JPH03274217A - Desulfurizing agent for molten iron - Google Patents

Desulfurizing agent for molten iron

Info

Publication number
JPH03274217A
JPH03274217A JP7497790A JP7497790A JPH03274217A JP H03274217 A JPH03274217 A JP H03274217A JP 7497790 A JP7497790 A JP 7497790A JP 7497790 A JP7497790 A JP 7497790A JP H03274217 A JPH03274217 A JP H03274217A
Authority
JP
Japan
Prior art keywords
aluminum
weight
hot metal
agent
desulfurization
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.)
Granted
Application number
JP7497790A
Other languages
Japanese (ja)
Other versions
JP2875579B2 (en
Inventor
Kiyoshi Yasui
潔 安井
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 Nisshin Co Ltd
Original Assignee
Nisshin Steel 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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=13562861&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=JPH03274217(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Nisshin Steel Co Ltd filed Critical Nisshin Steel Co Ltd
Priority to JP7497790A priority Critical patent/JP2875579B2/en
Publication of JPH03274217A publication Critical patent/JPH03274217A/en
Application granted granted Critical
Publication of JP2875579B2 publication Critical patent/JP2875579B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Abstract

PURPOSE:To provide the highly efficient desulfurizing agent at a low cost by using the aluminum ash generated in the process for producing aluminum as a by-product in the agent consisting essentially of a calcareous material. CONSTITUTION:This desulfurizing agent consists essentially of a calcareous material and is added with the aluminum ash contg. 30-50wt.% metallic aluminum and the balance alumina, fluorite and carbonaceous material. For example, the agent contains, by weight, 5-20% aluminum ash, 65-80% calcareous material, <10% fluorite and 5-15% carbonaceous material. Although the aluminum ash less expensive than the metallic aluminum is mixed into the agent, high desulfurization efficiency is obtained, and the cost is reduced.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、溶銑中の硫黄分をインジェクション法により
効率的に除去するために用いられる溶銑脱硫剤に関する
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a hot metal desulfurization agent used for efficiently removing sulfur content from hot metal by an injection method.

従来技術 溶銑中の硫黄分を除去する方法として、溶銑中にインジ
ェクションランスを突込んで脱硫剤をキャリアガスによ
って溶銑内に吹込む方法が主に行われており、脱硫剤と
して炭化カルシウムCaC2、炭酸ナトリウムNazC
Oa、酸化マグネシウムMgO1石灰質を主成分とした
ものなどが使用されてきた。
Conventional technology The main method for removing sulfur from hot metal is to insert an injection lance into the hot metal and inject a desulfurizing agent into the hot metal using a carrier gas. NazC
Oa, magnesium oxide MgO1, which has calcareous material as its main component, etc. have been used.

とくに最近ではコストや環境問題等の面から石灰質をベ
ースとした脱硫剤が多く使用されるようになり、石灰質
としては生石灰或いは石灰石が用いられ、これに脱硫効
率を高めるため螢石、炭素質、金属アルミニウム等が添
加されていた。
Particularly recently, calcareous-based desulfurization agents have come into widespread use due to cost and environmental concerns.The limestone used is quicklime or limestone, and in order to increase the desulfurization efficiency, fluorite, carbonaceous, Metallic aluminum etc. were added.

発明が解決しようとする課題 石灰質をベースとした脱硫剤において、脱硫効率を高め
るための助剤としては金属アルミニウムが最も有効であ
ることが知られているが、金属アルミニウムはアルミナ
A1.03を原料とし、電気エネルギーを使用して製造
されるため非常に高価である。アルミニウムスクラップ
を使用することも考えられるが、溶銑中に吹込むために
粉粒状に粉砕する必要があり、コスト高となる。
Problems to be Solved by the Invention It is known that metal aluminum is the most effective auxiliary agent for increasing desulfurization efficiency in calcareous-based desulfurization agents, but metal aluminum is made from alumina A1.03 as a raw material. It is very expensive because it is manufactured using electrical energy. Although it is possible to use aluminum scrap, it would be costly because it would need to be pulverized into powder to be injected into the hot metal.

本発明は、か\る問題を解消し、安価でかつ脱硫効率の
高い溶銑脱硫剤を提供することを目的とする。
The object of the present invention is to solve these problems and provide a hot metal desulfurization agent that is inexpensive and has high desulfurization efficiency.

