JPH06108136A - Production of low p and low s foundry pig iron - Google Patents

Production of low p and low s foundry pig iron

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Publication number
JPH06108136A
JPH06108136A JP26013492A JP26013492A JPH06108136A JP H06108136 A JPH06108136 A JP H06108136A JP 26013492 A JP26013492 A JP 26013492A JP 26013492 A JP26013492 A JP 26013492A JP H06108136 A JPH06108136 A JP H06108136A
Authority
JP
Japan
Prior art keywords
amount
removal
low
content
pig 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.)
Withdrawn
Application number
JP26013492A
Other languages
Japanese (ja)
Inventor
Junichiro Katsuta
順一郎 勝田
Takashi Fujita
藤田  貴
Masaru Endo
勝 遠藤
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP26013492A priority Critical patent/JPH06108136A/en
Publication of JPH06108136A publication Critical patent/JPH06108136A/en
Withdrawn legal-status Critical Current

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

Abstract

PURPOSE:To efficiently produce a low P and low S foundry pig iron having the aimed component composition by adjusting dephosphorizing agent, after-blowing scale and top-blowing oxygen quantities in dephosphorizing process after desiliconizing. CONSTITUTION:In the dephosphorizing process executing after desiliconizing treatment and removal of the desiliconized slag, the CaO-base dephosphorizing agent is used. Together with this, according to the aimed C and S contents in the foundry pig iron, the dephosphorizing agent, after-blowing scale and top-blowing oxygen quantities are adjusted so as to satisfy the equations I and II. At the time of the execution, according to the components in the molten pig iron after the removal of desiliconized slag, by introducing each supplying quantity of the preset dephosphorizing agent, after-blowing scale and top-blowing oxygen into the equation I, the decarbonizing content is calculated and deducted from the C content in the molten pig iron. This result is compared with the aimed C content in the foundry pig iron. In the case of being the excess or the shortage to the decarbonizing content, one or more kinds of each supplying quantity among the dephosphorizing agent, after-blowing scale and top-blowing oxygen are adjusted to secure the aimed C content. In the same way, S content after dephosphorization is calculated from the equation II and each supplying quantity is adjusted.

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、C量およびS量の調整
された低P・低S鋳物銑を経済的且つ効率よく製造する
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 economically and efficiently producing low P / low S cast pig iron having a controlled C and S content.

【0002】[0002]

【従来の技術】低P・低S鋳物銑は、従来より溶銑予備
処理工程で脱Si、脱P、脱Sの3工程を順次実施する
ことによって製造している。即ち高炉から出湯された溶
銑をまず最初に脱Si処理した後、高濃度のSiO2
含むスラグを排出し、次いで溶銑中のPが成分規格内に
収まる様に脱P処理を行ない、最後の予備処理工程で脱
S処理することによって低P・低S鋳物銑を得ている。
2. Description of the Related Art A low P / low S cast pig iron has been conventionally manufactured by sequentially performing three steps of Si removal, P removal and S removal in a hot metal pretreatment step. That is, the hot metal discharged from the blast furnace is first subjected to a de-Si treatment, then the slag containing a high concentration of SiO 2 is discharged, and then the P removal treatment is carried out so that the P in the hot metal falls within the component specifications. A low-P / low-S cast iron pig is obtained by removing S from the pretreatment process.

【0003】ところがこれらの方法では、各処理工程に
おける溶銑中のC量[C]には全く考慮が払われておら
ず、該鋳物銑の[C]はバッチ毎にかなりの変動が見ら
れるにもかかわらず、得られる低P・S硫鋳物銑の
[C]は出来上がり次第というのが実情であって、きめ
細かな[C]の調整は行なわれていない。
However, in these methods, no consideration is given to the amount of C [C] in the hot metal in each processing step, and the [C] of the cast iron shows a considerable variation from batch to batch. Nevertheless, the actual condition is that the [C] of the obtained low P / S cast iron pig is as soon as it is completed, and no fine adjustment of [C] has been made.

