JPH08302412A - Steel scrap melting furnace and its melting method - Google Patents

Steel scrap melting furnace and its melting method

Info

Publication number
JPH08302412A
JPH08302412A JP10837595A JP10837595A JPH08302412A JP H08302412 A JPH08302412 A JP H08302412A JP 10837595 A JP10837595 A JP 10837595A JP 10837595 A JP10837595 A JP 10837595A JP H08302412 A JPH08302412 A JP H08302412A
Authority
JP
Japan
Prior art keywords
scrap
furnace
slag
melting furnace
melting
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Withdrawn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
JP10837595A
Other languages
Japanese (ja)
Inventor
Kyoji Okumura
恭司 奥村
Hiroyuki Katayama
裕之 片山
Yoshihiro Hatsuta
好弘 八太
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 JP10837595A priority Critical patent/JPH08302412A/en
Publication of JPH08302412A publication Critical patent/JPH08302412A/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Withdrawn legal-status Critical Current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

Landscapes

  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Abstract

PURPOSE: To provide a steel scrap melting furnace capable of charging the raw materials such as the scrap and the iron ore into a furnace through a tube by connecting and piercing a raw material charging tube which is pierced from the outside of the furnace to the inside of the furnace, and provided with small gradient at the tip part in the range corresponding to the nose, the shoulder, and the belly. CONSTITUTION: In a top-blown or a top and bottom-blown steel scrap melting furnace 1, a scrap charging tube 5 which is inclined diagonally upward is arranged on a belly, a nose, or a shoulder while it is extended into the melting furnace 1. The scrap 7 can be pre-heated or melted preliminarily in the molten slag 3, the scattering of the slag splash and the cooling of the slag is eliminated when the raw materials are charged, and the efficient scrap melting can be realized to improve the productivity without providing the disturbance of the slag surface through the slag layer of high temperature to fluctuate the secondary combustion ratio or the heat gaining efficiency.

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、二次燃焼率および着熱
効率の優れた鋼スクラップ溶解炉及び溶解方法に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steel scrap melting furnace and a melting method which are excellent in secondary combustion rate and heat deposition efficiency.

【0002】[0002]

【従来の技術】近年、資源、環境問題から、スクラップ
などの固体金属原料をリサイクル使用して、効率的に溶
融金属を製造することが技術課題となって来ている。そ
の金属スクラップの種類は種々のものがあるが、発生量
の多い鉄鋼スクラップを用いて溶融鉄を得る方法とし
て、従来は殆ど電気炉で行われて来た。しかし、電気炉
の場合は、スクラップの溶解・精錬に多くの電力を消費
するため、わが国のように電力価格が著しく高い国では
溶解コストが増加するので好ましくない。そこで、電気
炉によらずに経済的にスクラップの溶解・精錬する方法
として、高送酸能力を有する転炉の余剰生産能力を利用
して安価な炭材を用いたスクラップの溶解・精錬方法が
検討されるようになって来た。
2. Description of the Related Art In recent years, it has become a technical subject to efficiently produce molten metal by recycling solid metal raw materials such as scrap due to resource and environmental problems. There are various kinds of metal scraps, but as a method for obtaining molten iron by using steel scrap, which has a large amount of generation, conventionally, most has been carried out in an electric furnace. However, the electric furnace consumes a large amount of electric power for melting and refining scrap, and therefore, the melting cost increases in a country with a significantly high electric power price such as Japan, which is not preferable. Therefore, as a method for economically melting and refining scrap without using an electric furnace, there is a method for melting and refining scrap using inexpensive carbonaceous materials by utilizing the surplus production capacity of a converter having a high acid transfer capacity. It has come to be considered.

