JP2001271113A - Converter-refining method for by-producing steel manufacturing slag having low free lime content - Google Patents

Converter-refining method for by-producing steel manufacturing slag having low free lime content

Info

Publication number
JP2001271113A
JP2001271113A JP2000085956A JP2000085956A JP2001271113A JP 2001271113 A JP2001271113 A JP 2001271113A JP 2000085956 A JP2000085956 A JP 2000085956A JP 2000085956 A JP2000085956 A JP 2000085956A JP 2001271113 A JP2001271113 A JP 2001271113A
Authority
JP
Japan
Prior art keywords
slag
converter
treatment
furnace
free lime
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Withdrawn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
JP2000085956A
Other languages
Japanese (ja)
Inventor
Hideaki Kimura
秀明 木村
Noriyuki Masumitsu
法行 升光
Masayuki Arai
雅之 荒井
Hiroaki Hayashi
浩明 林
Masahito Kobayashi
雅人 小林
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 Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP2000085956A priority Critical patent/JP2001271113A/en
Publication of JP2001271113A publication Critical patent/JP2001271113A/en
Withdrawn legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide an effective slag upgrading method in which the lowering of F-CaO as the main cause of expansion-collapsibility is extremely, quickly and efficiently be performed and the conventional aging treatment can be omitted or saved when the by-produced steel manufacturing slag is reused. SOLUTION: In a converter-refining method performing desiliconization and dephosphorization as a pre-treatment of molten iron by utilizing the converter, the following molten iron is charged in the state of leaving the slag after completing the dephosphorized treatment in the furnace without removing the slag after tapping the steel. Then, oxygen is supplied and the desiliconizing treatment is performed, and after desiliconizing, the oxygen-blowing is once interrupted and an intermediate slag-removing process for discharging the slag is performed, and the dephosphorizing refining is successively performed to by-produce the steel manufacturing slag having low free lime content.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、スラグの塩基度
(%CaO/%SiO2)が高く、遊離石灰(以下「F
−CaO」という。)を多く含む製鋼スラグの改質方法
に関するものである。
The present invention relates to a slag having a high basicity (% CaO /% SiO 2 ) and free lime (hereinafter referred to as “F”).
-CaO ". The present invention relates to a method for reforming steelmaking slag containing a large amount of slag.

【0002】[0002]

【従来の技術】鉄鋼スラグは、高炉スラグと製鋼スラグ
に大別され、このうち製鋼スラグは、銑鉄を転炉で精錬
する前に一部の不要な成分を除去する溶銑予備処理スラ
グ、銑鉄を転炉で精錬する際に発生する転炉スラグ、連
鋳鋳造終了後の取鍋スラグが主なものである。製鋼スラ
グは昭和50年代から本格的な利用技術開発および普及
促進活動が進められ、最近の主な用途は土木用と道路用
である。しかしながら、製鋼スラグは塩基度が高く、F
−CaOを多く含有しており、膨張崩壊性を有している
ことから、再利用に当っては膨張崩壊性の解決が必須で
あり、現在ではエージング処理(破砕後、空気および水
と反応させること)によって実用上問題の無いところま
で膨張を抑制する技術により対応がなされている。ま
た、蒸気を利用してさらにスラグの膨張率を低減するエ
ージング方法も開発されている。これら従来技術の他に
例えば特開平11−71160号公報に示される「海中
沈設用石材及びその製造方法」では鉄鋼スラグを素材と
して炭酸化反応にて生成させたCaCO3をバインダー
として固結させ、塊状化する等のスラグの改質化による
石材製造方法が開示されている。
2. Description of the Related Art Steel slag is roughly divided into blast furnace slag and steelmaking slag. Among these, steelmaking slag is pre-processed hot metal slag which removes some unnecessary components before refining pig iron in a converter, and pig iron. The main components are converter slag generated during refining in a converter and ladle slag after continuous casting. Steelmaking slag has been used in full-fledged technology development and spread promotion activities since the 1975's, and its recent main uses are for civil engineering and roads. However, steelmaking slag has a high basicity, and F
-Because it contains a large amount of CaO and has expansive disintegration properties, it is essential to solve the expansive disintegration properties for reuse. At present, aging treatment (reaction with air and water after crushing) That is, a technique for suppressing expansion to a point where there is no problem in practical use has been taken. An aging method that further reduces the expansion coefficient of slag using steam has been developed. In addition to these conventional techniques, for example, in Japanese Patent Application Laid-Open No. H11-71160, `` Stones for submersion in the sea and a method for producing the same '', CaCO 3 generated by a carbonation reaction using steel slag as a material is solidified as a binder, A method for producing a stone material by modifying a slag such as agglomeration is disclosed.

