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JPH07803B2 - Exhaust gas heat recovery method for dual melting furnace - Google Patents
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JPH07803B2 - Exhaust gas heat recovery method for dual melting furnace - Google Patents

Exhaust gas heat recovery method for dual melting furnace

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Publication number
JPH07803B2
JPH07803B2 JP7799486A JP7799486A JPH07803B2 JP H07803 B2 JPH07803 B2 JP H07803B2 JP 7799486 A JP7799486 A JP 7799486A JP 7799486 A JP7799486 A JP 7799486A JP H07803 B2 JPH07803 B2 JP H07803B2
Authority
JP
Japan
Prior art keywords
furnace
exhaust gas
melting
furnace shell
preheating
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 - Lifetime
Application number
JP7799486A
Other languages
Japanese (ja)
Other versions
JPS62235414A (en
Inventor
昌二 古谷
雅行 青鹿
貞夫 樋口
文夫 数土
浩之 上杉
Original Assignee
石川島播磨重工業株式会社
川崎製鉄株式会社
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 石川島播磨重工業株式会社, 川崎製鉄株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP7799486A priority Critical patent/JPH07803B2/en
Publication of JPS62235414A publication Critical patent/JPS62235414A/en
Publication of JPH07803B2 publication Critical patent/JPH07803B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明はスクラップを溶解する溶解炉に係り、特に2
基一対の炉を有する複式溶解炉の排ガス熱回収方法に関
する。
The present invention relates to a melting furnace for melting scrap, and more particularly to a melting furnace for melting scrap.
The present invention relates to an exhaust gas heat recovery method for a dual melting furnace having a pair of base furnaces.

〔従来の技術〕[Conventional technology]

従来、2基一対の炉を有する複式溶解炉として、操業側
の炉殻で発生した排ガスを待機側の炉殻内に導入するよ
うにして、待機側炉殻内に装入したスクラップを予熱す
る製鋼設備(特公昭59-47831号公報、特開昭48-45937号
公報)が提案されている。
Conventionally, as a double melting furnace having a pair of two furnaces, the exhaust gas generated in the operating side shell is introduced into the standby side shell to preheat the scrap charged in the standby side shell. Steelmaking facilities (Japanese Patent Publication No. 59-47831 and Japanese Patent Publication No. 48-45937) have been proposed.

上記のようにして操業することにより、出鋼後に補修,
原料装入を経て通電するまでのアイドルタイムを除くこ
とができるとともに操業に入る側の炉内のスクラップは
排ガスで予熱されるため溶解時間を短縮することができ
るとされている。
By operating as described above, repairing after tapping,
It is said that it is possible to eliminate the idle time from charging the raw materials to turning on the power, and to shorten the melting time because the scrap in the furnace on the side of the operation is preheated by the exhaust gas.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

上記従来の複式溶解炉では、操業側の炉殻から待機側の
炉殻内へ排ガスの全量が単純にそのまゝ導入されるだけ
なので、待機側の炉殻内を通過したのちそのまゝ排出さ
れることになり、その結果、排ガスエネルギーを十分に
回収することができず、また待機側の炉殻内で予熱され
原料から発生した臭気は、別途脱臭設備を設けない限り
そのまゝ大気中に放出されることになり、悪臭をまき散
らすことになる。このようなことから、取扱う原料には
臭気を含まないものに限定を受けるという欠点があっ
た。さらに排ガス中に未燃ガスが多量に含まれる場合に
は一層熱エネルギーの回収効率が低下するという問題が
ある。
In the above-mentioned conventional double melting furnace, the entire amount of exhaust gas is simply introduced from the operating side shell into the standby side shell, so after passing through the standby side shell, the exhaust gas is discharged as it is. As a result, the exhaust gas energy cannot be sufficiently recovered, and the odor generated from the raw material preheated in the standby side furnace shell will remain in the atmosphere unless separate deodorizing equipment is installed. Will be released into the air and will disperse the foul odor. For this reason, there is a drawback that the raw materials to be handled are limited to those that do not contain odor. Further, when a large amount of unburned gas is contained in the exhaust gas, there is a problem that the recovery efficiency of heat energy is further reduced.

