JPH0437129B2 - - Google Patents
Info
- Publication number
- JPH0437129B2 JPH0437129B2 JP27162387A JP27162387A JPH0437129B2 JP H0437129 B2 JPH0437129 B2 JP H0437129B2 JP 27162387 A JP27162387 A JP 27162387A JP 27162387 A JP27162387 A JP 27162387A JP H0437129 B2 JPH0437129 B2 JP H0437129B2
- Authority
- JP
- Japan
- Prior art keywords
- lance
- blowing
- soda ash
- hot metal
- 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.)
- Expired
Links
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 76
- 235000017550 sodium carbonate Nutrition 0.000 claims description 37
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 37
- 238000007664 blowing Methods 0.000 claims description 32
- 238000006477 desulfuration reaction Methods 0.000 claims description 29
- 230000023556 desulfurization Effects 0.000 claims description 29
- 239000002184 metal Substances 0.000 claims description 27
- 229910052751 metal Inorganic materials 0.000 claims description 27
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 13
- 239000000292 calcium oxide Substances 0.000 claims description 10
- 235000012255 calcium oxide Nutrition 0.000 claims description 10
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 6
- 238000007654 immersion Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 239000011449 brick Substances 0.000 claims description 4
- 239000010459 dolomite Substances 0.000 claims description 4
- 229910000514 dolomite Inorganic materials 0.000 claims description 4
- 230000003009 desulfurizing effect Effects 0.000 claims description 3
- 239000000395 magnesium oxide Substances 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- 239000004604 Blowing Agent Substances 0.000 description 11
- 229910000831 Steel Inorganic materials 0.000 description 8
- 239000010959 steel Substances 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000011247 coating layer Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 239000011819 refractory material Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000004347 Perilla Nutrition 0.000 description 1
- 244000124853 Perilla frutescens Species 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000012159 carrier gas Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
Landscapes
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Description
〈産業上の利用分野〉
本発明は、予め脱硅または脱燐された溶銑のソ
ーダ灰吹き込みによる脱硫法に関するものであ
る。
〈従来の技術〉
従来、脱硅または脱燐処理された溶銑をさらに
脱硫処理する場合は、脱硫反応効率がよいという
観点からソーダ灰吹き込みが用いられている(例
えば特開昭56−166315号公報参照)。
しかし、このようなソーダ吹込脱硫法において
は、ソーダ灰は分解吸熱量が大きく、また耐火物
への侵蝕性も極めて強いために以下のような問題
が生じている。
吹込ランス先端部での凝固鉄(ナードルと称
す)の生成によるランスの閉塞。
吹込ランス先端部によるランス寿命の低下。
前記のようなランスの閉塞は、ほとんど脱硫
処理中に発生し、以後のソーダ灰の吹き込みが不
可能となるので、一旦処理を中断してランスを新
しいものと交換した後再度処理をする必要があつ
た。ソーダ灰の吹き込み量が多い場合や溶銑温度
が低い場合には、このような閉塞が1ヒートの処
理中に数回にわたつて起こることがあり、全処理
時間の延長により、次工程(転炉)への溶銑の供
給がスムーズにいかなくなつたり、溶銑温度の低
下、ランス取替え作業負荷の増加といつた問題を
引き起こしていた。また不安定でかつ断続的な吹
き込みと、溶銑温度降下が大きくなるため脱硫効
率の低下をも招いていた。前記のようなランス
寿命の低下は、脱硫効率の低下とともに脱硫処理
コスト増加の一因ともなつていた。
〈発明が解決しようとする問題点〉
本発明は、脱硅または脱燐処理をされた溶銑を
さらにソーダ灰吹き込み法により脱硫処理するに
際して、従来の方法のランス先端部でのナードル
の生成によるランス閉塞の問題や、脱硫効率の低
下およびランス寿命の低下による処理コスト増と
いつた問題を解消し得るような、脱硅または脱燐
処理された溶銑のソーダ灰吹込による脱硫法を提
供するためになされたものである。
〈問題点を解決するための手段〉
本発明者らは、溶銑脱硫処理における浸漬ラン
スの閉塞防止などについて鋭意研究を重ねた結
果、脱硫剤のソーダ灰吹き込み前に生石灰などを
吹き込み、浸漬ランス先端に被覆層を形成するこ
とによつて目的を達することがきるとの知見を
え、この知見にもとづいて本発明をなすに至つ
た。
本発明は、脱硅または脱燐処理を行つた溶銑
に、浸漬ランスを用いてソーダ灰を吹き込み脱硫
処理を行うに際して、予め前記ランスによつてソ
ーダ灰吹き込み予定量100重量部に対して6重量
部以上の粉状の生石灰、ドロマイト・クリンカ
