガスを他方の炉体内にて燃焼
させることによつて、被溶解材料が予熱されるの
で、一方の炉体内で発生する熱が極めて有効に予
熱に利用され、高い熱効率が得られるのである。
そして、被溶解材料に低級スクラツプが含まれて
いても、予熱温度が高いので低級スクラツプに含
まれる油分が完全燃焼して設備環境の悪化が解消
されるのである。
In this way, the material to be melted before melting is preheated in the other furnace body, so the preheating temperature of the material to be melted can be increased, and the CO gas generated in one furnace body is transferred to the other furnace body. Since the material to be melted is preheated by combustion in one of the furnace bodies, the heat generated in one of the furnace bodies is used extremely effectively for preheating, resulting in high thermal efficiency.
Even if the material to be melted contains low-grade scrap, the preheating temperature is high, so the oil contained in the low-grade scrap is completely combusted, eliminating the deterioration of the facility environment.

また、溶解中の一方の炉体内においてCOガス
を発生させるために炭素が燃焼させられるので、
その燃焼熱が溶解に利用されて、高価な電力が大
幅に節減されるのである。
Also, since carbon is burned to generate CO gas in one of the furnace bodies during melting,
The heat of combustion is used for melting, resulting in significant savings in expensive electricity.

次に、本発明方法の一例を図面に基づいて詳細
に説明する。
Next, an example of the method of the present invention will be explained in detail based on the drawings.

第1図及び第2図に於いて、一対の基台10
a,10b上には対称的に配置された一対のアー
ク用炉体12a,12bが傾動可能に配設されて
いる。即ち、基台10a,10b上には直線上に
係合歯が形成された炉台14a,14bが固定さ
れており、円弧上に形成された係合歯を備えた炉
脚15a,15bがその係合歯と炉台14a,1
4bの係合歯とが係合した状態で炉台14a,1
4b上に夫々乗せられている。炉脚15a,15
bの一端は、伸縮可能な傾動駆動装置16a,1
6bによつて夫々支えられており、また、炉脚1
5a,15bには、一円周上に複数のローラ18
が配設されて、炉体12a及び12bがローラ1
8を介して夫々炉脚15a及び15b上に乗せら
れている。従つて、炉体12a及び12bは夫々
傾動駆動装置16a及び16bの駆動によつて傾
動させられ、夫々の内部の溶鋼が、出鋼口20
a,20bを介して取鍋22内に出鋼させられる
とともに、溶解中に於いては垂直中心軸まわりに
回転させられるようになつている。尚、炉体12
a及び12bには、夫々炭素注入ノズル24a,
24bと酸素注入ノズル26a,26bとが設け
られている。
In FIGS. 1 and 2, a pair of bases 10
A pair of symmetrically arranged arc furnace bodies 12a, 12b are tiltably disposed on the arcs a, 10b. That is, furnace stands 14a, 14b with engaging teeth formed on a straight line are fixed on the bases 10a, 10b, and furnace legs 15a, 15b with engaging teeth formed on an arc are fixed on the bases 10a, 10b. Matching teeth and hearth stand 14a, 1
In the state where the engagement teeth of 4b are engaged, the furnace stands 14a, 1
4b, respectively. Furnace legs 15a, 15
One end of b is an extendable tilting drive device 16a, 1
6b, respectively, and the furnace legs 1
5a and 15b, a plurality of rollers 18 are provided on one circumference.
are arranged, and the furnace bodies 12a and 12b are connected to the rollers 1.
8 on the furnace legs 15a and 15b, respectively. Therefore, the furnace bodies 12a and 12b are tilted by the tilting drive devices 16a and 16b, respectively, and the molten steel inside each is transferred to the tapping port 20.
The steel is tapped into the ladle 22 through the holes 20a and 20b, and is rotated around a vertical central axis during melting. Furthermore, the furnace body 12
carbon injection nozzles 24a and 12b, respectively.
24b and oxygen injection nozzles 26a, 26b.

