JPS5925911A - Dephosphorization treatment of molten iron - Google Patents
Dephosphorization treatment of molten ironInfo
- Publication number
- JPS5925911A JPS5925911A JP13424282A JP13424282A JPS5925911A JP S5925911 A JPS5925911 A JP S5925911A JP 13424282 A JP13424282 A JP 13424282A JP 13424282 A JP13424282 A JP 13424282A JP S5925911 A JPS5925911 A JP S5925911A
- Authority
- JP
- Japan
- Prior art keywords
- dephosphorization
- hot metal
- slag
- dephosphorizing
- dephosphorizing agent
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
Abstract
Description
【発明の詳細な説明】
本発明は浴銑の予備脱燐方法の改善に関し、転炉吹錬時
の副原料の削減、極低燐銅溶製の省工程化、および製鋼
工程から発生するスラグ量の低減を図る、溶銑の予備脱
燐方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to improvements in the preliminary dephosphorization method of bath pig iron, including reduction of auxiliary materials during converter blowing, process saving of ultra-low phosphorus copper melting, and reduction of slag generated from the steelmaking process. The present invention relates to a preliminary dephosphorization method for hot metal that aims to reduce the amount of phosphorization.
従来、溶銑の予備脱燐を行なうに当っては、脱燐剤を溶
銑浴面上に添加し、機械的攪拌または気体吹込みによる
攪拌を利用して反応効率を高める方法がとられていた。Conventionally, when performing preliminary dephosphorization of hot metal, a method has been used in which a dephosphorizing agent is added onto the surface of the hot metal bath and stirring using mechanical stirring or gas injection is used to increase reaction efficiency.
さらに近年、粉体吹込み技術が確立され、気体を搬送媒
体として微粉脱燐剤を溶銑浴面下に吹込む方法が盛んに
行なわれるようになった。Furthermore, in recent years, powder blowing technology has been established, and a method of blowing a fine powder dephosphorizing agent under the surface of a hot metal bath using gas as a carrier medium has become popular.
脱燐処理を司及的少祉の脱燐剤によ−って行なうために
は、脱燐剤と溶銑との接触・反応を促進する必要がある
。上記脱燐剤粉体を溶銑浴面下に吹込む方法は、反応界
面積が従来の浴面上に脱燐剤を添加する方法に比[7て
飛跡的に大きいこと、および、同時に行)よりれる気体
による溶銑と脱燐剤との激しい混合が期待できることに
よって、脱燐反応効率が高い。この方法の実施例を第1
図に示す。取鍋中の浴銑3内にランス4を介して脱燐剤
吹込み装置5内の微粉脱燐剤が吹き込まオシる。トピー
ド車内の溶銑についても同様の脱燐処理が行なわれ一〇
いる−
脱燐剤としては、生石灰またはソーダ灰を脱燐生成物の
吸収剤とし、酸素源とり、−C鉄鉱石、ミルスケール、
転炉ダストなどを用い、媒耐剤とじてほたる石、コレマ
ナイト、塩化カルシウムなどを加えて、最適組成になる
ように混合したものを用いている。In order to carry out the dephosphorization process using a controlled dephosphorizing agent, it is necessary to promote the contact and reaction between the dephosphorizing agent and the hot metal. The method of injecting the dephosphorizing agent powder below the surface of the hot metal bath is characterized by the fact that the reaction interfacial area is larger in trajectory than the conventional method of adding the dephosphorizing agent above the bath surface, and the process is carried out simultaneously. The dephosphorization reaction efficiency is high because intense mixing of the hot metal and the dephosphorizing agent can be expected due to the flowing gas. The first example of this method is
As shown in the figure. Fine powder dephosphorizing agent in a dephosphorizing agent blowing device 5 is blown into the bath pig iron 3 in the ladle through a lance 4. A similar dephosphorization process is also carried out on the hot metal inside the Torpedo car.The dephosphorizing agent uses quicklime or soda ash as an absorbent for the dephosphorization product, and as an oxygen source, -C iron ore, mill scale,
Converter dust is used, a mortar resistant agent is added, fluorite, colemanite, calcium chloride, etc. are added, and a mixture is used to achieve the optimum composition.
このような脱燐剤吹込みによる方法によって、脱燐剤原
単位すなわち、溶銑1トン当りの脱燐剤使用量は、処理
前の溶銑温度・成分によって異なるが、大略50〜70
に9/l−浴銑であった。By such a method of injecting a dephosphorizing agent, the dephosphorizing agent unit, that is, the amount of dephosphorizing agent used per 1 ton of hot metal, varies depending on the temperature and composition of the hot metal before treatment, but is approximately 50 to 70%.
