JPS5938432Y2 - Double pipe tuyere flow control device for refining - Google Patents

Double pipe tuyere flow control device for refining

Info

Publication number
JPS5938432Y2
JPS5938432Y2 JP3409080U JP3409080U JPS5938432Y2 JP S5938432 Y2 JPS5938432 Y2 JP S5938432Y2 JP 3409080 U JP3409080 U JP 3409080U JP 3409080 U JP3409080 U JP 3409080U JP S5938432 Y2 JPS5938432 Y2 JP S5938432Y2
Authority
JP
Japan
Prior art keywords
gas
flow rate
refining
control valve
pipe
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
Application number
JP3409080U
Other languages
Japanese (ja)
Other versions
JPS56138867U (en
Inventor
雅男 武田
純夫 渡辺
Original Assignee
新日本製鐵株式会社
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 新日本製鐵株式会社 filed Critical 新日本製鐵株式会社
Priority to JP3409080U priority Critical patent/JPS5938432Y2/en
Publication of JPS56138867U publication Critical patent/JPS56138867U/ja
Application granted granted Critical
Publication of JPS5938432Y2 publication Critical patent/JPS5938432Y2/en
Expired legal-status Critical Current

Links

Landscapes

  • Treatment Of Steel In Its Molten State (AREA)
  • Furnace Charging Or Discharging (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Description

【考案の詳細な説明】 本考案は鋼の溶製において溶鋼中にガスを吹込むための
二重管側口の冷却作用改善を図った装置に関する。
[Detailed Description of the Invention] The present invention relates to a device that improves the cooling effect of the side opening of a double tube for blowing gas into molten steel during steel melting.

近年ステンレス鋼等の溶製法として溶鋼を収容した精錬
容器の底部又は側壁部に二重管側口等を設け、該羽目か
ら不活性ガス又は及び反応性ガスを溶鋼中に吹込み、溶
鋼中の00分圧を下げ、クロム等の酸化を抑えながら、
溶鋼を攪拌して脱炭反応等を促進させ精錬を行う製鋼法
が採用されている。
In recent years, as a melting method for stainless steel, etc., a double pipe side port is installed at the bottom or side wall of a refining vessel containing molten steel, and an inert gas or a reactive gas is blown into the molten steel through the opening. 00 while lowering the partial pressure and suppressing the oxidation of chromium, etc.
A steelmaking method is used in which molten steel is stirred to promote decarburization reactions and other processes for refining.

しかして該二重前羽目によるガスの吹込方法は外管から
は羽目冷却用としてアルゴンガス等の保護ガスを吹込み
、内管からは精錬初期は酸素等の反応性ガスを主体とし
た不活性ガスとの混合ガスを吹込み、脱炭反応が進むに
つれて不活性ガスの比率を増加させてゆき精錬末期には
主に不活性ガスを主体にした反応性ガスとの混合ガスが
吹込1れる。
However, the method of blowing gas using the double front panel is that a protective gas such as argon gas is blown into the outer tube for cooling the panel, and an inert gas such as oxygen, which is mainly used in the early stages of refining, is injected through the inner tube. As the decarburization reaction progresses, the ratio of inert gas is increased.At the final stage of refining, a mixture of reactive gas and mainly inert gas is blown into the refining process.

第1図は二重前羽目における従来のガス流量制御装置の
一例を示し、図中1は内管であり矢印の方向から不活性
ガス又は及び酸素等の反応性ガスが流れ、2は該内管を
流れるガスの流量を測定する流量計であり、3は測定し
た流量を表示するとともに流量を設定調節するための流
量表示調節計であり、4は該調節計3によって内管ガス
流量を調節するための流量調節弁である。
Fig. 1 shows an example of a conventional gas flow rate control device for a double front panel. In the figure, 1 is an inner pipe through which an inert gas or a reactive gas such as oxygen flows from the direction of the arrow, and 2 is an inner pipe. A flow meter measures the flow rate of gas flowing through the pipe, 3 is a flow rate display controller for displaying the measured flow rate and setting and adjusting the flow rate, and 4 is the controller 3 to adjust the inner pipe gas flow rate. This is a flow control valve for