【0003】このような状況の中で、一般的には既存の
上底吹きの複合吹錬転炉を利用することで設備増を低く
抑えると共に、スクラップと一緒に炉内に装入した火種
に着火した後、上底吹き吹錬の際に炉上方から熱源とし
ての炭材を投入しながら溶解・精錬する方法が提案され
ている。この上吹き又は上底吹き転炉を用いてスクラッ
プを溶解する場合においては、通常は炭材やスクラップ
の原料投入は炉肩や炉上からスクラップ投入管を延ばし
て炭材等をスラグ中に投入する方法が行われているのが
実状である。
Under such circumstances, generally, by utilizing the existing upper-bottom-blown composite blowing converter, the increase in equipment can be suppressed to a low level, and at the same time, the fire species charged in the furnace together with scrap can be used. After igniting, a method of melting and refining while charging carbonaceous material as a heat source from above the furnace at the time of blowing from the top and bottom is proposed. When scrap is melted using this top-blown or top-blown converter, the raw material for the carbonaceous materials and scrap is usually put into the slag by extending the scrap feeding pipe from the furnace shoulder or above the furnace. It is the actual situation that the method of doing is done.

【0004】[0004]

【発明が解決しようとする課題】上述したように、炉肩
や炉上からの原料投入によると投入原料の落下時に溶融
スラグ飛沫の飛散が発生し、そのFeO含有スラグが炉
内壁耐火物表面に付着して耐火物損耗の原因となった
り、原料投入した時に炉内のスラグの一部が冷却されて
温度ムラ、流動ムラができたり、スラグ面を乱し、炉内
のガス流れや反応の定常状態を崩し、さらにはスクラッ
プや鉄鉱石が着熱する場所であるスラグ層を貫通してし
まうという問題がある。
As described above, when the raw material is charged from the furnace shoulder or on the furnace, splash of molten slag is generated when the charged raw material is dropped, and the FeO-containing slag is deposited on the refractory surface of the furnace inner wall. Adhesion may cause refractory wear, or part of the slag in the furnace may be cooled when the raw material is charged, resulting in temperature unevenness and flow unevenness, disturbing the slag surface and causing gas flow and reaction in the furnace. There is a problem that the steady state is disrupted and the scrap or iron ore penetrates the slag layer where it heats.

【0005】[0005]

【課題を解決するための手段】上述したような問題を解
消するため、発明者らは鋭意検討を重ねた結果、炉外側
から炉内部に貫通し、その先端部に緩やかな傾斜を有す
る原料投入用管を、炉口〜炉肩〜炉腹に相当する範囲に
連結・貫通させ、その投入管先端の投入孔の少なくとも
一部が溶融金属浴あるいは溶融スラグ層あるいはそれら
両方に接するように配設することによって、スクラップ
の投入・落下速度を極力落とすと同時に、熱供給源近く
にスクラップを長時間滞留させることを可能にし、これ
により溶融スラグ飛沫の飛散を防止でき、溶融スラグ層
や溶融スラグ−溶融金属浴界面の乱れを抑えることがで
き、さらに溶融スラグの温度ムラや流動ムラの発生をも
防止でき、二次燃焼率および着熱効率の低下あるいは変
動を防止できる鋼スクラップ溶解炉およびその溶解方法
を提供することにある。
[Means for Solving the Problems] In order to solve the above problems, as a result of intensive studies by the inventors, as a result, the raw material was introduced from the outside of the furnace to the inside of the furnace, and the tip end of which had a gentle inclination. The pipe is connected and penetrated in a range corresponding to the furnace mouth, the furnace shoulder, and the furnace belly, and at least a part of the charging hole at the tip of the charging pipe is arranged so as to be in contact with the molten metal bath, the molten slag layer, or both. By doing so, it is possible to reduce the throwing and dropping speed of the scrap as much as possible, and at the same time, allow the scrap to stay for a long time near the heat supply source, which can prevent the splash of molten slag and prevent the molten slag layer and molten slag. Steel that can suppress the disturbance of the molten metal bath interface, can also prevent the temperature unevenness and flow unevenness of the molten slag, and can prevent the secondary combustion rate and heat deposition efficiency from decreasing or fluctuating. Clap melting furnace and to provide the dissolution method.

