JPH052723B2 - - Google Patents

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Publication number
JPH052723B2
JPH052723B2 JP61304970A JP30497086A JPH052723B2 JP H052723 B2 JPH052723 B2 JP H052723B2 JP 61304970 A JP61304970 A JP 61304970A JP 30497086 A JP30497086 A JP 30497086A JP H052723 B2 JPH052723 B2 JP H052723B2
Authority
JP
Japan
Prior art keywords
blowing
slag
converter
hot metal
carbon steel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP61304970A
Other languages
Japanese (ja)
Other versions
JPS63157809A (en
Inventor
Matsuhide Aoki
Kiminori Hajika
Masaki Nitsuta
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 JP30497086A priority Critical patent/JPS63157809A/en
Publication of JPS63157809A publication Critical patent/JPS63157809A/en
Publication of JPH052723B2 publication Critical patent/JPH052723B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 転炉では予備処理炉等で処理した溶銑を対象と
して吹錬を行なうことが多いが、炉修やトラブル
等によつて予備処理を施すことができない場合も
あり、こうした場合は非予備処理溶銑が直接転炉
へ導入されることになる。本発明は、この様に非
予備処理溶銑を転炉で精錬する場合に適用される
転炉吹錬方法に関し、殊に上・底吹き転炉あるい
は底吹き転炉において非予備処理溶銑から中・高
炭素鋼を製造するに当たり優れた脱P性能を発揮
し、中・高炭素鋼の製造を可能にした転炉吹錬方
法に関するものである。 [従来の技術] 転炉吹錬方法には、上吹き法、底吹き法、上・
底吹き法等があるが、このうち底吹き法及び上・
底吹き法は底吹きガスのバブリングによる撹拌力
を利用し得る為精錬性能の優れた吹錬法とされて
いる。 しかるに主としてスラグ−メタル界面で進行す
ると言われている脱P反応については底吹きによ
る撹拌力が必ずしも効果を奏する訳ではなく、低
炭素鋼の製造においては一応満足し得る脱P効果
を得ることができるが、中・高炭素鋼の製造にお
ける底吹き法及び上・底吹き法の脱P性能は後述
する如くそれ程高いものとは言えない。 即ち中・高炭素鋼の製造において脱P能が低下
する理由は、中・高炭素鋼の製造に際してはC−
O平衡の関係から鋼中酸素ポテンシヤルを低くす
る必要があり、酸化能力を示すスラグ中のトータ
ル鉄(FeO、Fe2O3等)も低い値に止める必要が
あるからである。即ち脱P反応は下記反応式で示
されるトータル鉄の酸化能力とCaO活量に依存す
ると言われているが、 2P+5FeO+3CaO =3(CaO・P2O5)+5Fe 中・高炭素鋼の製造では上記の如く酸素ポテン
シヤルの低下に伴なつてスラグのP酸化能力が低
下し、しかもCaO活量を左右する塊状生石灰
(CaO源)の滓化も悪くなつて脱P性能が低下す
るのである。 結局底吹き転炉及び上・底吹き転炉は、脱炭等
の精錬反応には有効であつてもP濃度の高い非予
備処理溶銑から中・高炭素鋼を直接製造するのに
は適しておらず、溶銑予備処理の実施が不可欠と
されている。その為低炭素鋼と中・高炭素鋼の両
者を上・底吹き転炉で製造しなければならない製
鉄所では中・高炭素鋼生産時には底吹きガス流量
をノズルが詰まらない程度まで低下させて実質的
に上吹精錬を行ない、中・高炭素鋼のみを製造す
る製鉄所では底吹き転炉及び上・底吹き転炉の使
用は殆んど行なわれておらず底吹きの効果が享受
されておらない。 [発明が解決しようとする問題点] 本発明はこうした事情に着目してなされたもの
であつて、非予備処理溶銑から中・高炭素鋼を製
造するというプロセスを精錬性能の優れた底吹き
転炉あるいは上・底吹き転炉を使う場合において
実行可能ならしめ得る様な転炉吹錬方法を提供し
ようとするものである。 非予備処理溶銑から中・高炭素鋼を製造するに
当たつて隘路となつているのは、前述の如く脱P
性能の低下であり、脱P性能を向上させる為の手
段についていくつかの提案もなされている。即ち
脱P性能を向上させる考え方としては、前記脱P
反応式から理解される様にスラグ中のトータル
鉄を増大させるか、あるいは塊状生石灰の滓化
を促進させることがあげられ、前者の手段として
はスラグ層へのFeO添加という方法も提案されて
いるが、鋼中炭素を酸化して炭素濃度を低下させ
ることにもなるので中・高炭素鋼の製造において
は好ましい手段とは言えない。一方塊状生石灰の
滓化については、そのメカニズムは次の様に考え
られている。 Siの酸化による低塩基度スラグの生成 塊状生石灰表面での2CaO・SiO2の生成 2CaO・SiO2層のスラグ(液体)への溶解
(律速段階) 高塩基度でのCaOの溶解 そして上記〜の段階のうちが滓化律速段
階であり、滓化速度を高める為にはの溶解速度
を高めることが有効である。こうした観点から
CaF2を添加してスラグの流動性を良くするとい
う手段も提案されている。 本発明は、こうした状況の下塊状生石灰の滓化
を促進する方向で研究を進めた結果Mn酸化物の
添加が有効であるという知見を得、さらに研究を
重ねた結果その完成に至つたものである。 [問題点を解決するための手段] しかして本発明方法は、非予備処理溶銑を対象
として0.03Nm3/t・分以上の底吹きを行ない、
吹止炭素が0.13%以上で吹止スラグ中のトータル
鉄が15%以下となる様に転炉吹錬を行なうに当た
り、 吹錬開始前から全O2の60%を吹込むまでの間
にMn酸化物を装入して吹止スラグ中のMnOを4
〜8%にコントロールする点に要旨を有するもの
である。 [作用] スラグ中へMn酸化物を添加すると、塊生石灰
の融点が降下し、融点降下によつて塊状生石灰の
滓化が促進され、脱P反応速度が上昇する。反応
は吹錬全期間を通じて進行するが、塊生石灰の滓
化が前提となるのでMn酸化物は吹錬全期間うち
全吹込O2量の60%を吹込むまでに添加する必要
があり、吹錬開始後は勿論のこと吹錬開始前に添
加してもよい。Mn酸化物の添加量については、
吹止スラグ中のMnO量を目安に決定することが
でき、吹止スラグ中のMnOが4〜8%となる様
にMn酸化物を添加する必要がある。該MnO量が
4%未満ではMn酸化物の添加が不十分であり脱
P能を十分に高めることができず、一方該MnO
量が8%を超えるとスラグ中のMnOが高くなり
過ぎる為にCaO濃度が低下して却つて脱P能が低
下することになる。尚本発明において添加される
Mn酸化物としてはMn鉱石や鉄Mn鉱石等をあげ
ることができる。 本発明の構成要件は上記の通りであるが、前に
も述べた様に本発明方法は非予備処理溶銑の吹錬
によつて中・鉱炭素鋼を製造する場合に効果を発
揮するものであり、前提としては吹止炭素が0.13
%以上となり、且つ吹止スラグ中のトータル鉄が
15%以下となる様に吹錬を行なう必要がある。又
吹錬は少なくとも底吹きを行なう吹錬方法を採用
する必要があり、底吹き法あるいは上・底吹法が
適用され、底吹きガス量は0.03Nm3/t・分以上
とする必要がある。尚底吹きガス量が0.03m3/
t・分未満の場合にはスロツピングがひどくな
り、鉄ロスが多くなるという問題が生じる。 [実施例] 以下実施例に基づき本発明をさらに説明する。 コンピユーター解析による転炉反応シミユレー
シヨンシステムを用いてSi量が異なる非予備処理
溶銑から吹止炭素が0.13%以上の中・高炭素鋼を
製造する際の副原料投入条件を決定したところ第
1表に示す結果が得られた。尚吹上温度を1675℃
以下、塩基度3.0〜4.4、吹止スラグ中のMnO量を
5%(但し非予備処理溶銑中に含まれるMnO量
を2%)に夫々設定して条件を決定した。
