JPH08311525A - Method for melting steel scrap and melting furnace - Google Patents

Method for melting steel scrap and melting furnace

Info

Publication number
JPH08311525A
JPH08311525A JP11487595A JP11487595A JPH08311525A JP H08311525 A JPH08311525 A JP H08311525A JP 11487595 A JP11487595 A JP 11487595A JP 11487595 A JP11487595 A JP 11487595A JP H08311525 A JPH08311525 A JP H08311525A
Authority
JP
Japan
Prior art keywords
steel scrap
furnace
melting
burner
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.)
Withdrawn
Application number
JP11487595A
Other languages
Japanese (ja)
Inventor
Kyoji Okumura
恭司 奥村
Shinya Kitamura
信也 北村
Toshiya Harada
俊哉 原田
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP11487595A priority Critical patent/JPH08311525A/en
Publication of JPH08311525A publication Critical patent/JPH08311525A/en
Withdrawn legal-status Critical Current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

Abstract

PURPOSE: To provide a method and a melting furnace for melting steel scrap which can prevent the insertion of a metal into a burner tuyere at the time of stopping gas supply, by preventing the remaining of non-melting scrap in the melting furnace and using the tuyeres for burner and for stirring jointly. CONSTITUTION: In the method for melting the steel scrap with an electric furnace or a top-bottom combined blowing refining furnace 1, while conducting an electrode of supplying oxygen, the steel scrap is melted, and gas for stirring is blown from at least one tuyere 5 arranged at the furnace bottom to stir the molten iron. While injecting carbonaceous material and oxygen-containing gas through the burner 7 arranged at the furnace bottom separated from the tuyere 5, the steel scrap is melted, and after melting a part of the steel scrap, the gas for stirring is blown from the burner 7.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、鋼スクラップの溶解法
及び溶解炉に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steel scrap melting method and a melting furnace.

【0002】[0002]

【従来の技術】従来、上底吹き転炉あるいは上底吹き溶
解炉を用いて、残留又は装入ないしは少量の溶銑を種湯
として炉上方から鋼スクラップ、炭材を装入し、上吹き
吹酸により炭材を燃焼させて得た熱で鋼スクラップを溶
解して、炉内の溶銑を増量させ、所定の溶銑量に達した
後出湯する鋼スクラップ溶解法は、鋼スクラップから電
力を用いることなく、容易に溶銑を製造することができ
るため、新しい溶銑製造方法として、例えば「最近のア
ーク炉製鋼法の進歩」(1986.6.21発行)日本
鉄鋼協会、第212頁記載のKS転炉技術や出願人らの
特開平2−141511号公報などのように広く行われ
ている。出湯時は転炉の一部の溶銑を残留せしめ、この
残留溶銑を次のチャージの種湯として用いることが多
い。
2. Description of the Related Art Conventionally, an upper-bottom blowing converter or an upper-bottom blowing melting furnace is used to charge steel scrap and carbonaceous material from the upper side of the furnace with residual or charged or a small amount of hot metal as a seed hot water, and then blow-blown. The steel scrap melting method, in which steel scrap is melted by the heat obtained by burning the carbonaceous material with an acid to increase the amount of hot metal in the furnace, and the molten metal is discharged after reaching a predetermined amount of hot metal, uses electricity from the steel scrap. Therefore, as a new hot metal production method, for example, "Recent Advances in Arc Furnace Steelmaking" (issued on June 21, 1986) by the Iron and Steel Institute of Japan, KS Converter It is widely practiced as in technology and Japanese Patent Laid-Open No. 2-141511 by the applicants. At the time of tapping, a part of the hot metal in the converter is allowed to remain, and this residual hot metal is often used as the seed hot water for the next charge.

