WO2002101096A1 - Method of preliminarily processing converter type hot metal - Google Patents

Method of preliminarily processing converter type hot metal Download PDF

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Publication number
WO2002101096A1
WO2002101096A1 PCT/JP2002/005563 JP0205563W WO02101096A1 WO 2002101096 A1 WO2002101096 A1 WO 2002101096A1 JP 0205563 W JP0205563 W JP 0205563W WO 02101096 A1 WO02101096 A1 WO 02101096A1
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WO
WIPO (PCT)
Prior art keywords
converter
molten metal
refined
refining
molten
Prior art date
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PCT/JP2002/005563
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French (fr)
Japanese (ja)
Inventor
Keiji Shin
Masao Yamauchi
Syunsuke Nagata
Tamotsu Matsumura
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Nippon Steel Corporation
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Publication of WO2002101096A1 publication Critical patent/WO2002101096A1/en

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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C1/00Refining of pig-iron; Cast iron
    • C21C1/02Dephosphorising or desulfurising

Definitions

  • the present invention relates to a dephosphorization scouring (hereinafter, referred to as de-P scouring) mainly for dephosphorization in a converter or a converter type steelmaking furnace (hereinafter, referred to as a converter), and a decarburization mainly for decarburization.
  • de-P scouring a dephosphorization scouring mainly for dephosphorization in a converter or a converter type steelmaking furnace (hereinafter, referred to as a converter), and a decarburization mainly for decarburization.
  • the present invention relates to a converter-type hot metal pretreatment method for refining (hereinafter referred to as de-C refining). Background art
  • hot metal pretreatment such as dephosphorization of hot metal
  • a torpedo car or the like that transports hot metal from a blast furnace to a converter.
  • techniques for hot metal pretreatment in converters are becoming widespread.
  • a plurality of converters as described in Japanese Patent Application Laid-Open No. 6-73425 are used, and one of the converters is used only for de-P refining and the other is used for de-P refining.
  • one converter as disclosed in Japanese Patent Application Laid-Open No.
  • Figure 3 shows an overview of the cycle time in the same furnace type hot metal pretreatment method.
  • the same furnace type hot metal pretreatment method after de-P scouring, after tapping the P-free iron into a pan, the pot is moved from the bottom of the furnace to the charging side, and the transportation time for lifting to the charging position is appear.
  • the converter performs waste after the tapping, and a non-operating time is generated from the end of the waste to the charging of the molten metal.
  • Fig. 4 shows an example of the refining schedule of a dedicated furnace type hot metal pretreatment method.
  • the cycle time from charging of de-P refining to waste is shorter than the cycle time of de-C refining. Therefore, in the dedicated furnace type hot metal pretreatment method, since the refining pitch of the P-removing furnace is matched with the pitch of the C-removing furnace, the non-operating time of the converter between the refining of the P-removing furnace is as shown in the figure. appear. Disclosure of the invention
  • the present invention provides a converter-type hot metal pretreatment method with high productivity that effectively utilizes the non-operation time of the converter.
  • the present invention has been made to solve the above problems, and the gist thereof is as follows.
  • a converter-type hot metal pretreatment method that performs de-P refining and de-C refining of molten metal
  • the P furnace is charged into the converter for de-C refining.
  • the converter is characterized in that the molten metal that has been removed or the molten metal that has been de-P treated in a converter or other similar equipment and that has been placed on standby in advance is charged into the converter and the C-refining is continued.
  • Furnace hot metal pretreatment method Furnace hot metal pretreatment method.
  • the molten metal charged into the converter is a molten metal (hereinafter, molten metal B) other than the molten metal (hereinafter, molten metal A) which has just been de-P scoured and discharged in the converter.
  • Converter type hot metal pretreatment method In the converter-type hot metal pretreatment method in which the molten metal that has been de-P-refined is de-C-purified in the converter after the molten metal is de-P-refined in the converter, for this reason, the molten metal charged into the converter is a molten metal (hereinafter, molten metal B) other than the molten metal (hereinafter, molten metal A) which has just been de-P scoured and discharged in the converter.
  • Converter type hot metal pretreatment method In the converter-type hot metal pretreatment method in which the molten metal that has been de-P-refined is de-C-purified in the converter after the molten metal is de-P-refined
  • the molten metal B charged into the converter for de-C refining is a molten metal that has been de-P-purified in the converter (hereinafter, molten metal A ') prior to the molten metal A.
  • molten metal A ' molten metal that has been de-P-purified in the converter
  • a converter-type hot metal pretreatment method in which the molten metal that has been de-P-purified is de-C-purified in the converter or another converter after the molten metal is de-P-refined in the converter and discharged.
  • the molten iron is charged into the converter or another converter, the ordinary converter is refined and the steel is removed, and then the P-refined molten metal is removed.
  • a converter-type hot metal pretreatment method characterized by charging and decarbonizing.
  • the converter-type hot metal pretreatment method for removing de-P-purified molten metal in a converter de-P-refining the molten metal in the converter-type hot metal pretreatment method.After that, ordinary hot metal is charged into the converter, and then ordinary converter refining is performed.
  • a method for preheating a converter type hot metal which comprises charging a molten metal (melt A) that has been de-P-refined in the converter and then discharged, and de-C-refined.
  • the molten iron is subjected to de-P refining in the converter or another converter.
  • the molten metal is de-P-refined and discharged.
  • the molten metal (Molten A) is charged into another converter and de-C-refined, and ordinary molten iron is charged into the converter.
  • a converter-type hot metal pretreatment method characterized by charging a molten metal (melt C) that has been de-P-purified in another converter, and then de-C-refined after the steel has been refined in a converter.
  • the molten metal is de-P-refined in the converter or another converter.
  • At least one of the converters is a converter for de-P, and the other converter is a converter for de-C.
  • De-P refining is continuously performed in the P-removal converter, and when the non-operating time of the P-removal converter exceeds the cycle time required for ordinary hot metal refining, the P-removal is performed.
  • a converter-type hot metal pretreatment method characterized by performing ordinary converter refining in a converter.
  • the molten metal is de-P-refined in the converter or another converter. At least one of the converters is a converter for de-P, and the other converter is a converter for de-C. At the same time, the de-P refining is performed, and the molten metal that has been de-P-refined in the de-C converter is (Molten A). The molten metal (Molten C) de-P refined in the P-removing converter is alternately charged and de-C refined, and the P-removing converter performs de-P refining.
  • a converter-type hot metal pretreatment method characterized by performing ordinary converter refining for refining ordinary hot metal.
  • the molten metal de-P-refined in the C-free converter and the molten metal de-P-refined in the P-free converter are alternately charged into the C-free converter.
  • the de-C-removing converter de-P-refined the molten metal (melt C) that has been de-P-refined in the P-removing converter, and then de-P-refined in the de-C-removing converter.
  • FIG. 1 is a diagram showing an embodiment of the converter type hot metal pretreatment method of the present invention. (Part 1 )
  • FIG. 2 is a diagram showing an embodiment of the converter type hot metal pretreatment method of the present invention. (Part 2)
  • FIG. 3 is a diagram showing a refining cycle of the same furnace type.
  • FIG. 4 is a diagram showing a refining schedule of a dedicated furnace type. BEST MODE FOR CARRYING OUT THE INVENTION
  • the present invention deals with the following method.
  • the de-P-refined molten metal is separately kept at the charging position of the converter, and Immediately after the de-P scouring in the furnace is completed and the discharge of the converter is completed, the separately de-P-purified molten metal (Molten B) that has been put on standby is charged into the converter, and C scouring.
  • molten A refers to the charge refined in the converter.
  • the molten metal removed from the molten metal is continuously removed in the converter.
  • the molten metal A other than the molten metal charged into the converter for de-C refining, which is de-P-refined in the converter and discharged (hereinafter, molten metal A)
  • the other molten metal hereinafter, “Molten B”. This allows the converter to operate effectively while the molten metal A de-P-purified in the converter is moving for recharging.
  • the other molten metal B charged to the converter for de-C refining is added to the molten metal A.
  • the molten metal was de-P-refined in the converter (hereinafter referred to as molten metal A ').
  • the other molten metal B charged into the converter for de-C purification is Molten metal that has been de-P scoured in another converter (hereinafter, molten metal C).
  • the operation rate in the converter can be increased, Also, this method can be performed mutually between a plurality of converters. That is, in claim 5, as shown in pattern 2 of FIG. 1, after the molten metal was removed from the melt in the converter, the molten metal was discharged, and then the molten metal was removed from the melt in the converter or another converter.
  • the molten metal is de-P-refined in the converter and discharged, and then de-P-refined in another converter to discharge the molten metal.
  • the molten metal (Molten C) is charged and de-C scouring is performed, and the molten metal (Molten A) de-P scoured and discharged in the converter is charged into another converter and de-molten. C to refine. In this way, multiple converters can mutually increase efficiency.
  • the de-P-purified molten metal that is de-C-purified in the converter is converted into the molten metal of the charge (
  • the molten metal that is de-C-purified in the converter is de-P-purified in another converter.
