JPS6140013B2 - - Google Patents
Info
- Publication number
- JPS6140013B2 JPS6140013B2 JP56158115A JP15811581A JPS6140013B2 JP S6140013 B2 JPS6140013 B2 JP S6140013B2 JP 56158115 A JP56158115 A JP 56158115A JP 15811581 A JP15811581 A JP 15811581A JP S6140013 B2 JPS6140013 B2 JP S6140013B2
- Authority
- JP
- Japan
- Prior art keywords
- blowing
- converter
- furnace
- diameter
- bottom blowing
- 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
Links
- 238000007664 blowing Methods 0.000 claims description 54
- 238000010079 rubber tapping Methods 0.000 claims description 5
- 230000001133 acceleration Effects 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000011449 brick Substances 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 238000011161 development Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 210000001015 abdomen Anatomy 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000013016 damping Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 238000005261 decarburization Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/42—Constructional features of converters
- C21C5/46—Details or accessories
- C21C5/48—Bottoms or tuyéres of converters
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
Description
この発明は、底吹き機能をもつ転炉に関するも
のである。
ここに底吹き機能をもつ転炉というのは、炉底
羽口を有し、この炉底羽口を通して酸化性ガスお
よび/又は溶融金属に対して事実上不活性なN2
やArなどを、LD転炉におけるような上吹きラン
スによる酸化性ガスとともに吹込むいわゆる上底
吹き転炉、および炉底羽口のみからの上記吹込み
を行う底吹き転炉の如き、精錬容器を指すものと
する。
上例に掲げた種類の転炉での吹錬中、炉内装入
物は激しく撹拌される故、製鋼精錬の際にはスラ
グ中の鉄分濃度(T・Fe)がLD転炉に比較して
著しく低くなり鉄歩留りが向上する利点に加えて
とくに低炭域での脱炭速度も高く、さらに脱硫能
にもすぐれるなどの長所をもたらすが、その反面
で炉底羽口から吹込まれるガスによる撹拌作用の
ために装入浴に一定周期の強い振動を伴うので、
転炉本体の据付けに振動防止対策が必要である。
そこで底吹き専用に設置された転炉にあつて
は、転炉の支持架構として各種の方策が講じられ
ていたのに反し在来のLD転炉では通常上記のよ
うな振動を生じないため、これに底吹き機能をも
たせて、いわゆる上底吹き併用の操業を行おうと
するとき、底吹き転炉におけるような振動防止対
策を欠き、ここに支持架構の改造を施すには莫大
な費用が嵩むので、LD転炉を、上底吹き転炉と
して活用する妨げとなつていたのであり、その改
造なしに転用を強行したとすると、その支持架構
は激しい振動に耐え得ずして炉体破損や、耐久性
の劣化が余儀なくされて、重大な事故を招くおそ
れがある。
この発明は、上記のような底吹き機能をもつ転
炉に特有な吹錬振動を、とくに有利に防止するこ
とによつて、LD転炉における上底吹き併用吹錬
への転用を容易ならしめ、また底吹き転炉の設置
に当つてはその堅固な据付けを不用ならしめ得る
操業方法について開発成果を提案しようとするも
のである。
ここに底吹き機能をもつ転炉における激しい振
動は、装入浴に生じる強力な撹拌に基く振動を主
要な外力とする強制振動であり、そこで炉内装入
浴振動の低減こそが、転炉の振動の抑制を結果す
ると考え、撹拌作用の減退を伴わない装入浴の振
動の軽減を図ることが、第1発明の目的である。
次に上に触れたLD転炉に底吹き機能を付加し
ようとするとき、その炉体のプロフイルは、底吹
き転炉につき第1図に示すように炉腹が、背丈に
比べて広いのに反して一般に第2図のように炉腹
の狭い胴長をなすので、その溶銑装入のための傾
動姿勢において底吹き羽口が浸漬され、底吹きガ
スの供給に至るまでの間に炉体損耗を生じる原因
となり、とくにステンレス鋼の吹錬操業ではクロ
ム損失を回避すべく浴深を大きくすることが有利
とされ、ここに上記羽口浸漬による難点が一層か
酷になるところ、かような問題点を、上記転炉振
動の抑制にあわせ、有利に回避することが、第2
発明の目的である。
この発明は炉底で互いに間隔をおき列状をなし
て開口する複数の底吹き羽口を、炉体のトラニオ
ン軸と平行な炉底径に対しその0.025〜0.1倍に相
当する距りをおき、かつ炉底径0.75倍以内に納ま
る配列領域幅で、偏心配置することを、上記基本
的な問題点の解決手段とするものであり、またそ
の偏心配置をとくに炉体の出鋼側に偏らせること
を第2の問題点に対する点服手段とするものであ
り、何れの場合も、底吹き羽口の配列領域幅を、
炉底径の0.2倍以上にすること、該羽口を一直線
上配列とすることが実施態様としてのぞましいと
ころである。
上述偏心配置は、以下その開発経過と、その実
炉操業への展開について詳しく述べるとおり、転
炉の制振に関してとくに有利に奏効することの実
験上の知見に由来し、とくに炉体の出鋼側への偏
心は、転炉の装入の際に出鋼側つまり出鋼孔のあ
る側を上にし炉体が傾動されるので、このとき底
吹き羽口には、装入浴面に対してより距ることに
なるからそれによる浸漬が有効に回避され得るわ
けである。
発明者らは、この発明の開発研究に当り、まず
水を溶融金属に見たてて、いわゆる転炉の水モデ
ル実験により、底吹き羽口の配列と、炉の形状と
に関連して、浴の振動挙動が異なることの知見を
得、これにつき、ホツトモデル、実炉の測定結果
により確認を行つた。
さて80トン底吹き転炉の1/20相当の縮小、水モ
デルにおいて、透明アクリル樹脂製モデル水槽内
に生じる浴の振動挙動を、上吹き153/min、底
吹き51/minの同時吹込みを行なつた場合につ
き第3図に示した内径Dが365mmの水槽底壁に、
その直径に対する距りが種々に異なる数本の噴
気管を、種々な配列領域幅Lにわたつて配置し、
モデル水槽に生じる振動の加速度の計測を行つて
次表に示す成績を得た。
The present invention relates to a converter having a bottom blowing function. A converter with a bottom-blowing function has a bottom tuyere through which N 2 , which is virtually inert to oxidizing gases and/or molten metal, is pumped.