【0006】その発明の要旨とするところは、 (1)上吹き又は上底吹き鋼スクラップ溶解炉におい
て、炉腹部、炉口又は炉肩に斜め上向きに傾斜したスク
ラップ投入管を溶解炉の炉内まで延長させて配設するこ
とを特徴とする鋼スクラップ溶解炉。 (2)上吹き又は上底吹き鋼スクラップ溶解炉におい
て、斜め上向きに傾斜したスクラップ投入管を炉腹部に
配設することを特徴とする鋼スクラップ溶解炉。 (3)スクラップ投入管が水平面に対し2種類以上の傾
斜角を有し、かつスラグと接する側の該スクラップ投入
管の先端に近い程、該傾斜角が小さいことを特徴とする
(1)又は(2)記載の鋼スクラップ溶解炉。
The gist of the invention is as follows: (1) In a top-blown or top-blown-blown steel scrap melting furnace, a scrap charging pipe inclined obliquely upward to the furnace belly, furnace mouth, or furnace shoulder is used in the furnace of the melting furnace. Steel scrap melting furnace characterized by being installed up to (2) In a top-blown or top-blown steel scrap melting furnace, a scrap charging pipe inclined obliquely upward is arranged in the furnace belly. (3) The scrap input pipe has two or more types of inclination angles with respect to the horizontal plane, and the inclination angle is smaller as the tip of the scrap input pipe on the side in contact with the slag is closer (1) or (2) The steel scrap melting furnace as described above.

【0007】(4)上吹き又は上底吹き鋼スクラップ溶
解方法において、(1)〜(3)のいずれか1に記載の
溶解炉を用いて炭材を添加し、スラグを形成しながらス
クラップを溶解するに際し、スクラップ投入管と該溶解
炉の連結部の一部又は全部に溶融スラグを導入させ、該
溶融スラグによってスクラップ投入管中に投入された鋼
スクラップを滞留させて該溶融スラグ中でスクラップの
予熱、溶解を促進させることを特徴とする鋼スクラップ
溶解方法にある。
(4) In the top-blown or top-bottomed steel scrap melting method, the melting furnace described in any one of (1) to (3) is used to add carbonaceous material to form scrap while forming slag. When melting, the molten slag is introduced into a part or all of the connection part between the scrap charging pipe and the melting furnace, and the steel scrap charged into the scrap charging pipe by the molten slag is retained to scrap in the molten slag. A steel scrap melting method characterized by accelerating preheating and melting of steel scrap.

【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は本発明に係る鋼スクラップ溶解炉の概略断
面図である。図1に示すように、溶解炉1は耐火物ある
いは水冷構造を有するパネルで内張りされた、例えば上
吹き溶解炉であって、酸素上吹きランス2を備えてい
る。また、電気炉による溶解炉であれば酸素上吹きラン
ス2が電極となる。そこで酸素上吹き精錬である場合に
は、酸素上吹きランス2から酸素ガスを溶融金属4上の
溶融スラグ3上に吹き付ける。
The present invention will be described in detail below with reference to the drawings. FIG. 1 is a schematic sectional view of a steel scrap melting furnace according to the present invention. As shown in FIG. 1, the melting furnace 1 is, for example, a top-blown melting furnace lined with a refractory material or a panel having a water-cooled structure, and includes an oxygen top-blown lance 2. If the melting furnace is an electric furnace, the oxygen top-blown lance 2 serves as an electrode. Therefore, in the case of oxygen top blowing refining, oxygen gas is blown from the oxygen top blowing lance 2 onto the molten slag 3 on the molten metal 4.