  • the molten metal de-P-purified in the converter is de-C-purified in another converter, thereby eliminating the non-operating time caused when the de-P-purified molten metal is transported to the charging position. Things.
  • the non-operating time caused by this transportation is replaced with the use of ordinary molten iron instead of the separate introduction of the P-refined molten metal and the removal of the C-refining, followed by ordinary converter refining.
  • claim 6 is a converter-type hot metal reserve in which the molten metal that has been de-P-refined is de-C-refined in the converter or another converter after the molten metal is de-P-refined in the converter and discharged.
  • ordinary hot metal is charged into the converter or another converter, ordinary converter refining and tapping, and then de-P refining.
  • the molten metal is charged and decarbonized.
  • This method can respond by placing ordinary hot metal on standby as necessary, which is extremely useful for eliminating downtime. In addition to being effective, it is also effective in controlling slag contamination as described below.
  • ordinary converter refining means refining ordinary molten iron into molten steel in a converter (also abbreviated as N refining).
  • ordinary hot metal means hot metal that is not subjected to P removal treatment.
  • claim 7 is a converter-type hot metal pretreatment method in which after the molten metal is de-P-refined in the converter and the molten metal is discharged, the de-P-refined molten metal is further de-C-refined in the converter. After de-P refining and tapping, the molten metal is continuously charged with the ordinary molten iron into the converter, and then subjected to ordinary converter refining and tapping. (Molten A) is charged and decarbonized.
  • the above method can be performed between a plurality of converters.
  • claim 8 is a hot metal pretreatment for removing the P from the molten metal in the converter and discharging the molten metal, and then removing the de-P-purified molten metal from the molten metal in the converter or another converter.
  • the molten metal is removed from the furnace by de-P refining, and the molten metal is supplied to another converter.
  • ordinary molten iron is charged into the converter, and the ordinary converter is refined. Then, the molten metal (Molten C) that has been de-P scoured in another converter is charged, and de-C scouring is performed. It is what you do.
  • One of the furnaces (B furnace in pattern 2 in Fig. 1) removes P and scours the molten metal, and supplies the molten metal to another converter (A furnace in pattern 2 in Fig. 1) to remove C.
  • the converter After the slag is discharged, ordinary hot metal that has been previously placed in a standby position at the charging position of the converter is charged, the ordinary converter is refined, and tapping is performed. Next, in the converter, the molten metal de-P-purified in another converter is charged and de-C-purified. This processing pattern is performed in each furnace.
  • the invention of claim 9 is a hot metal pretreatment in which the molten metal de-P-refined in the converter or another converter is de-C-refined in the converter or another converter.
  • a converter-type hot metal pretreatment method of a dedicated furnace type in which at least one of the multiple converters is used as a converter for removing P and the other converter is used as a converter for removing C,
  • the P removal is continuously performed, and when the non-operating time of the P removal converter is longer than the cycle time required for ordinary converter refining of the normal molten iron, the P removal is performed.
  • the furnace is used for ordinary converter purification.
  • this is a converter for de-C conversion (A furnace).
  • the de-P converter In the converter for de-P (B furnace), the de-P converter is continuously de-C-purified, and the non-operating time is concentrated.
  • the normal converter refining In the mining, the normal converter refining is sandwiched between the de-P refining. As a result, it is possible to effectively contribute to the production of non-operating time due to the difference in cycle time between de-P scouring and de-C scouring.
  • the P-removing converter (B furnace) continuously performs 5 charges of P-free refining, and the cycle time difference from C-free refining accumulates. Since non-operating time for one ordinary converter refining is generated, one ordinary converter refining can be performed for every five charges after de-P refining, and the non-operating time can be eliminated.
  • the normal furnace converter 1 charge was applied to the hot metal pretreatment 5 charges.
  • the continuous converter (CC) that receives the refined molten copper If the continuous steelmaking machine (CC) that receives the hot metal pretreated molten steel, that is, the low phosphorus steel, is separated, the number of charges supplied to the two continuous steelmaking machines will be unbalanced.
  • claim 10 is a special furnace type in which the hot metal pretreatment is performed by using at least one of the plurality of converters as a converter for removing P and the other converter as a converter for removing C.
  • the de-P refining is performed also in the de-C converter, and the molten metal de-P-purified in the de-C converter is added to the de-C converter.
  • the de-C converter (A furnace) mainly performs de-C refining and de-P refining at any time.
  • the converter for C removal is a dedicated furnace that mainly performs C removal, but unlike pattern 3 in Fig. 1, P removal is also performed at an arbitrary timing. Therefore, in the outline of pattern 4 in Fig. 2 and pattern 4-2 in Fig. 2 described later, it is treated as the same furnace and described as the same furnace-dedicated furnace mixture.
  • the pattern for removing P from the C-removing furnace side is defined as follows.
  • the molten metal removed in the P-removing converter and in the converter for removing C are removed.
  • the molten metal is charged alternately to remove C.
  • the processing ratio of the ordinary steel and the low-phosphorus steel is almost the same.
  • the non-P converter may have a non-operating time. In such a case, priority should be given to the molten metal that has been de-P-refined in the P-P converter.
  • the molten metal de-P-purified in the C-free converter and the molten metal de-P-purified in the P-free converter are alternately placed in the C-free converter in claim 10.
  • the molten metal de-P-refined in the de-P converter is de-C-refined, and then the temporarily-removed de-C converter is placed. It is a process in which molten metal (Molten A ') that has been de-P-purified in a furnace is charged and de-C-purified. This is because, as shown in pattern 4-2 in Fig.
  • the molten metal that has been de-P-refined in the C-removal converter is temporarily placed, and the molten metal is removed by the P-removal converter.
  • P Refined molten metal (Molten C) Is charged, de-C refining and tapping are performed, and then the temporarily placed de-P-purified molten metal (Molten A,) is de-C refined.
  • Molten C the temporarily placed de-P-purified molten metal
  • the point of the present invention is that the hot metal is removed from the molten P
  • the other furnace is charged with the de-P molten metal of another charge and de-C refined, or the molten iron is de-P refined, and then the de-P molten metal is discharged, and then the converter is put into the converter.
  • normal molten iron is charged, the converter becomes a normal converter, copper is removed, and then other molten metal from other channels is charged and decarbonized.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Abstract

A method of preliminarily processing converter type hot metal that has higher productivity. A method of preliminarily processing converter type hot metal for p-removal refining and C-removal refining of molten metal, characterized in that in effecting C-removal refining, molten metal having its P removed by the converter that is charged into the converter for C-removal refining, or molten metal put on standby in advance and having its p removed in some other converter or a similar facility, is charged into the converter to continue C-removal refining.

Description

明 細 書 転炉型溶銑予備処理方法 技術分野  Description Converter type hot metal pretreatment method Technical field
本発明は、 転炉または転炉形式の製鋼炉 (以下、 転炉という) に おいて主に脱燐を行う脱燐精練 (以下、 脱 P精練という) 、 及び主 に脱炭を行う脱炭精練 (以下、 脱 C精練という) を行う転炉型溶銑 予備処理方法に関するものである。 背景技術  The present invention relates to a dephosphorization scouring (hereinafter, referred to as de-P scouring) mainly for dephosphorization in a converter or a converter type steelmaking furnace (hereinafter, referred to as a converter), and a decarburization mainly for decarburization. The present invention relates to a converter-type hot metal pretreatment method for refining (hereinafter referred to as de-C refining). Background art
従来、 溶銑の脱燐などを行ういわゆる溶銑予備処理は、 高炉から 出銑された溶銑を転炉まで運搬する トーピー ドカーなどによって行 なわれていたが、 近年、 その設備集約などを目的と して、 転炉で溶 銑予備処理を行う技術が普及されつつある。 例えば、 特開平 6-7342 5号公報に記載されているよ うな複数の転炉を使用し、 一つを脱 P精 鍊専用の脱 P炉、 他の一つを脱 C精鍊専用とする脱 C炉と して使用 する、 いわゆる専用炉タイプの転炉型溶銑予備処理方法がある。 ま た、 特開平 11- 181512号公報に開示されているよ うな一つの転炉を 使用し、 高炉からの溶銑を脱 P精練した後、 当該溶湯を一旦出湯し 、 脱 P精練の結果残留した脱 Pスラグを排出し、 この脱 P精練した溶 湯を再度同じ転炉に装入し、 脱 C精練を行う、 いわゆる同一炉タイ プの転炉型溶銑予備処理方法がある。 いずれにおいても転炉にて、 溶銑予備処理が可能とな り 、 設備集約などのメ リ ッ トは大きい。  Conventionally, so-called hot metal pretreatment, such as dephosphorization of hot metal, has been carried out using a torpedo car or the like that transports hot metal from a blast furnace to a converter. However, techniques for hot metal pretreatment in converters are becoming widespread. For example, a plurality of converters as described in Japanese Patent Application Laid-Open No. 6-73425 are used, and one of the converters is used only for de-P refining and the other is used for de-P refining. There is a so-called dedicated furnace type converter-type hot metal pretreatment method used as a C furnace. In addition, after using one converter as disclosed in Japanese Patent Application Laid-Open No. 11-181512 to remove the P from the hot metal from the blast furnace, the molten metal was discharged once, and as a result of the P removal, There is a so-called converter type hot metal pretreatment method of so-called converter type in which the de-P slag is discharged, the de-P-purified molten metal is charged again into the same converter and de-C-refining is performed. In any case, the hot metal pretreatment can be performed in the converter, and the advantages such as equipment consolidation are great.