[Industrial field of application] In converters, blowing is often performed on hot metal that has been treated in a pretreatment furnace, etc. However, there are cases where preliminary treatment is not possible due to furnace repairs or troubles, etc. In this case, non-pretreated hot metal will be introduced directly into the converter. The present invention relates to a converter blowing method that is applied when refining non-pretreated hot metal in a converter, and particularly in a top/bottom blowing converter or a bottom blowing converter from non-pretreated hot metal to medium/ The present invention relates to a converter blowing method that exhibits excellent dephosphorous performance in producing high carbon steel and makes it possible to produce medium to high carbon steel. [Conventional technology] Converter blowing methods include top blowing method, bottom blowing method, top blowing method, and top blowing method.
There are bottom blowing methods, among which the bottom blowing method and top blowing method.
The bottom blowing method is considered to be a blowing method with excellent refining performance because it can utilize the stirring power generated by bubbling the bottom blowing gas. However, for the dephosphorization reaction, which is said to proceed mainly at the slag-metal interface, the stirring force of bottom blowing is not necessarily effective, and it is difficult to obtain a satisfactory dephosphorization effect in the production of low carbon steel. However, the dephosphorization performance of the bottom blowing method and the top/bottom blowing method in the production of medium and high carbon steel cannot be said to be very high, as will be described later. In other words, the reason why the dephosphorization ability decreases in the production of medium- to high-carbon steel is that the C-
This is because it is necessary to lower the oxygen potential in the steel due to O equilibrium, and it is also necessary to keep the total iron (FeO, Fe 2 O 3, etc.) in the slag, which indicates oxidizing ability, to a low value. In other words, the dephosphorization reaction is said to depend on the total iron oxidation ability and CaO activity shown by the reaction formula below. As the oxygen potential decreases, the P oxidation ability of the slag decreases, and furthermore, the slag formation of lump quicklime (CaO source), which influences CaO activity, deteriorates, resulting in a decrease in P removal performance. In the end, although bottom-blown converters and top/bottom-blown converters are effective for refining reactions such as decarburization, they are not suitable for directly producing medium- to high-carbon steel from non-pretreated hot metal with a high P concentration. Therefore, the implementation of hot metal pretreatment is considered essential. Therefore, in steel plants that must produce both low carbon steel and medium/high carbon steel in top/bottom blowing converters, when producing medium/high carbon steel, the bottom blowing gas flow rate is reduced to a level that does not clog the nozzle. In ironworks that essentially carry out top-blowing refining and produce only medium- and high-carbon steel, bottom-blowing converters and top/bottom-blowing converters are rarely used, and the effects of bottom-blowing are not enjoyed. I don't have it. [Problems to be Solved by the Invention] The present invention has been made in view of these circumstances, and the present invention has been made by focusing on the above-mentioned circumstances. The purpose of this invention is to provide a converter blowing method that can be carried out when using a furnace or a top/bottom blowing converter. As mentioned above, the bottleneck in producing medium- to high-carbon steel from non-pretreated hot metal is the dephosphorization process.
This is a decrease in performance, and several proposals have been made regarding means for improving P removal performance. In other words, the idea of improving P removal performance is to