【0003】しかし、この鋼スクラップ溶解法におい
て、上方からランスを通して吹き込まれる酸素ガスは炭
材および発生COなどの可燃ガス成分を燃焼させて発熱
し、スクラップの溶解熱を供給することが主目的であ
り、底吹きガスは熱供給の補助的な役割の他に溶融鉄浴
を攪拌する目的がある。すなわち、溶融鉄浴面上で発生
する熱の溶融鉄浴全体への伝達促進のために底吹きガス
を供給しており、従来の底吹き羽口はスラグ−溶融鉄浴
攪拌を目的としているのが実状である。
However, in this steel scrap melting method, the main purpose of the oxygen gas blown through the lance from above is to generate heat by burning combustible gas components such as carbonaceous material and generated CO to supply the melting heat of scrap. The bottom blowing gas has the purpose of stirring the molten iron bath in addition to the auxiliary role of heat supply. That is, the bottom blowing gas is supplied to promote the transfer of heat generated on the surface of the molten iron bath to the entire molten iron bath, and the conventional bottom blowing tuyere is intended for stirring the slag-molten iron bath. Is the actual situation.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上述し
た上底吹き複合吹錬においては、底吹ガスによる攪拌が
炭材と酸素の燃焼率を阻害することがあって、余り底吹
ガス量(攪拌力)を増大させることができず、炉内でス
クラップの溶け残りが生じたり、溶け残り対策などのた
め出湯せず残留させた一部の溶銑を次チャージの種湯と
して必要とする場合が多かった。従って、スクラップの
溶け残りや種湯なしによる方法の一つの対策として例え
ば、別にバーナーを追加する方法が考えられるが、炉底
部のバーナーはスクラップの溶解後に不要となって、バ
ーナー羽口からのガス供給を止めるとバーナー羽口部に
溶鉄が差し込んで固まって閉塞し、次チャージで使えな
くなるという問題が生ずる。また、上方或いは横方向か
らのバーナーは、酸素上吹きランスと干渉して必ずしも
熱供給の補助にならなかったり、上吹ランスを溶損する
こともあり、更に、溶け残りは溶融鉄浴下部に存在する
ので余り効果がない。
However, in the above-described top-bottom blowing composite blowing, the agitation by the bottom-blowing gas may impede the burning rate of carbonaceous material and oxygen, and the amount of the bottom-bottom gas (agitation In many cases, some of the hot metal left in the furnace cannot be used as the seed water for the next charge because of the unmelted residue of the scrap in the furnace, and some measures to prevent the unmelted residue. It was Therefore, as one countermeasure against the method of removing the unmelted scrap and leaving no seed water, for example, a method of adding a separate burner may be considered, but the burner at the bottom of the furnace becomes unnecessary after melting the scrap and gas from the burner tuyere When the supply is stopped, molten iron is inserted into the burner tuyere, solidifies and is blocked, and there is a problem that it cannot be used with the next charge. Also, the burner from above or from the side may interfere with the oxygen top blowing lance and may not necessarily assist the heat supply, or may melt the top blowing lance, and the unmelted residue is present in the lower part of the molten iron bath. Because it does, there is not much effect.

【0005】[0005]

【課題を解決するための手段】本発明は、上述したよう
な、従来の鋼スクラップ溶解の問題を解消し、溶解炉内
のスクラップの溶け残りを防止し、バーナー用と攪拌用
を併用した羽口とすることによりガス供給停止時のバー
ナー羽口への地金差しを防止できる鋼スクラップ溶解法
及びその溶解炉を提供するものである。その発明の要旨
とするところは (1)電炉又は上底吹き精錬炉により鋼スクラップを溶
解する方法において、電極を通電しながら又は送酸しな
がら鋼スクラップを溶解し、炉底に設けた少なくとも1
つの羽口から攪拌用ガスを吹き込み溶融鉄を攪拌し、該
羽口と別に炉底に設けたバーナーにより炭材と酸素含有
ガスを吹き込みながら該鋼スクラップを溶解し、該鋼ス
クラップの一部を溶解後は該バーナーから攪拌用ガスを
吹き込むことを特徴とする鋼スクラップの溶解法。
DISCLOSURE OF THE INVENTION The present invention solves the conventional problems of melting steel scrap as described above, prevents the unmelted scrap from remaining in the melting furnace, and uses a blade for both burner and stirring. The present invention provides a method for melting steel scrap and a melting furnace for the same, which can prevent the insertion of metal into the burner tuyere when the gas supply is stopped. The gist of the invention is (1) In a method of melting steel scrap in an electric furnace or a top-bottom blowing smelting furnace, at least 1 which is provided on the bottom of the furnace is used to melt steel scrap while energizing electrodes or feeding oxygen.
A stirring gas is blown from two tuyere to stir the molten iron, and the steel scrap is melted while a carbon material and an oxygen-containing gas are blown by a burner provided separately from the tuyere to the furnace bottom, and a part of the steel scrap is removed. After melting, a method for melting steel scrap is characterized in that a stirring gas is blown from the burner.