ー、マグネシアクリンカーのうちの1種または2
種以上の混合物、、もしくはこれらの1種または
混合物を原料とする煉瓦屑粉を吹き込んだ後、所
定量のソーダ灰を吹き込むことを特徴とする脱硅
または脱燐処理後の溶銑の脱硫法である。
〈本発明をなすに至つた経過および作用〉
ソーダ灰吹き込み用ランスは、例えば第3図の
ような構造をしている。すなわち、鋼管の表面に
キヤスタブル耐火物を張り付けたものである。こ
のような構造の吹き込み用ランスによるソーダ灰
吹き込み時のナードル発生によるランス先端閉塞
機構は、以下のように考えられる。
(a) ソーダ灰による化学侵蝕によるランス先端の
キヤスターブル耐火物の溶損、鋼管先端部の露
出、
(b) ランス先端の鋼管露出部の熱による軟化、一
部溶融、
(c) 熱により軟化、一部溶融した鋼管内部へのソ
ーダ灰付着およびしその分解吸熱によるナード
ルの発生、
(d) ナードルの成長によるランス先端閉塞、
これらを図に示すと第4図a,b,c,dのよ
うになる。
したがつて、ナードル発生によるランス先端の
閉塞を防止するためには、先端部のキヤスタブル
耐火物の溶損を防止し、鋼管が露出し溶銑に直接
接触することを防ぐことが肝要である。本発明
は、脱硅または脱燐処理を行つた溶銑に、浸漬ラ
ンスを用いてソーダ灰を吹き込み脱硫処理を行う
に際して、ソーダ灰の吹き込みに先立つて、生石
灰、ドロマイト・クリンカー、マグネシアクリン
カー等、塩基性の高融点、高耐火度の材料粉末、
またはこれ等の1種または2種以上の混合物から
なる塩基性レンガ屑粉末を予備吹き込みすること
により、前述のようなランス先端のキヤスタブル
耐火物の表面に高融点、高耐火度の被覆層が形成
され、この被覆層により、ソーダ灰の化学侵蝕作
用が防止されキヤスタブル耐火物の溶損が防止さ
れるため、前述のような機構によるランス先端閉
塞が防止され、同時にランスの寿命も延長される
という作用効果が生ずる。なおこのような作用効
果が期待できる予備吹き込み剤の量は、第2図か
ら明らかなように、予備吹き込み剤の種類を問わ
ず、トピードのソーダ灰合計吹き込み量100重量
部に対して6重量部以上であり、この値を下廻る
と予備吹き込み剤による被覆効果が小さく、1ト
ピード(250t)の溶銑脱硫に当りランス先端の閉
塞が0回ではなくなり、予備吹き込み剤比率の減
少に伴い、ランス先端閉塞回数(回/1トピー
ド)は増加し、予備吹き込み剤比率0の場合は、
平均約3回/1トピードも閉塞を生じた。なお予
備吹き込み剤の比率の上限は、ランス先端閉塞防
止効果から見ると6重量部以上でほとんど変化が
なく、これら予備吹き込み剤は、脱硅または脱燐
溶銑の脱硫には、あまり寄与しないので溶銑の温
度降下や経済性や吹き込み時間を考えると30重量
部以下が望ましい。
<Industrial Application Field> The present invention relates to a desulfurization method by injecting soda ash into hot metal that has been previously desiliconized or dephosphorized. <Prior art> Conventionally, when hot metal that has been desiliconized or dephosphorized is further desulfurized, soda ash injection has been used from the viewpoint of high desulfurization reaction efficiency (for example, Japanese Patent Application Laid-open No. 166315/1983). reference). However, in such a soda blow desulfurization method, the following problems arise because soda ash has a large decomposition heat absorption amount and is extremely corrosive to refractories. Blockage of the lance due to the formation of solidified iron (referred to as nurdle) at the tip of the blowing lance. Reduced lance life due to the tip of the blowing lance. The lance blockage described above almost always occurs during the desulfurization process, making it impossible to blow soda ash into the desulfurization process, so it is necessary to stop the process, replace the lance with a new one, and then start the process again. It was hot. When a large amount of soda ash is injected or when the hot metal temperature is low, such blockage may occur several times during one heat treatment, and the total treatment time is extended, resulting in a delay in the next process (converter ), leading to problems such as the smooth supply of hot metal, a drop in hot metal temperature, and an increase in the workload of lance replacement. In addition, unstable and intermittent blowing and a large drop in hot metal temperature led to a decrease in desulfurization efficiency. The decrease in lance life as described above has been a cause of a decrease in desulfurization efficiency and an increase in desulfurization treatment costs. <Problems to be Solved by the Invention> The present invention provides a method for desulfurizing hot metal that has been desiliconized or dephosphorized by a soda ash blowing method. To provide a desulfurization method by injecting soda ash into hot metal that has been desiliconized or dephosphorized, which can solve problems such as blockage, decreased