JPH073379A - Production of low-silicon, low-sulfur and high-carbon ferrochrome - Google Patents

Production of low-silicon, low-sulfur and high-carbon ferrochrome

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Publication number
JPH073379A
JPH073379A JP19825093A JP19825093A JPH073379A JP H073379 A JPH073379 A JP H073379A JP 19825093 A JP19825093 A JP 19825093A JP 19825093 A JP19825093 A JP 19825093A JP H073379 A JPH073379 A JP H073379A
Authority
JP
Japan
Prior art keywords
low
carbon ferrochrome
silicon
chromium
scale
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
JP19825093A
Other languages
Japanese (ja)
Inventor
Yoshi Ichihara
佳 市原
Hiroyuki Hara
宏幸 原
Kiyoaki Takai
清明 高井
Isamu Nakada
勇 中田
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.)
Japan Metals and Chemical Co Ltd
Original Assignee
Japan Metals and Chemical 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 Japan Metals and Chemical Co Ltd filed Critical Japan Metals and Chemical Co Ltd
Priority to JP19825093A priority Critical patent/JPH073379A/en
Publication of JPH073379A publication Critical patent/JPH073379A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To produce a low-silicon, low-sulfur and high-carbon ferrochrome in a high yield with a high productivity by adding a chromium ore and a basic slag making agent to a molten high-carbon ferrochrome received in a ladle from an elctric furnace, agitating and refining the mixture. CONSTITUTION:The molten high-carbon ferrochrome produced by reducing a chromium ore with carbon in an electric furnace is tapped in a ladle from the furnace. A chromium ore and a basic slag making agent, scale and a basic slag making agent or a chromium ore, scale and a basic slag making agent are added to the molten high-carbon ferrochrome, and the mixture is agitated, desiliconized and desulfurized. The basic slag making agent contains CaO and/or MgO and about 80% of CaO, MgO or (CaO+MgO), a hammer scale produced in forging and hammering or a mill scale formed in rolling is used as the scale. A low-silicon, low-sulfur and high-carbon is obtained in this way in a high chromium yield with improved productivity.

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、低珪素・低硫黄・高炭
素フェロクロムの製造法、より詳しくは、レードル内で
脱珪、脱硫を行い、低珪素・低硫黄・高炭素フェロクロ
ムを製造する方法に関するものである。
FIELD OF THE INVENTION The present invention relates to a method for producing low silicon, low sulfur, high carbon ferrochrome, more specifically, desiliconization and desulfurization in a ladle to produce low silicon, low sulfur, high carbon ferrochrome. It is about the method.

【0002】[0002]

【従来の技術】一般に、高炭素フェロクロムは、電気炉
を用いて、クロム鉱石の炭素還元により製造される。そ
の用途は、主として鉄鋼、特にステンレス鋼製造時のク
ロム成分添加剤である。従来、特に転炉法によるステン
レス鋼製造時に使用する高炭素フェロクロムは、低珪素
・低硫黄品が求められていた。
BACKGROUND OF THE INVENTION High carbon ferrochromium is generally produced by carbon reduction of chromium ore using an electric furnace. Its application is mainly as a chromium component additive in the production of steel, especially stainless steel. Conventionally, low-silicon / low-sulfur products have been required for high-carbon ferrochrome, which is used especially when producing stainless steel by a converter method.

【0003】その理由は 1)転炉法による製鋼工程で珪素含有率の低い高炭素フ
ェロクロムをクロム成分添加剤として用いることによ
り、(1) 酸素吹精工程でSi除去用に使用する精製酸素
量の低減。(2) 酸素吹精によって生成するSiO2に対
応するCaO添加量の低減。(3) スラグ量の低減による
クロムのロスの低減及び炉材溶損の低減。および、 2)硫黄含有率の低い高炭素フェロクロムをクロム成分
添加剤として用いることにより、製鋼原料である溶銑の
脱硫費用の低減を図るためである。
The reasons are: 1) By using high carbon ferrochromium having a low silicon content as a chromium component additive in the steelmaking process by the converter method, (1) the amount of purified oxygen used for removing Si in the oxygen blowing process. Reduction of. (2) Reduction in the amount of CaO added corresponding to SiO 2 generated by oxygen blowing. (3) Reduction of chromium loss and furnace material melting loss by reducing the amount of slag. And 2) by using high carbon ferrochrome having a low sulfur content as a chromium component additive, it is possible to reduce the desulfurization cost of the hot metal which is a raw material for steelmaking.

