JP3187461B2 - Slag smelting reduction method - Google Patents

Slag smelting reduction method

Info

Publication number
JP3187461B2
JP3187461B2 JP20747491A JP20747491A JP3187461B2 JP 3187461 B2 JP3187461 B2 JP 3187461B2 JP 20747491 A JP20747491 A JP 20747491A JP 20747491 A JP20747491 A JP 20747491A JP 3187461 B2 JP3187461 B2 JP 3187461B2
Authority
JP
Japan
Prior art keywords
slag
furnace
reduced
oxidized
iron
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
JP20747491A
Other languages
Japanese (ja)
Other versions
JPH0525528A (en
Inventor
正幸 高橋
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.)
Astec Irie Co Ltd
Original Assignee
Astec Irie Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Astec Irie Co Ltd filed Critical Astec Irie Co Ltd
Priority to JP20747491A priority Critical patent/JP3187461B2/en
Publication of JPH0525528A publication Critical patent/JPH0525528A/en
Application granted granted Critical
Publication of JP3187461B2 publication Critical patent/JP3187461B2/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

  • Furnace Details (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)
  • Manufacture And Refinement Of Metals (AREA)

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、鋼の精錬の過程におい
て発生する製鋼スラグの有効利用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 method for effectively utilizing steelmaking slag generated in the process of refining steel.

【0002】[0002]

【従来の技術】鋼の精錬炉は多量のスラグが発生し、一
部は再利用されているが、大部分は埋め立てあるいは廃
棄処理が行われている。特に、電気炉における酸化精錬
スラグにおいてはスラグの膨張性からその利用が極めて
制限されるという欠点がある。そこで、特公昭55−2
7140号公報に記載のように、電気炉から発生するス
ラグを溶滓収納容器に入れて、保温電極によって流動性
を損なわないような温度に保持しながら処理する方法が
提案されている。
2. Description of the Related Art Steel smelting furnaces generate a large amount of slag, and some of them are reused, but most of them are buried or disposed of. In particular, oxidized refining slag in an electric furnace has a drawback that its use is extremely restricted due to the slag's expandability. Therefore, Japanese Patent Publication No. 555-2
As described in Japanese Patent No. 7140, a method has been proposed in which slag generated from an electric furnace is placed in a slag storage container and treated while maintaining a temperature at which the fluidity is not impaired by a heat retaining electrode.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、前記方
法によってスラグを処理すると、大量の電力を必要と
し、コスト高になり、更に電極等の特別な装置が必要で
ある。本発明はかかる事情に鑑みてなされたもので、比
較的安価な方法でスラグを処理し、しかも該スラグを有
効に使用できるスラグ溶融還元処理方法を提供すること
を目的とする。
However, treating slag by the above method requires a large amount of power, increases the cost, and requires special equipment such as electrodes. The present invention has been made in view of such circumstances, and has as its object to provide a slag smelting reduction treatment method that can treat slag by a relatively inexpensive method and can effectively use the slag.

【0004】[0004]

【課題を解決するための手段】前記目的に沿う請求項第
1項記載のスラグ溶融還元処理方法は、鋼の精錬の際に
発生する酸化スラグと還元スラグとをスラグ溶解炉に入
れた後、該スラグ溶解炉にて金属鉄粉を添加して吹酸溶
解を行い、スラグ塩基度を1.9以下に調整し、これに
よって製造されたスラグを、高炉(還元精錬炉をいう)
に入れて高炉スラグとして回収し、含まれる鉄は銑鉄と
して回収している。なお、ここで、前記金属鉄粉には転
炉精製鉄粉(OGP)を使用するのが形状から見た取扱
いの容易性及び安価な点から好ましい。
According to a first aspect of the present invention, there is provided a slag smelting reduction method according to the first aspect, comprising: placing oxidized slag generated during steel refining and reduced slag in a slag melting furnace; In the slag melting furnace, metallic iron powder is added to dissolve the acid by blowing, and the slag basicity is adjusted to 1.9 or less.
The steel is collected as blast furnace slag and the iron contained is recovered as pig iron. Here, it is preferable to use converter refined iron powder (OGP) as the metal iron powder from the viewpoint of easy handling and inexpensive in view of the shape.

