JPS599117A - Method and device for removing slag in oxygen steel making converter - Google Patents

Method and device for removing slag in oxygen steel making converter

Info

Publication number
JPS599117A
JPS599117A JP11626582A JP11626582A JPS599117A JP S599117 A JPS599117 A JP S599117A JP 11626582 A JP11626582 A JP 11626582A JP 11626582 A JP11626582 A JP 11626582A JP S599117 A JPS599117 A JP S599117A
Authority
JP
Japan
Prior art keywords
converter
slag
furnace
iron
vessel
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.)
Pending
Application number
JP11626582A
Other languages
Japanese (ja)
Inventor
Kyoji Nakanishi
中西 恭二
Kenichiro Suzuki
健一郎 鈴木
Michio Tanaka
道夫 田中
Shinji Kojima
小島 信司
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.)
JFE Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP11626582A priority Critical patent/JPS599117A/en
Publication of JPS599117A publication Critical patent/JPS599117A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/42Constructional features of converters
    • C21C5/46Details or accessories
    • C21C5/4653Tapholes; Opening or plugging thereof

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)

Abstract

PURPOSE:To improve the yield of iron, by flowing slag once into an auxiliary vessel to increase the layer thickness of the slag and to make the skimming easy and returning metal again to a converter, in the stage of skimming. CONSTITUTION:A vessel 2 which is opened at the top and has an axial center intersecting approximately orthogonally with the axial center of the furnace 1 is stuck in the port part of a converter 1 by bringing the opened surface at the top thereof into contact with the edge on the counter tapping side of the port 6 of the furnace 1. The furnace 1 is first tilted to admit the dephosphorized slag floating on the bath surface of the molten iron 3 in the furnace 1 into the auxiliary vessel 2. Since the depth of the slag 4 in the vessel 2 is large, the slag can be easily ladled away by a siphon type slag remover or the like. If the furnace 1 is returned perpendicularly thereafter the iron 3 flowed out into the vessel 2 is returned again into the furnace 1. The successing oxidation refining is thus started immediately, and the loss of the iron 3 in the stage of skimming of the converter 1 is reduced considerably.

Description

【発明の詳細な説明】 本発明は、溶融銑鉄とスクラップとから鋼を製造するL
 D転炉、OBM/Q−BOP転炉、上下吹き複合転炉
などの精錬工程において、鉄歩止ま妙を高めることので
きる除滓方法およびその装置に関するつ 溶融銑鉄とスクラップとを転炉に装入して、気体酸素と
、生石灰、ドロマイト、螢石などの補助材料とを添加し
て溶鋼を製造する工程においては、鉄浴面上に溶融滓が
生成する。溶融滓中には銑鉄、スクラップ中に含まれて
いた不純物、特に燐、硫黄などが移行して存在する。こ
のため、転炉精錬途中において、不純物を含むスラグな
除き、新しい補助材料を添加して再び吹錬を行なう必要
性が生ずる。特に通常の酸化精錬の場合、吹錬の比較的
前期1で脱燐が進行する。この段階のスラグを炉内に保
持したままで吹錬を続けると、鋼浴温度の上昇に伴い、
一旦スラグ中に移行した燐が再び溶鋼中へ戻る現象が見
られる。これは吹錬の効率から言って非常に好ましくな
い。このようなスラグ畦速やかに転炉外に排出すべきで
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for producing steel from molten pig iron and scrap.
In the refining process of D converter, OBM/Q-BOP converter, top-bottom blowing combined converter, etc., molten pig iron and scrap are loaded into the converter. In the process of producing molten steel by adding gaseous oxygen and auxiliary materials such as quicklime, dolomite, and fluorite, molten slag is produced on the surface of the iron bath. Impurities contained in the pig iron and scrap, especially phosphorus and sulfur, migrate into the molten slag. Therefore, during the converter refining process, it becomes necessary to remove slag containing impurities, add new auxiliary materials, and perform blowing again. Particularly in the case of normal oxidation refining, dephosphorization progresses in the relatively early stage 1 of blowing. If blowing continues while the slag at this stage is kept in the furnace, as the steel bath temperature increases,
A phenomenon is observed in which phosphorus, which has once migrated into the slag, returns to the molten steel. This is extremely unfavorable in terms of blowing efficiency. Such slag should be promptly discharged from the converter.