溶解用炉蓋28及び電極棒30と予熱用炉蓋3
2とは、炉体12aと12bとに交互に適用され
るようになつており、また、炉体12a及び12
bが夫々の中に於いて溶解及び予熱が交互に為さ
れるようになつている。即ち、炉体12a及び1
2bの両側には一対のレール34が敷設されてお
り、そのレール34上にガントリー36が炉体1
2a及び12bを跨ぐ状態で走行するように配設
されている。ガントリー36には溶解用炉蓋28
が昇降可能に吊り下げられるとともに、電極棒3
0の昇降装置38が設けられている。昇降装置3
8は、第3図に示されるように、ガントリー36
の一方の脚部に設けられた昇降可能な支柱40
と、その支柱40の上端から水平に突き出たアー
ム42とを備え、アーム42の先端に固定された
電極棒30が昇降させられるようになつている。
電極棒30は、夫々水冷母線管44によつて電源
装置46に接続されており、電源装置46の電力
が電極棒30に給電されるようになつている。
Melting furnace lid 28, electrode rod 30, and preheating furnace lid 3
2 is applied alternately to the furnace bodies 12a and 12b, and is applied to the furnace bodies 12a and 12b alternately.
In each case, melting and preheating are performed alternately. That is, the furnace bodies 12a and 1
A pair of rails 34 are laid on both sides of 2b, and a gantry 36 is mounted on the rails 34.
The vehicle is arranged so as to run across 2a and 12b. The gantry 36 has a melting furnace lid 28
is suspended so that it can be raised and lowered, and the electrode rod 3
0 lifting device 38 is provided. Lifting device 3
8 is a gantry 36 as shown in FIG.
A column 40 that can be raised and lowered is provided on one leg of the
and an arm 42 projecting horizontally from the upper end of the support 40, and the electrode rod 30 fixed to the tip of the arm 42 can be moved up and down.
The electrode rods 30 are each connected to a power supply device 46 through a water-cooled bus tube 44, so that power from the power supply device 46 is supplied to the electrode rods 30.

一方、第2図に示されるように、炉体12aと
炉体12bとの中間位置には、排気路の一部を兼
ねる垂直な垂直管48が立設されており、垂直管
48の先端部には予熱用炉蓋32に接続された回
転ダクト50が垂直管48の軸まわりの回転が可
能に接続されている。予熱用炉蓋32は、図示し
ない吊り下げ装置によつて昇降させられるととも
に、垂直管48を中心として回転させられ、炉体
12aまたは12bの開口部に嵌合されるように
なつている。垂直管48の下端部は、排気ダクト
52によつて追装用被溶解材料を収容する共通の
予熱室としてのクラムシエル形バケツト54に接
続されており、バケツト54からは図示しない排
気フアンに接続された排気ダクト56によつて吸
引排気されるようになつている。
On the other hand, as shown in FIG. 2, a vertical pipe 48 that also serves as a part of the exhaust path is installed at an intermediate position between the furnace bodies 12a and 12b. A rotating duct 50 connected to the preheating furnace lid 32 is connected to the vertical pipe 48 so as to be rotatable about the axis thereof. The preheating furnace lid 32 is raised and lowered by a hanging device (not shown), rotated about a vertical tube 48, and fitted into an opening of the furnace body 12a or 12b. The lower end of the vertical pipe 48 is connected by an exhaust duct 52 to a clamshell type bucket 54 serving as a common preheating chamber for accommodating materials to be melted for additional loading, and the bucket 54 is connected to an exhaust fan (not shown). The air is sucked and exhausted through an exhaust duct 56.

炉体12a及び12bは、接続ダクト58によ
つて相互に接続されており、一方の溶解中に発生
させられるCO(一酸化炭素)ガスが他方に送られ
るようになつている。尚、接続ダクト58と排気
ダクト52との間は、開閉ダンパ60を備えたバ
イパスダクト62によつて接続され、予熱用CO
ガス等の風量が調節されるようになつている。
The furnace bodies 12a and 12b are interconnected by a connecting duct 58 so that CO (carbon monoxide) gas generated during melting of one is sent to the other. Note that the connection duct 58 and the exhaust duct 52 are connected by a bypass duct 62 equipped with an opening/closing damper 60, and a CO2 for preheating is connected.
The air volume of gas etc. can be adjusted.