【0005】[0005]

【作用】本発明に係るスラグ溶融還元処理方法において
は、塩基度が1.9以下になるようにして適当量の酸化
スラグと還元スラグとがスラグ溶解炉に入れられた後、
金属鉄粉を入れて吹酸溶解を行うようにしているので、
鉄粉を熱源にできる。そして、酸化スラグと還元スラグ
とをブレンドすると共に吹酸溶解を行うので、酸化スラ
グ中の酸化物と還元スラグ中の非酸化物によって生じる
反応熱を積極的に利用することができる。また、スラグ
の塩基度を1.9以下として吹酸溶解を行うので、スラ
グの流動性が増し、略完全なスラグ改質が可能となり、
更に還元精錬炉用スラグに活用し、該還元精錬炉によっ
て生成排出するスラグを付加価値の高いものとすること
ができる。なお、ここで配合されるスラグの塩基度が
1.9よりも高いと高炉中のスラグメタル反応に支障を
きたす。更には、この処理により、各スラグ中に含有さ
れた鉄分、酸化鉄あるいはその他の有価金属は、高炉内
での反応処理時に溶融スラグから溶鉄中に還元回収され
る。
In the slag smelting reduction treatment method according to the present invention, an appropriate amount of oxidized slag and reduced slag are placed in a slag melting furnace so that the basicity is 1.9 or less.
Since metal acid powder is added to dissolve acid,
Iron powder can be used as a heat source. Since the oxidized slag and the reduced slag are blended and the blowing acid is dissolved, the reaction heat generated by the oxide in the oxidized slag and the non-oxide in the reduced slag can be positively used. In addition, since the acidity of dissolving the slag is increased by setting the basicity of the slag to 1.9 or less, the fluidity of the slag increases, and almost complete slag reforming becomes possible.
Furthermore, the slag produced and discharged by the reduction smelting furnace by utilizing the slag for the reduction smelting furnace can have high added value. If the basicity of the slag mixed here is higher than 1.9, the slag metal reaction in the blast furnace will be hindered. Further, by this treatment, the iron, iron oxide and other valuable metals contained in each slag are reduced and recovered from the molten slag into the molten iron during the reaction treatment in the blast furnace.

【0006】[0006]

【実施例】続いて、添付した図面を参照しつつ、本発明
を具体化した実施例につき説明する。図1には本発明の
一実施例に係るスラグ溶融還元処理方法の概略工程を示
すが、まず精錬炉の一例である電気炉10から酸化スラ
グ11と、還元スラグ12とを取出し、これをスラグ溶
解炉13に入れる。この場合の酸化スラグ11と還元ス
ラグ12の投入量は、その塩基度(Ca/SiO2 比を
いう) が1.9以下の範囲になるようにその量を調整す
る。即ち、電気炉の酸化スラグ及び還元スラグの成分は
一般的には表1の通りであるから、その塩基度は酸化ス
ラグの場合には1.4、還元スラグの場合には、2.1
となる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments embodying the present invention will be described below with reference to the accompanying drawings. FIG. 1 shows schematic steps of a slag smelting reduction treatment method according to one embodiment of the present invention. First, an oxidized slag 11 and a reduced slag 12 are taken out from an electric furnace 10 which is an example of a refining furnace. Place in melting furnace 13. In this case, the amounts of the oxidized slag 11 and the reduced slag 12 are adjusted so that the basicity (referred to as the Ca / SiO 2 ratio) is in the range of 1.9 or less. That is, the components of the oxidized slag and the reduced slag of the electric furnace are generally as shown in Table 1, and their basicities are 1.4 in the case of oxidized slag and 2.1 in the case of reduced slag.
Becomes

【0007】[0007]

【表1】 [Table 1]

【0008】そこで、塩基度を1.9以下とする為に
は、酸化スラグの量1に対して還元スラグの量をxとし
て、次式を満足するようにすれば良い。
Therefore, in order to make the basicity 1.9 or less, the amount of reduced slag is set to x with respect to the amount of oxidized slag of 1 so as to satisfy the following expression.

【0009】[0009]

【数1】 (Equation 1)

【0010】この式を解くと、x≦1.99となるの
で、酸化スラグ1に対し、その1.99倍以下(好まし
くは1以上)の還元スラグを投入することによって塩基
度の調整が行われることになる。
When this equation is solved, x ≦ 1.99. Therefore, the basicity is adjusted by adding 1.99 times or less (preferably 1 or more) reduced slag to 1 oxidized slag. Will be

【0011】従って、前記所定量の酸化スラグ11と還
元スラグ12をスラグ溶解炉13に入れた後、図に示す
ように金属鉄粉の一例である転炉生成鉄粉(OGP)を
エアーまたは窒素で吹き込みながら、酸素を吹き込み、
該転炉生成鉄粉を燃焼させる。この転炉生成鉄粉の吹き
込み量は、投入された還元スラグ及び酸化スラグの量に
よるが、充分流動性があるように考慮し、更には投入さ
れたスラグ量の8〜15%の範囲になるようにするのが
好ましい。
Accordingly, after the predetermined amounts of the oxidized slag 11 and the reduced slag 12 are put into the slag melting furnace 13, as shown in FIG. While blowing oxygen,
The converter-produced iron powder is burned. The amount of the blown iron powder generated by the converter depends on the amount of the supplied reducing slag and the oxidized slag, but is considered to have sufficient fluidity, and furthermore, is in the range of 8 to 15% of the amount of the supplied slag. It is preferable to do so.

