JPH03281720A - Production of dead-soft carbon steel - Google Patents
Production of dead-soft carbon steelInfo
- Publication number
- JPH03281720A JPH03281720A JP8229290A JP8229290A JPH03281720A JP H03281720 A JPH03281720 A JP H03281720A JP 8229290 A JP8229290 A JP 8229290A JP 8229290 A JP8229290 A JP 8229290A JP H03281720 A JPH03281720 A JP H03281720A
- Authority
- JP
- Japan
- Prior art keywords
- blowing
- inert gas
- gas
- vacuum
- molten 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.)
- Pending
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 239000010962 carbon steel Substances 0.000 title abstract 3
- 229910021384 soft carbon Inorganic materials 0.000 title abstract 3
- 239000007789 gas Substances 0.000 claims abstract description 36
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 34
- 239000010959 steel Substances 0.000 claims abstract description 34
- 239000011261 inert gas Substances 0.000 claims abstract description 25
- 238000007664 blowing Methods 0.000 claims abstract description 24
- 238000009849 vacuum degassing Methods 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims abstract description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 5
- 238000007670 refining Methods 0.000 claims abstract description 5
- 229910001209 Low-carbon steel Inorganic materials 0.000 claims description 10
- 230000001105 regulatory effect Effects 0.000 abstract description 3
- 238000005261 decarburization Methods 0.000 description 18
- 238000002347 injection Methods 0.000 description 7
- 239000007924 injection Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000011465 paving brick Substances 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 229910000532 Deoxidized steel Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】
「産業上の利用分野」
本発明は微圧下精錬装置を用いた極低炭素鋼の製造方法
に関するものである。DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a method for producing ultra-low carbon steel using a micro-pressure refining apparatus.
「従来の技術」
従来、極低炭素鋼の製造方法としては、RH環流方式の
真空脱ガス処理装置を用いて、未脱酸溶鋼中に不活性ガ
スを吹き込み、溶鋼を真空槽内に循環させることにより
溶鋼中の脱炭が行なわれてきた。このような、溶鋼の処
理に際して脱炭反応効率の向上のために浸漬管径拡大、
環流Arガス流量の増加による溶鋼環流量の増大化を図
ると共に、溶鋼の撹拌力を増大せしめることに重点が置
かれ、その例として特開昭57−110611号公報記
載の真空脱ガス処理装置が知られている。"Conventional technology" Conventionally, as a manufacturing method for ultra-low carbon steel, an RH circulation type vacuum degassing treatment device is used to blow inert gas into undeoxidized molten steel and circulate the molten steel in a vacuum chamber. This has led to decarburization in molten steel. In order to improve the decarburization reaction efficiency when processing molten steel, the diameter of the immersion pipe is increased.
Emphasis has been placed on increasing the flow rate of molten steel by increasing the flow rate of circulating Ar gas, as well as increasing the stirring power of the molten steel. As an example, a vacuum degassing treatment device described in JP-A-57-110611 has been developed. Are known.
この装置は第4図に示すように真空槽8の底部でしかも
浸漬管9A、9Bの槽開口端間の位置に気体噴出口11
を設けた装置であり、真空槽内の溶鋼量(高さ)を50
0〜1000mmに増大させた条件下で気体噴出口11
より、500〜2000Np、/sinのAr等不活性
ガス及び中性又は酸化性のフラックスを溶鋼中に吹き込
むことにより、溶鋼2の粒滴化を促進すると共に、真空
槽内に露出する面積を増大させ、これにより脱炭等を有
効に促進せしめようとするものである。As shown in FIG. 4, this device has a gas jet port 11 located at the bottom of a vacuum tank 8 and between the open ends of the tank 9A and 9B.
The amount of molten steel (height) in the vacuum chamber is 50
The gas outlet 11 under the condition of increasing from 0 to 1000 mm.
By injecting 500 to 2000 Np/sin of an inert gas such as Ar and a neutral or oxidizing flux into the molten steel, the molten steel 2 is promoted to form droplets and the exposed area in the vacuum chamber is increased. This is intended to effectively promote decarburization.