Refining vessels, such as so-called top-bottom-blown converters, in which oxidizing gas and Ar are blown in together with oxidizing gas by a top-blowing lance, as in an LD converter, and bottom-blown converters, in which the above-mentioned gas is blown only from the bottom tuyere. shall refer to. During blowing in a converter of the type mentioned above, the contents in the furnace are vigorously stirred, so during steelmaking and refining, the iron concentration (T Fe) in the slag is lower than that in an LD converter. In addition to the advantage of significantly lower iron yield and improved iron yield, the decarburization rate is particularly high in the low coal range, and it also has excellent desulfurization ability. Because the charging bath is accompanied by strong vibrations at a constant period due to the stirring action of
Vibration prevention measures are required when installing the converter main body. Therefore, in the case of converters installed exclusively for bottom blowing, various measures were taken to support the converter, whereas conventional LD converters usually do not produce the above-mentioned vibrations. When adding a bottom blowing function to this converter and attempting to perform a combined top and bottom blowing operation, it lacks the vibration prevention measures of a bottom blowing converter, and the cost of modifying the support structure increases enormously. This hindered the use of the LD converter as a top-bottom blowing converter, and if conversion were to be carried out without modification, the support frame would not be able to withstand the intense vibrations, leading to damage to the furnace body. , durability may inevitably deteriorate, leading to a serious accident. This invention facilitates conversion to top and bottom blowing combined blowing in an LD converter by particularly advantageously preventing the blowing vibrations that are characteristic of converters with a bottom blowing function as described above. In addition, we will propose the results of the development of an operating method that can eliminate the need for solid installation when installing a bottom-blowing converter. The severe vibrations in a converter with a bottom-blowing function are forced vibrations whose main external force is the vibration caused by the strong stirring that occurs in the charging bath, so reducing the bathing vibration inside the furnace is the key to reducing converter vibration. It is an object of the first invention to reduce the vibration of the charging bath without reducing the stirring action. Next, when trying to add a bottom-blowing function to the LD converter mentioned above, the profile of the furnace body is such that the bottom-blowing converter has a wide belly compared to its height, as shown in Figure 1. On the other hand, as shown in Figure 2, the furnace belly generally has a narrow body length, so the bottom blowing tuyeres are immersed in the tilted position for charging hot metal, and the furnace body is immersed until the bottom blowing gas is supplied. In order to avoid loss of chromium, especially in stainless steel blowing operations, it is considered advantageous to increase the depth of the bath. The second problem is to advantageously avoid this problem by suppressing the converter vibration.