As can be understood from the reaction equation, the two methods are to increase the total iron in the slag or to promote the formation of lump quicklime into slag, and for the former method, adding FeO to the slag layer has also been proposed. However, since it also oxidizes the carbon in the steel and lowers the carbon concentration, it cannot be said to be a preferable means for producing medium- to high-carbon steel. On the other hand, the mechanism of turning lump quicklime into slag is thought to be as follows. Generation of low basicity slag by oxidation of Si Generation of 2CaO/SiO 2 on the surface of lump quicklime Dissolution of two layers of 2CaO/SiO into slag (liquid) (rate-limiting step) Dissolution of CaO at high basicity and the above One of these steps is the rate-determining step of slag formation, and in order to increase the sludge formation rate, it is effective to increase the dissolution rate. From this perspective
It has also been proposed to add CaF 2 to improve the fluidity of slag. The present invention was developed as a result of research aimed at promoting the slag formation of lumpy quicklime under such circumstances, and as a result, it was discovered that the addition of Mn oxide was effective, and as a result of further research, it was completed. be. [Means for solving the problems] However, the method of the present invention performs bottom blowing of 0.03 Nm 3 /t・min or more on non-pretreated hot metal,
When performing converter blowing so that the blow-off carbon is 0.13% or more and the total iron in the blow-off slag is 15 % or less, Mn is By charging oxide, the MnO in the blowing slag is
The key point is to control the amount to 8%. [Function] When Mn oxide is added to the slag, the melting point of the lump quicklime is lowered, and the lowering of the melting point promotes slag formation of the lump quicklime, increasing the dephosphorization reaction rate. The reaction progresses throughout the blowing period, but since it is assumed that the lump quicklime turns into slag, Mn oxide must be added during the entire blowing period before 60% of the total amount of O 2 is blown. It may be added not only after the start of refining but also before the start of blowing. Regarding the amount of Mn oxide added,
It can be determined based on the amount of MnO in the blow-off slag, and it is necessary to add Mn oxide so that the MnO content in the blow-off slag is 4 to 8%. If the amount of MnO is less than 4%, the addition of Mn oxide is insufficient and the dephosphorization ability cannot be sufficiently increased;
If the amount exceeds 8%, MnO in the slag becomes too high, resulting in a decrease in CaO concentration and a decrease in P removal ability. In addition, added in the present invention
Examples of Mn oxide include Mn ore and iron-Mn ore. The constituent elements of the present invention are as described above, but as stated earlier, the method of the present invention is effective in producing medium- and mineral-carbon steel by blowing non-pretreated hot metal. Yes, the assumption is that the blow-off carbon is 0.13
% or more, and the total iron in the blowstop slag is
It is necessary to carry out blowing so that it is less than 15%. In addition, it is necessary to adopt a blowing method that performs at least bottom blowing, and the bottom blowing method or top/bottom blowing method is applied, and the amount of bottom blowing gas needs to be 0.03 Nm 3 /t・min or more. . Furthermore, the amount of bottom-blown gas is 0.03m 3 /
When the time is less than t.minutes, the problem arises that slopping becomes severe and iron loss increases. [Examples] The present invention will be further described below based on Examples. Using a converter reaction simulation system based on computer analysis, we determined the conditions for inputting auxiliary materials when producing medium- to high-carbon steel with a blowout carbon of 0.13% or more from non-pretreated hot metal with different amounts of Si. The results shown in Table 1 were obtained. Furthermore, the blowing temperature is 1675℃
The conditions were determined by setting the basicity to 3.0 to 4.4 and the amount of MnO in the blow-off slag to 5% (however, the amount of MnO contained in the non-pretreated hot metal was 2%).