It was 9/l-bath iron.
本発明者らは、脱燐剤吹込みによる溶銑脱燐の反応機構
を種々研究して来た結果、脱燐反応が反応進行位置にお
ける酸素ポテンシャルと密接に関連スることを見出した
。ここで酸素ポテンシャルとは、平衡する気体酸素、の
分圧で表示し、酸化性または還元性雰囲気の尺度となる
ものである。The present inventors have conducted various studies on the reaction mechanism of hot metal dephosphorization by injecting a dephosphorizing agent, and as a result, they have found that the dephosphorization reaction is closely related to the oxygen potential at the position where the reaction is proceeding. Here, the oxygen potential is expressed as the partial pressure of gaseous oxygen in equilibrium, and is a measure of the oxidizing or reducing atmosphere.
溶銑の脱燐反応は、溶銑中燐の酸化によって生成された
P2O5を強塩基性酸化物であるCaO1N、+20な
どにより吸収・固定しスラグとして溶鉄と分離すること
によって進行する。従って脱燐には酸化性雰囲気が有利
であり、炭素濃度が商い溶銑の脱燐では、酸化鉄または
気体酸素により脱燐反応位置の酸素ポテンシャルを高め
る必要がある。The dephosphorization reaction of hot metal proceeds by absorbing and fixing P2O5 generated by oxidation of phosphorus in the hot metal with strong basic oxides such as CaO1N, +20, and separating it from the molten iron as slag. Therefore, an oxidizing atmosphere is advantageous for dephosphorization, and when dephosphorizing hot metal with a low carbon concentration, it is necessary to increase the oxygen potential at the dephosphorization reaction site using iron oxide or gaseous oxygen.
酸素ポテンシャルをPO2(単位:atm)で表わせば
、溶銑の酸素ポテンシャルはPO2= ] 0−+aa
im程度である゛のに対し、生石灰系のスラグではPO
2: 100−12ai程度の高酸化性雰囲気に保たな
ければ十分な脱燐を行なえない(厳密に扁えばスラグ/
メタル間の燐配分を高くできない)ことが種々の研究に
よって明らかになっている。If the oxygen potential is expressed in PO2 (unit: atm), the oxygen potential of hot metal is PO2 = ] 0-+aa
In contrast, quicklime-based slag has PO
2: Sufficient dephosphorization cannot be achieved unless it is maintained in a highly oxidizing atmosphere of about 100-12ai (strictly speaking, slag/
Various studies have revealed that the phosphorus distribution between metals cannot be increased.
本発明者らは、第1図に示した従来の溶銑脱燐法におい
て、吹込み処理中の溶銑中のPO2を実611jし、ま
た熱力学データより推算した。The present inventors actually measured PO2 in hot metal during blowing treatment in the conventional hot metal dephosphorization method shown in FIG. 1, and also estimated it from thermodynamic data.
一連の研究から明らかになったことは、第1図中1で示
したランス4の吐出口近傍のPozは、lo −10〜
10 ”atmと脱燐反応にとって十分高い酸素ポテ
ンシャルに保たれているのに対し、浴面上スラグと溶銑
とが接触している図中2の部分では、PO2: 1’0
”〜10 ”atmとなり低酸素ポテンシャルであっ
た。What has become clear from a series of studies is that Poz near the discharge port of lance 4, indicated by 1 in Figure 1, is lo -10~
10" atm and the oxygen potential is kept high enough for the dephosphorization reaction, whereas in the part 2 in the figure where the slag and hot metal on the bath surface are in contact, PO2: 1'0
It was a low oxygen potential of ~10'' atm.
従って、ランスより溶銑浴面下に吹込まれた脱燐剤は、
ランス吐出口近傍ではPO2が高いので直ちに浴銑中燐
と反応し、3CaO−P2O5などの脱燐生成物として
浮上し、浴面上スラグとなる。Therefore, the dephosphorizing agent injected from the lance below the surface of the hot metal bath,
Since PO2 is high in the vicinity of the lance discharge port, it immediately reacts with phosphorus in the bath pig iron, floats up as dephosphorization products such as 3CaO-P2O5, and becomes slag on the bath surface.
しかし、浴面上スラグはPO2が低い状態にあり、スラ
グの脱燐能が比較的小さい場合には、スラグ中にP 2
0 sとして保てず、溶銑中へ燐が移行する。However, the slag on the bath surface has low PO2, and if the slag's dephosphorizing ability is relatively small, P2 is present in the slag.