This is the object of the invention. In this invention, a plurality of bottom blowing tuyeres opened in a row at intervals from each other in the furnace bottom are spaced at a distance corresponding to 0.025 to 0.1 times the furnace bottom diameter parallel to the trunnion axis of the furnace body. The solution to the above basic problem is to use eccentric arrangement with an arrangement area width that is within 0.75 times the diameter of the furnace bottom. The solution to the second problem is to
It is desirable that the diameter be at least 0.2 times the furnace bottom diameter, and that the tuyeres be arranged in a straight line. The above-mentioned eccentric arrangement is derived from experimental findings that it is particularly effective in damping converter vibrations, as will be described in detail below regarding its development progress and its application to actual furnace operation. Eccentricity is caused by the fact that when charging the converter, the furnace body is tilted with the tapping side, that is, the side with the tapping hole, facing up. Therefore, immersion due to this can be effectively avoided. In researching the development of this invention, the inventors first compared water to molten metal and conducted a so-called converter water model experiment to determine the arrangement of the bottom blowing tuyere and the shape of the furnace. We obtained the knowledge that the vibration behavior of the baths is different, and confirmed this using the hot model and the measurement results of the actual furnace. Now, in the water model, which is equivalent to 1/20 scale down of the 80-ton bottom blowing converter, the vibration behavior of the bath that occurs in the transparent acrylic resin model water tank is simulated by simultaneous top blowing of 153/min and bottom blowing of 51/min. In this case, on the bottom wall of the aquarium with an inner diameter D of 365 mm as shown in Figure 3,
Several fumarole pipes with various distances to their diameters are arranged over various array area widths L,
We measured the acceleration of vibrations occurring in the model aquarium and obtained the results shown in the table below.
【表】【table】
【表】
この基礎実験の結果を踏まえ、そこにL/Dが
0.75以下で、/Dは0.025〜0.10となる各場合に
加速度が最小となることから、第2図に示した5
トン上、底吹き実験転炉を用い、次の条件で試験
吹錬を行つた。
炉底径D100mmの炉底壁1を底吹き転炉におけ
る慣例に従つて脱着自在とし、Lおよびの値が
種々に異なるように底吹き羽口2をカセツト式と
して差換えを行い、この底吹き羽口2は、内径8
mmφの2重管羽口を用いて底吹き酸素量は5.0N
m3/min、また上吹きランス3により上吹き酸素
量7.5Nm3/minに定め、吹錬開始後7〜8分間で
振動加速度の計測を、炉体トラニオン軸と平行な
向きで行い、かつ同時に各吹錬後における出鋼側
およびトラニオン側のれんが損耗量も測定した。
第2図において4は溶銑、5はスラグ、そして
6は吹錬火点を示す。なお対応番号を第1図の底
吹き転炉の場合に共通に用いて対応させた。また
第4図には溶銑装入のための傾動姿勢を示し、7
は出鋼孔である。
各試験吹錬の結果を、L/D0.575の場合に/D
が加速度および出鋼側れんが損耗量に及ぼす影響
を第5図にまとめて示し、また/D0.025〜0.10
の範囲にわたつてL/Dが加速度およびトラニオン
側れんが損耗量にもたらす傾向をまとめて第6図
にあらわした。
まず第5図の/Dの変動に伴加速度の推移を
みると、/D=0、すなわち底吹き羽口2を炉
底の直径上に沿つて配列したとき加速度は約
0.04Gであるが/D=0.025に偏心させるとそれ
が0.1に達するまでの間、約0.02Gに半減してほぼ
一定値を示すが/Dが0.1をこえると0.15に至つ
て0.05Gをこれるまで急増する。一方出鋼側のれ
んが損耗量についても/Dが0.1をこえ0.15に至
る間に急増するが/D≦0.1においては1.5mm/ヒ
ートに達しない程度に軽微である。