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

上記従来技術の問題点を解決するため、この発明におい
ては、2基一対で一方が操業側となるとき他方が原料予
熱側となる溶解用の炉殻と、これら各溶解用の炉殻と連
通して燃料吹込みのための初期溶湯を供給する初期溶湯
供給用炉殻とを備えた複式溶解炉であって、前記2つの
溶解用の炉殻を接続する排ガスダクト中に介装され操業
側の溶解用の炉殻からの排ガス中の未燃ガスを燃焼させ
る燃焼筒とを用い、操業側の溶解用の炉殻の排ガス中の
未燃ガスを燃焼筒で燃焼させて得た高温燃焼ガスを前記
排ガスダクトで予熱側の炉殻へ導入し、当該予熱側の溶
解用の炉殻内の原料を予熱したのち、この予熱後の排ガ
スを初期溶湯を溶解中の前記初期溶湯供給用炉殻内に導
入して排ガス中の臭気成分を熱分解して排気するように
したことを特徴とするものである。
In order to solve the above-mentioned problems of the prior art, in the present invention, a pair of two melting furnaces, one of which is an operating side and the other of which is a raw material preheating side, and a melting shell for communicating with each of these A double-sided melting furnace having an initial molten metal supply furnace shell for supplying an initial molten metal for injecting fuel, the operating side being installed in an exhaust gas duct connecting the two melting furnace shells. High temperature combustion gas obtained by burning the unburned gas in the exhaust gas of the melting furnace of the operating side in the combustion tube with a combustion tube that burns the unburned gas in the exhaust gas from the furnace shell for melting Is introduced into the furnace shell on the preheating side through the exhaust gas duct, and the raw material in the furnace shell for melting on the preheating side is preheated, and the exhaust gas after the preheating is used to melt the initial molten metal in the initial molten metal supply furnace shell. Introduced into the interior of the exhaust gas to thermally decompose the odorous components in the exhaust gas and exhaust it. Is shall.

〔作用〕[Action]

上記の方法を採用することにより、炭材,酸素等の吹込
み溶解により発生するCOを主成分とする多量の未燃ガス
を燃焼して排ガスの熱エネルギーを高め、その高温排ガ
スを予熱側の炉殻内へ導入するため、排ガスエネルギー
の有効利用がはかられ、また予熱側の炉殻からの排ガス
を初期溶湯供給用溶解炉へ導入して高温の炉内で熱分解
させることにより、臭気を発生するスクラップの予熱で
あっても操業側の炉からの高温排ガスのすべてを予熱に
使用することができ、スクラップの種類に関係なく無臭
高温予熱を行なうことができる。
By adopting the above method, a large amount of unburned gas containing CO as a main component generated by blowing and melting carbonaceous materials, oxygen, etc. is burned to increase the thermal energy of the exhaust gas, and the high temperature exhaust gas is preheated. Since it is introduced into the furnace shell, the exhaust gas energy can be effectively used.In addition, the exhaust gas from the furnace shell on the preheating side is introduced into the melting furnace for supplying the initial molten metal and is thermally decomposed in the high temperature furnace to produce an odor. Even in the preheating of scraps that generate heat, all of the high-temperature exhaust gas from the furnace on the operating side can be used for preheating, and odorless high-temperature preheating can be performed regardless of the type of scrap.

〔実施例〕〔Example〕

以下この発明の実施例を添付図面を参照して説明する。 Embodiments of the present invention will be described below with reference to the accompanying drawings.