It cannot be maintained at 0 s, and phosphorus migrates into the hot metal.
第2図は、処理途中まで脱燐剤の吹込みを行ない、途中
から脱燐剤の供給を停止し気体のみ吹込んで攪拌を行な
った実験中の溶銑中燐濃度の変化を示した図である。こ
のように、処理条件によっては、脱燐剤を溶銑浴面下に
吹込み、脱燐反応を進行させていても、浴面上スラグか
もの俊燐が同時に進行し、結果として脱燐効率を低下さ
せていたことが判明した。Figure 2 is a diagram showing changes in the phosphorus concentration in hot metal during an experiment in which the dephosphorizing agent was injected until the middle of the treatment, and then the supply of the dephosphorizing agent was stopped and only gas was injected and stirring was performed. . In this way, depending on the processing conditions, even if a dephosphorizing agent is injected under the surface of the hot metal bath and the dephosphorization reaction is progressing, slag on the bath surface and rapid phosphorusation may proceed at the same time, resulting in a decrease in dephosphorization efficiency. It was found that it was decreasing.
また、本出願人は、底吹き転炉を用いて石灰系フラック
スを大量に吹込み、極めて短時間に浴銑脱燐を行なう方
法を提案している。この底吹き転炉を用いて溶銑脱燐を
行なう場合、人絹のキー\・リアガスと太hi、のフラ
ックスとを吹き込むことにより、浴銑内の火点近傍の脱
燐と、脱燐能の高い浴面上のスラグど溶銑との接触界面
での脱燐との、両方のステップにおいて脱燐が進行する
ものである。The applicant has also proposed a method of dephosphorizing bath pig iron in an extremely short time by injecting a large amount of lime-based flux using a bottom-blowing converter. When dephosphorizing hot metal using this bottom-blowing converter, by blowing the key/rear gas of human silk and the flux of Taihi, the dephosphorization near the hot point in the hot metal and the dephosphorization ability can be improved. Dephosphorization occurs in both steps: slag on a high bath surface and dephosphorization at the contact interface with hot metal.
これに比し、溶銑予備処理容器における脱燐剤吹込み処
理においては、キャリアガス吹込量に限界があり従って
フラックス供給量にも限界があるので、溶銑内で起る脱
燐は進行するものの、浴面上のスラグは燐濃度が高く脱
燐能力が低い場合もあり、逆に溶銑中に復燐する場合も
ある点に差があるので改善の予地があることが知られる
。In contrast, in the dephosphorization agent injection process in the hot metal pretreatment vessel, there is a limit to the amount of carrier gas blown and therefore a limit to the amount of flux supplied, so although the dephosphorization that occurs in the hot metal progresses, The difference is that the slag on the bath surface may have a high phosphorus concentration and low dephosphorizing ability, and conversely, it may rephosphorize in the hot metal, so it is known that there is room for improvement.
以上の知見から、本発明者らは、復燐を防止することに
よって脱燐効率を向上し、脱燐剤原単位を低減する方法
について研究の結果、本発明を完成するに至った。Based on the above findings, the present inventors have completed the present invention as a result of research on a method for improving dephosphorization efficiency and reducing the unit consumption of a dephosphorizing agent by preventing rephosphorization.
ずなわち本発明は、従来の取鍋に脱燐剤を吹き込む簡易
な設備を用いて、効率よ(溶銑予備脱燐を行なう脱燐方
法を提供することを目的とするもので、その要旨とする
ところは、浴銑の脱燐処理を該浴銑浴面下への脱燐剤の
吹込みによって行なうに当り、浴面上に形成される脱燐
反応後の溶融スラグを前記脱燐剤の吹込みと同時期に連
続的に除去することにまり脱燐効率を高めることを特徴
とする溶銑の脱燐処理方法に存する。The purpose of the present invention is to provide an efficient (preliminary dephosphorization of hot metal) dephosphorization method using a simple equipment for blowing a dephosphorizing agent into a conventional ladle. This is because when the dephosphorization treatment of hot iron baths is carried out by blowing a dephosphorizing agent under the surface of the hot iron bath, the molten slag formed on the bath surface after the dephosphorization reaction is treated with the dephosphorizing agent. The present invention relates to a method for dephosphorizing hot metal, which is characterized by increasing dephosphorization efficiency by continuously removing phosphorus at the same time as blowing.