【0004】一般に、高炭素フェロクロムは、クロム鉱
石、コークスのような炭素質還元剤及び造滓剤を原料と
して、電気炉でクロム鉱石中の酸化クロム及び酸化鉄を
炭素で還元することによって製造される。高炭素フェロ
クロムを経済的に製造するためには、クロム収率を上げ
ることが最も大切である。従ってこの場合、還元剤とし
て使用する炭素質物質をクロム鉱石中の酸化クロム及び
酸化鉄を還元するために必要な理論量の炭素より多く加
える。
In general, high carbon ferrochromium is produced by reducing chromium oxide and iron oxide in chromium ore with carbon in an electric furnace using a chromium ore, a carbonaceous reducing agent such as coke and a slag-forming agent as raw materials. It Increasing the chromium yield is of paramount importance for the economical production of high carbon ferrochrome. Therefore, in this case, the carbonaceous material used as the reducing agent is added in an amount larger than the theoretical amount of carbon required to reduce the chromium oxide and iron oxide in the chromium ore.

【0005】その結果として、過剰の炭素が一部の二酸
化珪素を還元して珪素とし、その珪素は高炭素フェロク
ロム中に含まれる。一般的な高炭素フェロクロムは、通
常2.5%以上の珪素を含有する。
As a result, excess carbon reduces some silicon dioxide to silicon, which is contained in high carbon ferrochromium. Typical high carbon ferrochromes usually contain 2.5% or more of silicon.

【0006】高炭素フェロクロム中の硫黄含有率は、原
料中の硫黄含有量及び後述するように高炭素フェロクロ
ム中の珪素含有率によって変るが、通常の方法では、製
鋼での要求を満足する硫黄含有率をもつ高炭素フェロク
ロムを製造することはできない。
The sulfur content in the high carbon ferrochrome varies depending on the sulfur content in the raw material and the silicon content in the high carbon ferrochrome as described later, but in the usual method, the sulfur content satisfying the requirements for steelmaking is satisfied. It is not possible to produce high carbon ferrochrome with a high index.

【0007】従来、低珪素・低硫黄・高炭素フェロクロ
ムを製造する場合は、通常の珪素含有率および硫黄含有
率の高炭素フェロクロム(以下、通常品と記す)を製造
する場合に比べ、クロム鉱石に対する還元剤としての炭
材の配合割合を減らして、電気炉内で低珪素・高炭素フ
ェロクロムを製造し、その低珪素・高炭素フェロクロム
を炉外で脱硫剤を加えて脱硫処理して低珪素・低硫黄・
高炭素フェロクロムを製造していた。
[0007] Conventionally, when producing low-silicon, low-sulfur, high-carbon ferrochrome, compared with the case of producing high-carbon ferrochrome having a normal silicon content and sulfur content (hereinafter, referred to as a normal product), a chromium ore To produce low-silicon / high-carbon ferrochrome in an electric furnace, and desulfurize the low-silicon / high-carbon ferrochrome by adding a desulfurizing agent outside the furnace.・ Low sulfur ・
Manufactured high carbon ferrochrome.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、従来の
方法は、前述したように、通常品を製造する場合に比
べ、クロム鉱石に対する還元剤としての炭材の配合割合
を減らして製錬する方法のため、高炭素フェロクロム中
の珪素含有率は低下するが、還元されずにスラグへ移行
するクロム量が増え、クロム収率が低下するという欠点
があった。
However, as described above, the conventional method is a method of smelting by reducing the compounding ratio of the carbonaceous material as the reducing agent to the chromium ore as compared with the case of producing a normal product. Therefore, the silicon content in the high-carbon ferrochromium is reduced, but the amount of chromium transferred to the slag without reduction is increased, and the chromium yield is reduced.

【0009】また、高炭素フェロクロムの珪素と硫黄と
の間には負の相関があるため、高炭素フェロクロム中の
珪素含有率が低下すると硫黄含有率が上昇する。従っ
て、脱硫に際して、脱硫剤が多く必要となり、そのため
に溶湯の温度低下が著しく、鋳付きによる損失、作業効
率の悪化などの欠点があった。従来は、それらを防止す
るために低周波炉などの保温設備の利用も行われてい
た。
Further, since there is a negative correlation between silicon and sulfur in the high carbon ferrochrome, the sulfur content increases as the silicon content in the high carbon ferrochrome decreases. Therefore, in desulfurization, a large amount of desulfurization agent is required, which causes a remarkable decrease in the temperature of the molten metal, and there are drawbacks such as loss due to casting and deterioration of work efficiency. In the past, heat insulating equipment such as a low frequency furnace was used to prevent them.