図はこの発明の一構成例を示すもので、符号1および
1′は一対の溶解炉の炉殻を示し、これら炉殻1,1′の
間に初期溶湯供給用溶解炉の炉殻2が設置されており、
上記一対の溶解炉の炉殻1,1′と、初期溶湯供給用溶解
炉の炉殻2とは排ガスダクト3,3′で接続されている。
The figure shows an example of the structure of the present invention. Reference numerals 1 and 1'represent a pair of furnace shells of a melting furnace, and a furnace shell 2 of a melting furnace for supplying an initial molten metal is provided between these furnace shells 1, 1 '. Has been installed,
Exhaust gas ducts 3, 3'connect the furnace shells 1, 1'of the pair of melting furnaces and the furnace shell 2 of the melting furnace for supplying the initial molten metal.

上記排ガスダクト3,3′の途中にはダンパ4,4′が介装さ
れ、このダンパ4,4′の前後部は、固定されたダクトか
ら炉体を切り離すためのブレークフランジ5,5′、6,6′
で接続されている。
Dampers 4, 4 ′ are provided in the middle of the exhaust gas ducts 3, 3 ′, and front and rear parts of the dampers 4, 4 ′ are break flanges 5, 5 ′ for separating the furnace body from the fixed ducts, 6,6 ′
Connected by.

また、一対の溶解炉の炉殻1,1′間は別の排ガスダクト
7で接続されている。この排ガスダクト7は、各炉殻1,
1′にブレークフランジ8,8′を介して接続され、この排
ガスダクト7の途中には、操業側の溶解炉の炉殻1また
は1′内で発生した未燃ガスを含む排ガスを燃焼させる
燃焼筒9が接続されている。
Further, another exhaust gas duct 7 is connected between the furnace shells 1 and 1 ′ of the pair of melting furnaces. This exhaust gas duct 7 is for each furnace shell 1,
1'is connected via break flanges 8 and 8 ', and in the middle of this exhaust gas duct 7, combustion for burning exhaust gas containing unburned gas generated in the furnace shell 1 or 1'of the melting furnace on the operating side The tube 9 is connected.

前記初期溶湯供給用溶解炉の炉殻2には、集塵装置10に
通ずるバイパスラインの排ガスダクト11が接続されてい
る。
An exhaust gas duct 11 of a bypass line communicating with the dust collector 10 is connected to the furnace shell 2 of the melting furnace for supplying the initial molten metal.

図において符号12,12′はスパウト、13は電極、14は二
次側導体、15は給電用ケーブル、16は電源(炉用変圧
器)、17は溶湯供給用樋をそれぞれ示している。
In the figure, reference numerals 12 and 12 'are spouts, 13 are electrodes, 14 is a secondary side conductor, 15 is a power supply cable, 16 is a power supply (furnace transformer), and 17 is a molten metal supply gutter.

そして、これら通電溶解のための設備13〜16は、初期溶
湯供給用溶解炉2のみならず一対の溶解炉1および1′
にも供用できるように設備されている。
The facilities 13 to 16 for electric current melting include not only the melting furnace 2 for supplying the initial molten metal but also the pair of melting furnaces 1 and 1 '.
It is equipped so that it can also be used.

つぎに操業の態様について説明する。Next, the mode of operation will be described.

いま、一対の溶解炉のうち一方の炉殻1を操業側の炉と
し、他方の炉殻1′を予熱側の炉とするとき、操業中の
炉殻1では溶湯中に炭材,酸素などの燃料が吹込まれ、
炉殻1内に装入されたスクラップが溶解されている。
Now, when one of the pair of melting furnaces is used as a furnace on the operating side and the other furnace shell 1'is a furnace on the preheating side, carbonaceous materials, oxygen, etc. are contained in the molten metal in the operating furnace shell 1. Fuel of
The scrap charged in the furnace shell 1 is melted.

また、初期溶湯供給用溶解炉の炉殻2では、スクラップ
を通電溶解中である。
Further, in the furnace shell 2 of the melting furnace for supplying the initial molten metal, scrap is being melted by electric current.