スラグを連続的に排除する具体的な方法は、例えば近年
開発された、真空吸引式スラグ除去装置の使用Jが最適
である。この装置はスラグとメタルの比重差を利用し、
真空吸引によりスラグのみを吸い」二げるものであり、
吸い十けたスラグは水噴流によって粒状化され回収され
る。As a specific method for continuously removing slag, for example, the most suitable method is to use a vacuum suction type slag removal device that has been developed in recent years. This device utilizes the difference in specific gravity between slag and metal,
It uses vacuum suction to suck up only the slag,
The slag that has been absorbed is granulated and recovered by a water jet.
第3図はこの装置を用いて処理を行なう概−要を示し、
3は溶銑、4はランス、5は脱燐剤吹込み装+M’−1
6は集塵フード、7は真空吸上げ式スラグ除去装置であ
る。Figure 3 shows the outline of processing using this device.
3 is hot metal, 4 is lance, 5 is dephosphorizing agent injection device +M'-1
6 is a dust collection hood, and 7 is a vacuum suction type slag removal device.
6174図は、本発明方法と従来法(第1図)とにおけ
る脱燐処坤中の浴銑中燐嬢度の変化を比較して示したも
のである。溶銑中燐濃度が同一レベルになるまで脱燐す
るために約5分(脱燐剤として約1okg/l−浴銑)
程度節約できる。Figure 6174 shows a comparison of changes in phosphorus content in the bath iron during dephosphorization between the method of the present invention and the conventional method (Figure 1). Approximately 5 minutes to dephosphorize until the phosphorus concentration in the hot metal reaches the same level (approximately 1 okg/l-bath iron as dephosphorizing agent)
You can save some money.
本発明方法により多くの実験を行ブエつた結果、スラグ
の真空吸引を容易にするには、吹込みランス位置を容器
の鉛直軸心より壁側に偏心さぜ、ランスと対向する壁近
(にスラグ真空吸引のヘッド部を設置すれば効果が犬で
ある。ランスから吹込まれる気体と脱燐剤とにより、溶
銑浴の揺動は激しく、その程度はランスの近傍はど犬で
ある。ランスより離れた位置ではスラグ面位置の変動が
小さく、真空吸引のヘッド部位置を頻繁に変動させなく
てもスラグ吸引・除去が可能である。After conducting many experiments using the method of the present invention, we found that in order to facilitate the vacuum suction of slag, the position of the blowing lance should be eccentrically placed toward the wall from the vertical axis of the container, and the lance should be placed near the wall opposite to the lance. If a slag vacuum suction head is installed, the effect will be even greater.The gas blown in from the lance and the dephosphorizing agent will cause the hot metal bath to shake violently, and the extent of the shaking will be greater than that in the vicinity of the lance. At a more distant position, the fluctuation of the slag surface position is small, and the slag can be suctioned and removed without frequently changing the position of the vacuum suction head.
第5図は、ランスと真空吸引のヘッド部との位置関係を
例示′Jる平面図である。4はランス、7は真空吸上げ
式スラグ除去装置である。FIG. 5 is a plan view illustrating the positional relationship between the lance and the vacuum suction head. 4 is a lance, and 7 is a vacuum suction type slag removal device.
本発明により、従来、脱燐剤の使用量は50〜70kg
/を一浴銑であったが、同一条件において5〜10kg
/を一溶銑削減することが可能となった。さらに、脱燐
剤吹込み量が減少したことにより、脱燐剤吹込み時間(
処理時間)も短縮することができ、脱燐処理後に改めて
排滓する必要がないので、予備処理工程の大幅な時間短
縮が可能となり、省力・省エネルギー効果が犬である。According to the present invention, the amount of dephosphorizing agent used in the past is reduced from 50 to 70 kg.
/ was a single-bath pig iron, but under the same conditions 5 to 10 kg
/ has become possible to reduce the amount of hot metal. Furthermore, the dephosphorizing agent injection time (
Since there is no need to drain the slag again after the dephosphorization process, it is possible to significantly shorten the time required for the preliminary treatment process, resulting in significant labor and energy savings.
実施例
溶銑鍋を用いて本発明を実施した例を従来法と比較して
示す。本発明方法の実施に使用した装置は第3図の通り
であり、従来法は第1図の通りである。EXAMPLE An example of implementing the present invention using a hot metal ladle will be shown in comparison with a conventional method. The apparatus used to carry out the method of the present invention is shown in FIG. 3, and the conventional method is shown in FIG.