一方5は外管であり矢印の方向から保護ガス(アルゴン
ガス等)が流れ、6は該外管5を流れるガスの圧力を調
節する圧力調節弁であり、7は該圧力を表示する圧力計
である。
On the other hand, 5 is an outer tube through which protective gas (argon gas, etc.) flows from the direction of the arrow, 6 is a pressure control valve that adjusts the pressure of the gas flowing through the outer tube 5, and 7 is a pressure gauge that displays the pressure. It is.

9は溶鋼中にガスを吹込むための二重前別口である。9 is a double front separate port for blowing gas into the molten steel.

このような従来装置においてガス吹込み調整は内管ガス
と外管ガスが、二重管側口9でバランスするように外管
ガスを圧力で、内管ガスを流量で調整する。
In such a conventional device, the gas blowing is adjusted by adjusting the outer tube gas by pressure and the inner tube gas by flow rate so that the inner tube gas and the outer tube gas are balanced at the double tube side port 9.

しかして脱炭の進行につれて内管ガスの酸素とアルゴン
の混合比率を例えば3:1から1:2に変更すると特に
外管の羽目詰りが発生し、外管からはガスが殆んど出な
くなり外管羽口の冷却が悪くなって羽口の溶損が大きく
なる。
However, as decarburization progresses, if the mixing ratio of oxygen and argon in the inner tube gas is changed from 3:1 to 1:2, for example, the outer tube becomes clogged, and almost no gas comes out from the outer tube. Cooling of the outer tube tuyere deteriorates and the tuyere becomes more susceptible to melting.

これは冷却作用を持つアルゴンの比率が増すため羽口近
傍の溶鋼が冷却され流動性が悪くなること、および溶鋼
が凝固して羽口9に付着するためと考えられる。
This is thought to be because the ratio of argon, which has a cooling effect, increases, which cools the molten steel near the tuyeres and deteriorates fluidity, and also because the molten steel solidifies and adheres to the tuyere 9.

従ってこの場合の対策としては詰りを生じた外管のガス
圧力を増す方法があるが、ガス圧力を増せば外管ガスか
ら内管ガスへの干渉が生じ内管ガスの流量が低下すると
いう問題が発生し外管羽口詰りを解決し得ない。
Therefore, as a countermeasure in this case, there is a method of increasing the gas pressure in the clogged outer pipe, but increasing the gas pressure causes interference from the outer pipe gas to the inner pipe gas, resulting in a decrease in the flow rate of the inner pipe gas. occurs and the clogging of the outer tube tuyere cannot be solved.

本考案はこのような問題を解決するため外管ガスの吹込
み制御を外管に設けた流量調節弁で流量を一定となし、
一方圧力を所定の圧力よりやや高く設定しておき、流量
が一定になるよう制御すると前述の如くして羽口詰りか
発生した場合、流量調節弁が開き設定された圧力の範囲
内で羽口内圧力が高くなり流量が一定に保たれ羽口詰り
による流量低下が防止されるものである。
In order to solve this problem, the present invention uses a flow control valve installed in the outer tube to control the blowing of gas into the outer tube, keeping the flow constant.
On the other hand, if the pressure is set slightly higher than the predetermined pressure and the flow rate is controlled to be constant, if the tuyere is clogged as described above, the flow control valve will open and the flow rate will be within the set pressure range. This increases the pressure, keeps the flow rate constant, and prevents a drop in flow rate due to clogging of the tuyeres.

以下本考案を第2図に示す実施例によって詳細に説明す
る。
The present invention will be explained in detail below with reference to an embodiment shown in FIG.