【表】 実験1 第1表の副原料投入条件に基づいて造滓条件を
定め、第2表に示す溶銑(85t)の転炉吹錬を行
なつたところ、第2表に示す結果が得られた。一
方従来の造滓条件で同じ成分組成の溶銑の転炉吹
錬を行ない、その結果を上記実施例と比較した。
[Table] Experiment 1 The slag making conditions were determined based on the auxiliary material input conditions in Table 1, and the hot metal (85 tons) shown in Table 2 was subjected to converter blowing, and the results shown in Table 2 were obtained. It was done. On the other hand, hot metal having the same composition was subjected to converter blowing under conventional slag-making conditions, and the results were compared with those of the above examples.

【表】【table】

【表】 第2表に示す様に本発明に係る造滓条件を採用
することにより、造滓剤コストは余り低減できな
くともMn歩留りが向上し、次の様な効果が得ら
れた。即ち本発明では脱P反応促進の為に投入す
るMn鉱石が鋼中のMn量を高める結果となり、
転炉吹錬後改めてFe−Mnを添加する必要がな
く、この分のFe−Mnコストの削減及びアーク炉
でFe−Mnを溶解する為に要するアーク電力コス
トの削減が経済的に大きな効果を上げる要因とな
つている。 実験2 非予備処理溶銑を下記造滓条件で吹錬し、本発
明方法の脱S結果及び脱P結果を調べたところ第
1,2図に示す結果が得られた。比較例として同
じ溶銑を従来の造滓条件で吹錬した場合の結果を
併記した。尚吹止温度は1675℃以下、吹止炭素は
0.15〜0.40%とした。又吹錬終了後スラグを鎮静
化させる為炉を対向方向に2回振幅させ、出鋼開
始時炉口からのスラグの流出を防止した。 第1図に示す様に脱Sに関しては実施例の方が
比較例より僅かに優れている程度で殆んど差がな
かつた。 一方脱Pに関しては、実施例の方が吹止P濃度
を低下させており、本発明方法の脱P効果の優れ
ていることを確認することができた。 [発明の効果] 本発明は以上の様に構成されており、従来脱P
能の点で問題のあつた中・高炭素鋼の底吹きある
いは上・底吹き転炉吹錬において十分な脱P効果
をあげることに成功し、転炉において非予備処理
溶銑から中・高炭素鋼を生産することが可能とな
つた。
[Table] As shown in Table 2, by adopting the slag-forming conditions according to the present invention, the Mn yield was improved even though the slag-forming agent cost could not be reduced much, and the following effects were obtained. That is, in the present invention, the Mn ore added to promote the dephosphorization reaction increases the amount of Mn in the steel,
There is no need to add Fe-Mn again after converter blowing, and the reduction in Fe-Mn cost and the arc power cost required to melt Fe-Mn in an arc furnace have great economic effects. This is a contributing factor to the increase. Experiment 2 Non-pretreated hot metal was blown under the following slag making conditions, and the results of S removal and P removal using the method of the present invention were investigated, and the results shown in FIGS. 1 and 2 were obtained. As a comparative example, the results obtained when the same hot metal was blown under conventional slag forming conditions are also shown. The blow-off temperature is below 1675℃, and the blow-off carbon is
It was set at 0.15-0.40%. In addition, after blowing, the furnace was oscillated twice in opposite directions to calm down the slag, thereby preventing slag from flowing out from the furnace mouth when tapping started. As shown in FIG. 1, in terms of S removal, the Examples were slightly superior to the Comparative Examples, with almost no difference. On the other hand, regarding P removal, the Example lowered the blowout P concentration, confirming that the method of the present invention has an excellent P removal effect. [Effect of the invention] The present invention is configured as described above, and conventionally