[発明が解決しようとする課題」
前記の従来技術の極低炭素鋼の製造装置では、脱炭効率
を高めるためには(具体的には脱炭処理時間の短縮及び
極低炭素鋼到達濃度の低減)、真空槽内溶鋼量を増加さ
せた条件下で気体噴出口11から吹き込むガス流量を増
加させて、溶鋼の反応領域を拡大させる方法を採ってい
る。しかしこの方法では、脱炭反応促進のための吹き込
みガス流量には上限が有り、その上限を越えるとガスの
吹き抜けが生じ、逆に溶鋼との反応領域が減少してしま
う。このように(環流)溶鋼底部でしかも開口端から不
活性ガスを吹き込む手法は、ガスの吹き抜けが生じない
ようなガス流量の上限があるため、脱炭効率向−Fに限
界があると共に、真空槽底。[Problems to be Solved by the Invention] In the conventional ultra-low carbon steel production equipment described above, in order to increase the decarburization efficiency (specifically, to shorten the decarburization treatment time and to reduce the concentration achieved in ultra-low carbon steel) (reduction), the amount of molten steel in the vacuum chamber is increased, and the flow rate of gas blown from the gas outlet 11 is increased to expand the reaction area of molten steel. However, in this method, there is an upper limit to the flow rate of the blown gas for promoting the decarburization reaction, and when the upper limit is exceeded, gas blow-through occurs, and the reaction area with molten steel is conversely reduced. This method of blowing inert gas into the bottom of the molten steel (recirculation) and from the open end has an upper limit on the gas flow rate so that gas blow-through does not occur, so there is a limit to the decarburization efficiency -F, and the vacuum Tank bottom.
から上方(排気口方向)に向かってガスもしくはガス+
フランクスを吹き込むため、真空槽内のみならず真空排
気装置のガスクーラーにまで地金が飛散し実質」―操業
不可能となる。Gas or gas+ from upwards (towards the exhaust port)
Because Franks is injected, metal is scattered not only inside the vacuum chamber but also into the gas cooler of the vacuum evacuation equipment, making it virtually impossible to operate.
本発明者等は前記従来技術の欠点を打開する手段として
第2図、第3図に示す如く、真空脱ガス槽と組合せた取
鍋内の未脱酸?tj網に、限定された操業条件下で不活
性ガス等のガスを吹き込み減圧精錬する方法を発明した
が、更に研究を進めた結果溶鋼中〔C〕濃度に応じてラ
ンスの浸漬深さを変更することによって更に効率的に極
低炭素鋼の製造が可能なことを見出した。As a means of overcoming the drawbacks of the prior art, the present inventors have developed an undeoxidized solution in the ladle in combination with a vacuum degassing tank, as shown in FIGS. 2 and 3. We invented a method for vacuum refining by blowing inert gas or other gas into a TJ net under limited operating conditions, but as a result of further research, we decided to change the immersion depth of the lance depending on the [C] concentration in the molten steel. We have discovered that it is possible to produce ultra-low carbon steel more efficiently by doing this.
「課題を解決するための手段」
本発明は前記の如き従来技術の欠点を有利に解決したも
のであり、その要旨は下記のとおりである。"Means for Solving the Problems" The present invention advantageously solves the drawbacks of the prior art as described above, and the gist thereof is as follows.
(1)真空脱ガス槽と組合せた取鍋内の溶鋼に不活性ガ
ス等のガスを吹き込み減圧精神する方法において、真空
脱ガス槽内を減圧にすると共に、未脱酸)容鋼への不活
性ガスの吹き込み深さを、溶鋼中〔C〕濃度に応じて変
更することを特徴とする極低炭素鋼の製造方法。(1) In a method of blowing gas such as an inert gas into the molten steel in a ladle combined with a vacuum degassing tank to reduce the pressure, the pressure inside the vacuum degassing tank is reduced and the deoxidization of the undeoxidized steel is A method for producing ultra-low carbon steel, characterized in that the depth of active gas injection is changed depending on the [C] concentration in molten steel.
(2) 5〜16 N e /5in−tsの吹き込
みガス流量において、〔C〕≧30ppmの高炭素濃度
領域ではh/H=0.5〜0.8の範囲で、(C〕<3
0ppmの領域ではh/H=0.05〜0.15の範囲
で、不活性ガスを吹き込むことを特徴とする前項I記載
の極低炭素鋼の製造方法。(2) At a blowing gas flow rate of 5 to 16 N e /5 in-ts, in the high carbon concentration region of [C] ≧ 30 ppm, in the range of h/H = 0.5 to 0.8, (C] < 3
The method for producing ultra-low carbon steel according to the above item I, characterized in that in the 0 ppm region, inert gas is blown in a range of h/H = 0.05 to 0.15.
ただし、H−真空界面と取鍋底との距離h=真空界面と
不活性ガス吹き込み
ランスのガス吹き出し口との距
離
すなわち、本発明は真空槽内に設置した取鍋的溶鋼に減
圧雰囲気下で上方より不活性ガスを吹き込み、脱炭末期
にガス吹き込み深さを浅くして溶鋼の粒滴化を促進させ
、真空槽内気液界面積を増大させることによって脱炭反
応促進を図るものである。However, H - Distance between the vacuum interface and the bottom of the ladle h = Distance between the vacuum interface and the gas outlet of the inert gas blowing lance, that is, in the present invention, the ladle-shaped molten steel installed in the vacuum chamber is exposed to the upper part under a reduced pressure atmosphere. The decarburization reaction is promoted by injecting more inert gas and reducing the gas injection depth at the final stage of decarburization to promote the formation of molten steel droplets and increase the air-liquid interface area within the vacuum chamber.