この場合において、ダンパ4を閉じの状態にしておき、
操業側の溶解炉の炉殻1からの排ガスを燃焼筒9に導入
し、この燃焼筒9において操業側の炉殻1内で発生した
COガスなどの未燃ガスを含む排ガスを燃焼させ、排ガス
の熱エネルギーを高め、その高温ガスを予熱側の炉殻
1′へ導入してスクラップの予熱効果を増大し、予熱後
の臭気を含んだ排ガスは通電操業中の初期溶湯供給用溶
解炉の炉殻2内で熱分解して無臭とし、集塵装置10を通
じて大気に放出される。
In this case, keep the damper 4 closed,
Exhaust gas from the furnace shell 1 of the melting furnace on the operating side was introduced into the combustion tube 9 and generated in the furnace tube 1 on the operating side in the combustion tube 9.
The exhaust gas containing unburned gas such as CO gas is burned to increase the heat energy of the exhaust gas, and the high temperature gas is introduced into the preheating side of the furnace shell 1 ′ to increase the preheating effect of scrap and to include the odor after preheating. The flue gas is thermally decomposed in the furnace shell 2 of the melting furnace for supplying the initial molten metal to be odorless during the energization operation, and is discharged to the atmosphere through the dust collector 10.

操業側の溶解炉の炉殻1内のスクラップの溶解が完了す
ると、従来と同様にブレークフランジを開らき、炉殻1
を傾動して出湯する。
When the melting of the scrap in the furnace shell 1 of the melting furnace on the operation side is completed, the break flange is opened in the same manner as in the conventional case, and the furnace shell 1 is opened.
Tilt and tap the water.

なお、溶解炉の炉殻1での操業が完了する直前に炉殻
1′での操業開始準備として燃料吹込みのための初期溶
湯を樋17を通じてスパウト12′より炉殻1′内に供給し
ておく。そして炉殻1での操業を完了したと同時に今度
は炉殻1′が操業側の炉となり、炭材,酸素等の燃料を
吹込み、溶解作業を開始する。このときダンパ4′を閉
じておくことにより、前記と同様に炉殻1′からの排ガ
スを排ガスダクト7を通じて燃焼筒9に導入し、こゝで
COガスなどの未燃ガスを燃焼させ、熱エネルギーが高め
られた高温ガスを予熱側となっている炉殻1内へ導入し
てスクラップを効率よく予熱する。
Immediately before the completion of the operation in the furnace shell 1 of the melting furnace, the initial molten metal for fuel injection was supplied from the spout 12 'into the furnace shell 1'through the gutter 17 as a preparation for starting the operation in the furnace shell 1'. Keep it. At the same time when the operation in the furnace shell 1 is completed, the furnace shell 1'becomes the furnace on the operation side, and the fuel such as carbonaceous material and oxygen is blown to start the melting work. At this time, by closing the damper 4 ', the exhaust gas from the furnace shell 1'is introduced into the combustion tube 9 through the exhaust gas duct 7 in the same manner as described above.
The unburned gas such as CO gas is burned, and the high-temperature gas with increased thermal energy is introduced into the furnace shell 1 on the preheating side to efficiently preheat the scrap.

上記実施例の説明は、通常の省電力操業の場合である
が、例えば電気料金が低廉な夜間などにおいては、初期
溶湯生成のための溶解の合間に操業側の炉の方へ通電溶
解のための装置13〜15を旋回移動し、(駆動設備は図示
略)燃料吹込み溶解に加えて通電溶解を併用して、操業
時間の短縮をはかることもできる。
The description of the above embodiment is for the case of normal power-saving operation, but, for example, at night when the electricity rate is low, for example, during the melting for the initial molten metal generation, the electric power is melted toward the furnace on the operating side. It is also possible to shorten the operating time by rotating the devices 13 to 15 of (1) and (in addition to driving equipment) not only fuel injection melting but also electric melting.

なお図示の実施例においては、三相交流アーク炉を用い
た場合について示してあるが、これに限定されるもので
はなく、直流アーク炉,燃焼炉などの溶解炉であっても
よいことはもちろんである。
In the illustrated embodiment, the case of using a three-phase AC arc furnace is shown, but the present invention is not limited to this, and needless to say, a melting furnace such as a DC arc furnace or a combustion furnace may be used. Is.