しかしながら、 上記のよ うな転炉型予備精鍊においては、 脱 P精 鍊、 及び脱 C精鍊共に装入、 精練、 出湯などの作業が各 2回必要で あり、 1 チャージ当たりの転炉を占有する時間が長く なるこ とが避 けられず、 生産性の低下を招いており、 よ り生産性を向上する転炉 型溶銑予備処理方法が必要となっている。 However, in the converter type pre-purification as described above, charging, scouring, tapping, etc. are required twice for both de-P and de-C refining, occupying the converter per charge. Avoiding longer time As a result, productivity has declined, and a converter-type hot metal pretreatment method that further improves productivity is needed.
図 3は、 同一炉タイプの溶銑予備処理方法におけるサイクルタイ ムの概要を示したものである。 同一炉タイプの溶銑予備処理方法に おいては、 脱 P精練後、 当該脱 P銑を鍋に出湯した後、 当該鍋を炉 下から装入側に移動し、 装入位置まで吊り上げる運搬時間が発生す る。 その間、 当該転炉は、 前記出湯後、 排滓を行い、 排滓終了から 前記脱 P溶湯を装入するまでの間、 非稼動時間が発生する。  Figure 3 shows an overview of the cycle time in the same furnace type hot metal pretreatment method. In the same furnace type hot metal pretreatment method, after de-P scouring, after tapping the P-free iron into a pan, the pot is moved from the bottom of the furnace to the charging side, and the transportation time for lifting to the charging position is appear. During that time, the converter performs waste after the tapping, and a non-operating time is generated from the end of the waste to the charging of the molten metal.
一方、 図 4は、 専用炉タイプの溶銑予備処理方法の精鍊スケジュ ールの一例を示したものである。  On the other hand, Fig. 4 shows an example of the refining schedule of a dedicated furnace type hot metal pretreatment method.
通常、 脱 P精練の装入から排滓までのサイクルタイムは、 脱 C精 鍊のサイクルタイムよ り も短い。 従って、 専用炉タイプの溶銑予備 処理方法では、 脱 P炉の精鍊ピッチを脱 C炉のピッチに合わせるた め、 図のよ うに脱 P炉の精練と精練の間に転炉の非稼動時間が発生 する。 発明の開示  Normally, the cycle time from charging of de-P refining to waste is shorter than the cycle time of de-C refining. Therefore, in the dedicated furnace type hot metal pretreatment method, since the refining pitch of the P-removing furnace is matched with the pitch of the C-removing furnace, the non-operating time of the converter between the refining of the P-removing furnace is as shown in the figure. appear. Disclosure of the invention
本発明は、 これら上記転炉の非稼動時間を有効に活用する生産性 の高い転炉型溶銑予備処理方法を提供するものである。  The present invention provides a converter-type hot metal pretreatment method with high productivity that effectively utilizes the non-operation time of the converter.
本発明は、 上記の課題を解決するためになされたものであって、 その要旨とするところは以下のとおりである。  The present invention has been made to solve the above problems, and the gist thereof is as follows.
( 1 ) 溶湯の脱 P精練および脱 C精練を行う転炉型溶銑予備処理 方法において、 脱 C精練する際に、 脱 C精練するために転炉に装入 される当該転炉で脱 P処理された溶湯を、 或いはそれ以外の転炉も しく は類似設備で脱 P処理され予め待機させておいた溶湯を、 当該 転炉に装入して脱 C精練を続行することを特徴とする転炉型溶銑予 備処理方法。 ( 2 ) 転炉内にて溶湯を脱 P精練して出湯した後、 引き続き当該 転炉にて、 脱 P精練された溶湯を脱 C精鍊する転炉型溶銑予備処理 方法において、 脱 C精鍊のために当該転炉に装入される溶湯が、 当 該転炉で直前に脱 P精練して出湯した当該溶湯 (以下、 溶湯 A) 以 外の溶湯 (以下、 溶湯 B) であることを特徴とする転炉型溶銑予備 処理方法。 (1) In a converter-type hot metal pretreatment method that performs de-P refining and de-C refining of molten metal, during de-C refining, the P furnace is charged into the converter for de-C refining. The converter is characterized in that the molten metal that has been removed or the molten metal that has been de-P treated in a converter or other similar equipment and that has been placed on standby in advance is charged into the converter and the C-refining is continued. Furnace hot metal pretreatment method. (2) In the converter-type hot metal pretreatment method in which the molten metal that has been de-P-refined is de-C-purified in the converter after the molten metal is de-P-refined in the converter, For this reason, the molten metal charged into the converter is a molten metal (hereinafter, molten metal B) other than the molten metal (hereinafter, molten metal A) which has just been de-P scoured and discharged in the converter. Converter type hot metal pretreatment method.
( 3 ) 脱 C精練のために当該転炉に装入される前記溶湯 Bは、 前 記当該溶湯 Aに先立って、 当該転炉にて脱 P精練された溶湯 (以下 、 溶湯 A' ) であることを特徴とする ( 2 ) に記載の転炉型溶銑予 備処理方法。  (3) The molten metal B charged into the converter for de-C refining is a molten metal that has been de-P-purified in the converter (hereinafter, molten metal A ') prior to the molten metal A. (2) The converter type hot metal pretreatment method according to (2).
( 4 ) 脱 C精練のために当該転炉に装入される前記溶湯 Bは、 他 の転炉にて脱 P精練された溶湯 (以下、 溶湯 C) であることを特徴 とする ( 2 ) に記載の転炉型溶銑予備処理方法。  (4) The molten metal B charged into the converter for de-C refining is molten metal de-P-refined in another converter (hereinafter, molten metal C). (2) 2. A converter type hot metal pretreatment method according to item 1.
( 5 ) 転炉内にて溶湯を脱 P精練して出湯した後、 引き続き当該 転炉または他の転炉にて、 脱 P精練された溶湯を脱 C精練する転炉 型溶銑予備処理方法において、 転炉内にて溶湯を脱 P精練して出湯 した後、 当該転炉には、 他の転炉で脱 P精練して出湯した溶湯 (溶 湯 C) を装入して、 脱 C精練を行う と ともに、 当該転炉にて脱 P精 練して出湯した当該溶湯 (溶湯 A) は、 他の転炉に装入して脱 C精 鍊することを特徴とする転炉型溶銑予備処理方法。  (5) In the converter type hot metal pretreatment method, after the molten metal is de-P-refined in the converter and discharged, and then the de-P-refined molten metal is de-C-refined in the converter or another converter. Then, after the molten metal is removed from the melt in the converter and the molten metal is discharged, the molten metal (melt C) that has been removed from the melt and discharged from the other converter is charged into the converter, and the molten metal is removed from the melt. The molten iron (Molten A) that has been de-P-refined in the converter and discharged from the converter is charged into another converter and de-C-purified. Processing method.
( 6 ) 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉また は他の転炉にて、 脱 P精練された溶湯を脱 C精鍊する転炉型溶銑予 備処理方法において、 転炉にて脱 P精練して出湯した後、 当該転炉 または他の転炉に普通溶銑を装入し、 普通転炉精練して出鋼した後 、 次いで、 脱 P精練された溶湯を装入して脱 C精練するこ とを特徴 とする転炉型溶銑予備処理方法。  (6) A converter-type hot metal pretreatment method in which the molten metal that has been de-P-purified is de-C-purified in the converter or another converter after the molten metal is de-P-refined in the converter and discharged. In the above, after removing the P and refining in the converter, the molten iron is charged into the converter or another converter, the ordinary converter is refined and the steel is removed, and then the P-refined molten metal is removed. A converter-type hot metal pretreatment method characterized by charging and decarbonizing.
( 7 ) 転炉内にて溶湯を脱 P精練して出湯した後、 引き続き当該 転炉において、 脱 P精練された溶湯を脱 C精練する転炉型溶銑予備 処理方法において、 脱 P精練して出湯した後、 引き続き、 当該転炉 に普通溶銑を装入し、 普通転炉精練して出鋼した後、 次いで、 当該 転炉にて脱 P精練して出湯した溶湯 (溶湯 A ) を装入し、 脱 C精鍊 することを特徴とする転炉型溶銑予備処理方法。 (7) After removing the molten metal in the converter, In the converter-type hot metal pretreatment method for removing de-P-purified molten metal in a converter, de-P-refining the molten metal in the converter-type hot metal pretreatment method.After that, ordinary hot metal is charged into the converter, and then ordinary converter refining is performed. A method for preheating a converter type hot metal, which comprises charging a molten metal (melt A) that has been de-P-refined in the converter and then discharged, and de-C-refined.