【0006】(2)炉底に設けたバーナーの代わりに、
炉壁に設けたバーナーにより炭材と酸素含有ガスを吹き
込みながら該鋼スクラップを溶解し、該鋼スクラップの
溶解後は該バーナーから攪拌用ガスを吹き込むことを特
徴とする(1)記載の鋼スクラップの溶解法。 (3)攪拌用ガスとして、窒素、アルゴン、酸素、CO
2 ,CO,LPGの1種又は2種以上を吹き込むことを
特徴とする(1)又は(2)記載の鋼スクラップの溶解
法。
(2) Instead of the burner provided at the bottom of the furnace,
A steel scrap according to (1), characterized in that the steel scrap is melted by blowing a carbonaceous material and an oxygen-containing gas with a burner provided on the furnace wall, and a stirring gas is blown from the burner after melting the steel scrap. Dissolution method. (3) Nitrogen, argon, oxygen, CO as a stirring gas
2. The method for melting steel scrap according to (1) or (2), wherein one or more of CO, LPG and LPG is blown.

【0007】(4)種湯なしで鋼スクラップのみを溶解
することを特徴とする(1)〜(3)のいずれか1項に
記載の鋼スクラップの溶解法。 (5)電極を有する鋼スクラップの溶解炉において、炉
底部に2個以上の攪拌ガス吹き込み用羽口を有し、該羽
口の間に相当する炉底部又は炉壁部に単管、2重管以上
の多重管又は2種以上の集合細管からなるバーナーを少
なくとも1つ有することを特徴とする鋼スクラップの溶
解炉にある。
(4) The method for melting steel scrap according to any one of (1) to (3), characterized in that only the steel scrap is melted without a seed bath. (5) In a steel scrap melting furnace having an electrode, a furnace bottom has two or more stirring gas blowing tuyere, and a single pipe or double pipe is provided in the furnace bottom or the furnace wall portion corresponding to the tuyere. A melting furnace for steel scrap, characterized in that it has at least one burner consisting of multiple tubes or more tubes or two or more kinds of aggregated thin tubes.

【0008】[0008]

【作用】以下、本発明について図面に従って詳細に説明
する。図1は本発明に係る上底吹き転炉による鋼スクラ
ップの溶解炉の縦断面図である。溶解炉1は耐火物2で
内張りされた、例えば転炉で酸素上吹きランス6を備え
ている。酸素上吹きランス6から酸素ガスを溶融鉄3上
の溶融スラグ4に吹き付ける。石炭やコークスなどの炭
材及びスクラップを炉上方から炉内の溶融スラグ4上に
投入する。これらの炭材と上吹き酸素の燃焼熱を溶融ス
ラグ層からその下方にある溶融鉄浴に伝えるために、底
吹き羽口5から、例えばN2 ,Ar,CO,CO2 ,O
2 ,LPGなどのガスを吹込みスラグ層および溶融鉄を
攪拌するものである。
The present invention will be described in detail below with reference to the drawings. FIG. 1 is a vertical sectional view of a melting furnace for steel scrap by an upper-bottom blowing converter according to the present invention. The melting furnace 1 is lined with a refractory material 2, for example, a converter, and is provided with an oxygen top blowing lance 6. Oxygen gas is blown onto the molten slag 4 on the molten iron 3 from the oxygen top blowing lance 6. Charcoal materials such as coal and coke and scrap are charged from above the furnace onto the molten slag 4 in the furnace. In order to transfer the heat of combustion of these carbon materials and top-blown oxygen from the molten slag layer to the molten iron bath therebelow, for example, N 2 , Ar, CO, CO 2 , O
2. Gases such as LPG are blown in to stir the slag layer and molten iron.