desulfurization efficiency, and increased processing costs due to decreased lance life. It has been done. <Means for Solving the Problems> As a result of intensive research into prevention of clogging of immersion lances in hot metal desulfurization treatment, the present inventors have found that, before injecting soda ash as a desulfurizing agent, quicklime etc. are blown into the tip of the immersion lance. The present inventors have found that the objective can be achieved by forming a coating layer on the material, and based on this knowledge, the present invention has been completed. In the present invention, when performing a desulfurization treatment by blowing soda ash into hot metal that has been subjected to a desiliconization or dephosphorization treatment using an immersion lance, the invention provides that, when performing a desulfurization treatment by blowing soda ash into hot metal that has been subjected to a desiliconization or dephosphorization treatment, 6 parts by weight of soda ash is injected in advance by the lance to 100 parts by weight of soda ash. 1 or 2 of powdered quicklime, dolomite clinker, and magnesia clinker
A desulfurization method for hot metal after desiliconization or dephosphorization treatment, which is characterized by blowing in a mixture of more than one species, or brick scrap powder made from one or a mixture of these, and then blowing in a predetermined amount of soda ash. be. <Process and operation leading to the invention> A soda ash injection lance has a structure as shown in FIG. 3, for example. That is, a castable refractory is pasted onto the surface of a steel pipe. The lance tip blockage mechanism due to the generation of nurdles during soda ash injection using the blowing lance having such a structure is thought to be as follows. (a) Erosion of the castable refractory at the tip of the lance due to chemical attack by soda ash, exposing the tip of the steel pipe; (b) Softening and partial melting of the exposed portion of the steel pipe at the tip of the lance due to heat; (c) Softening due to heat. , the adhesion of soda ash inside the partially melted steel pipe and the generation of nurdles due to heat absorption from the decomposition of perilla, and (d) the lance tip blockage due to the growth of nurdles. These are shown in Figure 4 a, b, c, and d. It becomes like this. Therefore, in order to prevent clogging of the lance tip due to knurling, it is important to prevent the castable refractory material at the tip from melting and to prevent the steel pipe from being exposed and coming into direct contact with hot metal. In the present invention, when carrying out desulfurization treatment by blowing soda ash into hot metal that has been subjected to desiliconization or dephosphorization treatment using an immersion lance, a base such as quicklime, dolomite clinker, magnesia clinker, etc. High melting point, high refractory material powder,