第2図において第1図と番号の同じものは第1図と同じ
各称および作用をなすためその説明を省略する。
In FIG. 2, the same numbers as in FIG. 1 have the same names and functions as in FIG. 1, so the explanation thereof will be omitted.

10は外管ガスの流量調節計、11は流量調節弁、2′
は流量計であり、流量計2′で測定された流量が流量調
節計10に表示されるとともに流量調節計10に設定し
た流量が流量調節弁11によって調節される。
10 is an outer pipe gas flow rate controller, 11 is a flow rate adjustment valve, 2'
1 is a flowmeter, and the flow rate measured by the flowmeter 2' is displayed on a flow rate controller 10, and the flow rate set in the flow rate controller 10 is regulated by a flow rate adjustment valve 11.

しかして内管ガスの比率が変化する前は流量調節計10
に設定された流量によって外管ガスが制御される。
However, before the ratio of inner pipe gas changes, the flow rate controller 10
The outer tube gas is controlled by the flow rate set to .

次に内管ガス比率が変化し前記の如くして外管ガス流速
が低下した場合にも外管ガス流量が一定になるように外
管圧力調節弁6を所定の圧力よりも高く設定しておく。
Next, the outer pipe pressure control valve 6 is set higher than a predetermined pressure so that the outer pipe gas flow rate remains constant even when the inner pipe gas ratio changes and the outer pipe gas flow rate decreases as described above. put.

このようになしておくと内管ガスの酸素とアルゴンガス
の比率を第1図の場合と同様に3=1から1:2に変更
し、前記の如くして外管羽口からのガスの吹き出しが弱
くなった場合、圧力調節弁6が所定の圧力より高く設定
された状態で、流量調節弁11が設定流量になるように
作動するから外管ガス圧力が高1ってゆく。
In this way, the ratio of oxygen and argon gas in the inner tube gas can be changed from 3=1 to 1:2 as in the case of Fig. 1, and the gas from the outer tube tuyeres can be adjusted as described above. When the blowing becomes weak, the pressure regulating valve 6 is set higher than a predetermined pressure, and the flow regulating valve 11 is operated to reach the set flow rate, so the outer pipe gas pressure increases.

この場合流量は内管流量とバランスするように設定され
ているため、二重前羽口において外管ガスの内管ガスへ
の干渉はなく流量は一定で圧力のみが増加するため羽口
を過冷却することなく外管羽口からのガス吹き出しを強
くすることができ羽目詰りを解消するものである。
In this case, the flow rate is set to be in balance with the inner pipe flow rate, so in the double front tuyeres, there is no interference between the outer pipe gas and the inner pipe gas, and the flow rate is constant and only the pressure increases, so the tuyeres pass through the tuyere. This makes it possible to strengthen the gas blowout from the outer tube tuyere without cooling, thereby eliminating clogging of the tuyeres.

本考案は以上の如く簡単な構成によって二重前羽口の詰
りを防止でき鋼の溶製上多大の効果を発揮するものであ
る。
As described above, the present invention has a simple structure that prevents clogging of the double front tuyeres, and is highly effective in melting steel.