【0009】一方、底吹き羽口5とは別に設けたバーナ
ー7により炭材と酸素含有ガスを吹き込みながら、溶融
鉄浴下部に存在する未溶解鋼スクラップの一部を溶解
し、溶解操業末期はこのバーナー7から、底吹き羽口5
と同様に攪拌用ガスを吹き込むように構成するものであ
る。すなわち、溶融鉄浴攪拌のためのガス吹き込み用に
設けた底吹き羽口5とは別であって、底吹き羽口5と底
吹き羽口5の間に、別の炉底羽口であるバーナー7を設
け、このバーナー7からは酸素と微粉炭などの炭材や灯
油を吹き込み溶解及び加熱バーナーとするものである。
バーナー7直上及び周辺の鋼スクラップの溶解後は溶解
熱供給用バーナーとしての役目は不要になるため、この
バーナー羽口からの酸素や炭材などの燃料の吹き込みを
止め、これと同時にガス種を変更して攪拌用ガス吹き込
み羽口として用いれば、バーナー羽口に溶鉄が差し込ん
で閉塞することがなくなる。また、溶融鉄浴攪拌用の底
吹き羽口5のみとして、溶解バーナー併用とするため2
種類以上の集合細管羽口を用いて溶解初期は灯油あるい
は酸素と炭材を吹き込み、溶解後は攪拌用ガス(例えば
窒素)やCOガスに切替え可能とするものである。
On the other hand, while the carbonaceous material and the oxygen-containing gas are blown by a burner 7 provided separately from the bottom blowing tuyere 5, a part of the unmelted steel scrap existing in the lower portion of the molten iron bath is melted, and at the end of the melting operation, From this burner 7, bottom blown tuyere 5
Similarly to the above, the stirring gas is blown in. That is, it is different from the bottom blowing tuyere 5 provided for blowing gas for stirring the molten iron bath, and is another furnace bottom tuyere between the bottom blowing tuyere 5 and the bottom blowing tuyere 5. A burner 7 is provided, and oxygen and carbonaceous materials such as pulverized coal and kerosene are blown from the burner 7 to be a melting and heating burner.
After melting the steel scrap directly above and around the burner 7, the function as a melting heat supply burner is no longer necessary. Therefore, the injection of fuel such as oxygen and carbonaceous material from the burner tuyere is stopped, and at the same time, the gas species is changed. If changed and used as a stirring gas blowing tuyere, molten iron will not be plugged into the burner tuyere and clogged. Also, only the bottom blowing tuyere 5 for stirring the molten iron bath is used together with the melting burner.
Kerosene or oxygen and carbonaceous materials are blown in the initial stage of melting by using more than one kind of collecting thin tube tuyere, and after the melting, it is possible to switch to a stirring gas (for example, nitrogen) or CO gas.

【0010】図2は本発明に係る他の実施例を示す横吹
き溶解炉の縦断面図である。図2に示すように、炉底に
設けたバーナーの代わりに、炉壁、特にスラグ層の存在
する位置あるいは操業中溶融鉄浴に相当する位置に設け
た横吹きバーナー8により炭材と酸素含有ガスを吹き込
みながら、炉内壁のそばに存在する鋼スクラップを溶解
し、鋼スクラップの溶解後はこの横吹きバーナー8から
攪拌用ガスに変えて吹き込む。すなわち、攪拌用ガスと
してN2 ,Ar,CO2 ,CO,O2 ,LPGの1種又
は2種以上を吹き込む。
FIG. 2 is a vertical sectional view of a horizontal blowing melting furnace showing another embodiment according to the present invention. As shown in FIG. 2, instead of the burner provided at the bottom of the furnace, the side wall burner 8 provided at the position where the furnace wall exists, particularly the slag layer or the position corresponding to the molten iron bath during operation, contains carbonaceous materials and oxygen. While the gas is being blown, the steel scrap existing near the inner wall of the furnace is melted, and after the steel scrap is melted, the side blowing burner 8 is changed to a stirring gas and blown. That, N 2, Ar, CO 2 , CO, O 2, blown LPG 1 or more kinds of the stirring gas.