( 8 ) 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉ある いは他の転炉において、 脱 P精練された溶湯を脱 C精鍊する溶銑予 備処理であって、 転炉にて溶湯を脱 P精練して出湯し、 当該溶湯 ( 溶湯 A ) を他の転炉に装入して脱 C精練するとともに、 当該転炉に は、 普通溶銑を装入し、 普通転炉精練して出鋼した後、 次いで、 他 の転炉で脱 P精練した溶湯 (溶湯 C ) を装入し、 脱 C精練を行う こ とを特徴とする転炉型溶銑予備処理方法。  (8) In the converter or another converter, after the molten metal is removed from the molten metal in the converter and the molten metal is discharged, the molten iron is subjected to de-P refining in the converter or another converter. In the converter, the molten metal is de-P-refined and discharged. The molten metal (Molten A) is charged into another converter and de-C-refined, and ordinary molten iron is charged into the converter. A converter-type hot metal pretreatment method characterized by charging a molten metal (melt C) that has been de-P-purified in another converter, and then de-C-refined after the steel has been refined in a converter.
( 9 ) 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉また は他の転炉にて、 脱 P精練した溶湯を脱 C精鍊する溶銑予備処理を 、 複数の転炉のうちの少なく とも 1つを脱 P用転炉と し、 他の転炉 を脱 C用転炉と して行う専用炉タイプの転炉型溶銑予備処理方法に おいて、  (9) After removing the molten metal in the converter and removing the molten metal from the furnace, the molten metal is de-P-refined in the converter or another converter. At least one of the converters is a converter for de-P, and the other converter is a converter for de-C.
脱 P用転炉において、 脱 P精鍊を連続的に行い、 当該脱 P用転炉 の非稼働時間が普通溶銑を普通転炉精練するに要するサイクルタイ ム以上となった時点で、 当該脱 P用転炉で普通転炉精鍊を行う こと を特徴とする転炉型溶銑予備処理方法。  De-P refining is continuously performed in the P-removal converter, and when the non-operating time of the P-removal converter exceeds the cycle time required for ordinary hot metal refining, the P-removal is performed. A converter-type hot metal pretreatment method characterized by performing ordinary converter refining in a converter.
( 10) 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉また は他の転炉にて、 脱 P精練した溶湯を脱 C精鍊する溶銑予備処理を 、 複数の転炉のうちの少なく とも 1つを脱 P用転炉と し、 他の転炉 を脱 C用転炉と して行う専用炉タイプの転炉型溶銑予備処理方法に おいて、 脱 C用転炉においても脱 P精鍊を行う と ともに、 当該脱 C 用転炉には、 当該脱 C用転炉で脱 P精練された溶湯 (溶湯 A ) と、 脱 P用転炉で脱 P精練された溶湯 (溶湯 C ) とを、 交互に装入して 脱 C精練すると ともに、 脱 P用転炉では脱 P精鍊を行い、 その非稼 働時間には普通溶銑を精練する普通転炉精練を行う ことを特徴とす る転炉型溶銑予備処理方法。 (10) After removing the molten metal in the converter and removing the molten metal from the furnace, the molten metal is de-P-refined in the converter or another converter. At least one of the converters is a converter for de-P, and the other converter is a converter for de-C. At the same time, the de-P refining is performed, and the molten metal that has been de-P-refined in the de-C converter is (Molten A). The molten metal (Molten C) de-P refined in the P-removing converter is alternately charged and de-C refined, and the P-removing converter performs de-P refining. A converter-type hot metal pretreatment method characterized by performing ordinary converter refining for refining ordinary hot metal.
( 11) 前記当該脱 C用転炉に、 前記当該脱 C用転炉で脱 P精練さ れた溶湯と、 前記脱 P用転炉で脱 P精練された溶湯とを、 交互に装 入して脱 C精練するに際し、 前記脱 C用転炉では、 前記脱 P用転炉 で脱 P精練された溶湯 (溶湯 C ) を脱 C精練した後に、 前記当該脱 C用転炉で脱 P精練された溶湯 (溶湯 A ' ) を脱 C精鍊することを 特徴とする (10) に記載の転炉型溶銑予備処理方法。 図面の簡単な説明  (11) The molten metal de-P-refined in the C-free converter and the molten metal de-P-refined in the P-free converter are alternately charged into the C-free converter. In the de-C-refining, the de-C-removing converter de-P-refined the molten metal (melt C) that has been de-P-refined in the P-removing converter, and then de-P-refined in the de-C-removing converter. The converter-type hot metal pretreatment method according to (10), wherein the molten metal (molten metal A ′) is de-C-purified. BRIEF DESCRIPTION OF THE FIGURES
図 1は、 本発明の転炉型溶銑予備処理方法の実施例を示す図であ る。 (その 1 )  FIG. 1 is a diagram showing an embodiment of the converter type hot metal pretreatment method of the present invention. (Part 1 )
図 2は、 本発明の転炉型溶銑予備処理方法の実施例を示す図であ る。 (その 2 )  FIG. 2 is a diagram showing an embodiment of the converter type hot metal pretreatment method of the present invention. (Part 2)
図 3は、 同一炉タイプの精鍊サイクルを示す図である。  FIG. 3 is a diagram showing a refining cycle of the same furnace type.
図 4は、 専用炉タイプの精鍊スケジュールを示す図である。 発明を実施するための最良の実施形態  FIG. 4 is a diagram showing a refining schedule of a dedicated furnace type. BEST MODE FOR CARRYING OUT THE INVENTION
以下、 本発明を具体的に説明する。  Hereinafter, the present invention will be described specifically.
図 3で示したように、 同一炉タイプの溶銑予備処理方法において は、 転炉で脱 P精練して鍋に出湯された溶湯は、 脱 C精練するため に、 出湯位置から当該転炉または他の転炉の装入位置に移動させら れる。 この移動過程で、 転炉に非稼働時間が生じる。 これに対して 、 本発明では、 以下のような方法で対処する。  As shown in Fig. 3, in the hot metal pretreatment method of the same furnace type, the molten metal discharged from the pot after de-P refining in the converter is de-C-refined. To the charging position of the converter. During this transfer process, the converter generates downtime. On the other hand, the present invention deals with the following method.
すなわち、 転炉で脱 P精練終了後、 当該精練された溶湯 (以下、 溶湯 A ) を出湯し、 当該転炉の装入位置まで運搬されてく るのを待 つのではなく、 別に脱 P精練された溶湯を、 当該転炉の装入位置に 待機させておき、 当該転炉での当該脱 P精練が終了し、 転炉の排滓 が終了後、 直ちに、 待機させておいた別に脱 P精練された溶湯 (溶 湯 B ) を、 当該転炉に装入し、 脱 C精練を行う ものである。 That is, after de-P scouring is completed in the converter, the scoured molten metal (hereinafter, referred to as Rather than waiting for the molten metal A) to be discharged and transported to the charging position of the converter, the de-P-refined molten metal is separately kept at the charging position of the converter, and Immediately after the de-P scouring in the furnace is completed and the discharge of the converter is completed, the separately de-P-purified molten metal (Molten B) that has been put on standby is charged into the converter, and C scouring.
なお、 当該溶湯 (以下、 溶湯 A ) とは、 当該転炉にて精練された チャージをいう ものとする。  The molten metal (hereinafter, “molten A”) refers to the charge refined in the converter.
すなわち、 請求項 2は、 図 1 のパターン 1〜 2に示すように、 転 炉内にて溶湯を脱 P精練して出湯した後、 引き続き当該転炉にて、 脱 P精練された溶湯を脱 C精鍊する転炉型溶銑予備処理方法におい て、 脱 C精鍊のために当該転炉に装入される溶湯を、 当該転炉で脱 P精練して出湯した当該溶湯 (以下、 溶湯 A ) 以外の別の溶湯 (以 下、 溶湯 B ) とするものである。 これによ り、 当該転炉で脱 P精鍊 した溶湯 Aが再装入のために移動している間にも、 転炉を有効に稼 働させることができる。  That is, as shown in the patterns 1 and 2 in FIG. 1, after the molten metal is removed from the molten metal in the converter and the molten metal is discharged, the molten metal removed from the molten metal is continuously removed in the converter. In the converter-type hot metal pretreatment method for C-refining, other than the molten metal charged into the converter for de-C refining, which is de-P-refined in the converter and discharged (hereinafter, molten metal A) The other molten metal (hereinafter, “Molten B”). This allows the converter to operate effectively while the molten metal A de-P-purified in the converter is moving for recharging.
また、 請求項 3は、 図 1 のパターン 1 に示すように、 請求項 2に おいて、 脱 C精練のために当該転炉に装入される前記別の溶湯 Bを 、 前記当該溶湯 Aに先立って、 当該転炉にて脱 P精練された溶湯 ( 以下、 溶湯 A ' ) とするものである。  In addition, as shown in Pattern 1 in FIG. 1, in claim 3, in claim 2, the other molten metal B charged to the converter for de-C refining is added to the molten metal A. Prior to that, the molten metal was de-P-refined in the converter (hereinafter referred to as molten metal A ').