次に、以上のように構成されたアーク炉の溶解
方法を説明する。
Next, a method of melting the arc furnace configured as described above will be explained.

例えば、炉体12a内に電極棒30が挿入され
るとともに、電源装置46から電力が供給されて
被溶解材料が溶解させられている状態に於いて
は、他方の炉体12b内には既に図示しないバケ
ツトから被溶解材料が装入されており、またバケ
ツト54内には追装用の被溶解材料が装入されて
いる。この様な状態に於いて、炉体12a内に於
いては、予め被溶解材料に混ぜられた炭素及び炭
素注入ノズル24aから注入される炭素が、酸素
注入ノズル26aから注入される酸素または空気
等の酸素含有気体中の酸素によつて燃焼させられ
て、COガスが発生させられる。このCOガスは接
続ダクト58を通して他方の炉体12b内に送ら
れ、そこで酸素含有気体の供給を受けて燃焼させ
られる。このため、炉体12b内の被溶解材料は
COガスの燃焼によつて極めて高い温度に予熱さ
れるのである。即ち、被溶解材料が炉体12b内
に装入された状態で予熱されるので、被溶解材料
の溶解を心配することなく高い温度に予熱するこ
とができるとともに、溶解中の炉体12a内の熱
が効果的に炉体12b内の予熱に利用されるの
で、高い熱効率が得られるのである。しかも、被
溶解材料が高い温度で予熱されることによつて、
被溶解材料に含まれる低級スクラツプの油分が完
全燃焼させられて、設備環境が悪化することが全
く解消されるのである。
For example, when the electrode rod 30 is inserted into the furnace body 12a and the material to be melted is being melted by being supplied with power from the power supply device 46, there is already a state in the other furnace body 12b that is not shown in the figure. The material to be melted is charged from a bucket that does not have a casing, and the material to be melted for additional loading is charged into the bucket 54. In such a state, in the furnace body 12a, the carbon mixed in advance with the material to be melted and the carbon injected from the carbon injection nozzle 24a are mixed with oxygen, air, etc. injected from the oxygen injection nozzle 26a. is combusted by oxygen in the oxygen-containing gas to generate CO gas. This CO gas is sent into the other furnace body 12b through the connecting duct 58, where it is supplied with oxygen-containing gas and combusted. Therefore, the material to be melted in the furnace body 12b is
It is preheated to extremely high temperatures by burning CO gas. That is, since the material to be melted is preheated while being charged into the furnace body 12b, the material to be melted can be preheated to a high temperature without worrying about melting, and the temperature inside the furnace body 12a during melting can be preheated. Since the heat is effectively used for preheating the inside of the furnace body 12b, high thermal efficiency can be obtained. Moreover, by preheating the material to be melted at a high temperature,
The oil content of low-grade scrap contained in the material to be melted is completely combusted, and the deterioration of the equipment environment is completely eliminated.

そして、炉体12bから排出される排ガスは、
回転ダクト50、垂直管48、及び排気ダクト5
2を通してバケツト54内に供給され、そのバケ
ツト54内に予め収容された追装用被溶解材料が
予熱される。
The exhaust gas discharged from the furnace body 12b is
Rotating duct 50, vertical pipe 48, and exhaust duct 5
2 is supplied into the bucket 54, and the material to be melted for reloading, which has been previously accommodated in the bucket 54, is preheated.