【0011】図3は本発明に係る他の実施例を示す電気
炉の縦断面図である。図3に示すように、底吹き可能な
電気炉9の上部中心部分には1本の電極10が設けら
れ、この電極10に通電することによりスクラップを溶
解する。また、炉底11の炉体中心付近には底吹きバー
ナー7を、その周囲には3つの底吹き羽口5を設ける。
炉壁には水冷パネル12を内張りして、底吹き羽口5か
らは炉体9内の溶融鉄浴3にガスを吹き込む構造をな
し、外部の攪拌ガスの供給源(図示せず)に連通してい
る。一方、炉底中心付近に設けた底吹きバーナー7は酸
素と微粉炭などの炭材や灯油を吹き込み溶解用及び加熱
用バーナーである。炉内の電極下端から遠い位置であっ
て溶融鉄浴下部炉壁付近に存在する鋼スクラップを溶解
した後あるいは炉内溶融鉄浴満杯状態になった後は、前
述と同様バーナーとしての役目は不要となるため、この
バーナー羽口からはガス種を変更して攪拌ガスを吹き込
む。
FIG. 3 is a vertical sectional view of an electric furnace showing another embodiment according to the present invention. As shown in FIG. 3, one electrode 10 is provided in the central portion of the upper part of the electric furnace 9 capable of bottom blowing, and the scrap is melted by energizing this electrode 10. Further, a bottom blowing burner 7 is provided near the center of the furnace body of the furnace bottom 11, and three bottom blowing tuyeres 5 are provided around it.
A water cooling panel 12 is lined inside the furnace wall so that gas is blown from the bottom blowing tuyere 5 into the molten iron bath 3 inside the furnace body 9 and communicated with an external stirring gas supply source (not shown). are doing. On the other hand, a bottom blowing burner 7 provided near the center of the furnace bottom is a burner for melting and heating by blowing oxygen and carbonaceous materials such as pulverized coal and kerosene. After melting steel scrap existing near the bottom of the molten iron bath lower furnace wall at a position far from the lower end of the electrode in the furnace, or after the molten iron bath in the furnace is full, the role as a burner is not required as described above. Therefore, the gas species are changed and the stirring gas is blown from the burner tuyere.

【0012】図4は本発明に係るバーナーの構造の例を
示す断面図である。この図4に示すように、バーナー中
心部から燃料として炭材、灯油等の燃料14と窒素13
との混合ガス体17を、その外周には酸素15、さらに
外周には冷却用LPG16を流すように構成されるバー
ナー構造からなる。このバーナーにより溶解初期は、例
えば灯油あるいは酸素と炭材を吹き込み、スクラップが
溶解した後は燃料吹き込み部は停止させて、窒素ガス等
の攪拌用ガスに変更して吹き込むように構成している。
FIG. 4 is a sectional view showing an example of the structure of the burner according to the present invention. As shown in FIG. 4, fuel 14 such as carbonaceous material and kerosene and nitrogen 13 are used as fuel from the center of the burner.
The mixed gas body 17 is composed of a burner structure in which oxygen 15 flows on the outer circumference and LPG 16 for cooling flows on the outer circumference. With this burner, for example, kerosene or oxygen and carbonaceous materials are blown in the initial stage of melting, and after the scrap is melted, the fuel blowing section is stopped and changed to a stirring gas such as nitrogen gas and blown.