次に第6図によればL/Dの加速度およびトラニ
オン側れんが損耗に及ぼす影響は、L/Dが0.75を
こえると、0.75までのときに比べて著しく急増す
ることが確認された。
以上の確認実験に従つて上述水モデル実験の制
振成績が、実炉操業にほぼそのまま反映されて、
この発明に従い、炉体振動の有効な低減が、元来
胴長のLD転炉に底吹き機能を付加した場合にお
いてすら、確実にもたらされ得ることが験証され
たのである。なお底吹き羽口の配列は第3図に示
した一直線上の場合だけでなく、いわゆるちどり
配列であつてもほぼ同様な結果が得られる。
従つて第1発明によれば、底吹き転炉での活用
によつてそこに激しい振動に耐えるための支持架
構および基礎の簡略化が可能であり、またLD転
炉に底吹き機能を付加する上底吹き吹錬のために
従来必要とされた支持架構の補強を事実上不要な
らしめる点において、転炉の振動抑制に著しい卓
効が、炉体に生じる損耗の著しい低減にあわせも
たらされる。
また第2発明によれば、さらに炉体の装入傾動
姿勢下に装入浴面から底吹き羽口を有利に離隔し
その浸漬による消耗を有利に回避できるので、ス
テンレス鋼の吹錬にも、よく適合し得る著効が、
さらに加わる。[Table] Based on the results of this basic experiment, L/D is
0.75 or less, the acceleration is minimum in each case where /D is 0.025 to 0.10.
Test blowing was conducted using a top and bottom blowing experimental converter under the following conditions. The furnace bottom wall 1 with a furnace bottom diameter D100 mm is made removable according to the customary practice in bottom-blowing converters, and the bottom-blowing tuyere 2 is replaced with a cassette type so that the values of L and are different. Port 2 has an inner diameter of 8
Bottom-blown oxygen amount is 5.0N using mmφ double tube tuyeres.
m 3 /min, and the top blowing oxygen amount was set at 7.5 Nm 3 /min using the top blowing lance 3, and the vibration acceleration was measured in a direction parallel to the furnace trunnion axis for 7 to 8 minutes after the start of blowing. At the same time, the amount of brick wear on the tapping side and trunnion side after each blowing was also measured. In FIG. 2, 4 indicates hot metal, 5 indicates slag, and 6 indicates the blowing point. Note that the corresponding numbers are commonly used in the case of the bottom blowing converter shown in Fig. 1. Figure 4 also shows the tilting posture for charging hot metal.
is the tap hole. The results of each test blowing are /D in the case of L/D0.575.
Figure 5 summarizes the influence of the
Figure 6 summarizes the trends that L/D has on acceleration and trunnion side brick wear over the range of . First, looking at the transition of acceleration as /D changes in Figure 5, when /D=0, that is, when the bottom blowing tuyeres 2 are arranged along the diameter of the hearth bottom, the acceleration is approximately
0.04G, but when eccentricity is set to /D=0.025, until it reaches 0.1, it is halved to about 0.02G and remains almost constant, but when /D exceeds 0.1, it reaches 0.15 and becomes 0.05G. It will rapidly increase until it reaches On the other hand, the amount of loss of bricks on the tapping side increases rapidly when /D exceeds 0.1 and reaches 0.15, but when /D≦0.1, it is so slight that it does not reach 1.5 mm/heat. Next, according to FIG. 6, it was confirmed that the influence of L/D acceleration and trunnion side brick wear significantly increases when L/D exceeds 0.75 compared to when L/D exceeds 0.75. According to the above confirmation experiment, the damping results of the water model experiment described above are reflected almost directly in the actual reactor operation.