【0009】一方、炉腹部に斜め上向きに傾斜したスク
ラップ投入管5よりスクラップ7を装入する。この場合
にスクラップ投入管5にプッシャー8またはベルトコン
ベアを連結させて、プッシャー8によりスクラップ投入
管内に装入する。また、炉腹部に斜め上向きに配設した
スクラップ投入管5と溶解炉1との連結部における上向
き傾斜角度θを3〜85°の範囲内に設定する。その理
由として、3°未満であると投入管5内におけるスクラ
ップの滑り落ちる速度が遅くなり過ぎて、投入管5内で
スクラップが詰まってしまったり、溶解炉1から投入管
5内に流出入する溶融スラグの入替えが円滑に行われな
くなって、溶融スラグの一部が滞留して冷えてしまった
り、スクラップが投入管5内で溶融あるいは溶解した後
も傾斜角度に沿って溶解炉1側に自然移動しなくなり、
融着してしまうなどの問題が起きる。反対に傾斜角度θ
を増やし過ぎて85°を越えると、溶解炉1の真上から
スクラップを投入する場合のスクラップ移動・落下速度
(溶融スラグ層への衝突エネルギー)と余り差が見られ
ず、本発明の硬化が期待できなくなる。
On the other hand, the scrap 7 is loaded into the furnace abdomen through the scrap charging pipe 5 which is inclined obliquely upward. In this case, a pusher 8 or a belt conveyor is connected to the scrap input pipe 5, and the scraper 8 is loaded into the scrap input pipe. Further, the upward inclination angle θ at the connecting portion between the scrap charging pipe 5 and the melting furnace 1 arranged obliquely upward in the furnace belly is set within the range of 3 to 85 °. If the angle is less than 3 °, the slipping speed of the scrap in the charging pipe 5 becomes too slow and the scrap is clogged in the charging pipe 5, or the melt flowing from the melting furnace 1 into the charging pipe 5 flows in and out. The slag is not replaced smoothly, part of the molten slag stays and cools, and even after the scrap is melted or melted in the charging pipe 5, it naturally moves to the melting furnace 1 side along the inclination angle. No longer
Problems such as fusion will occur. Conversely, the tilt angle θ
If it exceeds 85 ° by increasing too much, there is not much difference between the scrap movement / falling speed (collision energy to the molten slag layer) when the scrap is charged from directly above the melting furnace 1, and the hardening of the present invention can be performed. I can not expect it.

【0010】また、傾斜角度θを1種類とするのが設備
投資費用としては安価で良いが、投入管5先端部(溶融
スラグ存在部位)での滞留時間確保の観点と、投入管5
後端(溶融スラグ不在部位)におけるスクラップ融着や
詰まりなどの操業障害の観点とを兼ね合わせると、投入
管5先端部位の傾斜角度θ1 と投入管5後部の傾斜角度
θ2 に関し、θ1 <θ2 とするのが好ましい。逆に、投
入管5後部の傾斜角度θ2 を小さくすると、ここでのス
クラップ滞留時間が確保できて、高温ガスによるスクラ
ップ予熱時間・温度を充分確保できるので、従来は殆ど
の投入管はθ1 >θ2 であった。そこで上記のθ1 <θ
2 条件を満たす傾斜角度θ2 の投入管5後部の更に後部
に傾斜角度θ3 部位を少なくとも1つ追加し、θ2 >θ
3 としても良い。勿論段階的に傾斜角度をθ1 、θ2
θ3 と設ける代わりに、少なくとも1種類の曲率を持つ
曲面にしても良い。
[0010] Further, although one type of inclination angle θ may be inexpensive as a capital investment cost, the viewpoint of securing the retention time at the tip of the charging pipe 5 (the portion where the molten slag exists) and the charging pipe 5
Taking into consideration the operational problems such as scrap fusion and clogging at the rear end (the part where the molten slag is not present), the inclination angle θ 1 at the tip of the charging pipe 5 and the inclination angle θ 2 at the rear of the charging pipe 5 are θ 12 is preferable. Conversely, reducing the injection tube 5 the rear of the inclination angle theta 2, can be ensured scrap residence time here, it is possible to sufficiently secure the scrap preheating time and temperature due to high temperature gas, the conventional most feeding pipe theta 1 > Θ 2 . Therefore, the above θ 1
2 satisfies the inclination angle theta 2 of the further inclination angle theta 3 site at the rear of the feeding pipe 5 rear adding at least one, theta 2> theta
Good as 3 . Of course, the tilt angles are gradually changed to θ 1 , θ 2 ,
Instead of providing θ 3 , a curved surface having at least one type of curvature may be used.