【0012】次に、この状態で冷却させて塊あるいは粒
状に処理し、還元炉の一例である高炉14の原料として
使用する。これによって、スラグ中の酸化鉄は還元され
た銑鉄となり、スラグは高炉スラグとなり、適当に破砕
して高炉バラスあるいは砂を製造でき、建築材料として
使用できることになる。この実施例においては、還元炉
として高炉を使用したが、近年開発された石炭及び鉄鉱
石をコークス化及び塊成化等の事前処理なしに直接使用
して銑鉄を製造するプロセス(通常、DIOS法と言わ
れる)である鉄浴溶融還元炉において処理を行うことも
可能である。
Next, in this state, the blast furnace is cooled and processed into lumps or granules, and is used as a raw material for a blast furnace 14 which is an example of a reduction furnace. As a result, iron oxide in the slag becomes reduced pig iron, and the slag becomes blast furnace slag, which can be appropriately crushed to produce blast furnace ballast or sand, which can be used as a building material. In this embodiment, a blast furnace was used as a reduction furnace. However, a process for producing pig iron by directly using recently developed coal and iron ore without prior treatment such as coking and agglomeration (usually a DIOS method) It is also possible to carry out the treatment in an iron bath smelting reduction furnace.

【0013】[0013]

【発明の効果】請求項第1項記載のスラグ溶融還元処理
方法は、以上の説明からも明らかなように、精錬炉で発
生する酸化スラグ及び還元スラグを適当にブレンドして
高炉の原料として使用できるようにしているので、その
用途が拡大されることになった。また、前記酸化スラグ
及び還元スラグを加熱するに際しては金属鉄粉を使用し
ているので、製造コストを下げることができ、更に該金
属鉄粉と酸素が化合した酸化鉄は次の還元炉で溶融還元
されるので、鉄分の回収もできる。
According to the first aspect of the present invention, the slag smelting reduction method is used as a raw material for a blast furnace by appropriately blending oxidized slag and reduced slag generated in a smelting furnace as described above. The ability to do so has expanded its use. Further, when heating the above-mentioned oxidized slag and reduced slag, metal iron powder is used, so that the production cost can be reduced, and the iron oxide in which the metal iron powder and oxygen are combined is melted in the next reduction furnace. Since it is reduced, iron can be recovered.

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

【図1】本発明の一実施例に係るスラグ溶融還元処理方
法の概略工程図である。
FIG. 1 is a schematic process diagram of a slag smelting reduction treatment method according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10:電気炉(精錬炉)、11:酸化スラグ、12:還
元スラグ、13:スラグ溶解炉、14:還元炉
10: Electric furnace (refining furnace), 11: Oxidized slag, 12: Reduction slag, 13: Slag melting furnace, 14: Reduction furnace

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C21C 5/28,7/00 C22B 7/04 F27D 15/00 C21B 3/04,3/06 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) C21C 5 / 28,7 / 00 C22B 7/04 F27D 15/00 C21B 3 / 04,3 / 06

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 鋼の精錬の際に発生する酸化スラグと還
元スラグとをスラグ溶解炉に入れた後、該スラグ溶解炉
にて金属鉄粉を添加して吹酸溶解を行い、スラグ塩基度
を1.9以下に調整し、これによって製造されたスラグ
を、高炉に入れて高炉スラグとして回収し、含まれる鉄
は銑鉄として回収することを特徴とするスラグ溶融還元
処理方法。
Claims 1. After oxidized slag and reduced slag generated during the refining of steel are put into a slag melting furnace, metallic iron powder is added to the slag melting furnace to perform blowing acid dissolution, and the slag basicity is increased. Slag is adjusted to 1.9 or less, the slag produced thereby is put into a blast furnace and collected as blast furnace slag, and the contained iron is collected as pig iron.
JP20747491A 1991-07-23 1991-07-23 Slag smelting reduction method Expired - Lifetime JP3187461B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20747491A JP3187461B2 (en) 1991-07-23 1991-07-23 Slag smelting reduction method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20747491A JP3187461B2 (en) 1991-07-23 1991-07-23 Slag smelting reduction method

Publications (2)

Publication Number Publication Date
JPH0525528A JPH0525528A (en) 1993-02-02
JP3187461B2 true JP3187461B2 (en) 2001-07-11

Family

ID=16540354

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20747491A Expired - Lifetime JP3187461B2 (en) 1991-07-23 1991-07-23 Slag smelting reduction method

Country Status (1)

Country Link
JP (1) JP3187461B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102952952B (en) * 2012-09-26 2014-08-20 东北大学 Method for directly restoring and recovering copper iron from smelting copper slag

Also Published As

Publication number Publication date
JPH0525528A (en) 1993-02-02

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