According to this invention, it has been experimentally verified that an effective reduction in furnace vibration can be reliably brought about even when a bottom blowing function is added to an originally long-boiled LD converter. It should be noted that almost the same results can be obtained not only when the bottom blowing tuyeres are arranged in a straight line as shown in FIG. Therefore, according to the first invention, when used in a bottom blowing converter, it is possible to simplify the support structure and foundation to withstand severe vibration therein, and also to add a bottom blowing function to the LD converter. In that the reinforcement of the support frame conventionally required for top-bottom blowing is virtually unnecessary, a remarkable effect on vibration suppression of the converter is brought about as well as a marked reduction in wear and tear on the furnace body. Further, according to the second invention, the bottom blowing tuyere is advantageously separated from the charging bath surface under the charging tilting posture of the furnace body, and wear due to immersion can be advantageously avoided, so that it is also possible to blow stainless steel. The effects that can be well matched are
More will be added.
第1図は、底吹き転炉の断面図、第2図はLD
転炉炉体を活用する上底吹き転炉の断面図、第3
図は炉底の平面図、また第4図は装入傾動姿勢を
示す断面図であり、第5図、第6図はそれぞれ
/D、L/Dが炉体振動の加速度、炉壁損耗に及
ぼす影響を示すグラフである。
1……炉底、2……羽口、3……ランス、…
…距り、L……配列領域幅、D……炉底径。
Figure 1 is a cross-sectional view of a bottom blowing converter, Figure 2 is a LD
Cross-sectional view of a top-bottom blowing converter utilizing a converter body, Part 3
Figure 4 is a plan view of the bottom of the furnace, Figure 4 is a sectional view showing the tilted charging posture, and Figures 5 and 6 are respectively
It is a graph showing the influence of /D and L/D on the acceleration of furnace body vibration and furnace wall wear. 1... Hearth bottom, 2... Tuyere, 3... Lance,...
...distance, L... array area width, D... hearth bottom diameter.
Claims (1)
る複数の底吹き羽口を、炉体のトラニオン軸と平
行な炉底径に対し、その0.025〜0.10倍に相当す
る距りをおき、かつ炉底径の0.75倍以内に納まる
配列領域幅で偏心配置したことを特徴とする底吹
き転炉。 2 複数の底吹き羽口の配列領域幅が炉底径の
0.2倍以上である特許請求の範囲1記載の転炉。 3 複数の底吹き羽口が、一直線上配列である特
許請求の範囲1または2記載の転炉。 4 炉底で互いに間隔をおき列状をなして開口す
る複数の底吹き羽口を、炉体のトラニオン軸と平
行な炉底径に対し炉体の出鋼側に偏つて、該炉底
径の0.025〜0.10倍に相当する距りをおき、かつ
炉底径の0.75倍以内に納まる配列領域幅で、偏心
配置したことを特徴とする底吹き転炉。 5 複数の底吹き羽口の配列領域幅が炉底径の
0.2倍以上である特許請求の範囲4記載の転炉。 6 複数の底吹き羽口が、一直線上配列である特
許請求の範囲4または5記載の転炉。[Scope of Claims] 1. A plurality of bottom blowing tuyere openings in a row at intervals from each other at the furnace bottom are provided with a diameter corresponding to 0.025 to 0.10 times the furnace bottom diameter parallel to the trunnion axis of the furnace body. A bottom-blowing converter is characterized in that it is eccentrically arranged with a distance between the two and an arrangement area width that is within 0.75 times the furnace bottom diameter. 2 The width of the array area of multiple bottom blowing tuyeres is equal to the furnace bottom diameter.