【0011】このような構成によって、スクラップ投入
管5と溶解炉1との連結部6の一部又は全部に溶解炉か
らの溶融スラグを導入して流出入させ、その先端部に溶
融スラグが導入されたスクラップ投入管5中に反連結部
側から鋼スクラップを導入し、この流動する溶融スラグ
によって鋼スクラップを該スクラップ投入管5中に滞留
させることで、この溶融スラグ中でスクラップが予熱、
溶融、溶解され、更に溶解された金属は随時溶解炉内の
溶融金属浴中に落下するように流動スラグによって加熱
攪拌され、溶解炉1内に溜まる。更には、スクラップ投
入管5上部にガス吹込み羽口9を設けて高温ガスあるい
は燃焼となるCO,LPG,O2 などのガスを吹き込ん
で加熱しても良く、更にこのガス吹込み羽口9より高温
ガスと同時に炭材等を投入しても良い。すなわち、スク
ラップ投入管5の連結部あるいは投入孔6を上吹き酸素
と化石燃料との燃焼点近傍まで延長し、高温ガスとスラ
グを攪拌しながら混合し、その混合物を投入孔からスク
ラップ投入管内に常時流出入させる。このようにしてス
クラップ投入管内先端部において、鋼スクラップを予
熱、溶融、溶解を促進させて生産性を高めるものであ
る。
With such a structure, the molten slag from the melting furnace is introduced into and discharged from a part or all of the connecting portion 6 between the scrap charging pipe 5 and the melting furnace 1, and the molten slag is introduced into the tip portion thereof. Steel scrap is introduced into the scrap input pipe 5 from the side opposite to the connecting portion, and the steel scrap is retained in the scrap input pipe 5 by the flowing molten slag, whereby the scrap is preheated in the molten slag.
The molten, melted, and further melted metal is heated and agitated by the fluidized slag so as to drop into the molten metal bath in the melting furnace at any time, and is accumulated in the melting furnace 1. Further, a gas blowing tuyere 9 may be provided above the scrap feeding pipe 5 to blow hot gas or a gas such as CO, LPG or O 2 which becomes a combustion gas to heat the gas, and the gas blowing tuyere 9 Carbonaceous material may be added at the same time as the higher temperature gas. That is, the connection portion of the scrap charging pipe 5 or the charging hole 6 is extended to the vicinity of the combustion point of the top-blown oxygen and fossil fuel, the high temperature gas and the slag are mixed with stirring, and the mixture is introduced into the scrap charging pipe from the charging hole. Always flow in and out. In this way, the steel scrap is preheated, melted and melted at the tip of the scrap feeding pipe to enhance productivity.

【0012】スクラップ投入管5先端部位に導入する溶
融スラグの組成について、上吹き酸素と炭材との燃焼点
(以下、火点という)の燃焼熱を、溶解炉1内の溶融金
属浴および投入管5内滞留スクラップなどに伝熱するた
めの伝熱媒体が必要となるが、これは従来の炭材(チャ
ーなど)や粒鉄(Fe−C系あるいはFeO)などで良
いが、出来れば粒鉄と炭材の両方を共存させるのが好ま
しい。粒鉄だけでは、いずれ酸化されてFeOとなって
しまうし、熱伝導度が落ちる上、投入管5及び溶解炉1
内壁の耐火物を損耗させてしまし、炭材だけでは熱伝導
度が低いからであり、両者を共存させると粒鉄の酸化・
脱炭を防止しながら高熱伝導度のままで良好な熱媒体を
確保できるからである。
Regarding the composition of the molten slag introduced to the tip portion of the scrap charging pipe 5, the combustion heat at the combustion point (hereinafter referred to as the fire point) between the top-blown oxygen and the carbonaceous material is supplied to the molten metal bath in the melting furnace 1 and charged. A heat transfer medium is required to transfer heat to the scrap retained in the pipe 5, which may be conventional carbonaceous material (such as char) or granular iron (Fe-C-based or FeO), but if possible, granular It is preferable to coexist both iron and carbonaceous material. If only granular iron is used, it will eventually be oxidized into FeO, the thermal conductivity will decrease, and the charging pipe 5 and the melting furnace 1 will
This is because the refractory on the inner wall is worn away and the thermal conductivity is low with carbon material alone.
This is because it is possible to secure a good heat medium with high thermal conductivity while preventing decarburization.