【0010】[0010]

【課題を解決するための手段】本発明は、上記課題を解
決するもので、クロム収率を低下させることなく、かつ
保温設備を使うこともなく、珪素及び硫黄含有率の低い
高炭素フェロクロムを製造する方法を提供する。すなわ
ち、本発明は、クロム鉱石の炭素還元によって電気炉で
製造し、出湯、レードル受けした高炭素フェロクロム溶
湯に、クロム鉱石と塩基性造滓剤を、またはスケールと
塩基性造滓剤を、またはクロム鉱石とスケールと塩基性
造滓剤を添加し、撹拌して精練することを特徴とする低
珪素・低硫黄・高炭素フェロクロムの製造法である。
SUMMARY OF THE INVENTION The present invention is to solve the above-mentioned problems by providing a high carbon ferrochromium having a low silicon and sulfur content without lowering the chromium yield and using a heat-retaining facility. A method of manufacturing is provided. That is, the present invention, produced in an electric furnace by carbon reduction of chromium ore, tapping, ladle-received high carbon ferrochrome melt, chromium ore and basic slag forming agent, or scale and basic slag forming agent, or It is a method for producing low silicon, low sulfur, and high carbon ferrochrome, which comprises adding chromium ore, scale, and a basic slag forming agent, and stirring and refining.

【0011】[0011]

【作用】本発明の、低珪素・低硫黄・高炭素フェロクロ
ムの製造法について説明する。電気炉から出湯した、通
常品の溶湯をレードルに受け、この通常品の溶湯に、ク
ロム鉱石、スケール、あるいはクロム鉱石とスケールを
添加し撹拌することにより、高炭素フェロクロム中の珪
素と、クロム鉱石またはスケール中の酸化クロムまたは
酸化鉄とを反応させ、脱珪する。その反応を次に示す。
The method for producing low silicon, low sulfur and high carbon ferrochrome of the present invention will be described. The ordinary molten metal discharged from the electric furnace is received by the ladle, and chromium ore, scale, or chromium ore and scale are added to this molten molten metal, and the mixture is stirred, whereby silicon in high carbon ferrochrome and chromium ore are added. Alternatively, it is reacted with chromium oxide or iron oxide in the scale to desiliconize. The reaction is shown below.

【0012】 3Si+2Cr23=4Cr+3SiO2……………(1) Si+2FeO =2Fe+ SiO2……………(2) 反応生成物であるSiO2は、クロム鉱石と/またはス
ケールとともに添加した塩基性造滓剤中のCaOと/ま
たはMgOと結合させてスラグとなし、さらにこの生成
スラグによって脱硫を行い、低珪素・低硫黄・高炭素フ
ェロクロムを製造するものである。
3Si + 2Cr 2 O 3 = 4Cr + 3SiO 2 (1) Si + 2FeO = 2Fe + SiO 2 (2) The reaction product SiO 2 is a base added together with chromium ore and / or scale. A slag is formed by combining with CaO and / or MgO in a slag forming agent, and desulfurization is performed by this slag produced to produce low silicon / low sulfur / high carbon ferrochrome.

【0013】スラグ生成反応を次に示す。 SiO2+2CaO=2CaO・SiO2……………(3) SiO2+2MgO=2MgO・SiO2……………(4) クロム鉱石を添加する場合は、クロム鉱石中に塩基性造
滓剤成分が含有されているため、スケールだけを添加す
る場合に比べ、必要な塩基性造滓剤は少ない量で良い。
The slag formation reaction is shown below. SiO 2 + 2CaO = 2CaO · SiO 2 ............... (3) When SiO 2 + 2MgO = 2MgO · SiO 2 ............... to (4) addition of chromium ore, basic slag component to the chromium ore As compared with the case where only the scale is added, the amount of the basic slag-forming agent required is small.

【0014】本発明で使用する塩基性造滓剤は、CaO
と/またはMgOを含有し、かつその含有率がCaO,
MgOあるいはCaO+MgOが80%以上のものをい
う。また本発明で使用するスケールは、鍛錬、鍛造で発
生するハンマースケールおよび圧延時に生成するミルス
ケールいずれも使用可能である。
The basic slag forming agent used in the present invention is CaO.
And / or MgO, and its content is CaO,
It means that MgO or CaO + MgO is 80% or more. As the scale used in the present invention, any of a hammer scale generated by forging and forging and a mill scale generated during rolling can be used.