【0013】[0013]

【実施例】図4に示す多重管よりなるバーナーを用い
て、窒素1Nm3 /min、微粉炭1kg/minと酸
素1Nm3 /minを吹いて溶解炉内の鋼スクラップの
一部を溶解後、底吹きバーナーの微粉炭及び酸素の吹き
込みを停止して、その代わりに、窒素を4Nm3 /mi
n吹き込んで攪拌を行った。これによって微粉炭及び酸
素の吹き込み停止によるバーナー羽口の地金付着はな
く、かつ、スクラップ溶け残りもなく、溶解効果の向上
が図られ、溶解エネルギーコストが従来法に比べて20
%削減できた。これに対して、比較例として電気炉の場
合には電極とは別に炉肩に配したバーナーを設け、さら
にガス攪拌用底吹き羽口を設けてスクラップ溶け残りを
防止する方法を行った。この結果、底吹きガス量を増や
すと溶融鉄浴が冷えてスクラップの溶け残りは解決せ
ず、バーナーも炉下部の溶け残りスクラップには効果が
なく、溶解エネルギーコストは2%の改善にとどまっ
た。
EXAMPLE A burner consisting of multiple tubes shown in FIG. 4 was used to blow 1 Nm 3 / min of nitrogen, 1 kg / min of pulverized coal and 1 Nm 3 / min of oxygen to melt a part of the steel scrap in the melting furnace. The blowing of pulverized coal and oxygen of the bottom-blown burner was stopped and nitrogen was replaced with 4 Nm 3 / mi.
The mixture was blown in and stirred. As a result, there is no metal adhesion to the burner tuyere due to the stoppage of pulverized coal and oxygen, and there is no unmelted scrap remaining, and the melting effect is improved, and the melting energy cost is 20% lower than the conventional method.
It has been reduced by%. On the other hand, as a comparative example, in the case of an electric furnace, a burner arranged on the furnace shoulder was provided separately from the electrodes, and a bottom blown tuyere for gas stirring was provided to prevent scrap unmelted residue. As a result, when the amount of bottom-blown gas is increased, the molten iron bath cools and the unmelted scrap remains unsolved. The burner has no effect on the unmelted scrap in the lower part of the furnace, and the melting energy cost is only improved by 2%. .

【0014】[0014]

【発明の効果】以上述べたように、本発明の溶解炉の実
施によってスクラップ溶け残りは全くなくなり、かつ、
種湯なしで鋼スクラップのみを溶解することが可能とな
り、しかも、設備的に安価で低コストで操業することが
できる等工業上極めて優れた効果を奏するものである。
As described above, by implementing the melting furnace of the present invention, there is no scrap unmelted residue, and
Only the steel scrap can be melted without using the seed water, and furthermore, it is extremely inexpensive in terms of equipment and can be operated at low cost.

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

【図1】本発明に係る上底吹き転炉による鋼スクラップ
の溶解炉の縦断面図、
FIG. 1 is a vertical cross-sectional view of a steel scrap melting furnace by an upper-bottom blowing converter according to the present invention,

【図2】本発明に係る他の実施例を示す横吹き溶解炉の
縦断面図、
FIG. 2 is a vertical sectional view of a horizontal blowing melting furnace showing another embodiment according to the present invention,

【図3】本発明に係る他の実施例を示す電気炉の縦断面
図、
FIG. 3 is a longitudinal sectional view of an electric furnace showing another embodiment according to the present invention,

【図4】本発明に係るバーナーの構造の例を示す断面図
である。
FIG. 4 is a cross-sectional view showing an example of the structure of the burner according to the present invention.

【符号の説明】[Explanation of symbols]

1 溶解炉 2 耐火物 3 溶融鉄 4 溶融スラグ 5 底吹き羽口 6 酸素上吹きランス 7 バーナー 8 横吹きバーナー 9 電気炉 10 電極 11 炉底 12 水冷パネル 13 窒素 14 燃料 15 酸素 16 冷却用LPG 1 Melting Furnace 2 Refractory 3 Molten Iron 4 Molten Slag 5 Bottom Blowing Tuyer 6 Oxygen Top Blowing Lance 7 Burner 8 Side Blowing Burner 9 Electric Furnace 10 Electrode 11 Furnace Bottom 12 Water Cooling Panel 13 Nitrogen 14 Fuel 15 Oxygen 16 LPG for Cooling