転炉の除滓方法は従来次のように実施されていた。すな
わち、脱燐吹錬を終了した転炉な炉型状態から装入側に
傾転してスラグが自然流出する角度まで傾け、スラグの
流動性が高い場合には自然流出に任せ、スラグの流動性
が劣る場合には、クララチャーなどの掻き出し機を操作
して浴面上に浮遊するスラグを転炉の内部から炉口側に
掻き寄せ、炉口かも排出する方法がとられていた。
Conventionally, the method for removing slag from a converter was carried out as follows. In other words, from the converter-like furnace state after dephosphorization blowing, the furnace is tilted toward the charging side until the slag flows out naturally, and if the slag has high fluidity, it is allowed to flow naturally and the slag flows. In cases where the slag was poor, a scraper such as a clarifier was used to scrape the slag floating on the bath surface from the inside of the converter to the furnace mouth, and then discharge the slag from the furnace mouth as well.

これらの除滓方法では、転炉を傾転した状態におけるス
ラグ層厚が薄いために、スラグと共に不可避的にメタル
が流出してしまい、経済性を著しく阻害する。
In these slag removal methods, since the slag layer is thin when the converter is tilted, metal inevitably flows out together with the slag, which significantly impedes economic efficiency.

本発明は、上述の欠点を除去し、鉄歩止[7の向上を図
る除滓方法を提供することを目的とするものである。
An object of the present invention is to provide a slag removal method that eliminates the above-mentioned drawbacks and improves the quality of iron slag [7].

メタル流出の最大原因は、転炉傾転時に鉄浴面の面積が
広く、スラグ層が浴面上に薄く広がっていることにあり
、これを除滓しようとすれば、不可避的にメタルも流出
してしまうことによる。
The biggest cause of metal leakage is that when the converter is tilted, the surface area of the iron bath is wide and the slag layer is thinly spread over the bath surface.If you try to remove this, metal will inevitably flow out as well. It depends on what you end up doing.

メタル流出を防ぐことは、スラグ層厚を高めて除滓を容
易ならしめ、かつ、メタルを再び転炉に戻す操作によっ
て達成される。本発明は、酸素製鋼炉の除滓に当り、転
炉を炉型状態から装入側に傾転し、溶融鉄浴面上に浮遊
するスラグを一旦補助容器に流入せしめ、次いで該補助
容器からスラグのみを排除し、しかる後に該転炉を炉型
状態とし、前記補助容器に残留した溶鉄を転炉に戻すこ
とを特徴とする除滓方法である。
Preventing metal outflow is achieved by increasing the slag layer thickness to facilitate slag removal and returning the metal to the converter. The present invention involves tilting the converter from a furnace-type state to the charging side when removing slag from an oxygen steelmaking furnace, allowing the slag floating on the surface of the molten iron bath to flow into an auxiliary container, and then from the auxiliary container. This slag removal method is characterized in that only slag is removed, the converter is then brought into a furnace-type state, and the molten iron remaining in the auxiliary container is returned to the converter.

第1図は、本発明方法の説明図で、転炉の傾転時の縦断
面図である。第1図は、転炉1を傾転し転炉中の溶融鉄
3の浴面上に浮遊する脱燐スラグ4を補助容器2に流入
させた状態を示す。
FIG. 1 is an explanatory diagram of the method of the present invention, and is a longitudinal cross-sectional view of the converter during tilting. FIG. 1 shows a state in which the converter 1 is tilted and the dephosphorization slag 4 floating on the bath surface of the molten iron 3 in the converter flows into the auxiliary container 2.

補助容器2中のスラグ4は、深さが深いので、例えばナ
イフオン式スラグ除去装置により容易に汲み出し除去す
ることができる。すなわち、補助容器2中に耐火物で内
張すされた鉄製管路の一端を浸漬し、真空ポンプ等によ
り管路内を一時的に減圧し、当該管路にザイフォン効果
が及ぶようにする。こうすることにより、補助容器内の
スラグは該管路内に吸い上げられ、該管路の他端からス
ラグボットなどの可搬式容器内に連続して排出すること
ができる。
Since the slag 4 in the auxiliary container 2 is deep, it can be easily pumped out and removed using, for example, a knife-on type slag removal device. That is, one end of an iron conduit lined with a refractory material is immersed in the auxiliary container 2, and the pressure inside the conduit is temporarily reduced using a vacuum pump or the like, so that the Zyphon effect is applied to the conduit. By doing so, the slag in the auxiliary container can be sucked up into the conduit and continuously discharged from the other end of the conduit into a portable container such as a slugbot.