本発明者等は、減圧下での脱炭速度に及ぼす諸要因の影
響を調査検討した。その結果、第1図に示すように減圧
下の脱炭速度の推移は〔C〕≧30ppn+の脱炭速度
の大きい1領域と、〔C〕〈30ppmで脱炭速度が小
さく脱炭が停滞するII iJf域のほぼ2つに分けら
れ、脱炭促進手段として1領域ではガス吹き込み深さを
深くし、且つガス吹き込み量を増加させ均一混合時間τ
を小さくすること、II jJf域ではガス吹き込み深
さを浅くし、且つガス吹き込み量を増加させスプラッシ
ュ発生量を増加させて真空槽内気液界面積を増大させる
ことが有効であることを見出した。更に、同一ガス流量
であってもガス吹き込み深さhが大きいとてか小さくな
ること、bが小さく真空界面近傍にガスを吹き込むとτ
が大きくなるがスプラッシュ発生量が大きくなることが
分かった。The present inventors investigated and examined the influence of various factors on the decarburization rate under reduced pressure. As a result, as shown in Fig. 1, the decarburization rate changes under reduced pressure in one region where the decarburization rate is high at [C]≧30ppn+, and at [C]〈30ppm, the decarburization rate is low and decarburization stagnates. II iJf region, and in one region, the decarburization promotion means is to deepen the gas injection depth and increase the gas injection amount to increase the uniform mixing time τ.
In the II jJf region, it was found that it is effective to reduce the gas injection depth, increase the amount of gas injection, increase the amount of splash generation, and increase the gas-liquid interface area in the vacuum chamber. . Furthermore, even if the gas flow rate is the same, the larger the gas injection depth h, the smaller the value, and if b is small and the gas is blown near the vacuum interface, τ
It was found that the amount of splash generated increases as the amount of water increases.
以下に本発明の詳細を述べる。The details of the present invention will be described below.
本発明においでは、溶鋼は所謂通常の未脱酸鋼が用いら
れる。In the present invention, so-called ordinary non-deoxidized steel is used as the molten steel.
まず溶鋼を入れた取鍋は、真空脱ガス槽と組合わされる
。この場合、装置上では真空脱ガス処理と並行して不活
性ガスを溶鋼中に吹き込むことが可能であることが前提
である。First, a ladle containing molten steel is combined with a vacuum degassing tank. In this case, the premise is that it is possible to blow inert gas into the molten steel on the device in parallel with the vacuum degassing treatment.
真空脱ガス槽内は先ず減圧され始め、J常の真空状態に
至る。これらの減圧過程に略々並行1〜で不活性ガスを
溶鋼中に吹き込む。The inside of the vacuum degassing tank first begins to be depressurized and reaches a normal vacuum state. Inert gas is blown into the molten steel approximately in parallel with these pressure reduction processes.
すなわち、5〜16 N 127IIlin−tsの吹
き込みガス流量において、〔C〕≧30ppraの高炭
素濃度領域ではh / H= 0.5〜0.8の範囲で
、〔C〕< 3o ppmの領域ではh/H=0.05
〜0.15の範囲で不活性ガスを吹き込み、短時間で且
つ安定に極低炭素鋼を製造する方法である。That is, at a blowing gas flow rate of 5 to 16 N 127 IIlin-ts, h/H = 0.5 to 0.8 in the high carbon concentration region of [C] ≧ 30 ppm, and h / H = 0.5 to 0.8 in the region of [C] < 30 ppm. h/H=0.05
This is a method for producing ultra-low carbon steel in a short time and stably by blowing inert gas in the range of 0.15 to 0.15.
吹き込みガス流量を増加させることにより脱炭速度は増
大するが、撹拌力の増大に伴う溶鋼の揺動及びスプラッ
シュ発生量増大に伴う地金流出量の増大が顕著になり、
実用上吹き込みガス流量は5〜16Nj2/m1n=t
sの範囲内に規制される。Although the decarburization rate increases by increasing the blowing gas flow rate, the amount of metal flowing out becomes noticeable due to the shaking of the molten steel and the increase in the amount of splash generated due to the increase in stirring force.
In practice, the blowing gas flow rate is 5 to 16 Nj2/m1n=t
It is regulated within the range of s.