【0004】即ち脱Si後に行なわれる脱P工程では、
脱P促進のため大量の酸素(もしくは空気)が上吹きさ
れると共に、最終段階で温度調整および最終P量の調整
のためスケールが溶銑中に供給されるため、この工程で
[C]を微調整することは難しい。一方、鋳物銑中のS
量[S]についても上記脱P工程で同時に[S]を規格
内に調整するといったことは困難であるところから、そ
の後の脱S工程で[S]を調整する方法が採用されてい
る。そして脱S工程では、低窒素化を達成することの必
要上脱S剤としてソーダ灰等が添加されると共に、脱S
スラグの除去も必要になるので、トータルの処理工程が
長くなって生産効率が低下するばかりでなく、溶銑の温
度降下も大きくなって鋳造歩留りにまで悪影響が現れて
くる。
That is, in the dephosphorization process performed after desiliconization,
A large amount of oxygen (or air) is blown up to accelerate de-P, and scale is supplied into the hot metal for temperature adjustment and final P amount adjustment at the final stage, so [C] is slightly added in this step. It's difficult to adjust. On the other hand, S in cast pig iron
With respect to the amount [S], it is difficult to simultaneously adjust [S] within the standard in the above-mentioned P removal step, so a method of adjusting [S] in the subsequent S removal step is adopted. In the S-removing step, soda ash or the like is added as a S-removing agent in order to achieve low nitrogen content, and
Since it is necessary to remove slag, not only the total treatment process becomes long and the production efficiency is lowered, but also the temperature drop of the hot metal becomes large and the casting yield is adversely affected.

【0005】[0005]

【発明が解決しようとする課題】本発明は上記の様な事
情に着目してなされたものであって、その目的は、低P
・低S鋳物銑を製造するに際し、脱Si後の脱P工程で
溶銑中の[C]および[S]の成分調整も同時に行なえ
る様にし、それにより目標とする成分組成の低P・低S
鋳物銑を効率良く製造することのできる方法を確立しよ
うとするものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and its purpose is to achieve low P
-When manufacturing low S cast iron, it is possible to adjust the components of [C] and [S] in the hot metal at the same time in the P removal step after Si removal. S
It is intended to establish a method capable of efficiently producing cast pig iron.

【0006】[0006]

【課題を解決するための手段】上記課題を解決すること
のできた本発明の構成は、低P・低S鋳物銑を製造する
に当たり、脱Si処理および脱Siスラグ除去後に行な
われる脱P工程で、CaO系脱P剤を使用すると共に、
鋳物銑の目標C量および目標S量に応じて、下記[I]
式および[II]式を満足する様に脱P剤量、後吹きスケ
ール量および上吹き酸素量を調整するところに要旨を有
するものである。
The structure of the present invention which has been able to solve the above-mentioned problems is a de-P process performed after removing Si and removing Si slag when producing low P / low S cast iron. , Using CaO-based de-P agent,
Depending on the target C amount and target S amount of the cast pig iron, the following [I]
The gist is to adjust the amount of P-removing agent, the amount of post-blown scale, and the amount of top-blown oxygen so as to satisfy the formula and the formula [II].

【0007】 脱C量(%)=0.42×脱P剤量(kg/トン)+1.1 ×後吹きスケール量 (kg/トン)+6.7 ×上吹き酸素量(Nm3/トン)+4.9/100 …[I] 脱P後のS量(%)=0.41×脱P前S量(%)×103-0.19×脱P剤量 (kg/トン)+0.59×上吹き酸素量(Nm3/トン)+10.8/1000 …[II]C removal amount (%) = 0.42 x P removal agent amount (kg / ton) +1.1 x post-blown scale amount (kg / ton) +6.7 x top-blown oxygen amount (Nm 3 / ton) + 4.9 / 100 … [I] S amount after dephosphorization (%) = 0.41 × amount of S before deoxidation (%) × 10 3 -0.19 × amount of dephosphorization agent (kg / ton) + 0.59 × amount of top-blown oxygen (Nm 3 / (Ton) + 10.8 / 1000… [II]

【0008】[0008]