補助容器内のスラグ4は、クララチャーなどによる掻き
出しによってスラグのみを排除することももちろんでき
る。
Of course, only the slag 4 in the auxiliary container can be removed by scraping out with a clarifier or the like.

補助容器2内のスラグを排除した後、転炉を1垂に戻せ
ば、補助容器2内に流出していた溶融鉄2は転炉内に再
び戻される。
After the slag in the auxiliary container 2 is removed, the converter is returned to its original position, and the molten iron 2 that has flowed into the auxiliary container 2 is returned to the converter.

かくして引続く酸化精錬が直ちに開始され、転炉の除滓
時の溶融鉄損失を著しく低減することができ、所望の組
成の溶鋼を歩止まりよく吹製することができる。
In this way, the subsequent oxidation refining is started immediately, the loss of molten iron during slag removal from the converter can be significantly reduced, and molten steel of a desired composition can be blown with a good yield.

次に、第2図および第3図は、上述の発明の実施に直接
使用する装置の発明の実施例を示すものである。すなわ
ち、酸素製鋼転炉において、転炉]の炉口部に、転炉1
の軸心とほぼ直交する軸心を有する上面開放容器2を、
その」二面開放面と転炉Jの炉口6の反出鋼側縁とを当
接させて固着したことを特徴とする酸素製鋼転炉である
Next, FIGS. 2 and 3 show an embodiment of the invention of an apparatus directly used for carrying out the above-described invention. That is, in an oxygen steelmaking converter, the converter 1 is placed at the furnace mouth of the converter.
An open top container 2 having an axis substantially perpendicular to the axis of
This is an oxygen steelmaking converter characterized in that the two open faces of the converter J are brought into contact with the opposite side edge of the furnace opening 6 of the converter J and are fixed together.

第2図(a) ij:、第1図のA−A矢視、第2図(
b)は第1図の13−13矢視であり、容器2は、耐火
物で内張すされた容器で、従来の転炉1に着脱可能なよ
うに、恰も転炉の顎のように取りつけられる。
Figure 2 (a) ij:, A-A arrow view in Figure 1, Figure 2 (
b) is a view from arrow 13-13 in Fig. 1, and the container 2 is a container lined with refractory material, and is removably attached to the conventional converter 1, just like the jaws of the converter. Can be attached.

この容器の内張り後の内容積は、転炉内容積グ)30・
第以丁で1−分である。
The internal volume of this container after lining is 30.
It takes 1 minute at the first step.

第2図(b)におい−C15は出鋼1−1を示し、容器
21−、j 、 転炉1の炉[]6の反出鋼fI11の
周縁に上縁を接して11!りつけられ、転炉傾転時にス
ラグの流入を容易にする1゜ 第3図は別の実施例を示し、(a)は縦断面図、(b)
は(a)のC−C矢視四である。第3図の実施例は、転
炉1が恰も瓢慴形をなすように容器2を取りつけたもの
である。この場合も容器2のスラグ受は部(佳、反出鋼
側に設けらJz、その面1火物内張り後の内容積は転炉
内容積の30チ以下で十分でちる。
In FIG. 2(b), the odor C15 indicates the tapped steel 1-1, and the upper edge of the container 21-, j is in contact with the periphery of the unrolled steel fI11 of the furnace [ ] 6 of the converter 1. Figure 3 shows another embodiment, in which (a) is a longitudinal sectional view, (b)
is the fourth view of arrow C-C in (a). In the embodiment shown in FIG. 3, a container 2 is attached to the converter 1 so as to form a gourd-like shape. In this case as well, the slag receiver of the container 2 is provided on the side opposite to the exposed steel, and the internal volume of the container 2 after being lined with fireworks is sufficient to be 30 inches or less of the converter internal volume.

第3[閃の容器r(よ、未燃焼で転炉ガスを回収する場
合に、転炉炉口と〕−ド間の隙間を遮断−七る遮断が容
易で、回収効率上利点がある。
When recovering converter gas without combustion, it is easy to shut off the gap between the converter mouth and the third cylinder, which is advantageous in terms of recovery efficiency.

本発明装置により、転炉排滓を一時貯溜し、スラグ深さ
を深くしてスラグと溶融鉄とを容易に分離して除滓する
ことができ、除滓時の溶#I鉄損失を著減させることが
できる。
With the device of the present invention, it is possible to temporarily store the converter slag, increase the slag depth, easily separate the slag and molten iron, and remove the slag, thereby significantly reducing the loss of molten #I iron during slag removal. can be reduced.