【0003】[0003]

【発明が解決しようとする課題】以上のように製鋼スラ
グは副生品として再利用するに際し、膨張崩壊性の解決
が必要であり、その対策としてはスラグに含まれるF−
CaOの低減が有効である。しかしながら、現状の大気
エージング方法は、気温変動、散水時の浸透ムラ等のた
めにヤード内スラグの改質レベルが不均質となりやす
く、さらにエージング処理時間が長い、広大なヤードが
必要等の問題点がある。また、蒸気エージング方法は、
蒸気設備費、ランニングコスト、処理能力の観点からも
課題は多く、さらに前述の特許公報にもF−CaOの低
減方法についての記載は見られず、これらに代る新たな
スラグ改質技術の開発が望まれている。
As described above, when steelmaking slag is reused as a by-product, it is necessary to solve the expansive collapse property.
Reduction of CaO is effective. However, the current air aging method has problems that the reforming level of the slag in the yard tends to be non-uniform due to temperature fluctuations, uneven permeation at the time of watering, etc., furthermore, the aging processing time is long, and a large yard is required. There is. Also, the steam aging method,
There are many issues from the viewpoints of steam equipment cost, running cost, and processing capacity, and further, there is no description in the above-mentioned patent gazette of a method for reducing F-CaO, and development of a new slag reforming technology to replace them Is desired.

【0004】[0004]

【課題を解決するための手段】本発明は、以上の事情を
背景としてなされたもので、膨張崩壊性の主要因となる
F−CaOの低減を極めて迅速に効率良く行い、従来の
エージング処理の緩和または省略を可能とする効果的な
スラグ改質方法の提供を目的とする。本発明の要旨とす
るところは以下のとおりである。 (1)転炉を利用して溶銑予備処理として脱Siおよび
脱Pを行う転炉精錬法において、脱P処理終了後のスラ
グを出湯後排滓せず炉内に残留させたまま次ヒートの溶
銑を装入し、酸素を供給して脱Si処理を行ない、脱S
i後一旦吹錬を中断してスラグを排出する中間排滓工程
をもうけ、その後引続き脱P精錬を行うことを特徴とす
る遊離石灰含有量の低い製鋼スラグを副生する転炉精錬
法。 (2)脱P処理後スラグを炉内に残留させると共に他工
程で生成した遊離石灰を含有するスラグを脱Si処理前
に炉内に装入する前項(1)記載の転炉精錬法。 (3)転炉を利用して溶銑予備処理として脱Siおよび
脱Pを行う転炉精錬法において、吹錬に先立ち自工程ま
たは他工程で発生回収した遊離石灰を含有するスラグを
炉内に装入し、酸素を供給して脱Si処理を行ない、脱
Si後一旦吹錬を中断して改質スラグを排出する中間排
滓工程をもうけ、その後引続き脱P精錬を行うことを特
徴とする遊離石灰含有量の低い製鋼スラグを副生する転
炉精錬法。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above circumstances, and is capable of extremely quickly and efficiently reducing F-CaO, which is a main cause of expansion and collapse, to achieve a conventional aging treatment. An object of the present invention is to provide an effective slag reforming method that can be moderated or omitted. The gist of the present invention is as follows. (1) In a converter refining method for removing Si and P as molten iron pretreatment using a converter, the slag after the completion of the removal of P is left in the furnace without discharging after discharge from the hot water. Hot metal is charged, oxygen is supplied, and de-Si treatment is performed.
(b) A converter refining method for producing by-produced steel slag having a low free lime content, which comprises interrupting the blowing and temporarily discharging an intermediate slag after discharging the slag, and subsequently performing de-P refining. (2) The converter refining method according to the above (1), wherein the slag remaining in the furnace after the de-P treatment and the slag containing free lime generated in another step are charged into the furnace before the de-Si treatment. (3) In a converter refining method that uses a converter to remove Si and P as molten iron pretreatment, slag containing free lime generated and recovered in its own process or another process prior to blowing is loaded into the furnace. Injection and supply of oxygen to perform a de-Si treatment, and after the de-Si, a blowing process is temporarily interrupted to provide an intermediate waste discharging step of discharging the reformed slag, and then the de-P refining is continuously performed. Converter refining method that produces steelmaking slag with low lime content.