100 )ンの溶銑中に粉体吹込み装置べから200k
g/minの速度で脱燐剤を供給し、ランスを介して吹
き込んだ。同時に真空吸上げ式スラグ除去装置16“に
より浴面上スラグを連続的に除去した。−結果を第1表
に従来法(比較例)と比較して示す。100) Powder injection equipment into hot metal of 200k
The dephosphorizing agent was fed at a rate of g/min and blown through a lance. At the same time, the slag on the bath surface was continuously removed using a vacuum suction type slag removal device 16''.The results are shown in Table 1 in comparison with the conventional method (comparative example).
脱燐剤としては鉄鉱石60%、生石灰30%、はたる石
10%の混合粉を用い、キャリアガスとして酸素80%
窒素20%の混合ガスを用いた。As a dephosphorizing agent, a mixed powder of 60% iron ore, 30% quicklime, and 10% rock was used, and as a carrier gas, 80% oxygen was used.
A mixed gas containing 20% nitrogen was used.
脱燐剤原単位は従来法に比較1210〜15kg/l−
浴銑削減できた。Dephosphorizing agent consumption is 1210 to 15 kg/l compared to conventional method
We were able to reduce the amount of hot iron used.
第】図は従来法の溶銑脱燐方法を示す縦断面図、第2図
は従来法において処理途中まで脱燐剤を吹込み、その後
気体のみ吹込んだ実験の溶銑中燐濃度の経時変化を示づ
一グラフ、第3図は本発明法の実施例を示す縦断面図、
叱4図は脱燐処理中の溶銑中燐濃度の変化°を示すグラ
フ、第5図は本発明の実施態様を示す平面図である。
■・・・高酸素ポテンシャル領域、2・・・低酸素ポテ
ンシャル領域、3パ°溶銑、4・・・吹込ランス、5・
・・粉体吹込装飽、6・・・集塵フート、7・・・真空
吸上げ式スラグ除去装置
第1図
第2図
処チ里詩間(分)
第3図
第4図
処工T時間(今)
第5図Fig. 2 is a vertical cross-sectional view showing a conventional hot metal dephosphorization method, and Fig. 2 shows the change over time in the phosphorus concentration in hot metal in an experiment in which a dephosphorizing agent was injected halfway through the process in the conventional method, and then only gas was injected. Figure 3 is a vertical cross-sectional view showing an embodiment of the method of the present invention;
Figure 4 is a graph showing changes in phosphorus concentration in hot metal during dephosphorization treatment, and Figure 5 is a plan view showing an embodiment of the present invention. ■...High oxygen potential region, 2...Low oxygen potential region, 3. Hot metal, 4. Blowing lance, 5.
...Powder injection, 6. Dust collection foot, 7. Vacuum suction type slag removal device. Time (now) Figure 5
Claims (1)
みによって行なうに当り、浴面上に形成される脱燐反応
後の溶融スラグな該脱燐剤の吹込みと同時期に連続的に
除去することにより脱燐効率を高めることを特徴とする
溶銑の脱燐処理方法。 2 脱燐剤の吹込みを溶銑保持容器の鉛直軸心より偏心
した位置で行ない、対向する偏心位置でスラグを特徴す
る特許請求の範囲第1項記載の溶銑の脱燐処理方法。[Scope of Claims] 1. When dephosphorizing hot metal by blowing a dephosphorizing agent under the surface of the hot iron bath, the molten slag formed on the bath surface after the dephosphorization reaction is A hot metal dephosphorization treatment method characterized by increasing dephosphorization efficiency by continuously removing the agent at the same time as blowing the agent. 2. The method for dephosphorizing hot metal according to claim 1, wherein the dephosphorizing agent is injected at a position eccentric from the vertical axis of the hot metal holding container, and the slag is formed at an opposing eccentric position.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13424282A JPS5925911A (en) | 1982-07-31 | 1982-07-31 | Dephosphorization treatment of molten iron |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13424282A JPS5925911A (en) | 1982-07-31 | 1982-07-31 | Dephosphorization treatment of molten iron |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5925911A true JPS5925911A (en) | 1984-02-10 |
Family
ID=15123723
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13424282A Pending JPS5925911A (en) | 1982-07-31 | 1982-07-31 | Dephosphorization treatment of molten iron |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5925911A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995029137A1 (en) * | 1993-02-10 | 1995-11-02 | Sherwood William L | Metallurgical furnace vacuum slag removal |
-
1982
- 1982-07-31 JP JP13424282A patent/JPS5925911A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995029137A1 (en) * | 1993-02-10 | 1995-11-02 | Sherwood William L | Metallurgical furnace vacuum slag removal |
AU706193B2 (en) * | 1994-04-25 | 1999-06-10 | William Lyon Sherwood | Metallurgical furnace vacuum slag removal |
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