【作用】本発明では、高炉から出湯された溶銑を取鍋や
混銑車等に受銑し、脱Si、脱Siスラグの除滓、脱P
の順で溶銑予備処理を行なう。即ち脱Si工程では、脱
Si剤としてたとえば固体酸素(Fe23 等)などを
インジェクション方式等により吹込むが、この工程では
脱Siと同時に脱Mnも進行するため、低Si化,低M
n化が達成される。
In the present invention, the hot metal discharged from the blast furnace is received by a ladle or a mixed pig car to remove Si, remove slag from Si, and remove P.
Perform hot metal pretreatment in this order. That is, in the Si removal step, for example, solid oxygen (Fe 2 O 3 etc.) or the like is blown as a Si removal agent by an injection method or the like, but in this step, Si removal and Mn progress simultaneously, so that Si reduction and M reduction are achieved.
n-ization is achieved.

【0009】そしてその後に行なわれる脱Pを効率良く
進めるため、SiO2 濃度の高い脱Siスラグをドラッ
カー等によって系外に排出する。従来例では、その後脱
Pおよび脱S工程を順次実施することにより低P・低S
の鋳物銑を得ているが、この方法では、前述の如く生産
効率や溶銑の温度保障の問題に加えて出来上りC量が不
安定になるという問題がある。
Then, in order to efficiently proceed with the de-Ping performed thereafter, the de-Si slag having a high SiO 2 concentration is discharged to the outside of the system by a drucker or the like. In the conventional example, low P and low S are achieved by sequentially performing the P removal and S removal steps thereafter.
However, this method has a problem that the finished C content becomes unstable in addition to the problems of production efficiency and guarantee of the temperature of the hot metal as described above.

【0010】そこで本発明では、こうした問題点を一挙
に解消するための手段として、脱Siスラグ除去後に行
なわれる脱P工程で、同時に脱Sを行なうと共にC量の
調整を可能とし、P量,S量およびC量の調整された低
P・低S鋳物銑を生産良く製造することのできる方法を
確立するものである。
Therefore, in the present invention, as a means for solving all of these problems at once, it is possible to perform S removal at the same time and adjust the C content in the P removal step performed after the removal of the Si slag, and the P content, It is intended to establish a method capable of producing a low-P / low-S cast iron pig whose S content and C content are adjusted with good productivity.

【0011】即ち本発明では、まず脱P剤として脱Si
作用を兼備したCaO系の脱P剤を使用し、鋳物銑の目
標C量および目標S量に応じて、前記[I]式および
[II]式を満足する様に脱P剤量、後吹きスケール量お
よび上吹き酸素量を調整する。即ちCaO系の脱P剤を
用いて脱Pを行なう際における脱C量および脱S量は、
脱P剤量(kg/トン) と後吹きスケール量(kg/トン) およ
び上吹き酸素量(Nm3/ トン) と密接な関係を有してお
り、脱P処理時におけるそれら各量をコントロールして
やれば、得られる鋳物銑のC量およびS量をうまく調整
し得ることが判明した。
That is, in the present invention, first, Si removal is performed as a P removal agent.
Using a CaO-based de-P agent that also functions, depending on the target C amount and target S amount of the cast pig iron, the amount of the de-P agent and the post-blowing are performed so as to satisfy the above formulas [I] and [II]. Adjust the scale and top-blown oxygen. That is, the amount of de-C and the amount of de-S when performing de-P using a CaO-based de-P agent are
It has a close relationship with the amount of de-P agent (kg / ton), the amount of post-blown scale (kg / ton) and the amount of top-blown oxygen (Nm 3 / ton), and controls each of these amounts during de-P treatment. By doing so, it was found that the C content and S content of the obtained cast pig iron could be adjusted well.

【0012】したがって本発明を実施するに当たって
は、脱Siスラグ除去後の溶銑成分に応じて予め設定さ
れた脱P剤、後吹きスケールおよび上吹き酸素の各供給
量を前記[I]式に導入して脱C量を計算して当該溶銑
のC量から差し引きし、その結果を鋳物銑の目標C量と
比較する。そして結果、脱C量に過・不足がある場合
は、その過・不足分に応じて脱P剤、後吹きスケール、
上吹き酸素の各供給量のうち1種以上を増・減調整する
ことによって目標C量を確保する。
Therefore, in carrying out the present invention, the respective supply amounts of the P-removing agent, the post-blown scale and the top-blown oxygen which are set in advance in accordance with the hot metal component after the removal of the Si slag are introduced into the above formula [I]. Then, the C removal amount is calculated and subtracted from the C content of the hot metal, and the result is compared with the target C content of the cast iron. As a result, when there is an excess or deficiency in the C removal amount, the P removal agent, the post-blown scale,
The target C amount is secured by increasing / decreasing one or more of each supply amount of top-blown oxygen.