【0005】[0005]

【発明の実施の形態】転炉精錬工程では副原料として多
量の石灰を使用し生成するスラグの塩基度は通常脱P精
錬で1.1〜4.0、脱C精錬で2.0〜4.0程度で
あり、このような高塩基度スラグを効率良く滓化させる
ためにホタル石等が利用されている。しかしホタル石を
使用しても石灰の完全な滓化は困難であり、未滓化の石
灰は回収したスラグ中において遊離石灰となる。また、
滓化したスラグにおいても、特に塩基度が高い場合には
初晶として遊離石灰が晶出する。そのため、副生したス
ラグ中には通常遊離石灰(F−CaO)を1〜4%程度
含有している。遊離石灰を含有するスラグは、大気と反
応して体積が膨張するため、このままでは土木材料とし
て使用することができない。従って、このようなスラグ
を系外にて土木用、道路用として再利用する場合、普通
エージング処理が行われている。
BEST MODE FOR CARRYING OUT THE INVENTION In a converter refining process, a large amount of lime is used as an auxiliary material, and the slag generated usually has a basicity of 1.1 to 4.0 for de-P refining and 2.0 to 4 for de-C refining. It is about 0.0, and fluorite or the like is used to efficiently turn such high basicity slag into slag. However, even if fluorite is used, it is difficult to completely form lime, and lime that has not been lime becomes free lime in the recovered slag. Also,
Even in slag slag, particularly when the basicity is high, free lime crystallizes as primary crystals. Therefore, the by-product slag usually contains about 1 to 4% of free lime (F-CaO). Slag containing free lime reacts with the atmosphere and expands in volume, and thus cannot be used as a civil engineering material as it is. Therefore, when such slag is reused outside the system for civil engineering and road use, aging processing is usually performed.

【0006】本発明者らは、転炉を利用して脱Siおよ
び脱Pを行う溶銑予備処理プロセスにおいて、生成する
スラグのF−CaOを低減をはかるべく研究開発に当っ
た。本発明者らは実機規模の300TON転炉を用い、
約290TONの溶銑を装入するプロセスにおいて検討
を行った。
The present inventors conducted research and development to reduce the amount of F-CaO in slag generated in a hot metal pretreatment process for removing Si and P using a converter. The present inventors used a 300 TON converter on a full scale,
A study was conducted in the process of charging about 290 TON of hot metal.

【0007】従来法においては図3に示すように、転炉
に溶銑を装入後生石灰および鉄鉱石を添加し上吹酸素を
供給して脱Siおよび脱P処理を行い、処理終了後炉内
溶湯を取鍋に出湯し、出湯後脱P処理後スラグをスラグ
パンに排出する。このスラグの塩基度は平均1.8、F
−CaOは平均2.2%であった。このスラグはこのま
までは膨張崩壊性を有するため土木材料として使用する
ことはできない。
In the conventional method, as shown in FIG. 3, after the molten iron is charged into the converter, quick lime and iron ore are added, and oxygen is supplied to the converter to remove oxygen and remove Si. After the molten metal is poured into a ladle, the slag is discharged to a slag pan after de-P treatment after the molten metal is poured. The basicity of this slag is 1.8 on average, F
-CaO averaged 2.2%. This slag cannot be used as a civil engineering material because it has expandability and collapse properties as it is.