なお、Arガス吹き込み深さを極端に深くすると取鍋底
4の敷レンガの溶損が激しくなるので敷レンガに悪影響
を及ぼさないようにするにはh/H≦0.8とすること
が必要である。Note that if the Ar gas blowing depth becomes extremely deep, the erosion of the paving bricks on the ladle bottom 4 will be severe, so it is necessary to set h/H≦0.8 to avoid having a negative effect on the paving bricks. be.
なお、本発明により脱炭だけでなく脱水素等の脱ガスに
も改善効果が見られる。Note that the present invention has an improvement effect not only on decarburization but also on degassing such as dehydrogenation.
「作用及び実施例」
次に本発明方法による実施例と比較例とを第1図に示す
。第1図は溶鋼300t/chの実施例について脱炭推
移を示したもので従来技術と比較して示した。"Operation and Examples" Next, an example and a comparative example according to the method of the present invention are shown in FIG. FIG. 1 shows the progress of decarburization in an example of molten steel of 300 t/ch, and is compared with the conventional technology.
「発明の効果」
以上の如く、本発明に従えば、極低炭素溶鋼の安定した
製造が可能となる。"Effects of the Invention" As described above, according to the present invention, it is possible to stably produce ultra-low carbon molten steel.
第1図は本発明の実施例を従来技術と比較して示した図
、第2図、3図は本発明による処理方法の実施態様を示
す説明図、第4図は従来技術による処理方法の実施態様
を示す説明図である。
1・・・取鍋、2・・・未脱酸溶鋼、3・・・真空界面
、4・・・取鍋底、5・・・不活性ガス吹き込みランス
、6・・・不活性ガス吹き込みランスのガス吹き出し口
、7・・・スプラッシュ防止蓋、8・・・RH真空槽、
9A・・・吸い上げ管、9B・・・下降管、10・・・
不活性ガス噴出口、11・・・不活性ガス噴出口。
時間0分)
第
図
第3図Fig. 1 is a diagram showing an embodiment of the present invention in comparison with the prior art, Figs. 2 and 3 are explanatory diagrams showing embodiments of the processing method according to the present invention, and Fig. 4 is a diagram showing the processing method according to the prior art. It is an explanatory diagram showing an embodiment. 1... Ladle, 2... Undeoxidized molten steel, 3... Vacuum interface, 4... Ladle bottom, 5... Inert gas blowing lance, 6... Inert gas blowing lance. Gas outlet, 7... Splash prevention lid, 8... RH vacuum chamber,
9A...Suction pipe, 9B...Down pipe, 10...
Inert gas outlet, 11...Inert gas outlet. Time 0 minutes) Figure Figure 3
Claims (2)
ス等のガスを吹き込み減圧精錬する方法において、真空
脱ガス槽内を減圧にすると共に、未脱酸溶鋼への不活性
ガスの吹き込み深さを、溶鋼中〔C〕濃度に応じて変更
することを特徴とする極低炭素鋼の製造方法。(1) In a method of vacuum refining by blowing a gas such as an inert gas into the molten steel in a ladle combined with a vacuum degassing tank, the pressure inside the vacuum degassing tank is reduced and the inert gas is injected into the undeoxidized molten steel. A method for producing ultra-low carbon steel, the method comprising changing the blowing depth according to the [C] concentration in molten steel.
において、〔C〕≧30ppmの高炭素濃度領域ではh
/H=0.5〜0.8の範囲で、〔C〕<30ppmの
領域ではh/H=0.05〜0.15の範囲で、不活性
ガスを吹き込むことを特徴とする請求項1記載の極低炭
素鋼の製造方法。 ただし、H=真空界面と取鍋底との距離h=真空界面と
不活性ガス吹き込みランスのガス吹き出し口との距離(2) At a blowing gas flow rate of 5 to 16 Nl/min・ts, in the high carbon concentration region of [C]≧30 ppm, h
Claim 1, characterized in that inert gas is blown in the range of /H = 0.5 to 0.8, and in the range of h/H = 0.05 to 0.15 in the region of [C] < 30 ppm. The method for manufacturing the ultra-low carbon steel described. However, H = distance between the vacuum interface and the bottom of the ladle h = distance between the vacuum interface and the gas outlet of the inert gas blowing lance
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8229290A JPH03281720A (en) | 1990-03-29 | 1990-03-29 | Production of dead-soft carbon steel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8229290A JPH03281720A (en) | 1990-03-29 | 1990-03-29 | Production of dead-soft carbon steel |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03281720A true JPH03281720A (en) | 1991-12-12 |
Family
ID=13770468
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8229290A Pending JPH03281720A (en) | 1990-03-29 | 1990-03-29 | Production of dead-soft carbon steel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03281720A (en) |
-
1990
- 1990-03-29 JP JP8229290A patent/JPH03281720A/en active Pending
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