〔効果〕〔effect〕

以上説明したように、この発明は、2基一対とする炉殻
を有し、一方が操業側となるとき他方が予熱側となる複
式溶解炉において、上記各炉殻に連通する初期溶湯供給
用炉殻と、前記各炉殻を接続する排ガスダクト中に介装
する燃焼筒とを用い、操業側の炉殻からの排ガス中の未
燃ガスを燃焼筒で燃焼させたのちに予熱側の炉殻へ導入
し、当該予熱側の炉殻内でスクラップを予熱したのちの
排ガスを初期溶湯供給用炉殻内に導入して排ガス中の臭
気成分を分解するようにしたので、炭材や酸素等の燃料
の吹込みにより発生するCOを主成分とする大量の未燃ガ
スが燃焼筒において燃焼して排ガスの熱エネルギーが高
められ、その高温ガスを予熱側の炉へ導入することによ
り排ガスエネルギーの有効利用を高効率にはかることが
できる。また、予熱側のスクラップから発生する臭気成
分は初期溶湯供給用溶解炉に導入されて高温炉内で熱分
解されるため、臭気の排出がないと同時に臭気を発生す
るスクラップの予熱に際しても操業側の炉からの高温排
ガスの全量を予熱に使用することができる。これらによ
り炭材や酸素等の燃料吹込みにより発生する大量の排ガ
スエネルギーを有効に利用することが可能となるととも
に、スクラップの品質に制約を受けることなく無臭高温
予熱を行なうことができる優れた効果が得られる。
As described above, the present invention is a dual melting furnace having two pairs of furnace shells, one of which is on the operating side and the other of which is on the preheating side, for supplying the initial molten metal to each of the furnace shells. Using a furnace shell and a combustion cylinder interposed in an exhaust gas duct connecting the furnace shells, the unburned gas in the exhaust gas from the furnace shell on the operating side is burned in the combustion cylinder, and then the furnace on the preheating side. After introducing it into the shell and preheating the scrap in the preheating side furnace shell, the exhaust gas was introduced into the initial molten metal supply furnace shell to decompose the odorous components in the exhaust gas, so carbonaceous materials, oxygen, etc. A large amount of unburned gas containing CO as a main component is burned in the combustion cylinder to increase the thermal energy of the exhaust gas, and the high-temperature gas is introduced into the furnace on the preheating side. Effective utilization can be achieved with high efficiency. In addition, since the odor component generated from the scrap on the preheating side is introduced into the melting furnace for supplying the initial molten metal and pyrolyzed in the high temperature furnace, there is no discharge of odor and at the time of preheating the scrap that also generates odor All of the hot exhaust gas from the furnace can be used for preheating. These make it possible to effectively use a large amount of exhaust gas energy generated by injecting fuel such as carbonaceous materials and oxygen, and have an excellent effect that odorless high temperature preheating can be performed without being restricted by scrap quality. Is obtained.

【図面の簡単な説明】[Brief description of drawings]

図はこの発明の一実施例を示す構成図である。 1,1′……溶解炉の炉殻、2……初期溶湯供給用溶解炉
の炉殻、3,3′,7……排ガスダクト、4,4′……ダンパ、
9……燃焼筒、10……集塵装置。
The drawing is a block diagram showing an embodiment of the present invention. 1,1 ′ …… Smelting furnace shell, 2 …… Smelting furnace shell for initial molten metal supply, 3,3 ′, 7 …… Exhaust gas duct, 4,4 ′ …… Damper,
9 ... Combustion cylinder, 10 ... Dust collector.