【0008】本発明者らは、脱Si処理後に中間排滓を
行ってその後脱P処理を行い、処理終了後炉内溶湯を取
鍋に出湯し、出湯後炉内に脱P処理後スラグを残留させ
た。このスラグの組成は上記従来法と同様、塩基度は平
均1.8、F−CaOは平均2.2%であった。該スラ
グの滓化をさらに向上させ、F−CaOを低減するため
に、該スラグを炉内に残留させたまま次ヒートの溶銑を
装入し、酸素を供給することで溶銑の脱Si処理を行
い、生成するSiO2にてスラグ塩基度を低減し、残留
スラグ中のF−CaOを滓化させることを試みた。転炉
装入時の該溶銑の平均成分は[C]=4.6%,[S
i]=0.45%,[Mn]=0.23%,[P]=
0.095%、[S]=0.020%である。この結
果、該次ヒートの脱Si処理終了時において、スラグ中
のF−CaOは平均0.19%まで低下することを知見
した。該スラグは前ヒートの脱Pスラグとの混合物であ
るためP25を多量に含んでおり、このままでは該次ヒ
ートの脱P処理を行うことはできない。そのため、脱S
i処理後一旦吹錬を中断し炉傾動による中間排滓を実施
し系外に排出する。系外に排出したスラグは、F−Ca
Oが低いので膨張崩壊性を示さず、このまま土木材料と
して使用することができる。
[0008] The inventors of the present invention perform an intermediate waste after the de-Si treatment, perform a de-P treatment after that, discharge the molten metal in the furnace to the ladle after the treatment is completed, and after the tapping, remove the slag after the de-P treatment in the furnace. Remained. The composition of this slag had an average basicity of 1.8 and F-CaO an average of 2.2%, as in the conventional method. In order to further improve the slagification of the slag and reduce the amount of F-CaO, the hot metal of the next heat is charged while the slag remains in the furnace, and oxygen is supplied to remove the Si from the hot metal. An attempt was made to reduce the basicity of the slag with the generated SiO 2 and to slag F-CaO in the residual slag. The average composition of the hot metal at the time of charging the converter was [C] = 4.6%, [S]
i] = 0.45%, [Mn] = 0.23%, [P] =
0.095%, [S] = 0.020%. As a result, it was found that at the end of the de-Si treatment of the next heat, F-CaO in the slag was reduced to an average of 0.19%. Since the slag is a mixture with the de-P slag from the previous heat, it contains a large amount of P 2 O 5 , and the de-P treatment of the next heat cannot be performed as it is. Therefore, S
After the i-treatment, the blowing is temporarily interrupted, the intermediate waste is discharged by tilting the furnace, and discharged out of the system. The slag discharged out of the system is F-Ca
Since O is low, it does not exhibit expansion collapse property and can be used as it is as a civil engineering material.

【0009】その後脱P用の副原料を転炉に再装入し、
引続き脱P精錬を実施し、以降前述の工程を繰返すこと
で改質スラグだけを系外排出し製造できる。
Then, the auxiliary material for removing P is recharged into the converter,
Subsequently, the de-P refining is performed, and thereafter, the above-described steps are repeated, whereby only the reformed slag can be discharged out of the system and manufactured.

【0010】図1に本発明における請求項1および2の
処理フローを、図2は本発明における請求項3の処理フ
ローを、図3は比較例として通常の転炉型溶銑予備脱S
i脱P処理フローを示す。
FIG. 1 shows the processing flow of claims 1 and 2 of the present invention, FIG. 2 shows the processing flow of claim 3 of the present invention, and FIG.
15 shows an i-P removal processing flow.

【0011】本発明は非常に有効なF−CaO低減法で
ある。従って、例えば脱C後スラグのように塩基度が高
くF−CaOを多量に含有する他工程で発生回収したス
ラグについても、脱Si吹錬に先立ち炉内に装入し、脱
Si吹錬を行うことにより、生成するSiO2にて滓化
を促進でき、F−CaOを容易に低減することが可能と
なる。
The present invention is a very effective method for reducing F-CaO. Therefore, for example, slag generated and recovered in another process containing a large amount of F-CaO, such as slag after de-C, is charged into the furnace prior to de-Si blowing, and de-Si blowing is performed. By doing so, slagification can be promoted by the generated SiO 2 , and F-CaO can be easily reduced.

【0012】本発明が転炉を利用して溶銑予備処理を行
う転炉製鋼法に限定した理由は、転炉を利用する脱Si
処理であれば攪拌力が十分に得られ、前ヒートの脱Pス
ラグと次ヒートの脱Siスラグとが十分に混合してスラ
グ改質効果が発揮されるからである。また、転炉を利用
した溶銑予備処理であればスラグ組成の制御も良好に行
うことができ、スラグ改質時の復Pも確実に抑制するこ
とができる。
The reason that the present invention is limited to the converter steelmaking method in which the hot metal pretreatment is performed by using the converter is that the steel removal method using the converter is used.
This is because if the treatment is performed, sufficient stirring power can be obtained, and the P slag removed from the previous heat and the Si slag removed from the next heat are sufficiently mixed to exhibit the slag reforming effect. In addition, in the case of hot metal pretreatment using a converter, the control of the slag composition can be satisfactorily performed, and the return P at the time of slag reforming can also be reliably suppressed.