課題の解決手段 本発明の溶銑脱硫剤は、アルミニウム製造工程で副産物
として発生する安価なアルミニウム灰を用いることを特
徴とするものである。
Means for Solving the Problems The hot metal desulfurization agent of the present invention is characterized in that it uses inexpensive aluminum ash generated as a by-product in the aluminum manufacturing process.

すなわち本発明の溶銑脱硫剤は、石灰質を主成分とし、
これに金属アルミニウムを30〜50重量%含有し、残
部がアル逅すAl□0.であるアルミニウム灰、螢石及
び炭素質を配合したことを特徴とするものである。
That is, the hot metal desulfurization agent of the present invention has limestone as a main component,
This contains 30 to 50% by weight of metallic aluminum, and the balance is Al□0. It is characterized by containing aluminum ash, fluorite, and carbonaceous material.

作用 アルミニウム灰は、主成分がAltosであるが、アル
逅ニウム製造工程で発生した直後には、粒子状の金属ア
ルミニウムを通常、30〜50重量%含有する。その中
にはまた粒径が1m以上のインジェクションには適さな
い金属アルミニウムも存在するが、このような粒径の金
属アルミニウムは、アルミニウム製造用の原料として再
使用されるのが通例である。
Working aluminum ash is mainly composed of Altos, but immediately after it is generated in the aluminum production process, it usually contains 30 to 50% by weight of particulate metallic aluminum. Among them, there is also metal aluminum with a particle size of 1 m or more that is not suitable for injection, but metal aluminum with such a particle size is usually reused as a raw material for aluminum production.

アルミニウム灰中の金属アルミニウムは、溶銑に溶解し
、溶銑の酸素ポテンシャルを低下させて脱硫条件を改善
する。
Metallic aluminum in aluminum ash dissolves into the hot metal, lowering the oxygen potential of the hot metal and improving desulfurization conditions.

またアルミニウム灰中のAh03は本発明の脱硫剤の主
成分である石灰質の融点を下げ、脱硫を促進する機能を
果す。
Furthermore, Ah03 in the aluminum ash functions to lower the melting point of limestone, which is the main component of the desulfurization agent of the present invention, and to promote desulfurization.

以上のように、アルミニウム灰は含有する金属アルミニ
ウム及び^It’sにより脱硫反応を促進させる機能を
有し、5重量%以上配合するのが望ましいが、アルミニ
ウム灰自体には脱硫作用はなく、20重量%以上の配合
は、脱硫の主体となる石灰質の配合比が低下するため好
ましくない。
As mentioned above, aluminum ash has the function of accelerating the desulfurization reaction due to the metal aluminum and ^It's it contains, and it is desirable to mix it in at least 5% by weight, but aluminum ash itself has no desulfurization effect and A blending ratio of more than % by weight is not preferable because the blending ratio of limestone, which is the main component of desulfurization, decreases.

石灰質は、脱硫の基本成分てあり、65重量%以上配合
する必要がある。
Calcareous material is a basic component of desulfurization and needs to be added in an amount of 65% by weight or more.

石灰質としては主として生石灰が使用されるが、一部に
安価な石灰石を使用することもできる。石灰石はしかし
ながら溶銑中に入ると、CaOとCO!に分解し、多量
のガスを発生して溶銑の吹出し現象を発生するようにな
るため使用するにしても20重量%以下とするのが望ま
しい。
Quicklime is mainly used as the calcareous material, but inexpensive limestone can also be used in part. However, when limestone enters hot metal, it produces CaO and CO! It decomposes into 20% by weight or less, producing a large amount of gas and causing the phenomenon of hot metal blowing out.

炭素質は脱硫反応により発生する酵素を金属アルミニウ
ムとともに消費し、脱硫反応を促進するとともに脱硫剤
の流動性を改善する機能も有しており、そのためには5
重量%以上配合する必要があるが、アルミニウム灰と同
様、炭素質自体に脱硫作用があるわけではないため15
重量%以下とするのが望ましい。
Carbonaceous material has the function of consuming the enzyme generated by the desulfurization reaction together with metal aluminum, promoting the desulfurization reaction, and improving the fluidity of the desulfurizing agent.
Although it is necessary to mix at least 15% by weight, since carbonaceous material itself does not have a desulfurization effect like aluminum ash.
It is desirable that the amount is less than % by weight.