また、 請求項 4は、 図 1 のパターン 2に示すように、 請求項 2 ( 図 1 のパターン 1 ) において、 脱 C精鍊のために当該転炉に装入さ れる前記別の溶湯 Bを、 他の転炉にて脱 P精練された溶湯 (以下、 溶湯 C ) とするものである。  Further, according to claim 4, as shown in pattern 2 of FIG. 1, in claim 2 (pattern 1 of FIG. 1), the other molten metal B charged into the converter for de-C purification is Molten metal that has been de-P scoured in another converter (hereinafter, molten metal C).
このよ う に、 当該転炉に、 当該チャージの溶湯とは別に脱 P精鍊 された溶湯を装入して脱 C精鍊を行う ことによって、 当該転炉にお ける稼働率を高めることができ、 また、 この方法を複数の転炉間で 互いに行う こ とができる。 すなわち、 請求項 5は、 図 1 のパターン 2に示したように、 転炉 内にて溶湯を脱 P精練して出湯した後、 当該転炉または他の転炉に て、 脱 P精練された溶湯を脱 C精練する転炉型溶銑予備処理方法に おいて、 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉には 、 他の転炉で脱 P精練して出湯した溶湯 (溶湯 C ) を装入して、 脱 C精練を行う とともに、 当該転炉にて脱 P精練して出湯した当該溶 湯 (溶湯 A ) は、 他の転炉に装入して脱 C精鍊するものである。 こ れによって、 複数の転炉で、 相互によ り効率を上げることができる ものである。 In this way, by charging the de-P-purified molten metal separately from the molten metal of the charge into the converter and performing the C-refining, the operation rate in the converter can be increased, Also, this method can be performed mutually between a plurality of converters. That is, in claim 5, as shown in pattern 2 of FIG. 1, after the molten metal was removed from the melt in the converter, the molten metal was discharged, and then the molten metal was removed from the melt in the converter or another converter. In the converter-type hot metal pretreatment method in which the molten metal is de-C-purified, the molten metal is de-P-refined in the converter and discharged, and then de-P-refined in another converter to discharge the molten metal. The molten metal (Molten C) is charged and de-C scouring is performed, and the molten metal (Molten A) de-P scoured and discharged in the converter is charged into another converter and de-molten. C to refine. In this way, multiple converters can mutually increase efficiency.
このよ う に、 上記、 請求項 2 〜 4では、 転炉で溶湯を脱 P精練し て出湯した後、 当該転炉にて脱 C精練する脱 P精練された溶湯を、 当該チャージの溶湯 (溶湯 A ) ではなく別に脱 P精練された溶湯 ( 溶湯 B ) に置き換えることによ り、 また、 請求項 5では、 当該転炉 で脱 C精鍊する溶湯を、 他の転炉で脱 P精練した溶湯とすると とも に、 当該転炉で脱 P精練した溶湯は他の転炉で脱 C精鍊することに より、 脱 P精練した溶湯を装入位置まで運搬する際に生ずる非稼働 時間を解消するものである。  As described above, in the above claims 2 to 4, after the molten metal is de-P-purified in the converter and discharged, the de-P-purified molten metal that is de-C-purified in the converter is converted into the molten metal of the charge ( By replacing the molten metal A) with a molten metal that has been de-P-purified separately (melt B), in claim 5, the molten metal that is de-C-purified in the converter is de-P-purified in another converter. In addition to melting the molten metal, the molten metal de-P-purified in the converter is de-C-purified in another converter, thereby eliminating the non-operating time caused when the de-P-purified molten metal is transported to the charging position. Things.
さらに、 本発明では、 この運搬に伴って生じる非稼働時間を、 別 に脱 P精練された溶湯を装入して脱 C精練するのに代えて普通溶銑 を装入し、 普通転炉精鍊することによ り解消することができる。 すなわち、 請求項 6は、 転炉内にて溶湯を脱 P精練して出湯した 後、 当該転炉または他の転炉にて、 脱 P精練された溶湯を脱 C精練 する転炉型溶銑予備処理方法において、 転炉にて脱 P精練して出湯 した後、 当該転炉または他の転炉に普通溶銑を装入し、 普通転炉精 練して出鋼した後、 次いで、 脱 P精練された溶湯を装入して脱 C精 鍊するものである。 この方法では、 普通溶銑を必要に応じて待機さ せておく ことによ り対応できるため、 非稼働時間の解消にきわめて 有効であるほか、 後述のように、 スラグによる汚染の抑制にも効果 がある。 なお、 普通転炉精練とは、 転炉で普通溶銑を溶鋼に精練す ることを意味する (N精練とも略記する。 ) 。 但し、 普通溶銑とは 、 脱 P処理をしない溶銑を意味するものとする。 Furthermore, in the present invention, the non-operating time caused by this transportation is replaced with the use of ordinary molten iron instead of the separate introduction of the P-refined molten metal and the removal of the C-refining, followed by ordinary converter refining. This can be resolved. In other words, claim 6 is a converter-type hot metal reserve in which the molten metal that has been de-P-refined is de-C-refined in the converter or another converter after the molten metal is de-P-refined in the converter and discharged. In the treatment method, after de-P refining in the converter and tapping, ordinary hot metal is charged into the converter or another converter, ordinary converter refining and tapping, and then de-P refining. The molten metal is charged and decarbonized. This method can respond by placing ordinary hot metal on standby as necessary, which is extremely useful for eliminating downtime. In addition to being effective, it is also effective in controlling slag contamination as described below. Note that ordinary converter refining means refining ordinary molten iron into molten steel in a converter (also abbreviated as N refining). However, ordinary hot metal means hot metal that is not subjected to P removal treatment.
すなわち、 請求項 7は、 転炉内にて溶湯を脱 P精練して出湯した 後、 引き続き当該転炉において、 脱 P精練された溶湯を脱 C精練す る転炉型溶銑予備処理方法において、 脱 P精練して出湯した後、 引 き続き、 当該転炉に普通溶銑を装入し、 普通転炉精練して出鋼した 後、 次いで、 当該転炉にて脱 P精練して出湯した溶湯 (溶湯 A ) を 装入し、 脱 C精鍊するものである。  That is, claim 7 is a converter-type hot metal pretreatment method in which after the molten metal is de-P-refined in the converter and the molten metal is discharged, the de-P-refined molten metal is further de-C-refined in the converter. After de-P refining and tapping, the molten metal is continuously charged with the ordinary molten iron into the converter, and then subjected to ordinary converter refining and tapping. (Molten A) is charged and decarbonized.
これは、 図 2のパターン 5に示すように、 当該転炉での脱 P精鍊 後に、 予め、 普通溶銑を当該転炉の装入位置に待機させておき、 当 該転炉の排滓終了後、 この普通溶銑を装入し、 普通転炉精練を行つ て、 出鋼し、 その後、 当該転炉にて先に脱 P精練した溶湯 (溶湯 A , ) を装入し、 脱 C精鍊するものである。  As shown in pattern 5 in FIG. 2, after de-P refining in the converter, ordinary hot metal is made to stand by at the charging position of the converter in advance, and after completion of the discharge of the converter, The ordinary molten iron is charged, ordinary converter refining is performed, and tapping is performed. Then, in the converter, the molten metal that has been de-P refined first (the molten metal A,) is charged and de-C refined. Things.
すなわち、 図 2のパターン 5は、 パターン 1の脱 P精練の後、 別 の脱 P精練溶湯の代わりに、 普通溶銑を装入して普通転炉精練し、 次いで当該転炉で先に脱 P精練した溶湯 (溶湯 A ' ) を脱 C精練す る形となっていることがわかる。 これによ り非稼働時間の解消と と もに、 操業の自由度を拡大できる。  That is, in pattern 5 in Fig. 2, after de-P refining of pattern 1, instead of another de-P refining molten metal, ordinary hot metal is charged and ordinary converter refining is performed. It can be seen that the refined molten metal (Molten A ') is de-C-purified. This will eliminate downtime and increase operational flexibility.
さ らに、 上記の方法を複数の転炉間で行う ことができる。  Further, the above method can be performed between a plurality of converters.
すなわち、 請求項 8は、 転炉内にて溶湯を脱 P精練して出湯した 後、 当該転炉あるいは他の転炉において、 脱 P精練された溶湯を脱 C精鍊する溶銑予備処理であって、 転炉内にて溶湯を脱 P精練して 出湯し、 当該溶湯 (溶湯 A ) を他の転炉に供給するとともに、 当該 転炉には、 普通溶銑を装入し、 普通転炉精練して出鋼した後、 次い で、 他の転炉で脱 P精練した溶湯 (溶湯 C ) を装入し、 脱 C精練を 行う ものである。 In other words, claim 8 is a hot metal pretreatment for removing the P from the molten metal in the converter and discharging the molten metal, and then removing the de-P-purified molten metal from the molten metal in the converter or another converter. In the converter, the molten metal is removed from the furnace by de-P refining, and the molten metal is supplied to another converter. In addition, ordinary molten iron is charged into the converter, and the ordinary converter is refined. Then, the molten metal (Molten C) that has been de-P scoured in another converter is charged, and de-C scouring is performed. It is what you do.