【0013】但し上記各供給量は、脱C量だけでなく脱
P後のS含量にも影響を及ぼすので、同様に予め設定さ
れた脱P剤、後吹きスケールおよび上吹き酸素の各供給
量を前記[II]式に導入して脱P後のS含量を算出し、
脱S量の過・不足に応じて、上記[I]式による脱C量
の補正値とリンクさせながら上記各供給量のうち1種以
上を増減調整する。
However, since each of the above-mentioned supply amounts affects not only the C-depletion amount but also the S-content after the P-depletion, similarly, the preset supply amounts of the P-depleting agent, the post-blown scale and the top-blown oxygen are similarly set. Is introduced into the above formula [II] to calculate the S content after P removal,
Depending on the excess / deficiency of the S removal amount, one or more of the above supply amounts are increased / decreased while being linked to the correction value of the C removal amount according to the above formula [I].

【0014】これらの計算は、脱Siスラグ除去後の溶
銑の成分組成が明らかにされた後は、その分析値を基に
してコンピューター等により速やかに行なわれるので、
脱P後のC量およびS量は目標値に応じて迅速且つほぼ
正確に調整されることになる。
After the composition of the hot metal after the removal of the de-Si slag has been clarified, these calculations are carried out promptly by a computer or the like based on the analyzed values,
The C amount and S amount after P removal will be adjusted quickly and almost accurately according to the target value.

【0015】かくして1回の脱P処理を行なうだけでC
量やS量も同時に調整することができ、生産効率が高め
られると共に、予備処理工程での溶銑温度の低下も最小
限に抑えることができ、更には安定した成分組成の低P
・低S鋳物銑を得ることが可能となる。
Thus, it is possible to obtain C by performing only one P removal process.
Content and S content can be adjusted at the same time, production efficiency can be improved, and the decrease in hot metal temperature in the pretreatment process can be suppressed to a minimum.
-It becomes possible to obtain low S cast iron.

【0016】以下、本発明の実施例を示すが、本発明は
もとより下記実施例によって制限を受けるものではな
く、前後の趣旨に適合し得る範囲で適当に変更を加えて
実施することはいずれも本発明の技術的範囲に含まれ
る。
Examples of the present invention will be shown below, but the present invention is not limited by the following examples, and any modifications may be made within a range that is compatible with the purpose of the invention. It is included in the technical scope of the present invention.

【0017】[0017]

【実施例】脱Siおよび脱Siスラグ除去後の化学成分
が表1に示す通りである2種の溶銑,を使用して、
表2に示す目標成分組成の鋳物銑を得ることを目的と
し、それらの値を前記[I]式および[II]式に当ては
めて脱P工程で使用するCaO系脱P剤、後吹きスケー
ル、上吹き酸素の各供給量を算出し、表3に示す各供給
量を定めて脱P処理を行なった。得られた鋳物銑,
の成分組成は表4に示す通りであり、S量,P量,Si
量はもとよりC量においても目標成分組成を満たす鋳物
銑が得られている。
EXAMPLE Using two kinds of hot metal having chemical compositions after removing Si and removing Si slag as shown in Table 1,
Aiming at obtaining cast pig iron having the target component composition shown in Table 2, the values are applied to the above formulas [I] and [II] to be used in the depurification step, and the CaO-based depurifying agent, the post-blown scale, Each supply amount of top-blown oxygen was calculated, each supply amount shown in Table 3 was determined, and P removal processing was performed. The obtained cast iron,
The composition of the components is as shown in Table 4, and S content, P content, Si
Cast iron that satisfies the target composition is obtained not only in the amount of C but also in the amount of C.