【0013】[0013]

【実施例】溶銑予備脱Siおよび脱P炉として300T
ON転炉を用い280〜300TONの溶銑を装入し本
発明を適用した。表1は本発明の処理フローを適用した
結果であり、実施例1〜4は図1に示す処理フローを、
実施例5は図2に示す処理フローを適用した結果を示
す。また、表2は本発明の実施により改質されたスラグ
の水浸膨張率の測定結果を示す。表1において、スラグ
組成のうち「上段;炉内残留」は脱P処理後における炉
内残留スラグ組成を示し、「下段;脱Si後」は脱Si
処理後における炉内残留スラグ組成を示す。
[Example] 300T as a hot metal pre-removal Si and P removal furnace
The present invention was applied by charging 280 to 300 TON of hot metal using an ON converter. Table 1 shows the result of applying the processing flow of the present invention, and Examples 1 to 4 show the processing flow shown in FIG.
Example 5 shows the result of applying the processing flow shown in FIG. Table 2 shows the measurement results of the water immersion expansion coefficient of the slag modified by the practice of the present invention. In Table 1, among the slag compositions, “upper row; residual in the furnace” indicates the residual slag composition in the furnace after the de-P treatment, and “lower row;
3 shows the composition of slag remaining in the furnace after the treatment.

【0014】[0014]

【表1】 [Table 1]

【0015】[0015]

【表2】 [Table 2]

【0016】実施例1〜4における改質する炉内の脱P
後残留スラグは35〜50kg/t程度である。実施例
5は脱P後スラグを残留させず、他工程である脱C炉に
て発生回収した脱C滓だけを脱Si前に炉内に装入して
本発明を適用した結果であり、この時の脱C滓量は25
kg/t程度である。これら実施例における結果からわ
かるように、本発明を適用することによりF−CaOを
多く含む製鋼スラグの低F−CaO化が可能となり、表
2に示すとおり製鋼スラグ特有の課題である膨張安定性
についてもエージングを実施すること無く大幅な改善が
可能となり、路盤材、コンクリート適用基準(水浸膨張
率≦1.5%)を容易に達成することができる。
In Examples 1-4, the removal of P from the reforming furnace
The post residual slag is about 35 to 50 kg / t. Example 5 is a result of applying the present invention by leaving only slag generated and recovered in a decarbonization furnace, which is another process, in a furnace before desiliconization without leaving slag after P removal, and applying the present invention; The amount of C residue removed at this time is 25
It is about kg / t. As can be seen from the results in these examples, by applying the present invention, it is possible to lower the F-CaO content of the steelmaking slag containing a large amount of F-CaO, and as shown in Table 2, the expansion stability, which is a problem unique to steelmaking slag. Can be greatly improved without aging, and the standard for application of roadbed materials and concrete (water immersion expansion coefficient ≦ 1.5%) can be easily achieved.

【0017】また、実施例5に示すとおり脱P滓の代り
に脱C滓をリサイクルした場合でも同様の効果が確認さ
れ、さらに請求項2に示す方法を実施したケースでも効
果は確認された。なお、図3で示す比較例の通常操業で
発生するスラグの塩基度、F−CaO、膨張安定性は、
表1,2中の炉内残留スラグの実績値で示す。
Further, as shown in Example 5, the same effect was confirmed in the case where the C-removed slag was recycled instead of the P-removed slag, and the effect was also confirmed in the case where the method described in claim 2 was carried out. The basicity, F-CaO, and expansion stability of the slag generated in the normal operation of the comparative example shown in FIG.
The results are shown in Tables 1 and 2 with the actual values of residual slag in the furnace.

【0018】ところで、実施例に示すように、脱Si処
理後のスラグ塩基度を0.9〜1.1程度、T.Feを
15〜25%程度となるようにスラグ組成を制御するこ
とで、脱Si処理後の復Pを抑制でき、その後引続き行
う脱P処理も容易になる。このスラグ組成制御は鉄鉱石
または上吹酸素量で容易に制御可能である。
By the way, as shown in the examples, the slag basicity after the de-Si treatment is about 0.9 to 1.1, By controlling the slag composition so that the Fe content is about 15 to 25%, it is possible to suppress the recovery of P after the removal of Si, and to facilitate the subsequent removal of P. This slag composition control can be easily controlled by the amount of iron ore or the upper blowing oxygen.