これは、 図 2のパターン 6に示すよ うに、 請求項 4 (図 1のパタ —ン 2 ) と請求項 10 (図 2のパターン 5 ) の方法を折衷したような 形のパターンであり、 当該一方の炉 (図 1パターン 2の B炉) は、 脱 P精練して出湯し、 当該溶湯を他の転炉 (図 1パターン 2の A炉 ) に供給して脱 C精練する。 当該転炉では、 排滓後、 予め、 当該転 炉の装入位置に待機させておいた普通溶銑を装入して、 普通転炉精 鍊を行って出鋼する。 次に、 当該転炉では、 他の転炉で脱 P精練し た溶湯を装入し、 脱 C精鍊を行う。 この処理パターンを互いの炉で 行う ものである。  This is a pattern that is a compromise between the methods of claim 4 (pattern 2 of FIG. 1) and claim 10 (pattern 5 of FIG. 2), as shown in pattern 6 of FIG. One of the furnaces (B furnace in pattern 2 in Fig. 1) removes P and scours the molten metal, and supplies the molten metal to another converter (A furnace in pattern 2 in Fig. 1) to remove C. In the converter, after the slag is discharged, ordinary hot metal that has been previously placed in a standby position at the charging position of the converter is charged, the ordinary converter is refined, and tapping is performed. Next, in the converter, the molten metal de-P-purified in another converter is charged and de-C-purified. This processing pattern is performed in each furnace.
この方法によ り、 複数の転炉間で、 処理時間のずれおよび搬送時 間などに伴う非稼働時間を解消することができると ともに、 操業の 自由度を拡大できる。  With this method, it is possible to eliminate the non-operating time due to the processing time shift and the transport time among a plurality of converters, and to expand the degree of freedom of operation.
次に、 図 4で説明したよ うに、 専用炉タイプの転炉型溶銑予備処 理方法では、 脱 C精練と脱 P精練のサイクルタイムが異なっており 、 両者のピッチを合わせるために、 通常、 脱 P精鍊側に非稼働時間 が発生する。 本発明においては、 以下の方法によって、 この非稼働 時間を解消するものである。  Next, as described in FIG. 4, in the converter type hot metal pretreatment method of the dedicated furnace type, the cycle time of the de-C refining and the de-P refining is different. Non-operating time occurs on the P-free side. In the present invention, this non-operation time is eliminated by the following method.
すなわち、 請求項 9の発明は、 転炉内にて溶湯を脱 P精練して出 湯した後、 当該転炉または他の転炉にて、 脱 P精練した溶湯を脱 C 精練する溶銑予備処理を、 複数の転炉のうちの少なく とも 1つを脱 P用転炉と し、 他の転炉を脱 C用転炉と して行う専用炉タイプの転 炉型溶銑予備処理方法において、 脱 P用転炉において、 脱 P精練を 連続的に行い、 当該脱 P用転炉の非稼働時間が普通溶銑を普通転炉 精練するに要するサイクルタイム以上となった時点で、 当該脱 P用 転炉で普通転炉精鍊を行う ものである。  That is, the invention of claim 9 is a hot metal pretreatment in which the molten metal de-P-refined in the converter or another converter is de-C-refined in the converter or another converter. In a converter-type hot metal pretreatment method of a dedicated furnace type in which at least one of the multiple converters is used as a converter for removing P and the other converter is used as a converter for removing C, In the P converter, the P removal is continuously performed, and when the non-operating time of the P removal converter is longer than the cycle time required for ordinary converter refining of the normal molten iron, the P removal is performed. The furnace is used for ordinary converter purification.
これは、 図 1のパターン 3に示すよ うに、 脱 C用転炉 (A炉) で は脱 C精鍊を行なう一方、 脱 P用転炉 (B炉) においては、 脱 P精 鍊を連続的に行ない、 非稼働時間が集約されて、 普通転炉精練のサ ィ クルタイムに達したタイ ミ ングで普通転炉精鍊を脱 P精練の間に 挟むものである。 これによ り、 脱 P精練と脱 C精練のサイ クルタイ ムの差による非稼働時間の発生を有効に生産に寄与させるこ とがで さる。 As shown in Pattern 3 in Fig. 1, this is a converter for de-C conversion (A furnace). In the converter for de-P (B furnace), the de-P converter is continuously de-C-purified, and the non-operating time is concentrated. In the mining, the normal converter refining is sandwiched between the de-P refining. As a result, it is possible to effectively contribute to the production of non-operating time due to the difference in cycle time between de-P scouring and de-C scouring.
たとえば、 図 1 のパターン 3では、 脱 P用転炉 ( B炉) で、 脱 P 精練 5チャージを連続的に実施するこ とによ り、 脱 C精練とのサイ クルタイムの差が累積し、 普通転炉精練 1 回分の非稼働時間が発生 するため、 脱 P精鍊 5チャージ毎に、 1 回の普通転炉精鍊を実施す るこ とができ、 非稼働時間を解消するこ とができる。  For example, in pattern 3 in Fig. 1, the P-removing converter (B furnace) continuously performs 5 charges of P-free refining, and the cycle time difference from C-free refining accumulates. Since non-operating time for one ordinary converter refining is generated, one ordinary converter refining can be performed for every five charges after de-P refining, and the non-operating time can be eliminated.
また、 図 1 のパターン 3では、 溶銑予備処理 5チャージに対し、 普通転炉精鍊 1 チャージのパターンであつたが、 例えば、 普通転炉 精練をした溶銅を受ける連続铸造装置 ( C C ) と、 溶銑予備処理し た溶鋼、 すなわち、 低燐鋼を受ける連続铸造装置 (C C ) とが分か れている場合、 二つの連続铸造装置に供給するチャージ数にアンバ ランスが発生する。  In addition, in pattern 3 in Fig. 1, the normal furnace converter 1 charge was applied to the hot metal pretreatment 5 charges. For example, the continuous converter (CC) that receives the refined molten copper If the continuous steelmaking machine (CC) that receives the hot metal pretreated molten steel, that is, the low phosphorus steel, is separated, the number of charges supplied to the two continuous steelmaking machines will be unbalanced.
この場合、 図 1 のパターン 3の脱 C用転炉でも、 任意のタイ ミ ン グで脱 P精鍊を行う よ うにするものである。 すなわち、 請求項 10は 、 溶銑予備処理を、 複数の転炉のう ちの少なく とも 1つを脱 P用転 炉と し、 他の転炉を脱 C用転炉と して行う専用炉タイプの転炉型溶 銑予備処理方法において、 脱 C用転炉においても脱 P精鍊を行う と と もに、 当該脱 C用転炉には、 当該脱 C用転炉で脱 P精練された溶 湯 (溶湯 A ) と、 脱 P用転炉で脱 P精練された溶湯 (溶湯 C ) とを 、 交互に供給して脱 C精練する と と もに、 脱 P用転炉では脱 P精練 を行い、 その非稼働時間には普通溶銑を精練する普通転炉精鍊を行 う ものである。 これは、 図 2のパターン 4に示すように、 複数の転炉のうち、 少 なく とも 1つを脱 P用転炉 (B炉) と し、 他の転炉を脱 C用転炉 ( A炉) と して溶銑予備処理を行う ものであって、 脱 P用転炉 (B炉 ) では、 図 1パターン 3の B炉のよ うに普通転炉精鍊を挟みつつ脱 P精練を行い、 一方、 脱 C用転炉 (A炉) では、 主と して脱 C精練 を行う と ともに、 任意のタイ ミ ングで脱 P精鍊を行う ものである。 ここで、 図 2のパターン 4では、 脱 C用転炉は主と して脱 C精練 を行う専用炉であるが、 図 1のパターン 3 と異なり、 任意のタイ ミ ングで脱 P精鍊も行うので、 図 2のパターン 4、 及び後述する図 2 のパターン 4— 2での概要では、 同一炉と して扱い、 同一炉—専用 炉混合と記した。 In this case, even in the de-C converter of pattern 3 in Fig. 1, de-P purification is performed at an arbitrary timing. That is, claim 10 is a special furnace type in which the hot metal pretreatment is performed by using at least one of the plurality of converters as a converter for removing P and the other converter as a converter for removing C. In the converter-type hot metal pretreatment method, the de-P refining is performed also in the de-C converter, and the molten metal de-P-purified in the de-C converter is added to the de-C converter. (Molten A) and the molten metal (Molten C) de-P refined in the P-removing converter are alternately supplied to de-C refining, and P-removing is performed in the P-removing converter. During the non-operation time, ordinary converter refining for refining ordinary hot metal is performed. As shown in pattern 4 of Fig. 2, at least one of the converters is a converter for de-P (B furnace) and the other converter is a converter for de-C (A In the converter for de-P (B furnace), de-P scouring is carried out while sandwiching the ordinary converter as shown in pattern B in Fig. 1, pattern 3. On the other hand, the de-C converter (A furnace) mainly performs de-C refining and de-P refining at any time. Here, in pattern 4 in Fig. 2, the converter for C removal is a dedicated furnace that mainly performs C removal, but unlike pattern 3 in Fig. 1, P removal is also performed at an arbitrary timing. Therefore, in the outline of pattern 4 in Fig. 2 and pattern 4-2 in Fig. 2 described later, it is treated as the same furnace and described as the same furnace-dedicated furnace mixture.