Alternatively, by pre-injecting basic brick waste powder consisting of one or a mixture of two or more of these, a high melting point, high refractory coating layer is formed on the surface of the castable refractory at the tip of the lance as described above. This coating layer prevents the chemical erosion of soda ash and prevents the castable refractory from being eroded, thereby preventing the lance tip from clogging due to the mechanism described above, and at the same time extending the life of the lance. Effects occur. As is clear from Figure 2, the amount of pre-blowing agent that can be expected to have such effects is 6 parts by weight per 100 parts by weight of the total amount of soda ash blown into Torpedo, regardless of the type of pre-blowing agent. Below this value, the coating effect of the pre-blowing agent will be small, and the lance tip will no longer be clogged 0 times per torpedo (250t) of hot metal desulfurization, and as the pre-blowing agent ratio decreases, the lance tip will become clogged. The number of blockages (times/1 torpedo) increases, and when the pre-blowing agent ratio is 0,
On average, about 3 times/1 topedo resulted in occlusion. Note that the upper limit of the ratio of the pre-blowing agent is 6 parts by weight or more and there is almost no change from the viewpoint of the lance tip clogging prevention effect, and these pre-blowing agents do not contribute much to the desulfurization of desiliconization or dephosphorization of hot metal. Considering the temperature drop, economy, and blowing time, it is desirable to use 30 parts by weight or less.
【表】【table】
【表】【table】
【表】
なお、第2図の予備吹き込み剤の吹き込みおよ
びソーダ灰の吹き込みに用いた吹き込みランスの
キヤスタブル耐火物の材質特性は第1表に示すも
ので、予備吹き込み剤およびソーダ灰吹き込み速
度は70〜100Kg/minである。
〈実施例〉
〈実施例 1〉
350tトピードにおいて、脱燐処理を行つた溶銑
280tにソーダ灰吹き込みによる脱硫処理を行つ
た。脱硫処理前成分は第2表に示す通りである。[Table] The material properties of the castable refractory of the blowing lance used for blowing the pre-blowing agent and soda ash in Figure 2 are shown in Table 1, and the blowing speed of the pre-blowing agent and soda ash was 70 ~100Kg/min. <Example><Example1> Hot metal subjected to dephosphorization treatment in a 350t torpedo
Desulfurization treatment was performed on 280 tons by blowing soda ash. The components before desulfurization treatment are shown in Table 2.
【表】
上記の溶銑に対し、キヤリアガス(ドライエヤ
ー)流量2.0Nm3/nimでソーダ灰1500Kgを吹き込
む予定で処理を開始した。70Kg/minの吹き込み
速度で、350Kg吹き込んだところでランス先端が
閉塞し吹き込み継続不可能となつた。そこで吹き
込みランスの交換を行つたのち再処理を行つたが
累計800Kg吹き込んだ時点で再度ランス先端が閉
塞し、1500Kg全量吹き込み終わるまでに先端閉塞
が3回発生した。ソーダ圧処理後の成分は第3表
に示す通りであつた。
一方、上記の溶銑に対しソーダ灰1500Kg、生石
灰150Kgを第1図に示すように生石灰が最下層を
形成するようにデイスペンサーに入れて吹き込み
を行つた。この場合、ランス先端閉塞の発生は全
くなく安定した処理ができた。処理後の成分を第
4表に示す。石灰系フラツクスの予備吹き込みに
よるランス先端詰まり防止により、処理後温度の
上昇および脱硫反応効率の向上が達成できた。[Table] Treatment was started with plans to blow 1500 kg of soda ash into the above hot metal at a carrier gas (dry air) flow rate of 2.0 Nm 3 /nim. At a blowing speed of 70 kg/min, the lance tip became clogged when 350 kg was blown into it, making it impossible to continue blowing. Therefore, the blowing lance was replaced and reprocessing was carried out, but the lance tip was blocked again when a total of 800 kg had been blown into the lance, and the tip was blocked three times before the entire 1500 kg had been blown. The components after the soda pressure treatment were as shown in Table 3. On the other hand, 1,500 kg of soda ash and 150 kg of quicklime were placed in a dispenser and blown into the hot metal so that the quicklime formed the bottom layer as shown in FIG. In this case, stable treatment was achieved with no occurrence of lance tip blockage. The components after treatment are shown in Table 4. By pre-injecting lime-based flux to prevent clogging of the lance tip, we were able to increase the post-treatment temperature and improve the desulfurization reaction efficiency.