螢石は、Altosと同様、石灰質の融点を下げ、脱硫
を促進するために配合されるが、高価であるため10重
量%未満とする。
Like Altos, fluorite is blended to lower the melting point of calcareous material and promote desulfurization, but it is expensive and is therefore used in an amount of less than 10% by weight.

実施例 別表に示されるように、生石灰63重量%、石灰石14
重量%、螢石4重量%、炭素質9重量%及び金属アルミ
ニウム40重量%、AlxoJO重量%よりなるアルミ
ニウム灰10重量%とからなる脱硫剤を使用し、硫黄分
を0.025〜0.035%含有する160〜186 
tonの溶銑に常法のようにしてインショクジョンした
。その結果を図に示す。
As shown in the attached table of examples, quicklime 63% by weight, limestone 14%
Using a desulfurizing agent consisting of 4% by weight of fluorite, 9% by weight of carbon, 40% by weight of metal aluminum, and 10% by weight of aluminum ash consisting of % by weight of AlxoJO, the sulfur content was reduced to 0.025 to 0.035. % containing 160-186
It was injected into tons of hot metal in the usual manner. The results are shown in the figure.

比較例1 生石灰70重量%、石灰石15重量%、螢石5重量%、
炭素質10重量%とからなる脱硫剤を使用し、実施例と
同し条件の溶銑にインジェクションした。
Comparative Example 1 Quicklime 70% by weight, limestone 15% by weight, fluorite 5% by weight,
A desulfurization agent consisting of 10% by weight of carbonaceous material was used and injected into hot metal under the same conditions as in the example.

結果を図に示す。The results are shown in the figure.

比較例2 生石灰63重量%、石灰石14重量%、螢石4重量%、
炭素質9重量%、金属アルミニウム10重量%とからな
る脱硫剤を使用し、実施例と同し条件の溶銑にインジェ
クションした。結果を図に示す。
Comparative Example 2 Quicklime 63% by weight, limestone 14% by weight, fluorite 4% by weight,
A desulfurizing agent consisting of 9% by weight of carbonaceous material and 10% by weight of metallic aluminum was used and was injected into hot metal under the same conditions as in the example. The results are shown in the figure.

実施例と比較例1及び2を比較すると、溶銑中の硫黄分
を0.010%とするために必要な脱硫剤量は、比較例
1の8 kg/i銑1 tonに対し、本実施例では5
kg/溶銑1 tonと大幅に減少した。また溶銑中の
硫黄分を0.005%とするために必要な脱硫剤量は比
較例2の13睦/溶銑1 tonに対し、本実施例では
9 kg/i銑l tonと、安価なアルミニウム灰を
使用しているにもか\わらず大幅に減少させることがで
きた。
Comparing Example and Comparative Examples 1 and 2, the amount of desulfurization agent required to reduce the sulfur content in hot metal to 0.010% is 8 kg/i 1 ton of pig iron in Comparative Example 1, while in this example So 5
kg/1 ton of hot metal, a significant decrease. In addition, the amount of desulfurization agent required to reduce the sulfur content in hot metal to 0.005% was 13 mu/1 ton of hot metal in Comparative Example 2, but in this example it was 9 kg/1 ton of pig iron, which is cheap aluminum. Despite using ash, we were able to significantly reduce the amount.

発明の効果 本発明の溶銑脱硫剤によれば以上のように金属アルミニ
ウムよりも安価なアルミニウム灰を配合しているにもか
\わらず、高い脱硫作用が得られ、コストを低減させる
ことができる。
Effects of the Invention According to the hot metal desulfurization agent of the present invention, a high desulfurization effect can be obtained and costs can be reduced even though aluminum ash, which is cheaper than metal aluminum, is blended as described above. .