【0013】投入管5の先端部の投入孔の少なくとも一
部が、溶融スラグ層あるいは溶融スラグ−溶融金属界面
あるいは溶融金属浴に接するようにするのが良い理由
は、投入管5投入孔全体をスラグ層内に配設すると、高
温の酸化性ガスが直接投入管5内に流入せず、投入管5
内壁を保護できることと、高温の溶融スラグ中にスクラ
ップを滞留させて直接接触させた方が、スクラップ加熱
効率が良いからである。同一温度のスラグとガスを比較
した場合、スクラップとの接触時間も考慮すると溶融ス
ラグの方が効率が良い。
The reason why it is preferable that at least a part of the charging hole at the tip of the charging pipe 5 is in contact with the molten slag layer, the molten slag-molten metal interface or the molten metal bath is When it is arranged in the slag layer, the high temperature oxidizing gas does not directly flow into the charging pipe 5,
This is because the inner wall can be protected, and the scrap heating efficiency is better if the scrap is retained in the molten slag at high temperature and brought into direct contact with it. When slag and gas at the same temperature are compared, molten slag is more efficient in consideration of the contact time with scrap.

【0014】また、投入管5内のスラグのない位置で、
スクラップを予熱する方法は、溶解炉1内で生成する高
温排ガスによる方法が最も省エネルギーになる。そこで
投入管5投入孔の上側を溶融スラグ層から出しておけ
ば、投入孔上側から高温排ガスが流入して、投入孔内下
側には溶融スラグがあって直接スクラップに熱を与える
ことが可能となる。投入孔6下側を溶融スラグ層より下
方、すなわち、溶融スラグ−溶融金属界面あるいは溶融
金属浴とするのは、溶解・液化したスクラップが投入孔
6から溶解炉1内に落下・流入するに際し、再び別の溶
融スラグや炭材、あるいは未燃焼酸素など低温ガスによ
り冷却されると、熱のロスになるので回避した方が良い
から、投入孔6下側に溶融金属浴を導入しておくのが好
ましい。
At a position where there is no slag in the charging pipe 5,
As for the method of preheating scrap, the method of using high temperature exhaust gas generated in the melting furnace 1 is the most energy-saving. Therefore, if the upper side of the charging hole of the charging pipe 5 is taken out from the molten slag layer, high temperature exhaust gas flows in from the upper side of the charging hole, and there is molten slag in the lower side of the charging hole and heat can be directly applied to scrap. Becomes The lower side of the charging hole 6 is below the molten slag layer, that is, the molten slag-molten metal interface or the molten metal bath is used when molten and liquefied scrap is dropped from the charging hole 6 and flows into the melting furnace 1. If it is cooled by another molten slag, carbonaceous material, or low temperature gas such as unburned oxygen again, it causes heat loss and should be avoided. Therefore, the molten metal bath should be introduced below the charging hole 6. Is preferred.

【0015】図2は本発明に係る他の実施例を示す溶解
炉の概略断面図である。図2は、図1と同様に溶解炉1
に酸素上吹きランス2を備え、酸素上吹きランス2より
酸素ガスを溶融金属4上の溶融スラグ3上に吹き付け
る。石炭やコークスなどの炭材及びスクラップ7は炉腹
部に斜め上向きに傾斜したスクラップ投入管5より装入
する。投入管5先端の投入孔の上側はスラグ層上面より
上に、投入孔6の下側は溶融スラグ層3内になるように
配置した。この場合、スクラップ投入管5の下部にプッ
シャー8´を設け、このプッシャー8´を用いてスクラ
ップ等をスクラップ投入管内に装入するものである。ま
た、スクラップ投入管5に配設したガス吹込み羽口9か
ら溶解炉内と同様に酸素ガスを吹込んでスクラップおよ
び溶融スラグ3とを予熱、溶解するものである。
FIG. 2 is a schematic sectional view of a melting furnace showing another embodiment according to the present invention. FIG. 2 shows a melting furnace 1 similar to FIG.
Is equipped with an oxygen top blowing lance 2, and oxygen gas is blown onto the molten slag 3 on the molten metal 4 from the oxygen top blowing lance 2. Charcoal materials such as coal and coke and scrap 7 are charged into the furnace belly through a scrap charging pipe 5 inclined obliquely upward. The upper side of the charging hole at the tip of the charging pipe 5 was arranged above the upper surface of the slag layer, and the lower side of the charging hole 6 was arranged inside the molten slag layer 3. In this case, a pusher 8'is provided below the scrap input pipe 5, and scraps and the like are loaded into the scrap input pipe using this pusher 8 '. Further, oxygen gas is blown from the gas blowing tuyere 9 arranged in the scrap feeding pipe 5 in the same manner as in the melting furnace to preheat and melt the scrap and the molten slag 3.