本発明方法おLび装置Iri、高炉溶銑を主原料とする
脱燐吹錬後の中間除滓に用いられるだけでなく、高炉溶
銑の脱硫処理または脱珪処理かどの予備処理を転炉を用
いて実施する際の除滓方法および装置として用いること
ができる。
The method and apparatus Iri of the present invention are not only used for intermediate removal of slag after dephosphorization and blowing using blast furnace hot metal as the main raw material, but also for preliminary treatment of desulfurization or desiliconization of blast furnace hot metal using a converter. It can be used as a method and device for removing slag.

特に、ステンレス鋼など高価な金属を含む鋼の溶製にお
いても、C「還元回j反後の酸末スラグな本発明方法を
用いて除き、しかる後脱硫用のフラックスを添加して経
済的に脱硫処理を施すことができる。この場合、本発明
装置は転炉ではなく、AOD炉、CLU炉などに容器を
泡す付けたものとなる。
In particular, even in the production of steel containing expensive metals such as stainless steel, the method of the present invention can be used to remove the acid slag after the reduction process, and then add flux for desulfurization to make it economical. Desulfurization treatment can be performed.In this case, the apparatus of the present invention is not a converter, but an AOD furnace, a CLU furnace, etc., with a container attached to it.

実施例 51転炉に第2図に示す容器2を取り付けた装置を用い
、吹錬を行なった。
Example 51 Blowing was carried out using a converter equipped with the container 2 shown in FIG. 2.

成分が4.5%C1022%Si、  0.341Mn
Ingredients are 4.5%C1022%Si, 0.341Mn
.

0、129チP、0.006チSで温度が1324℃の
溶銑を4.73を装入し、混焼ドロマイ)23kg/溶
銑t1螢石4.9ky/溶銑t1鉱石とスケ−A・37
.6kg/溶銑t1気体酸素11.3Nff//溶銑t
を使用して吹錬を行なった。
Charge 4.73 of hot metal with a temperature of 1324℃ at 0.129cmP, 0.006cmS, and mix-fired dolomite) 23kg/hot metal t1 fluorite 4.9ky/hot metal t1 ore and scale A.37
.. 6kg/hot metal t1 gaseous oxygen 11.3Nff//hot metal t
The blowing was performed using the.

浴面上のスラグは一旦容器2内に集めた後、クラソチャ
ーにより機械的に掻き出した。最終的に転炉外に除滓さ
れたスラグ歇は秒置の結果3]−,2k17/溶銑tで
あった。一方スラグと共に転炉外に流出した溶鉄量は磁
選秤量の結果1.5 kg/溶銑1てさらに、中間倒炉
時の溶銑成分と温度は、3.25%C10,I9%Mn
、0.011.%P10.O05%S、1370℃と十
分な脱燐が進行していた。
The slag on the bath surface was once collected in the container 2 and then mechanically scraped out using a clay char. The amount of slag sludge finally removed outside the converter was 3]-, 2k17/t of hot metal. On the other hand, the amount of molten iron that flowed out of the converter along with the slag was 1.5 kg/1 hot metal as a result of magnetic separation weighing.Furthermore, the hot metal composition and temperature at the intermediate converter were 3.25%C10, I9%Mn.
, 0.011. %P10. O05%S, 1370°C, and sufficient dephosphorization was progressing.

従来の経験によれば、従来の同一転炉の場合、同一吹錬
パターンでの中間除滓において転炉外への流出溶銑量は
8kg/溶銑tである。
According to conventional experience, in the case of the same conventional converter, the amount of hot metal flowing out of the converter during intermediate slag removal with the same blowing pattern is 8 kg/t of hot metal.

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

第1図は転炉傾転時の転炉の縦断面図、第2図(a) 
、 (b)はそれぞれ第1図の転炉のA−A矢視、B−
13矢視図、第3図(a) 、 (b)は別の転炉の縦
断面図および(81図のC−C矢視図である。 ■・−・転炉 2・・・補助容器 3・・・溶融鉄 4・・・スラグ 5・・・出鋼口 6・・・炉[」 特許出願人 川崎製鐵株式会社 代理人 弁理士 小  杉  佳  男第1図 一 第2図
Figure 1 is a vertical cross-sectional view of the converter during tilting of the converter, Figure 2 (a)
, (b) are the A-A arrow view and B- of the converter in Fig. 1, respectively.
13, and FIGS. 3(a) and 3(b) are a vertical cross-sectional view of another converter and a view taken along the line C-C in FIG. 3... Molten iron 4... Slag 5... Steel tapping port 6... Furnace ['' Patent Applicant Kawasaki Steel Corporation Agent Patent Attorney Yoshio Kosugi Figures 1-2