【0015】上記(1)〜(4)式は発熱反応であるた
め、従来法のように溶湯温度を保持するための設備は必
要としないが、その総発熱量は、溶湯温度を保つために
十分な量ではない。したがってクロム鉱石、スケール、
塩基性造滓剤は、高炭素フェロクロム溶湯に添加する前
に、焼結しない温度以下で予熱しておくことが好まし
い。
Since the above equations (1) to (4) are exothermic reactions, no equipment for maintaining the temperature of the molten metal is required unlike the conventional method, but the total calorific value is to maintain the temperature of the molten metal. Not enough. Therefore chrome ore, scale,
The basic slag forming agent is preferably preheated to a temperature at which sintering is not performed or lower, before being added to the high carbon ferrochrome molten metal.

【0016】一方、電気炉から出湯した通常品の溶湯に
添加するクロム鉱石と/またはスケールおよび塩基性造
滓剤の各々の量は、各々の組成および通常品のSi%、
S%、および目標Si%、S%により決定される。ま
た、本発明に係る撹拌手段および時間は特に限定するも
のではなく、スターラー撹拌、リレードリング撹拌、ガ
スの底吹き撹拌あるいはそれらの組合せなど、処理量、
目標Si%、S%等の条件により、適宜、公知の手段を
用いて必要な時間行えば良い。
On the other hand, the respective amounts of chromium ore and / or scale and basic slag forming agent added to the molten metal of the normal product discharged from the electric furnace are as follows:
S% and target Si%, S%. Further, stirring means and time according to the present invention is not particularly limited, such as stirrer stirring, relay ring stirring, bottom blowing stirring of gas or a combination thereof, the throughput,
Depending on the conditions such as the target Si%, S%, etc., a known means may be appropriately used for the required time.

【0017】以上説明したように、本発明による低珪素
・低硫黄・高炭素フェロクロムの製造法は、電気炉内で
通常品を製造し、その通常品を電気炉外で脱珪、脱硫を
同時に行うことによって低珪素・低硫黄・高炭素フェロ
クロムを得る方法である。従って、本発明によれば、従
来法のように電気炉内で高炭素フェロクロムの珪素含有
率を低減するために、クロム鉱石に対して還元剤として
の炭材の配合割合を減らす必要がないので、還元されず
にスラグへ移行するクロム量が増えてクロム収率が低下
するという従来法の抱えていた欠点を解消することがで
きる。
As described above, in the method for producing low silicon, low sulfur, and high carbon ferrochrome according to the present invention, a normal product is manufactured in an electric furnace, and the normal product is simultaneously desiliconized and desulfurized outside the electric furnace. It is a method of obtaining low silicon / low sulfur / high carbon ferrochrome by carrying out. Therefore, according to the present invention, it is not necessary to reduce the blending ratio of the carbonaceous material as a reducing agent to the chromium ore in order to reduce the silicon content of the high carbon ferrochrome in the electric furnace unlike the conventional method. However, it is possible to solve the drawback of the conventional method that the amount of chromium that is not reduced and that migrates to slag increases and the chromium yield decreases.

【0018】また、従来法では電気炉内で高炭素フェロ
クロム中のSiを低くする結果、高炭素フェロクロム中
のSが通常品のSよりも多くなった低珪素・高炭素フェ
ロクロムに電気炉外で脱硫剤を加えて脱硫するのに対
し、本発明では、電気炉内では通常品を製造し、その通
常品を電気炉外で脱珪、脱硫するため、脱硫に係る高炭
素フェロクロム中のSは、従来法に比べ少なく、かつ脱
珪反応生成物であるSiO2と、添加した塩基性造滓剤
中のCaOと/またはMgOとが結合したスラグが脱硫
剤として働いて脱珪と同時に脱硫がなされ、低珪素・低
硫黄・高炭素フェロクロムが得られる。
Further, in the conventional method, as a result of lowering Si in the high-carbon ferrochrome in the electric furnace, S in the high-carbon ferrochrome is higher than that of a normal product in the low-silicon / high-carbon ferrochrome outside the electric furnace. In contrast to desulfurization by adding a desulfurizing agent, in the present invention, since a normal product is manufactured in an electric furnace and the normal product is desiliconized and desulfurized outside the electric furnace, S in the high carbon ferrochrome for desulfurization is The slag, which is less in quantity than the conventional method and is SiO 2 which is a desiliconization reaction product, and CaO and / or MgO in the added basic slag-forming agent acts as a desulfurizing agent to perform desulfurization and desulfurization simultaneously. Made to obtain low silicon, low sulfur, and high carbon ferrochrome.