フロントページの続き (72)発明者 樋口 貞夫 東京都千代田区大手町2丁目2番1号 石 川島播磨重工業株式会社本社内 (72)発明者 数土 文夫 千葉県千葉市千城台東3−30−1 (72)発明者 上杉 浩之 東京都杉並区本天沼1−22−20 (56)参考文献 特開 昭59−1982(JP,A) 特開 昭58−156185(JP,A) 特開 昭61−55579(JP,A)Front page continuation (72) Inventor Sadao Higuchi 2-2-1 Otemachi, Chiyoda-ku, Tokyo Ishi Kawashima Harima Heavy Industries Co., Ltd. (72) Inventor Fumio Sato 3-30-1 Chijodai, Chiba, Chiba Prefecture (72) Inventor Hiroyuki Uesugi 1-22-20, Amanuma, Suginami-ku, Tokyo (56) Reference JP-A-59-1982 (JP, A) JP-A-58-156185 (JP, A) JP-A 61- 55579 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】2基一対で一方が操業側となるとき他方が
原料予熱側となる溶解用の炉殻と、これら各溶解用の炉
殻と連通して燃料吹込みのための初期溶湯を供給する初
期溶湯供給用炉殻とを備えた複式溶解炉であって、前記
2つの溶解用の炉殻を接続する排ガスダクト中に介装さ
れ操業側の溶解用の炉殻からの排ガス中の未燃ガスを燃
焼させる燃焼筒とを用い、操業側の溶解用の炉殻の排ガ
ス中の未燃ガスを燃焼筒で燃焼させて得た高温燃焼ガス
を前記排ガスダクトで予熱側の炉殻へ導入し、当該予熱
側の溶解用の炉殻内の原料を予熱したのち、この予熱後
の排ガスを初期溶湯を溶解中の前記初期溶湯供給用炉殻
内に導入して排ガス中の臭気成分を熱分解して排気する
ようにしたことを特徴とする複式溶解炉の排ガス熱回収
方法。
Claim: What is claimed is: 1. A melting furnace shell having a pair of two units, one of which is on the operation side and the other of which is on the raw material preheating side, and an initial molten metal for injecting fuel in communication with each of the melting furnace shells. A double melting furnace having a furnace shell for supplying an initial molten metal to be supplied, which is disposed in an exhaust gas duct connecting the two furnace shells for melting and is disposed in an exhaust gas from the furnace shell for melting on the operating side. Using a combustion tube that burns unburned gas, the high-temperature combustion gas obtained by burning the unburned gas in the exhaust gas of the furnace shell for melting on the operating side in the combustion tube to the furnace shell on the preheating side in the exhaust gas duct. After introducing and preheating the raw material in the furnace shell for melting on the preheating side, the exhaust gas after this preheating is introduced into the initial molten metal supply furnace shell during melting of the initial molten metal to remove the odorous components in the exhaust gas. An exhaust gas heat recovery method for a double melting furnace, characterized in that it is thermally decomposed and exhausted.
JP7799486A 1986-04-04 1986-04-04 Exhaust gas heat recovery method for dual melting furnace Expired - Lifetime JPH07803B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7799486A JPH07803B2 (en) 1986-04-04 1986-04-04 Exhaust gas heat recovery method for dual melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7799486A JPH07803B2 (en) 1986-04-04 1986-04-04 Exhaust gas heat recovery method for dual melting furnace

Publications (2)

Publication Number Publication Date
JPS62235414A JPS62235414A (en) 1987-10-15
JPH07803B2 true JPH07803B2 (en) 1995-01-11

Family

ID=13649366

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7799486A Expired - Lifetime JPH07803B2 (en) 1986-04-04 1986-04-04 Exhaust gas heat recovery method for dual melting furnace

Country Status (1)

Country Link
JP (1) JPH07803B2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58156185A (en) * 1982-03-12 1983-09-17 川崎重工業株式会社 Preheater for scrap of electric furnace
JPS591982A (en) * 1982-06-28 1984-01-07 大同特殊鋼株式会社 Arc furnace melting method
JPS6155579A (en) * 1984-08-25 1986-03-20 合同製鉄株式会社 Method of preheating scrap by exhaust gas from electric steel-making furnace

Also Published As

Publication number Publication date
JPS62235414A (en) 1987-10-15

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