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

第1図は従来のガス流量制御装置の一例を示す図、第2
図は本考案装置の実施例を示す図である。 1.1′・・・内管、2 、2’・・流量計、3,3′
・・・流量表示調節計、4,4′・・・流量調節弁、5
,5′・・・外管、6.6′・・・圧力調節弁、7,7
′・・・圧力計、9,9′・・・二重前羽目、10・・
・流量調節計、11・・・流量調節弁。
Figure 1 shows an example of a conventional gas flow rate control device, Figure 2 shows an example of a conventional gas flow rate control device.
The figure shows an embodiment of the device of the present invention. 1.1'...inner pipe, 2,2'...flow meter, 3,3'
...Flow rate display controller, 4, 4'...Flow rate control valve, 5
, 5'...Outer pipe, 6.6'...Pressure control valve, 7,7
'...Pressure gauge, 9,9'...Double front panel, 10...
・Flow rate controller, 11...Flow rate control valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 精錬用二重前羽口の内管から不活性ガスと反応性ガスと
の混合ガスが、外管から不活性ガス等の保護ガスが流れ
、内管の不活性ガスと反応性ガスの混合比率が変化する
ガス吹込み装置に釦いて、外管に圧力調節弁6釦よび流
量調節弁11を配設し、さらに前記流量調節弁11によ
って外管ガス流量を設定流量に保持するための流量調節
計10を設けた精錬用二重管側ロ流量制御装置。
A mixed gas of inert gas and reactive gas flows from the inner pipe of the double front tuyere for refining, and protective gas such as inert gas flows from the outer pipe, and the mixture ratio of inert gas and reactive gas in the inner pipe is increased. A pressure control valve 6 button and a flow rate control valve 11 are arranged on the outer pipe of the gas blowing device in which the gas flow rate changes, and the flow rate control valve 11 is used to adjust the flow rate to maintain the outer pipe gas flow rate at a set flow rate. A total of 10 double pipe side flow rate control devices for refining.
JP3409080U 1980-03-15 1980-03-15 Double pipe tuyere flow control device for refining Expired JPS5938432Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3409080U JPS5938432Y2 (en) 1980-03-15 1980-03-15 Double pipe tuyere flow control device for refining

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3409080U JPS5938432Y2 (en) 1980-03-15 1980-03-15 Double pipe tuyere flow control device for refining

Publications (2)

Publication Number Publication Date
JPS56138867U JPS56138867U (en) 1981-10-20
JPS5938432Y2 true JPS5938432Y2 (en) 1984-10-26

Family

ID=29629728

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3409080U Expired JPS5938432Y2 (en) 1980-03-15 1980-03-15 Double pipe tuyere flow control device for refining

Country Status (1)

Country Link
JP (1) JPS5938432Y2 (en)

Also Published As

Publication number Publication date
JPS56138867U (en) 1981-10-20

Similar Documents

Publication Publication Date Title
WO2021073015A1 (en) Converter co2-o2 mixed injection smelting method and dynamic temperature control method in fire-point region
US4325730A (en) Process for conditioning slag during the refining of a metal bath
JPS5938432Y2 (en) Double pipe tuyere flow control device for refining
US4405365A (en) Method for the fabrication of special steels in metallurgical vessels
US4474361A (en) Oxygen-blown steelmaking furnace
CN105369010B (en) A kind of method of Boron contents in control boron steel
CN115927784B (en) Based on CO 2 Converter steelmaking end point control method by dynamic mixed blowing
GB2099021A (en) Preventing foaming when refining pig iron by top-slawing agent and device for carrying out the process
US4420334A (en) Method for controlling the bottom-blowing gas in top-and-bottom blown converter steel making
JPH0270372A (en) Detecting method for outflow of slug and preventing method for tandish nozzle from clogging
US4139368A (en) Metallurgical method
WO2002075003A2 (en) Argon oxygen decarburisation converter control method and system
CN112676544A (en) Nitrogen increasing method in high-nitrogen steel continuous casting process
JPS5776117A (en) Control of bottom blow gas at converter having bottom blowing function
US3754895A (en) Process for decarburization of steels
CN113462847B (en) Control method for ultralow titanium content of ultralow-carbon high-aluminum steel
JPS6318012A (en) Method for controlling flow rate of oxygen for refining for metallurgical refining furnace
EP0160375A2 (en) System and method for producing steel in a top-blown vessel
JP2921970B2 (en) Converter end point control method
CN105908101B (en) A kind of ultra-low carbon nitrogen steel and preparation method
JPS6246606B2 (en)
JPH1088217A (en) Method for injecting powdery material into molten iron
JP2803534B2 (en) Converter blowing control method
US4398949A (en) Method for stably refining high carbon steel
JPH0735530B2 (en) Molten Steel Temperature Control Method in Vacuum Ladle Refining of High Chromium Steel