The converter according to claim 1, which is 0.2 times or more. 3. The converter according to claim 1 or 2, wherein the plurality of bottom blowing tuyeres are arranged in a straight line. 4 A plurality of bottom blowing tuyeres opened in a row at intervals from each other at the furnace bottom are biased toward the tapping side of the furnace body with respect to the furnace bottom diameter parallel to the trunnion axis of the furnace body, and the furnace bottom diameter is 1. A bottom-blowing converter characterized in that the bottom blowing converter is eccentrically arranged with a distance equivalent to 0.025 to 0.10 times the diameter of the hearth and an array area width within 0.75 times the hearth bottom diameter. 5 The width of the arrangement area of multiple bottom blowing tuyeres is equal to the furnace bottom diameter.
The converter according to claim 4, which is 0.2 times or more. 6. The converter according to claim 4 or 5, wherein the plurality of bottom blowing tuyeres are arranged in a straight line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15811581A JPS5861212A (en) | 1981-10-06 | 1981-10-06 | Converter having bottom blowing function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15811581A JPS5861212A (en) | 1981-10-06 | 1981-10-06 | Converter having bottom blowing function |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5861212A JPS5861212A (en) | 1983-04-12 |
| JPS6140013B2 true JPS6140013B2 (en) | 1986-09-06 |
Family
ID=15664625
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15811581A Granted JPS5861212A (en) | 1981-10-06 | 1981-10-06 | Converter having bottom blowing function |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5861212A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5282396B2 (en) * | 2007-11-30 | 2013-09-04 | Jfeスチール株式会社 | Top-bottom blowing converter |
-
1981
- 1981-10-06 JP JP15811581A patent/JPS5861212A/en active Granted
Non-Patent Citations (3)
| Title |
|---|
| ARCH EISENHUTTENWES * |
| IRONMAKING AND STEELMAKING * |
| THE COMBINATION PROCESS A NEW DEVELOPMENT FOR STEELMAKING=1981 * |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5861212A (en) | 1983-04-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3953199A (en) | Process for refining pig iron | |
| JP2010070815A (en) | Ladle for refining molten steel and method for refining molten steel | |
| JPS6140013B2 (en) | ||
| FI67094C (en) | FOERFARANDE FOER ATT FOERHINDRA ATT SLAGGMETALL VAELLER UPP VI PNEUMATISK UNDER YTAN SKEENDE RAFFINERING AV STAOL | |
| JP2729458B2 (en) | Melting method of low nitrogen steel using electric furnace molten steel. | |
| EP0060305B1 (en) | Method for smelting using top-and bottom-blown converter | |
| JP2582316B2 (en) | Melting method of low carbon steel using vacuum refining furnace | |
| JP6874904B2 (en) | Top bottom blown converter type refining container | |
| JPS6210284B2 (en) | ||
| US4726033A (en) | Process to improve electric arc furnace steelmaking by bottom gas injection | |
| KR100225249B1 (en) | Remaining slag control method of of slopping control | |
| JPS6050842B2 (en) | Method for preventing slopping in top-bottom blowing converter | |
| US3782921A (en) | Production of steel with a controlled phosphorus content | |
| RU2214458C1 (en) | Method of production of steel in steel-making unit | |
| JPS5867815A (en) | Preventing method for vibration in blow refining by converter with bottom blow function | |
| JPS6152212B2 (en) | ||
| JP2551013B2 (en) | AOD furnace | |
| JPS6140012B2 (en) | ||
| JPS63235416A (en) | How to prevent slopping | |
| JP2005325394A (en) | Method for refining chromium-containing molten steel | |
| JP3282487B2 (en) | Manufacturing method of enamel steel | |
| JP4211631B2 (en) | Method for preventing melting of metal hearth of converter reactor | |
| JPH08311521A (en) | Melting method of steel scrap | |
| Webster et al. | Side-blow converter process for the production of low nitrogen steel ingots | |
| JP5460436B2 (en) | Dephosphorization method |