このよ う に、 脱 C炉側に脱 P精鍊を挟んだパターンと し、 脱 C用 転炉では、 脱 P用転炉で脱 P精練された溶湯と、 脱 C用転炉で脱 P 精練された溶湯とを交互装入して、 脱 C精鍊するものである。 これ によって、 普通鋼と低燐鋼との処理がほぼ同等の比率となる。  In this way, the pattern for removing P from the C-removing furnace side is defined as follows. In the converter for removing C, the molten metal removed in the P-removing converter and in the converter for removing C are removed. The molten metal is charged alternately to remove C. As a result, the processing ratio of the ordinary steel and the low-phosphorus steel is almost the same.
しかしながら、 この図 2のパターン 4の場合には、 脱 P用転炉に 非稼働時間が発生することがある。 このよ うな場合には、 脱 P用転 炉で脱 P精練された溶湯を優先処理するこどによ り対処するもので ある。  However, in the case of pattern 4 in FIG. 2, the non-P converter may have a non-operating time. In such a case, priority should be given to the molten metal that has been de-P-refined in the P-P converter.
すなわち、 請求項 11は、 請求項 10において、 脱 C用転炉に、 当該 脱 C用転炉で脱 P精練された溶湯と、 脱 P用転炉で脱 P精練された 溶湯とを交互に装入して脱 C精練するに際し、 前記脱 C用転炉では 、 前記脱 P用転炉で脱 P精練された溶湯を脱 C精練した後に、 仮置 きしておいた前記脱 C用転炉で脱 P精練された溶湯 (溶湯 A ' ) を 装入して脱 C精鍊するものである。 これは、 図 2のパターン 4— 2 に示したように、 脱 C用転炉で脱 P精練した溶湯を、 一旦仮置きし 、 この脱 C用転炉には、 脱 P用転炉で脱 P精練した溶湯 (溶湯 C ) を装入して、 脱 C精練し、 出鋼し、 そのあと、 仮置き した脱 P精鍊 された溶湯 (溶湯 A, ) を脱 C精鍊するものである。 これによ り脱 P用転炉側の非稼働時間を解消できる。 That is, in claim 11, the molten metal de-P-purified in the C-free converter and the molten metal de-P-purified in the P-free converter are alternately placed in the C-free converter in claim 10. At the time of charging and de-C refining, in the de-C de-converter, the molten metal de-P-refined in the de-P converter is de-C-refined, and then the temporarily-removed de-C converter is placed. It is a process in which molten metal (Molten A ') that has been de-P-purified in a furnace is charged and de-C-purified. This is because, as shown in pattern 4-2 in Fig. 2, the molten metal that has been de-P-refined in the C-removal converter is temporarily placed, and the molten metal is removed by the P-removal converter. P Refined molten metal (Molten C) Is charged, de-C refining and tapping are performed, and then the temporarily placed de-P-purified molten metal (Molten A,) is de-C refined. As a result, the non-operating time on the P-converter side can be eliminated.
と ころで、 脱 P精練後、 直ちに、 同じ転炉で脱 C精練する と、 炉 内に付着し、 P含有量の高いスラグから、 溶湯への復 P (復燐) が 起こるが、 請求項 6〜請求項 11のいづれかの 1項に記載した方法、 例えば、 図 2のパターン 4, 4 - 2 , 5 あるいは 6のよ うに、 脱 P 精練後、 脱 C精練前に、 普通転炉精練を挟み込んだ操業とすること によって、 P濃度の低いスラグが生成し、 先の P濃度の高い炉内付 着スラグが洗われ、 この後に続く脱 C精練での復 Pを抑制するこ と ができる という利点がある。  At this point, immediately after de-P scouring, if de-C scouring is performed in the same converter immediately, it will adhere to the furnace and return P (re-phosphorus) to the molten metal from slag with a high P content. The method described in any one of claims 6 to 11, for example, as shown in pattern 4, 4-2, 5 or 6 in FIG. By sandwiching the operation, slag with a low P concentration is generated, the slag attached to the furnace with a high P concentration is washed, and it is possible to suppress the recovery of P in the subsequent de-C refining. There are advantages.
以上、 図 1 のパターン 1 からパターン 3および図 2のパターン 4 からパターン 6などの例から判るよ う に、 本発明のポイ ン トは、 溶 銑を脱 P精鍊後、 この脱 P溶湯を出湯し、 その後、 当該転炉に、 他 チャージの脱 P溶湯を装入し、 脱 C精鍊を行うか、 或いは、 溶銑を 脱 P精練後、 この脱 P溶湯を出湯し、 その後、 当該転炉に、 普通溶 銑を装入して、 普通転炉精鍊となって、 出銅し、 その後に他チヤ一 ジの脱 P溶湯を装入し、 脱 C精練を行う こ とである。  As can be seen from the examples of Pattern 1 to Pattern 3 in FIG. 1 and Pattern 4 to Pattern 6 in FIG. 2, the point of the present invention is that the hot metal is removed from the molten P After that, the other furnace is charged with the de-P molten metal of another charge and de-C refined, or the molten iron is de-P refined, and then the de-P molten metal is discharged, and then the converter is put into the converter. In addition, normal molten iron is charged, the converter becomes a normal converter, copper is removed, and then other molten metal from other channels is charged and decarbonized.
本発明の方法による、 生産性の向上、 スラグによる溶湯の汚染抑 制 (復 Pの抑制) などの効果を、 図 1 および図 2のパターンの例と 併せて示した。 実施例  The effects of the method of the present invention, such as the improvement of productivity and the suppression of contamination of molten metal by slag (suppression of P), are shown together with the pattern examples of FIGS. Example
実操業の転炉を使用し、 図 1 のパターン 1 の操業に準じて、 当該 転炉で先に脱 P精練した溶湯 (溶湯 A, ) と、 他の転炉で脱 P精鍊 した溶湯 (溶湯 C ) とを使用し、 当該転炉で脱 C精練した。 従来の 同一炉タイプの溶銑予備処理方法に比較し、 約 5 %生産性が向上し た。 産業上の利用可能性 Using a converter in actual operation, according to the operation of Pattern 1 in Fig. 1, the molten metal (Molten A,) previously de-P-purified in the converter and the molten metal (P-melted) in other converters C) was used to remove C in the converter. Compared to the conventional hot metal pretreatment method of the same furnace type, the productivity is improved by about 5%. Was. Industrial applicability
本発明によ り、 転炉型溶銑予備処理方法において、 転炉の稼働率 が向上し、 生産性が向上する と と もに、 復 Pを抑制できる健全な脱 C精鍊を行う こ とができる。  ADVANTAGE OF THE INVENTION According to the present invention, in the converter type hot metal pretreatment method, it is possible to improve the operation rate of the converter and improve the productivity, and also to perform sound de-C refining capable of suppressing the recovery P. .

Claims

求 の 範 囲 Range of request
1 . 溶湯の脱 P精練および脱 C精練を行う転炉型溶銑予備処理方 法において、 脱 C精練する際に、 脱 C精練するために転炉に装入さ れる当該転炉で脱 P処理された溶湯を、 或いはそれ以外の転炉もし く は類似設備で脱 P処理され予め待機させておいた溶湯を、 当該転 言 1. In the converter-type hot metal pretreatment method for de-P refining and de-C refining of molten metal, when de-C refining is performed, the P-removing process is performed in the converter that is inserted into the converter for de-C refining. The molten metal that has been de-P treated in a converter or other similar equipment and that has been put on standby beforehand
炉に装入して脱 C精練を続行することを特徴とする転炉型溶銑予備 処理方法。 A converter-type hot metal pretreatment method comprising charging the furnace and continuing C-refining.
2 . 転炉内にて溶湯を脱 P精練して出湯した後、 引き続き当該転 炉にて、 脱 P精練された溶湯を脱 C精練する転炉型溶銑予備処理方 法において、  2. In the converter-type hot metal pretreatment method in which the molten metal that has been de-P-refined is de-P-refined in the converter and then de-C-refined in the converter,
脱 C精鍊のために当該転炉に装入される溶湯が、 当該転炉で直前 に脱 P精練して出湯した当該溶湯 (以下、 溶湯 A ) 以外の溶湯 (以 下、 溶湯 B ) であることを特徴とする転炉型溶銑予備処理方法。  The molten metal charged into the converter for de-C refining is a molten metal (hereinafter, “Molten B”) other than the molten metal (hereinafter, “Molten A”) that has just been de-P scoured and discharged from the converter. A converter type hot metal pretreatment method characterized by the above-mentioned.