Claims (1)

【特許請求の範囲】 1 酸素製鋼転炉の除滓に当や、転炉を炉型状態から装
入側に傾転し、溶融鉄浴面上に浮遊するスラグな一旦補
助容器に流入せしめ、次いで該保助容器からスラグのみ
を排除し、しかる後に該転炉を炉型状態とし、前記補助
容器に残留した溶鉄を転炉に戻すことを特徴とする酸素
製鋼転炉の除滓方法。 2 酸素製鋼転炉において、該転炉の炉口部に、該転炉
軸心とほぼ直交する軸心な有する上面開放容器を、該開
放面と該転炉炉口の反出鋼側縁とを当接させて固着した
ととを特徴とする酸素製鋼転炉。
[Claims] 1. When removing slag from an oxygen steelmaking converter, the converter is tilted from the furnace-type state to the charging side, and the slag floating on the surface of the molten iron bath flows into an auxiliary container, A method for removing slag from an oxygen steelmaking converter, comprising: then removing only slag from the auxiliary container, then returning the converter to a furnace-type state, and returning the molten iron remaining in the auxiliary container to the converter. 2. In an oxygen steelmaking converter, an open-top container having an axis substantially perpendicular to the converter axis is installed at the mouth of the converter, and the open surface and the side edge of the exposed steel at the mouth of the converter are connected to each other. An oxygen steelmaking converter characterized by abutting and fixing dowels.
JP11626582A 1982-07-06 1982-07-06 Method and device for removing slag in oxygen steel making converter Pending JPS599117A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11626582A JPS599117A (en) 1982-07-06 1982-07-06 Method and device for removing slag in oxygen steel making converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11626582A JPS599117A (en) 1982-07-06 1982-07-06 Method and device for removing slag in oxygen steel making converter

Publications (1)

Publication Number Publication Date
JPS599117A true JPS599117A (en) 1984-01-18

Family

ID=14682809

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11626582A Pending JPS599117A (en) 1982-07-06 1982-07-06 Method and device for removing slag in oxygen steel making converter

Country Status (1)

Country Link
JP (1) JPS599117A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102206726A (en) * 2011-05-04 2011-10-05 马鞍山钢铁股份有限公司 Method for removing desulfurizing slag from molten iron

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102206726A (en) * 2011-05-04 2011-10-05 马鞍山钢铁股份有限公司 Method for removing desulfurizing slag from molten iron

Similar Documents

Publication Publication Date Title
JP6421634B2 (en) Manufacturing method of molten steel
US3761242A (en) Method of treating molten metal by gas purging rhtough a porous plug
JP4912880B2 (en) Method for recovering metal elements, especially metal chromium, from slag containing metal oxides in an electric arc furnace
JPS6397332A (en) Steel-making process
JP7151494B2 (en) Method for recycling converter slag
US4373949A (en) Method for increasing vessel lining life for basic oxygen furnaces
JPS599117A (en) Method and device for removing slag in oxygen steel making converter
FI73241B (en) FOERFARANDE FOER HOEJANDE AV KYLAEMNESTILLSATSER VID FRAMSTAELLNING AV STAOL MEDELST SYREBLAOSNING.
JPS6176607A (en) Steel making equipment by pre-refining of pig iron
SU1109448A2 (en) Method for producing stainless steels
JPS56102514A (en) Manufacture of steel
SU1188209A1 (en) Method of refining low-manganese cast iron
JPH0892618A (en) Prerefining method
US4140522A (en) Method of refining of metal
SU910793A1 (en) Method for extrafurnace treatment of steel and martin furnace
JPS61149416A (en) Pretreatment of molten pig iron
JPS57158316A (en) Production of al-containing steel
JPS6154081B2 (en)
Pehlke An overview of contemporary steelmaking processes
SU584040A1 (en) Method of removing slag from surface of molten metal
JP2842248B2 (en) Hot metal desulfurization method
JPS5837366B2 (en) Pretreatment method for molten metal
SU1321755A1 (en) Method of rimming steel deoxidation
SU988877A1 (en) Method for smelting steel
JP2001152238A (en) Method of melting high cleanliness low carbon steel