JPH037383Y2 - - Google Patents

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Publication number
JPH037383Y2
JPH037383Y2 JP1985164604U JP16460485U JPH037383Y2 JP H037383 Y2 JPH037383 Y2 JP H037383Y2 JP 1985164604 U JP1985164604 U JP 1985164604U JP 16460485 U JP16460485 U JP 16460485U JP H037383 Y2 JPH037383 Y2 JP H037383Y2
Authority
JP
Japan
Prior art keywords
blowing
powder
valve
pressure
tank
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
JP1985164604U
Other languages
Japanese (ja)
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JPS6275059U (en
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
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Priority to JP1985164604U priority Critical patent/JPH037383Y2/ja
Publication of JPS6275059U publication Critical patent/JPS6275059U/ja
Application granted granted Critical
Publication of JPH037383Y2 publication Critical patent/JPH037383Y2/ja
Expired legal-status Critical Current

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  • Treatment Of Steel In Its Molten State (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Description

【考案の詳細な説明】 [産業上の利用分野] 本考案は溶解炉から搬出された溶融金属に種々
の粉粒状精練剤、例えば脱酸剤等を吹込むための
粉体吹込装置に関し、詳細には粉体吹込終了時に
多量のキヤリアガスが吹込ランス中に流れ込んで
溶融金属の吹上げや吹きこぼれ等が生じるのを防
止できる粉体吹込装置に関するものである。
[Detailed description of the invention] [Industrial application field] The present invention relates to a powder injection device for injecting various powdery scouring agents, such as deoxidizers, etc. into molten metal carried out from a melting furnace. The present invention relates to a powder blowing device that can prevent a large amount of carrier gas from flowing into a blowing lance at the end of powder blowing, thereby preventing molten metal from blowing up or boiling over.

[従来の技術] 転炉や電気炉等によつて生産される溶鋼は連続
鋳造装置や鋳型によつて造塊される前に、(イ)取鍋
内溶鋼温度の均一化と適正化、(ロ)溶鋼の清浄化、
(ハ)溶鋼成分の調整等の目的として取鍋内で各種の
溶鋼処理を受ける。
[Prior art] Before molten steel produced in a converter, electric furnace, etc. is ingot-formed in a continuous casting device or a mold, it is necessary to (a) equalize and optimize the temperature of the molten steel in the ladle; b) Cleaning of molten steel;
(c) The molten steel undergoes various treatments in a ladle for the purpose of adjusting the molten steel composition.

取鍋内溶鋼処理方法としては、Arガス等の不
活性ガスを底吹き穴やランスから取鍋溶鋼内へ吹
込むバブリング法と、真空槽内に溶鋼を吸い上げ
て真空部と接触させる真空脱ガス法とが主に利用
されている。
Methods for treating molten steel in a ladle include the bubbling method, in which inert gas such as Ar gas is blown into the molten steel in the ladle through a bottom blow hole or lance, and the vacuum degassing method, in which molten steel is drawn up into a vacuum chamber and brought into contact with the vacuum section. The law is mainly used.