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 電炉又は上底吹き精錬炉により鋼スクラ
ップを溶解する方法において、電極を通電しながら又は
送酸しながら鋼スクラップを溶解し、炉底に設けた少な
くとも1つの羽口から攪拌用ガスを吹き込み溶融鉄を攪
拌し、該羽口と別に炉底に設けたバーナーにより炭材と
酸素含有ガスを吹き込みながら該鋼スクラップを溶解
し、該鋼スクラップの一部を溶解後は該バーナーから攪
拌用ガスを吹き込むことを特徴とする鋼スクラップの溶
解法。
1. A method of melting steel scrap in an electric furnace or a top-bottomed refining furnace, wherein the steel scrap is melted while an electrode is energized or while acid is fed, and stirring is performed from at least one tuyere provided in the furnace bottom. Gas is blown to stir the molten iron, and the steel scrap is melted while blowing carbonaceous material and oxygen-containing gas by a burner provided on the furnace bottom separately from the tuyere, and after melting a part of the steel scrap, the burner is used A method for melting steel scrap, characterized by blowing a stirring gas.
【請求項2】 炉底に設けたバーナーの代わりに、炉壁
に設けたバーナーにより炭材と酸素含有ガスを吹き込み
ながら該鋼スクラップを溶解し、該鋼スクラップの溶解
後は該バーナーから攪拌用ガスを吹き込むことを特徴と
する請求項1記載の鋼スクラップの溶解法。
2. The steel scrap is melted while a carbonaceous material and an oxygen-containing gas are being blown by a burner installed in the furnace wall instead of the burner installed in the furnace bottom, and after the steel scrap is melted, stirring is performed from the burner. The method for melting steel scrap according to claim 1, wherein gas is blown into the steel scrap.
【請求項3】 攪拌用ガスとして、窒素、アルゴン、酸
素、CO2 ,CO,LPGの1種又は2種以上を吹き込
むことを特徴とする請求項1又は2記載の鋼スクラップ
の溶解法。
3. The method for melting steel scrap according to claim 1, wherein one or more of nitrogen, argon, oxygen, CO 2 , CO and LPG is blown in as the stirring gas.
【請求項4】 種湯なしで鋼スクラップのみを溶解する
ことを特徴とする請求項1〜3のいずれか1項に記載の
鋼スクラップの溶解法。
4. The method for melting steel scrap according to claim 1, wherein only the steel scrap is melted without a seed water.
【請求項5】 電極を有する鋼スクラップの溶解炉にお
いて、炉底部に2個以上の攪拌ガス吹き込み用羽口を有
し、該羽口の間に相当する炉底部又は炉壁部に単管、2
重管以上の多重管又は2種以上の集合細管からなるバー
ナーを少なくとも1つ有することを特徴とする鋼スクラ
ップの溶解炉。
5. A melting furnace for steel scrap having electrodes, comprising two or more tuyere for blowing a stirring gas at the bottom of the furnace, and a single pipe at the bottom or the wall of the furnace corresponding to the tuyere, Two
A melting furnace for steel scrap, comprising at least one burner consisting of multiple tubes of heavy tubes or more or two or more kinds of aggregated thin tubes.
JP11487595A 1995-05-12 1995-05-12 Method for melting steel scrap and melting furnace Withdrawn JPH08311525A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11487595A JPH08311525A (en) 1995-05-12 1995-05-12 Method for melting steel scrap and melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11487595A JPH08311525A (en) 1995-05-12 1995-05-12 Method for melting steel scrap and melting furnace

Publications (1)

Publication Number Publication Date
JPH08311525A true JPH08311525A (en) 1996-11-26

Family

ID=14648878

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11487595A Withdrawn JPH08311525A (en) 1995-05-12 1995-05-12 Method for melting steel scrap and melting furnace

Country Status (1)

Country Link
JP (1) JPH08311525A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100399229B1 (en) * 1999-10-30 2003-09-22 주식회사 포스코 Cold start operating method of a paused electric furnace
JP2013155273A (en) * 2012-01-30 2013-08-15 Nippon Steel & Sumitomo Metal Corp Soil improvement material and soil improvement method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100399229B1 (en) * 1999-10-30 2003-09-22 주식회사 포스코 Cold start operating method of a paused electric furnace
JP2013155273A (en) * 2012-01-30 2013-08-15 Nippon Steel & Sumitomo Metal Corp Soil improvement material and soil improvement method

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