【表】【table】
【表】
〈実施例 2〉
第5表に示すような脱硅、脱燐処理後の溶銑を
350tトーピードカーに260トン/回ずつ入れ、1
回当りのソーダ灰吹き込み量を平均1040Kg(4.0
Kg/溶銑トン)を吹き込むに当り、予め生石灰粉
またはドロマイトレンガ屑粉を外掛けで6.4%
(67Kg/回=0.26Kg/溶銑トン)を70〜100Kg/
minの流量で予備的に吹き込んでから、ソーダ灰
を第1表のような特性のキヤスタブル耐火物でラ
イニングした吹き込みランスを用いて、70〜100
Kg/minの流量で吹き込み、脱硫処理をそれぞれ
約10ヒートづつ合計20ヒートについて行つた。
比較例として、前記と同一条件で予め生石灰そ
の他の予備吹き込み剤の吹き込みなしで、ソーダ
灰吹き込み脱硫を10ヒートについて行つた。予め
生石灰の吹き込みを行つた本発明の実施例のラン
ス寿命がランス1本当りの吹き込みソーダ灰重量
で表わして3.5〜4.0t/本(平均3.75t/本)と、
比較例の1.0〜1.5t/本(1.25t/本)に対して平
均3倍の寿命を示した。また、ソーダ灰脱硫反応
効率も実施例の場合は17〜25%であり比較例の10
〜15%に比べて大巾に向上した。[Table] <Example 2> Hot metal after desiliconization and dephosphorization treatment as shown in Table 5 was
Put 260 tons/time into a 350t torpedo car, 1
The average amount of soda ash per injection is 1040Kg (4.0
Kg/ton of hot metal) before blowing, apply quicklime powder or dolomite brick waste powder to 6.4%.
(67Kg/time = 0.26Kg/ton of hot metal) 70~100Kg/
After preliminarily blowing soda ash at a flow rate of 70 to 100 min, using a blowing lance lined with castable refractory having the characteristics as shown in Table 1,
The desulfurization treatment was carried out for a total of 20 heats, approximately 10 heats each, by blowing at a flow rate of Kg/min. As a comparative example, soda ash blowing desulfurization was carried out for 10 heats under the same conditions as above without blowing quicklime or other preliminary blowing agent. The lance life of the embodiment of the present invention in which quicklime was blown in advance was 3.5 to 4.0 t/lance (average 3.75 t/lance), expressed as the weight of blown soda ash per lance.
The average lifespan was three times longer than that of the comparative example, which was 1.0 to 1.5 t/piece (1.25 t/piece). In addition, the soda ash desulfurization reaction efficiency was 17 to 25% in the example and 10% in the comparative example.
This was a huge improvement compared to ~15%.
【表】
〈発明の効果〉
本発明は、脱硅または脱燐処理した溶銑のソー
ダ灰吹き込み脱硫に際して以下のような効果があ
る。
吹き込みランスの先端閉塞がなくなり、処理
中のランス取替えによる全処理時間の延長の防
止、溶銑温度低下の減少、不安定かつ断続的な
吹き込みによる脱硫反応効率の低下が防止でき
短時間に安定した脱硫が行える。
吹き込みランスの寿命が約3倍に延長し、脱
硫反応効率の著しい向上と併せて脱硫コストが
低減できる。
処理中のランス取替えのような不安全かつ高
温下における作業が省略できる。[Table] <Effects of the Invention> The present invention has the following effects in the soda ash blowing desulfurization of hot metal that has been subjected to desiliconization or dephosphorization treatment. Blockage at the tip of the blowing lance is eliminated, preventing extension of the total processing time due to lance replacement during processing, reducing drop in hot metal temperature, and preventing decrease in desulfurization reaction efficiency due to unstable and intermittent blowing, resulting in stable desulfurization in a short time. can be done. The life of the blowing lance is extended by about three times, and the desulfurization cost can be reduced as well as the desulfurization reaction efficiency is significantly improved. Unsafe and high-temperature work such as lance replacement during processing can be omitted.