【0018】[0018]

【表1】 [Table 1]

【0019】[0019]

【表2】 [Table 2]

【0020】[0020]

【表3】 [Table 3]

【0021】[0021]

【表4】 [Table 4]

【0022】[0022]

【発明の効果】本発明は以上の様に構成されており、脱
Si後の脱P工程で同時に脱C量および脱S量を調整す
ることができ、鋳物銑を製造するための予備処理が著し
く簡略化されると共に生産性が高められ、且つ予備処理
時の放熱も抑えられて鋳造歩留りも向上し、更にはC量
も目標通りにコントロールすることができるので鋳物銑
としての品質も安定化するなど、実用に即した様々の利
益を得ることができる。
EFFECTS OF THE INVENTION The present invention is configured as described above, and it is possible to adjust the C removal amount and the S removal amount at the same time in the P removal step after Si removal, and the pretreatment for producing cast pig iron is It is remarkably simplified, the productivity is improved, the heat release during the pretreatment is suppressed, the casting yield is improved, and the C content can be controlled as desired, so that the quality of the cast pig iron is stabilized. It is possible to obtain various benefits according to practical use.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 低P・低S鋳物銑を製造するに当たり、
脱Si処理および脱Siスラグ除去後に行なわれる脱P
工程で、CaO系脱P剤を使用すると共に、鋳物銑の目
標C量および目標S量に応じて、下記[I]式および
[II]式を満足する様に脱P剤量、後吹きスケール量お
よび上吹き酸素量を調整することを特徴とする低P・低
S鋳物銑の製法。 脱C量(%)=0.42×脱P剤量(kg/トン)+1.1 ×後吹きスケール量 (kg/トン)+6.7 ×上吹き酸素量(Nm3/トン)+4.9/100 …[I] 脱P後のS量(%)=0.41×脱P前S量(%)×103-0.19×脱P剤量 (kg/トン)+0.59×上吹き酸素量(Nm3/トン)+10.8/1000 …[II]
1. When manufacturing low P / low S cast pig iron,
De-P treatment performed after de-Si treatment and de-Si slag removal
In the process, a CaO-based de-P agent is used, and according to the target C amount and target S amount of the cast pig iron, the de-P agent amount and the post-blown scale are satisfied so as to satisfy the following formulas [I] and [II]. A method for producing a low-P / low-S casting pig iron characterized by adjusting the amount and the amount of top-blown oxygen. C removal rate (%) = 0.42 x P removal agent amount (kg / ton) +1.1 x post-blown scale amount (kg / ton) +6.7 x top-blown oxygen amount (Nm 3 / ton) + 4.9 / 100… [I ] S amount after P removal (%) = 0.41 x S amount before P removal (%) x 10 3 -0.19 x P removal agent amount (kg / ton) + 0.59 x Top blown oxygen amount (Nm 3 / ton) + 10.8 / 1000… [II]
JP26013492A 1992-09-29 1992-09-29 Production of low p and low s foundry pig iron Withdrawn JPH06108136A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26013492A JPH06108136A (en) 1992-09-29 1992-09-29 Production of low p and low s foundry pig iron

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26013492A JPH06108136A (en) 1992-09-29 1992-09-29 Production of low p and low s foundry pig iron

Publications (1)

Publication Number Publication Date
JPH06108136A true JPH06108136A (en) 1994-04-19

Family

ID=17343781

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26013492A Withdrawn JPH06108136A (en) 1992-09-29 1992-09-29 Production of low p and low s foundry pig iron

Country Status (1)

Country Link
JP (1) JPH06108136A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012017504A (en) * 2010-07-08 2012-01-26 Sumitomo Metal Ind Ltd Method for suppressing heat dissipation of molten iron
JP2018035404A (en) * 2016-09-01 2018-03-08 株式会社木下製作所 Method of refining cast iron

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012017504A (en) * 2010-07-08 2012-01-26 Sumitomo Metal Ind Ltd Method for suppressing heat dissipation of molten iron
JP2018035404A (en) * 2016-09-01 2018-03-08 株式会社木下製作所 Method of refining cast iron

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