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

図は脱硫剤使用量と溶銑中硫黄分との関係を示すグラフ
図である。 表
The figure is a graph showing the relationship between the amount of desulfurization agent used and the sulfur content in hot metal. table

Claims (3)

【特許請求の範囲】[Claims] (1)石灰質を主成分とし、これに金属アルミニウムを
30〜50重量%含有し、残部がアルミナAl_2O_
3であるアルミニウム灰、螢石及び炭素質を配合したこ
とを特徴とする溶銑脱硫剤。
(1) The main component is calcareous material, which contains 30 to 50% by weight of metallic aluminum, and the balance is alumina Al_2O_
3. A hot metal desulfurization agent characterized by containing aluminum ash, fluorite and carbonaceous matter.
(2)アルミニウム灰5〜20重量%、石灰質65〜8
0重量%、螢石10重量%未満、炭素質5〜15重量%
とからなる請求項1記載の溶銑脱硫剤。
(2) Aluminum ash 5-20% by weight, limestone 65-8
0% by weight, less than 10% by weight of fluorite, 5-15% by weight of carbonaceous material
The hot metal desulfurization agent according to claim 1, comprising:
(3)石灰質には石灰石が20重量%以下含まれる請求
項2記載の溶銑脱硫剤。
(3) The hot metal desulfurization agent according to claim 2, wherein the calcareous substance contains 20% by weight or less of limestone.
JP7497790A 1990-03-22 1990-03-22 Hot metal desulfurizing agent Expired - Lifetime JP2875579B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7497790A JP2875579B2 (en) 1990-03-22 1990-03-22 Hot metal desulfurizing agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7497790A JP2875579B2 (en) 1990-03-22 1990-03-22 Hot metal desulfurizing agent

Publications (2)

Publication Number Publication Date
JPH03274217A true JPH03274217A (en) 1991-12-05
JP2875579B2 JP2875579B2 (en) 1999-03-31

Family

ID=13562861

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7497790A Expired - Lifetime JP2875579B2 (en) 1990-03-22 1990-03-22 Hot metal desulfurizing agent

Country Status (1)

Country Link
JP (1) JP2875579B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007302961A (en) * 2006-05-12 2007-11-22 Nisshin Steel Co Ltd Desulfurizing refining agent for molten iron containing chromium and desulfurizing method
JP2010229439A (en) * 2009-03-26 2010-10-14 Jfe Steel Corp Desulfurizing agent for molten pig iron, and desulfurizing method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007302961A (en) * 2006-05-12 2007-11-22 Nisshin Steel Co Ltd Desulfurizing refining agent for molten iron containing chromium and desulfurizing method
JP2010229439A (en) * 2009-03-26 2010-10-14 Jfe Steel Corp Desulfurizing agent for molten pig iron, and desulfurizing method

Also Published As

Publication number Publication date
JP2875579B2 (en) 1999-03-31

Similar Documents

Publication Publication Date Title
CN101717843B (en) Method for utilizing sulfur-containing refining waste residue for refining slag
CN101033498A (en) Electric furnace highly effective metallurgy complexing agent
CN103451373B (en) Magnesium ball used for converter steelmaking and production technology thereof
JPH0215130A (en) Utilization of zinc-containing metallurgical dust and sludge
US5916827A (en) Composite briquette for electric furnace charge
JPH03274217A (en) Desulfurizing agent for molten iron
CN111575442B (en) Low-melting-point high-efficiency desulfurizing agent and preparation and application methods thereof
CN1124780A (en) Steel foam dephosphorizing machine
CA1174855A (en) Method of producing molten metal consisting mainly of manganese and iron
JP2001348610A (en) Slag formation promoter
JP2001303113A (en) METHOD FOR UTILIZING COAL HAVING MUCH CaO COMPONENT AND Fe2O3 COMPONENT IN BURNT ASH
CN1035017C (en) Slag fomation agent for adding magnesium in magnesium balls for smelting steel
KR100290638B1 (en) Method for recycling calcium oxide sludge in converter refining process
KR900001889B1 (en) Desilicon agent for molten iron
KR100890138B1 (en) Method for accelerating slag making in electric arc furnace
JP4768921B2 (en) High pulverized coal injection low Si blast furnace operation method
RU2157411C1 (en) Method of smelting of pig iron in blast furnace
JP4751010B2 (en) Blast furnace operation method
JP3316270B2 (en) Manufacturing method of lime flux for metal refining
RU2134298C1 (en) Blast-furnace smelting method
KR890002607B1 (en) Flux of desulfur for pretreatment of molten iron
KR100400869B1 (en) Prevention of Slag Peroxidation in Electric Furnace
RU2087538C1 (en) Method of conduction of blast-furnace smelting
CN118109654A (en) Converter smelting method using iron-containing waste slag melting agent
JPH08209228A (en) Steel making method

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090114

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100114

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110114

Year of fee payment: 12

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110114

Year of fee payment: 12