【0016】[0016]

【実施例】スクラップ投入管入口の下端をスラグ層下面
から0.5m上方地点とし、スクラップ投入管口上端を
スラグ層上面から0.5m上方地点に設けた。スラグ層
の厚みを1.5mとし、溶解操業を行った。炉内で発生
する1850℃の高温排ガスをスクラップ投入管入口へ
導入し、このスクラップは連結部入口から流入したスラ
グと高温ガスを混合した部分で1300℃以上に予熱し
た後、炉内に投入した。一部は予熱・浸炭により溶解し
て液体になって流れ込んだ。これにより生産速度は従来
の100t/hから150t/hに向上した。このよう
に溶解炉に連結するスクラップ投入管を配設すること
で、スクラップ投入管内での溶融スラグによるスクラッ
プ予熱、溶解が可能となり生産性の向上を図ることが出
来た。
[Example] The lower end of the scrap feeding pipe inlet was located 0.5 m above the lower surface of the slag layer, and the upper end of the scrap feeding pipe inlet was located 0.5 m above the upper surface of the slag layer. The melting operation was performed with the slag layer having a thickness of 1.5 m. High-temperature exhaust gas of 1850 ° C generated in the furnace was introduced into the inlet of the scrap feeding pipe, and this scrap was preheated to 1300 ° C or higher at the portion where the slag and the high temperature gas mixed in from the inlet of the connection part were preheated and then fed into the furnace. . Part of it melted by preheating and carburizing to become a liquid and flowed in. As a result, the production speed was improved from the conventional 100 t / h to 150 t / h. By arranging the scrap charging pipe connected to the melting furnace in this way, it is possible to preheat and melt the scrap by the molten slag in the scrap charging pipe, thereby improving the productivity.

【0017】[0017]

【発明の効果】以上述べたように、本発明による溶解炉
に連結するスクラップ投入管内を通してスクラップや鉄
鉱石などの原料を溶解炉内に投入することにより、従来
の炉肩、炉上から投入するものに比較して予めスクラッ
プ層内でのFeOを製造することが出来、また、原料投
入落下時でのスラグ飛沫の飛散及びスラグ冷却がなく、
しかも、高温のスラグ層を貫通して、スラグ面を乱し、
二次燃焼率、着熱効率の変動を与えることなく効率良く
スクラップ溶解が可能となり、生産性向上を図ることが
出来る等々工業上極めて優れた効果を奏するものであ
る。
As described above, the raw materials such as scrap and iron ore are introduced into the melting furnace through the scrap introducing pipe connected to the melting furnace according to the present invention, so that they are introduced from the conventional shoulder and the furnace. FeO can be manufactured in advance in the scrap layer as compared with the above, and there is no scattering of slag droplets and slag cooling when the raw material is dropped,
Moreover, it penetrates the hot slag layer and disturbs the slag surface,
Scrap can be efficiently melted without changing the secondary combustion rate and the heat deposition efficiency, and productivity can be improved, which is an extremely excellent industrial effect.