3 . 脱 C精鍊のために当該転炉に装入される前記溶湯 Bは、 前記 当該溶湯 Aに先立って、 当該転炉にて脱 P精練された溶湯 (以下、 溶湯 A ' ) であることを特徴とする請求項 2に記載の転炉型溶銑予 備処理方法。  3. The molten metal B charged into the converter for de-C refining is a molten metal that has been de-P-refined in the converter prior to the molten metal A (hereinafter, molten metal A '). The converter-type hot metal pretreatment method according to claim 2, characterized in that:
4 . 脱 C精鍊のために当該転炉に装入される前記溶湯 Bは、 他の 転炉にて脱 P精練された溶湯 (以下、 溶湯 C ) であることを特徴と する請求項 2に記載の転炉型溶銑予備処理方法。  4. The molten metal B charged into the converter for de-C refining is a molten metal de-P-refined in another converter (hereinafter, molten metal C). A converter-type hot metal pretreatment method as described in the above.
5 . 転炉内にて溶湯を脱 P精練して出湯した後、 引き続き当該転 炉または他の転炉にて、 脱 P精練された溶湯を脱 C精鍊する転炉型 溶銑予備処理方法において、  5. In the converter type hot metal pretreatment method, after the molten metal is de-P-refined in the converter and the molten metal is discharged, and then the de-P-refined molten metal is de-C-refined in the converter or another converter.
転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉には、 他の 転炉で脱 P精練して出湯した溶湯 (溶湯 C ) を装入して、 脱 C精鍊 を行う とともに、 当該転炉にて脱 P精練して出湯した当該溶湯 (溶 湯 A ) は、 他の転炉に装入して脱 C精練することを特徴とする転炉 型溶銑予備処理方法。 After de-P scouring the molten metal in the converter and tapping, the molten metal (Molten C) de-P scoured and discharged in another converter is charged into the converter, and de-C refining is performed. At the same time, the molten metal (P Hot water A) is a converter-type hot metal pretreatment method characterized in that it is charged into another converter and decarbonized.
6 . 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉または 他の転炉にて、 脱 P精練された溶湯を脱 C精練する転炉型溶銑予備 処理方法において、  6. In the converter-type hot metal pretreatment method in which the molten metal de-P-refined in the converter or another converter is de-C-refined in the converter or another converter after the molten metal is de-P-refined in the converter.
転炉にて脱 P精練して出湯した後、 当該転炉または他の転炉に普 通溶銑を装入し、 普通転炉精練して出鋼した後、 次いで、 脱 P精練 された溶湯を装入して脱 C精練することを特徴とする転炉型溶銑予 備処理方法。  After de-P scouring in the converter and tapping, the hot metal is charged into the converter or another converter, ordinary converter scouring and tapping, and then the de-P scoured molten metal is removed. A converter-type hot metal pretreatment method characterized by charging and decarbonizing.
7 . 転炉內にて溶湯を脱 P精練して出湯した後、 引き続き当該転 炉において、 脱 P精練された溶湯を脱 C精鍊する転炉型溶銑予備処 理方法において、  7. In the converter-type hot metal pretreatment method for de-P refining the molten metal in the converter and discharging the molten metal, and then in the converter, de-P refining the molten metal,
脱 P精練して出湯した後、 引き続き、 当該転炉に普通溶銑を装入 し、 普通転炉精練して出銅した後、 次いで、 当該転炉にて脱 P精鍊 して出湯した溶湯 (溶湯 A ) を装入し、 脱 C精鍊するこ とを特徴と する転炉型溶銑予備処理方法。  After de-P scouring and tapping, the converter is charged with ordinary molten iron, ordinary converter scouring and tapping, and then de-P-refined and discharged from the converter. A) A converter-type hot metal pretreatment method characterized in that A) is charged and decarbonized.
8 . 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉あるい は他の転炉において、 脱 P精練された溶湯を脱 C精鍊する溶銑予備 処理であって、  8. In the converter or other converter, after the molten metal is removed from the molten metal in the converter and the molten metal is discharged, the molten metal is subjected to the de-P refining and the molten metal is de-C-purified.
転炉にて溶湯を脱 P精練して出湯し、 当該溶湯 (溶湯 A ) を他の 転炉に装入して脱 C精練する と ともに、 当該転炉には、 普通溶銑を 装入し、 普通転炉精練して出鋼した後、 次いで、 他の転炉で脱 P精 練した溶湯 (溶湯 C ) を装入し、 脱 C精練を行う ことを特徴とする 転炉型溶銑予備処理方法。  In the converter, the molten metal is de-P scoured and discharged, the molten metal (Molten A) is charged into another converter and de-C refined, and ordinary molten iron is charged into the converter. A converter-type hot metal pretreatment method characterized in that after the steel is refined in a normal converter and the steel is tapped, the molten metal (melt C) that has been de-P-purified in another converter is charged and then de-C-refined. .
9 . 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉または 他の転炉にて、 脱 P精練した溶湯を脱 C精鍊する溶銑予備処理を、 複数の転炉のうちの少なく とも 1つを脱 P用転炉と し、 他の転炉を 脱 C用転炉と して行う専用炉タイプの転炉型溶銑予備処理方法にお いて、 9. After removing the molten metal in the converter and de-pouring the molten metal, the pre-treatment of de-P-refined molten metal in the converter or another converter is performed in the converter. At least one of them is a converter for de-P In the converter-type hot metal pretreatment method of a dedicated furnace type performed as a de-C converter,
脱 P用転炉において、 脱 P精鍊を連続的に行い、 当該脱 P用転炉 の非稼働時間が普通溶銑を普通転炉精練するに要するサイクルタイ ム以上となった時点で、 当該脱 P用転炉で普通転炉精鍊を行う こと を特徴とする転炉型溶銑予備処理方法。  De-P refining is continuously performed in the P-removal converter, and when the non-operating time of the P-removal converter exceeds the cycle time required for ordinary hot metal refining, the P-removal is performed. A converter-type hot metal pretreatment method characterized by performing ordinary converter refining in a converter.
10. 転炉内にて溶湯を脱 P精練して出湯した後、 当該転炉または 他の転炉にて、 脱 P精練した溶湯を脱 C精練する溶銑予備処理を、 複数の転炉のうちの少なく とも 1つを脱 P用転炉と し、 他の転炉を 脱 C用転炉と して行う専用炉タイプの転炉型溶銑予備処理方法にお レ、て、  10. After removing the molten metal in the converter and removing the molten metal from the furnace, the molten iron preliminarily treated in the converter or another converter to remove the molten metal that has been de-P-purified is de-C-refined. At least one of them is a converter for de-P, and the other converter is a converter for de-C.
脱 C用転炉においても脱 P精鍊を行う とともに、 当該脱 C用転炉 には、 当該脱 C用転炉で脱 P精練された溶湯 (溶湯 A ) と、 脱 P用 転炉で脱 P精練された溶湯 (溶湯 C ) とを、 交互に装入して脱 C精 鍊すると ともに、 脱 P用転炉では脱 P精練を行い、 その非稼働時間 には普通溶銑を精練する普通転炉精鍊を行う ことを特徴とする転炉 型溶銑予備処理方法。  The de-P converter is also de-P-refined in the de-C converter, and the molten metal de-P-refined in the de-C converter (melt A) and the de-P converter in the de-P converter are removed. The refined molten metal (Molten C) is charged alternately and de-C-purified, while the de-P converter is de-P-refined, and during the non-operation time, the ordinary converter for refining ordinary molten iron A converter-type hot metal pretreatment method characterized by performing refining.
11 . 前記当該脱 C用転炉に、 前記当該脱 C用転炉で脱 P精練され た溶湯と、 前記脱 P用転炉で脱 P精練された溶湯とを、 交互に装入 して脱 C精練するに際し、  11. The molten metal de-P-refined in the converter for de-C and the molten metal de-P-refined in the converter for de-P are alternately charged into the converter for de-C, and then removed. C
前記脱 C用転炉では、 前記脱 P用転炉で脱 P精練された溶湯 (溶 湯 C ) を脱 C精練した後に、 前記当該脱 C用転炉で脱 P精練された 溶湯 (溶湯 A ' ) を脱 C精練することを特徴とする請求項 10に記載 の転炉型溶銑予備処理方法。  In the converter for removing C, the molten metal (molten metal C) which has been de-P-purified in the converter for removing P is de-C-refined, and then the molten metal (melt A which has been de-P-refined in the converter for removing C is melted. 11. The converter-type hot metal pretreatment method according to claim 10, wherein the ') is subjected to de-C refining.
PCT/JP2002/005563 2001-06-06 2002-06-05 Method of preliminarily processing converter type hot metal WO2002101096A1 (en)

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