【0019】さらに、本発明では、通常品中のSiを、
クロム鉱石と/またはスケールを用いて、炉外で脱珪す
る際に、前述の(1)式および(2)式に示すように、
クロム鉱石と/またはスケールに含まれる酸化クロムと
/または酸化鉄が還元され、クロムと/または鉄となっ
て高炭素フェロクロム中へ移行するため、本発明による
低珪素・低硫黄・高炭素フェロクロムの最終生成量は、
最初にレードル受けした通常品の量に比べ、2〜3%増
量し、生産性の向上となる。
Further, in the present invention, Si in a normal product is
When desiliconizing outside the furnace using chromium ore and / or scale, as shown in the above equations (1) and (2),
Since the chromium ore and / or the chromium oxide and / or iron oxide contained in the scale are reduced to form chromium and / or iron and migrate into the high carbon ferrochrome, the low silicon / low sulfur / high carbon ferrochrome of the present invention The final yield is
The amount is increased by 2 to 3% compared to the amount of the standard product that was initially received by ladle, which improves the productivity.

【0020】[0020]

【実施例】【Example】

実施例1 24000KVA電気炉で製造した高炭素フェロクロム
の通常品の溶湯約12トンをレードルに受けた時点で、
500℃に予熱したミルスケール1270kg、生石灰
660kgを添加し、さらに約13トンの通常品の溶湯
をレードルに受けて、合計受湯量25トンとした。その
後、スターラーにて1.5分間撹拌し低珪素・低硫黄・
高炭素フェロクロムを製造した。
Example 1 When about 12 tons of the molten metal of the high carbon ferrochrome ordinary product manufactured in the 24000 KVA electric furnace was received by the ladle,
1270 kg of mill scale preheated to 500 ° C. and 660 kg of quick lime were added, and about 13 tons of ordinary molten metal was further received by the ladle to make a total amount of received hot water of 25 tons. After that, stir for 1.5 minutes with a stirrer to reduce low silicon, low sulfur,
A high carbon ferrochrome was produced.

【0021】実施例2 実施例1と同じ24000KVA電気炉で製造した高炭
素フェロクロムの通常品の溶湯約12トンをレードルに
受けた時点で、500℃に予熱したクロム鉱石2440
kg、生石灰320kgを添加し、さらに約13トンの
通常品の溶湯をレードルに受けて、合計受湯量25トン
とした。その後、スターラーにて4分間撹拌し低珪素・
低硫黄・高炭素フェロクロムを製造した。
Example 2 A chromium ore 2440 preheated to 500 ° C. at the time when about 12 tons of a high carbon ferrochromium standard molten metal produced in the same 24000 KVA electric furnace as in Example 1 was received by the ladle.
kg and 320 kg of quick lime were added, and about 13 tons of the normal molten metal was received by the ladle, and the total amount of hot water received was 25 tons. Then, stir for 4 minutes with a stirrer to reduce the silicon content.
Produced low sulfur and high carbon ferrochrome.

【0022】実施例3 実施例1と同じ24000KVA電気炉で製造した高炭
素フェロクロムの通常品の溶湯約12トンをレードルに
受けた時点で、500℃に予熱した、クロム鉱石810
kg、ミルスケール850kg、生石灰300kg、マ
グネシア煉瓦屑200kgを添加し、さらに約13トン
の通常品の溶湯をレードルに受けて、合計受湯量を25
トンとした。その後、スターラーにて3分間撹拌し低珪
素・低硫黄・高炭素フェロクロムを製造した。
Example 3 Chromium ore 810, which was preheated to 500 ° C., when about 12 tons of a high carbon ferrochrome ordinary molten metal produced in the same 24000 KVA electric furnace as in Example 1 was received by the ladle
kg, mill scale 850 kg, quick lime 300 kg, magnesia brick waste 200 kg, and about 13 tons of normal molten metal are received by the ladle, and the total amount of molten metal received is 25
Tons. Then, the mixture was stirred with a stirrer for 3 minutes to produce low silicon / low sulfur / high carbon ferrochrome.