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

【図1】本発明に係る鋼スクラップ溶解炉の概略断面
図、
FIG. 1 is a schematic sectional view of a steel scrap melting furnace according to the present invention,

【図2】本発明に係る他の実施例を示す溶解炉の概略断
面図である。
FIG. 2 is a schematic sectional view of a melting furnace showing another embodiment according to the present invention.

【符号の説明】[Explanation of symbols]

1 溶解炉 2 酸素上吹きランス 3 溶融スラグ 4 溶融金属 5 スクラップ投入管 6 投入孔 7 スクラップ 8、8´ プッシャー 9 ガス吹込み羽口 1 Melting furnace 2 Oxygen top blowing lance 3 Molten slag 4 Molten metal 5 Scrap charging pipe 6 Charging hole 7 Scrap 8, 8'pusher 9 Gas blowing tuyere

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 上吹き又は上底吹き鋼スクラップ溶解炉
において、炉腹部、炉口又は炉肩に斜め上向きに傾斜し
たスクラップ投入管を溶解炉の炉内まで延長させて配設
することを特徴とする鋼スクラップ溶解炉。
1. In a top-blown or top-blown-blown steel scrap melting furnace, a scrap charging pipe inclined obliquely upward is installed at the furnace belly, furnace mouth or furnace shoulder so as to extend into the furnace of the melting furnace. And steel scrap melting furnace.
【請求項2】 上吹き又は上底吹き鋼スクラップ溶解炉
において、斜め上向きに傾斜したスクラップ投入管を炉
腹部に配設することを特徴とする鋼スクラップ溶解炉。
2. A steel scrap melting furnace in a top-blown or bottom-blown steel scrap melting furnace, wherein a scrap charging pipe inclined obliquely upward is disposed in a furnace belly.
【請求項3】 スクラップ投入管が水平面に対し2種類
以上の傾斜角を有し、かつスラグと接する側の該スクラ
ップ投入管の先端に近い程、該傾斜角が小さいことを特
徴とする請求項1又は2記載の鋼スクラップ溶解炉。
3. The scrap input pipe has two or more kinds of inclination angles with respect to a horizontal plane, and the inclination angle is smaller as the scrap input pipe is closer to the tip of the scrap input pipe on the side in contact with the slag. The steel scrap melting furnace according to 1 or 2.
【請求項4】 上吹き又は上底吹き鋼スクラップ溶解方
法において、請求項1〜3のいずれか1項に記載の溶解
炉を用いて炭材を添加し、スラグを形成しながらスクラ
ップを溶解するに際し、スクラップ投入管と該溶解炉の
連結部の一部又は全部に溶融スラグを導入させ、該溶融
スラグによってスクラップ投入管中に投入された鋼スク
ラップを滞留させて該溶融スラグ中でスクラップの予
熱、溶解を促進させることを特徴とする鋼スクラップ溶
解方法。
4. In a method for melting top-blown or bottom-blown steel scrap, carbon material is added using the melting furnace according to any one of claims 1 to 3 to melt scrap while forming slag. At this time, molten slag is introduced into a part or all of the connection part between the scrap input pipe and the melting furnace, and the steel scrap injected into the scrap input pipe is retained by the molten slag to preheat the scrap in the molten slag. , A method for melting steel scrap, characterized by accelerating the melting.
JP10837595A 1995-05-02 1995-05-02 Steel scrap melting furnace and its melting method Withdrawn JPH08302412A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10837595A JPH08302412A (en) 1995-05-02 1995-05-02 Steel scrap melting furnace and its melting method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10837595A JPH08302412A (en) 1995-05-02 1995-05-02 Steel scrap melting furnace and its melting method

Publications (1)

Publication Number Publication Date
JPH08302412A true JPH08302412A (en) 1996-11-19

Family

ID=14483182

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10837595A Withdrawn JPH08302412A (en) 1995-05-02 1995-05-02 Steel scrap melting furnace and its melting method

Country Status (1)

Country Link
JP (1) JPH08302412A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012172214A (en) * 2011-02-23 2012-09-10 Jfe Steel Corp Method for charging cold iron source into converter

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012172214A (en) * 2011-02-23 2012-09-10 Jfe Steel Corp Method for charging cold iron source into converter

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