第1図は、本発明の実施に用いる装置の説明
図、第2図は、予備吹き込み剤とランス先端閉塞
回数との関係を示すグラフ、第3図は、ソーダ灰
吹き込みランスの断面図、第4図は、ランス先端
での凝固鉄発生機構の説明図である。
1……鋼管、2……キヤスタブル耐火物、3…
…鋼管の露出部、3′……鋼管の軟化部、4……
ソーダ灰、5……凝固鉄(ナードル)、6……デ
イスペンサー、7……ソーダ灰、8……生石灰、
9……ドライエヤー、10……吹き込みランス、
11……トピードカー、12……溶銑、13……
配管。
FIG. 1 is an explanatory diagram of the apparatus used to carry out the present invention, FIG. 2 is a graph showing the relationship between the preliminary blowing agent and the number of times the lance tip is blocked, and FIG. 3 is a cross-sectional view of the soda ash blowing lance. FIG. 4 is an explanatory diagram of the solidified iron generation mechanism at the tip of the lance. 1... Steel pipe, 2... Castable refractory, 3...
...Exposed part of steel pipe, 3'...Softened part of steel pipe, 4...
Soda ash, 5... Solidified iron (nurdle), 6... Dispenser, 7... Soda ash, 8... Quicklime,
9... Dry air, 10... Blowing lance,
11... Torpedo car, 12... Hot metal, 13...
Piping.
Claims (1)
ンスを用いてソーダ灰を吹き込み脱硫処理を行う
に際して、予め前記ランスによつてソーダ灰吹き
込予定量100重量部に対して6重量部以上の粉状
の生石灰、ドロマイト・クリンカー、マグネシア
クリンカーのうちの1種または2種以上の混合
物、もしくはこれらの1種または混合物を原料と
する煉瓦屑粉を吹き込んだ後、所定量のソーダ灰
を吹き込むことを特徴とする脱硅または脱燐処理
後の溶銑の脱硫法。1. When carrying out desulfurization treatment by blowing soda ash into hot metal that has undergone desiliconization or dephosphorization treatment using an immersion lance, at least 6 parts by weight per 100 parts by weight of the planned amount of soda ash injected using the lance in advance. After blowing in one or a mixture of two or more of powdered quicklime, dolomite clinker, and magnesia clinker, or brick waste made from one or a mixture of these, a predetermined amount of soda ash is injected. A method for desulfurizing hot metal after desiliconization or dephosphorization treatment, characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27162387A JPH01116017A (en) | 1987-10-29 | 1987-10-29 | Method for desulfurizing molten iron after desiliconizing or dephosphorizing treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27162387A JPH01116017A (en) | 1987-10-29 | 1987-10-29 | Method for desulfurizing molten iron after desiliconizing or dephosphorizing treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01116017A JPH01116017A (en) | 1989-05-09 |
| JPH0437129B2 true JPH0437129B2 (en) | 1992-06-18 |
Family
ID=17502652
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27162387A Granted JPH01116017A (en) | 1987-10-29 | 1987-10-29 | Method for desulfurizing molten iron after desiliconizing or dephosphorizing treatment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01116017A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5910069B2 (en) * | 2011-12-22 | 2016-04-27 | Jfeスチール株式会社 | Desulfurization agent, hot metal desulfurization treatment method using the desulfurization agent, and hot metal desulfurization treatment method using refractory |
-
1987
- 1987-10-29 JP JP27162387A patent/JPH01116017A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01116017A (en) | 1989-05-09 |
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