炉体12a内の溶解が完了すると、電極棒30
及び溶解用炉蓋28が炉体12aから取り外され
るとともに、バケツト54が炉体12a上に移動
させられてバケツト54内の被溶解材料が炉体1
2aの上部開口から追加装入される。そして、再
び電極棒30及び溶解用炉蓋28が炉体12aに
戻されるとともに、炉体12a内に於いて追装さ
れた被溶解材料が溶解される。この溶解時に於い
ても、炭素注入ノズル24及び酸素注入ノズル2
6から炭素及び酸素含有気体が注入されて、CO
ガスが発生させられ、前述と同様に炉体12b内
の被溶解材料が効率よく予熱されるとともに、バ
ケツト54内に新たに収容された追装用被溶解材
料が予熱される。
When the melting inside the furnace body 12a is completed, the electrode rod 30
Then, the melting furnace lid 28 is removed from the furnace body 12a, and the bucket 54 is moved onto the furnace body 12a, so that the material to be melted in the bucket 54 is transferred to the furnace body 1.
Additional charges are made from the upper opening of 2a. Then, the electrode rod 30 and the melting furnace cover 28 are returned to the furnace body 12a, and the additional material to be melted is melted in the furnace body 12a. Even during this melting, the carbon injection nozzle 24 and the oxygen injection nozzle 2
Carbon and oxygen-containing gas is injected from 6 to produce CO
Gas is generated, and the material to be melted in the furnace body 12b is efficiently preheated in the same manner as described above, and the material to be melted for reloading newly accommodated in the bucket 54 is preheated.

そして、炉体12a内に於ける溶解が完了する
と、炉体12aが傾動駆動装置16aの作動によ
つて傾動させられ、溶鋼が取鍋22内に出鋼させ
られる。炉体12aが戻されると、炉体12a内
に被溶解材料が新たに装入されるとともに、炉体
12a上の溶解用炉蓋28及び電極棒30が炉体
12bに装着され、反対に炉体12b上の予熱用
炉蓋32が回転ダクト50とともに回転させられ
て、炉体12a上に装着される。そして、以後、
前述と同様の操作が為され、炉体12bに於いて
溶解が行われるとともに、炉体12aに於いて被
溶解材料の予熱が行われるのである。
When melting in the furnace body 12a is completed, the furnace body 12a is tilted by the operation of the tilting drive device 16a, and molten steel is tapped into the ladle 22. When the furnace body 12a is returned, the material to be melted is newly charged into the furnace body 12a, and the melting furnace lid 28 and electrode rod 30 on the furnace body 12a are attached to the furnace body 12b, and conversely, the furnace body 12a is loaded with the material to be melted. The preheating furnace lid 32 on the body 12b is rotated together with the rotating duct 50 and mounted on the furnace body 12a. And from then on,
The same operations as described above are performed, and melting is performed in the furnace body 12b, and at the same time, preheating of the material to be melted is performed in the furnace body 12a.

このように、本実施例によれば、溶解中の一方
の炉体12a内で発生させられたCOガスが、被
溶解材料が装入された他方の炉体12b内に導か
れ、そこでCOガスの燃焼熱によつて被溶解材料
が高い温度に予熱されるので、高い熱効率が得ら
れるのである。本発明者等の実験によれば、従来
溶解中の炉体から排ガスとともに放出されていた
熱量の50%を回収することができた。
Thus, according to this embodiment, the CO gas generated in one furnace body 12a during melting is guided into the other furnace body 12b into which the material to be melted is charged, where the CO gas is Since the material to be melted is preheated to a high temperature by the heat of combustion, high thermal efficiency can be obtained. According to experiments conducted by the present inventors, it was possible to recover 50% of the heat that was conventionally released along with the exhaust gas from the furnace body during melting.

また、被溶解材料が油分を多量に含む低級スク
ラツプであつても、COガスの燃焼とともにその
油分が完全に燃焼させられるので、悪臭、白煙等
が防止され、作業環境が好適に保持されるととも
に、COガスを発生させるために溶解中の一方の
炉体12a中において炭素が燃焼させられるの
で、その燃焼熱によつて高価な電力が大幅に節減
されるのである。
In addition, even if the material to be melted is low-grade scrap containing a large amount of oil, the oil is completely combusted with the combustion of the CO gas, preventing foul odors, white smoke, etc., and maintaining a favorable working environment. At the same time, since carbon is burnt in one of the furnace bodies 12a during melting to generate CO gas, expensive electric power can be significantly saved by the heat of combustion.