【0023】表1に、本発明例で使用したクロム鉱石、
ミルスケール、生石灰、マグネシア煉瓦屑の組成を示
す。また、表2に実施例1〜3の結果をまた表3に比較
例として従来法の代表例を示す。
Table 1 shows the chromium ores used in the examples of the present invention,
The composition of mill scale, quicklime and magnesia brick waste is shown. Table 2 shows the results of Examples 1 to 3 and Table 3 shows a representative example of the conventional method as a comparative example.

【0024】[0024]

【表1】 [Table 1]

【0025】[0025]

【表2】 [Table 2]

【0026】[0026]

【表3】 [Table 3]

【0027】表2によって明らかなように、本発明の実
施例1〜3によれば、最終目標Siを1.7〜1.8%に
した場合、従来法に比べ、還元されずにスラグへ移行す
るクロム量が減少し、クロム収率が2%余り向上する。
As is clear from Table 2, according to Examples 1 to 3 of the present invention, when the final target Si is 1.7 to 1.8%, slag is not reduced but reduced as compared with the conventional method. The amount of transferred chromium is reduced and the chromium yield is improved by more than 2%.

【0028】[0028]

【発明の効果】以上のように、本発明の低珪素・低硫黄
・高炭素フェロクロムの製造法によれば、従来法に比べ
てクロム収率および生産性が向上するとともに、従来法
のように特に脱硫剤を必要とせず、かつ溶湯温度保持の
ための設備も必要としない有用な方法である。
As described above, according to the method for producing low silicon, low sulfur, and high carbon ferrochromium of the present invention, the chromium yield and productivity are improved as compared with the conventional method, and at the same time as the conventional method. In particular, it is a useful method that does not require a desulfurizing agent and does not require equipment for maintaining the molten metal temperature.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 高井 清明 福岡県北九州市八幡東区大字前田字洞岡 2142−3 日本重化学工業株式会社九州工 場内 (72)発明者 中田 勇 福岡県北九州市八幡東区大字前田字洞岡 2142−3 日本重化学工業株式会社九州工 場内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Kiyoaki Takai 2142-3 Doraoka, Maeda, Hachimanto-ku, Kitakyushu, Fukuoka Prefecture Nippon Kyushu Kogyo Co., Ltd. Kyushu Plant (72) Inventor, Isamu Nakata Yahatahigashi, Kitakyushu, Fukuoka 2142-3 Maeda, Maeda-ku, Tokyo Kyushu Plant of Nippon Heavy Chemical Industry Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】クロム鉱石の炭素還元によって電気炉で製
造し、出湯、レードル受けした高炭素フェロクロム溶湯
に、クロム鉱石と塩基性造滓剤を、またはスケールと塩
基性造滓剤を、またはクロム鉱石とスケールと塩基性造
滓剤を添加し、撹拌して精練することを特徴とする低珪
素・低硫黄・高炭素フェロクロムの製造法。
1. A high-carbon ferrochromium melt produced by an electric furnace by carbon reduction of chromium ore and subjected to tapping and ladle, with chromium ore and a basic slag-forming agent, or scale and a basic slag-forming agent, or chromium. A method for producing low-silicon, low-sulfur, high-carbon ferrochrome, which is characterized by adding ore, scale, and a basic slag forming agent, stirring and refining.
JP19825093A 1993-04-22 1993-08-10 Production of low-silicon, low-sulfur and high-carbon ferrochrome Pending JPH073379A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19825093A JPH073379A (en) 1993-04-22 1993-08-10 Production of low-silicon, low-sulfur and high-carbon ferrochrome

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP9629093 1993-04-22
JP5-96290 1993-04-22
JP19825093A JPH073379A (en) 1993-04-22 1993-08-10 Production of low-silicon, low-sulfur and high-carbon ferrochrome

Publications (1)

Publication Number Publication Date
JPH073379A true JPH073379A (en) 1995-01-06

Family

ID=26437517

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19825093A Pending JPH073379A (en) 1993-04-22 1993-08-10 Production of low-silicon, low-sulfur and high-carbon ferrochrome

Country Status (1)

Country Link
JP (1) JPH073379A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114262832A (en) * 2021-12-21 2022-04-01 徐州宏阳新材料科技股份有限公司 Refining and impurity removing method for ferrochrome

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114262832A (en) * 2021-12-21 2022-04-01 徐州宏阳新材料科技股份有限公司 Refining and impurity removing method for ferrochrome

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