【0019】[0019]

【発明の効果】以上述べたように本発明によれば、従来
エージング等の処置を加えて改善を行っていた製鋼スラ
グの膨張安定性を、通常の転炉精錬サイクルの中で極め
て容易に得ることができ、またその改質レベルは従来の
エージング処理では達成できないレベルまで改善するこ
とが可能となり、製鋼スラグの有効利用という面でも非
常に有用な発明である。
As described above, according to the present invention, the expansion stability of steelmaking slag, which has been improved by adding measures such as aging, can be obtained very easily in a normal converter refining cycle. In addition, the reforming level can be improved to a level that cannot be achieved by the conventional aging treatment, and this is a very useful invention in terms of effective utilization of steelmaking slag.

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

【図1】本発明の炉内残留スラグ改質処理フローを示す
説明図。
FIG. 1 is an explanatory diagram showing a flow of a process for reforming residual slag in a furnace according to the present invention.

【図2】本発明の他工程スラグの改質処理フローを示す
説明図
FIG. 2 is an explanatory diagram showing a flow of a slag reforming process of another process of the present invention.

【図3】従来の転炉型脱Si脱P処理フローを示す説明
図。
FIG. 3 is an explanatory diagram showing a flow of a conventional converter-type de-Si / de-P process.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 荒井 雅之 室蘭市仲町12番地 新日本製鐵株式会社室 蘭製鐵所内 (72)発明者 林 浩明 室蘭市仲町12番地 新日本製鐵株式会社室 蘭製鐵所内 (72)発明者 小林 雅人 東京都千代田区大手町2−6−3 新日本 製鐵株式会社内 Fターム(参考) 4K002 AC09 AE02 AE06 4K014 AA01 AA03 AE01  ──────────────────────────────────────────────────の Continuing on the front page (72) Inventor Masayuki Arai 12, Nakamachi, Muroran City Inside Nippon Steel Corporation Muroran Works (72) Inventor Hiroaki Hayashi 12, Nakamachi, Muroran City Nippon Steel Corporation Muroran Inside the steelworks (72) Inventor Masato Kobayashi F-term in the Nippon Steel Corporation 2-6-3 Otemachi, Chiyoda-ku, Tokyo (reference) 4K002 AC09 AE02 AE06 4K014 AA01 AA03 AE01

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 転炉を利用して溶銑予備処理として脱S
iおよび脱Pを行う転炉精錬法において、脱P処理終了
後のスラグを出湯後排滓せず炉内に残留させたまま次ヒ
ートの溶銑を装入し、酸素を供給して脱Si処理を行な
い、脱Si後一旦吹錬を中断してスラグを排出する中間
排滓工程をもうけ、その後引続き脱P精錬を行うことを
特徴とする遊離石灰含有量の低い製鋼スラグを副生する
転炉精錬法。
1. De-S as hot metal pretreatment using a converter
In the converter refining method for performing i and P removal, the molten iron of the next heat is charged while the slag after the removal of the P treatment is left in the furnace without discharging after tapping, and oxygen is supplied to remove the Si. A converter for producing by-produced steelmaking slag with low free lime content, characterized in that after the removal of Si, a blowing process is temporarily interrupted to provide an intermediate waste disposal step of discharging the slag, and thereafter the P-refining is continuously performed. Refining method.
【請求項2】 脱P処理後スラグを炉内に残留させると
共に他工程で発生した遊離石灰を含有するスラグを脱S
i処理前に炉内に装入する請求項1記載の転炉精錬法。
2. After the de-P treatment, the slag is left in the furnace and the slag containing free lime generated in other steps is de-S
2. The converter refining method according to claim 1, wherein the converter is charged into the furnace before i treatment.
【請求項3】 転炉を利用して溶銑予備処理として脱S
iおよび脱Pを行う転炉精錬法において、吹錬に先立ち
自工程または他工程で発生回収した遊離石灰を含有する
スラグを炉内に装入し、酸素を供給して脱Si処理を行
ない、脱Si後一旦吹錬を中断して改質スラグを排出す
る中間排滓工程をもうけ、その後引続き脱P精錬を行う
ことを特徴とする遊離石灰含有量の低い製鋼スラグを副
生する転炉精錬法。
3. De-S as hot metal pretreatment using a converter.
In the converter refining method for performing i and de-P, prior to blowing, slag containing free lime generated and recovered in its own process or another process is charged into a furnace, oxygen is supplied, and de-Si treatment is performed. Converter refining by-producing steelmaking slag with a low free lime content, characterized by providing an intermediate waste disposal step to temporarily stop blowing after the removal of Si and discharge the reformed slag, and then continue to remove P. Law.
JP2000085956A 2000-03-27 2000-03-27 Converter-refining method for by-producing steel manufacturing slag having low free lime content Withdrawn JP2001271113A (en)

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