更に、本実施例によれば、追装用の被溶解材料
が他方の炉体12b中の被溶解材料の予熱に使用
されたCOガスの排ガスによつて予熱されるので、
その排ガス中に含まれる熱が更に回収されて、一
層高い熱効率が得られる利点がある。
Furthermore, according to this embodiment, the material to be melted for additional loading is preheated by the exhaust gas of the CO gas used to preheat the material to be melted in the other furnace body 12b.
There is an advantage that the heat contained in the exhaust gas is further recovered, resulting in higher thermal efficiency.

尚、上述したのはあくまでも本発明方法の一例
であり、本発明はその精神を逸脱しない範囲にお
いて種々変更され得るものであることは言うまで
もない。
It should be noted that the above-mentioned method is merely an example of the method of the present invention, and it goes without saying that the present invention can be modified in various ways without departing from its spirit.

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

第1図は、本発明方法の一例が適用されるアー
ク炉の一部を切欠いた正面図である。第2図は第
1図の平面図である。第3図は、異るサイクルを
示す第1図の一部を切欠いた側面図である。 12a,12b:炉体、54:バケツト(予熱
室)。
FIG. 1 is a partially cutaway front view of an arc furnace to which an example of the method of the present invention is applied. FIG. 2 is a plan view of FIG. 1. FIG. 3 is a partially cut away side view of FIG. 1 showing different cycles. 12a, 12b: Furnace body, 54: Bucket (preheating chamber).

Claims (1)

【特許請求の範囲】 1 一対のアーク炉用炉体を交互に用いて被溶解
材料を溶解するアーク炉溶解方法であつて、 溶解中の一方の炉体中に炭素、および酸素含有
気体を吹込み、該炭素を燃焼させてCOガスを生
成せしめるとともに、該COガスを他方の炉体内
へ導く工程と、 酸素含有気体を吹込むことによつて前記COガ
スを更に燃焼させて、前記他方の炉体内での溶解
のために該炉体内に予め装入された被溶解材料を
予熱する工程と を、含むことを特徴とするアーク炉溶解方法。
[Claims] 1. An arc furnace melting method for melting a material to be melted by alternately using a pair of arc furnace bodies, the method comprising blowing carbon and oxygen-containing gas into one of the furnace bodies during melting. a step of combusting the carbon to generate CO gas and guiding the CO gas into the other furnace body; further combusting the CO gas by blowing oxygen-containing gas into the other furnace; An arc furnace melting method comprising the step of preheating a material to be melted that has been previously charged into the furnace body for melting within the furnace body.
JP57111196A 1982-06-28 1982-06-28 Arc furnace melting method Granted JPS591982A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57111196A JPS591982A (en) 1982-06-28 1982-06-28 Arc furnace melting method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57111196A JPS591982A (en) 1982-06-28 1982-06-28 Arc furnace melting method

Publications (2)

Publication Number Publication Date
JPS591982A JPS591982A (en) 1984-01-07
JPS631366B2 true JPS631366B2 (en) 1988-01-12

Family

ID=14554928

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57111196A Granted JPS591982A (en) 1982-06-28 1982-06-28 Arc furnace melting method

Country Status (1)

Country Link
JP (1) JPS591982A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61128090A (en) * 1984-11-27 1986-06-16 石川島播磨重工業株式会社 Method and device for recovering waste gas from melting furnace
JPH0631686B2 (en) * 1984-12-03 1994-04-27 石川島播磨重工業株式会社 Exhaust gas heat recovery method and apparatus for melting furnace
JPH0721386B2 (en) * 1985-11-25 1995-03-08 石川島播磨重工業株式会社 Arc furnace equipment
JPH0746034B2 (en) * 1985-12-09 1995-05-17 石川島播磨重工業株式会社 Double melting equipment
JPH07803B2 (en) * 1986-04-04 1995-01-11 石川島播磨重工業株式会社 Exhaust gas heat recovery method for dual melting furnace
JP6492547B2 (en) * 2014-11-05 2019-04-03 大同特殊鋼株式会社 Method for producing molten metal
CN111094597A (en) * 2017-09-28 2020-05-01 大阳日酸株式会社 Melting and refining furnace operation method and melting and refining furnace

Also Published As

Publication number Publication date
JPS591982A (en) 1984-01-07

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