We succeeded in achieving a sufficient dephosphorization effect in bottom-blowing or top- and bottom-blowing converter blowing of medium- and high-carbon steels, which had problems in terms of performance, and have successfully removed medium- and high-carbon steel from non-pretreated hot metal in converters. It became possible to produce steel.

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

第1図は実施例方法と従来方法の脱S結果を示
すグラフ、第2図は実施例方法と従来方法の脱P
結果を示すグラフである。
Figure 1 is a graph showing the S removal results of the example method and the conventional method, and Figure 2 is a graph showing the P removal results of the example method and the conventional method.
It is a graph showing the results.

Claims (1)

【特許請求の範囲】 1 非予備処理溶銑を対象として0.03Nm3/t・
分以上の底吹きを行ない、吹止炭素が0.13%以上
で吹止スラグ中のトータル鉄が15%以下となる様
に転炉吹錬を行なうに当たり、 吹錬開始前から全O2の60%を吹込むまでの間
にMn酸化物を装入して吹止スラグ中のMnOを4
〜8%にコントロールすることを特徴とする転炉
吹錬方法。
[Claims] 1. 0.03Nm 3 /t・ for non-pretreated hot metal
When converter blowing is performed by bottom blowing for more than 10 minutes, and the blow-off carbon is 0.13% or more and the total iron in the blow-off slag is 15% or less, 60% of the total O 2 is emitted before the start of blowing. Before blowing, Mn oxide is charged to remove MnO in the blowing slag.
A converter blowing method characterized by controlling the temperature to ~8%.
JP30497086A 1986-12-19 1986-12-19 Blowing method for converter Granted JPS63157809A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30497086A JPS63157809A (en) 1986-12-19 1986-12-19 Blowing method for converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30497086A JPS63157809A (en) 1986-12-19 1986-12-19 Blowing method for converter

Publications (2)

Publication Number Publication Date
JPS63157809A JPS63157809A (en) 1988-06-30
JPH052723B2 true JPH052723B2 (en) 1993-01-13

Family

ID=17939500

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30497086A Granted JPS63157809A (en) 1986-12-19 1986-12-19 Blowing method for converter

Country Status (1)

Country Link
JP (1) JPS63157809A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3312536B2 (en) * 1995-08-25 2002-08-12 住友金属工業株式会社 Hot metal dephosphorization method
CN103555879B (en) * 2013-10-21 2015-01-21 莱芜钢铁集团有限公司 Control method for reducing total iron content of SPHC (steel plate heat commercial) final slag
DE102017104351A1 (en) 2017-03-02 2018-09-06 Cl Schutzrechtsverwaltungs Gmbh Device for the additive production of three-dimensional objects

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JPS58167707A (en) * 1982-03-29 1983-10-04 Nippon Kokan Kk <Nkk> Method of smelting high-carbon steel by top and bottom-blown converter

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