第2図は吹込ランスを使用するバブリング装置
(以下吹込装置という)の例を示すものである。
取鍋17内の溶融金属16中に吹込ランス15の
先端が浸漬さ、吹込ランス15の後端には粉体吹
込ライン14が連接される。粉体吹込ライン14
にはブロー回路4及び吹込タンク10が連接され
ており、粉体吹込ライン14と吹込タンク10の
間には吹込出口弁13及び粉体切出装置12が配
設される。また粉体切出装置12と吹込出口弁1
3の間からは吹込タンク10上部に通じる均圧管
8が分岐され、均圧管8の一部にはキヤリアガス
供給源1に連接される加圧回路7が接続される。
尚符号2はブロー用減圧弁、3はブロー元弁、5
は吹込元弁、6は加圧元弁を夫々示す。上記装置
による粉体吹込及び吹込停止は次の順序で行なわ
れる。まずキヤリアガス供給源1から供給される
Ar等の加圧キヤリアガスは加圧元弁6を介して
加圧回路7へ至り、逆止弁20a及び均圧管8を
介して吹込タンク10内へ導入される。そして吹
込タンク10内の圧力がキヤリアガスの圧力と同
等となつたところで、粉体切出装置12を稼動さ
せて吹込出口弁13を開き、吹込元弁5からキヤ
リアガスを粉体切出装置12の下方へ送り、吹込
タンク10内から落下する粉体11と共に粉体吹
込ライン14を通して吹込ランス15へ送り込
み、取鍋17内の溶融金属16中へ吹込む。
FIG. 2 shows an example of a bubbling device (hereinafter referred to as a blowing device) that uses a blowing lance.
The tip of the blowing lance 15 is immersed in the molten metal 16 in the ladle 17, and the powder blowing line 14 is connected to the rear end of the blowing lance 15. Powder injection line 14
A blow circuit 4 and a blow tank 10 are connected to each other, and a blow outlet valve 13 and a powder cutting device 12 are disposed between the powder blow line 14 and the blow tank 10. In addition, the powder cutting device 12 and the blowing outlet valve 1
A pressure equalizing pipe 8 that leads to the upper part of the blowing tank 10 is branched from between 3 and a pressure equalizing pipe 8 is connected to a part of the pressure equalizing pipe 8, which is connected to a carrier gas supply source 1.
Note that 2 is a blow pressure reducing valve, 3 is a blow source valve, and 5 is a blow pressure reducing valve.
6 indicates a blowing source valve, and 6 indicates a pressurizing source valve. Powder injection and injection stop using the above device are performed in the following order. First, it is supplied from carrier gas supply source 1.
The pressurized carrier gas such as Ar reaches the pressurizing circuit 7 via the pressurizing source valve 6, and is introduced into the blowing tank 10 via the check valve 20a and the pressure equalizing pipe 8. When the pressure inside the blowing tank 10 becomes equal to the pressure of the carrier gas, the powder cutting device 12 is operated, the blowing outlet valve 13 is opened, and the carrier gas is pumped from the blowing source valve 5 to the lower part of the powder cutting device 12. The powder is sent to the blowing lance 15 through the powder blowing line 14 together with the powder 11 falling from the blowing tank 10, and is blown into the molten metal 16 in the ladle 17.

粉体吹込の停止に際しては、まず粉体切出し装
置12を停止させて粉体の供給を停止し、極く僅
かな間キヤリアガスのみを流してから吹込出口弁
13を閉じてキヤリアガスの供給を完全に停止さ
せる。この間の事情は後に詳述する。その後配管
内に残存する粉体を除去するために、前記加圧回
路7を通過するキヤリアガスより低圧のキヤリア
ガスをブロー回路4から粉体吹込ライン14に流
通させてライン14内に残存する粉体を溶融金属
16中へ吹込む。なお、ブロー回路4のキヤリア
ガスを加圧回路7側より低圧とするのは、粉体切
出装置12を停止させると粉体吹込ライン14中
の粉体量が減少して粉体の圧送抵抗が低下するこ
とになり、加圧回路7側と同程度の圧力を有する
キヤリアガスを使用すると、粉体の圧送抵抗が低
下することにより、多量のキヤリアガスが流れる
恐れがあるからである。
When stopping powder blowing, first stop the powder cutting device 12 to stop the powder supply, and after allowing only the carrier gas to flow for a very short time, close the blowing outlet valve 13 to completely stop the carrier gas supply. make it stop. The circumstances during this time will be detailed later. Thereafter, in order to remove the powder remaining in the piping, a carrier gas having a lower pressure than the carrier gas passing through the pressurizing circuit 7 is passed from the blow circuit 4 to the powder blowing line 14 to remove the powder remaining in the line 14. Blow into molten metal 16. The reason why the pressure of the carrier gas in the blow circuit 4 is lower than that in the pressure circuit 7 is that when the powder cutting device 12 is stopped, the amount of powder in the powder blowing line 14 decreases and the resistance to pumping the powder increases. This is because if a carrier gas having a pressure comparable to that on the pressure circuit 7 side is used, a large amount of carrier gas may flow due to a decrease in powder pumping resistance.

[考案が解決しようとする問題点] 粉体吹込の終了に際して行なう上記操作のう
ち、粉体切出装置12の停止から吹込出口弁13
の閉鎖までに僅かな時間的遅れを設定したのは下
記の理由による。即ち粉体切出装置12の停止と
同時に吹込出口弁13を閉鎖しようとすると、吹
込出口弁13における弁座と弁体のシール部に粉
体を噛み込んでしまい、該弁を確実に閉鎖できな
くなるばかりでなく、さらにはシール部に損傷を
招くことになり、完全なガス気密が保てなくなつ
てしまうからである。
[Problems to be solved by the invention] Among the above-mentioned operations performed upon completion of powder blowing, from stopping the powder cutting device 12 to closing the blowing outlet valve 13.
The reason for setting a slight time delay before the closure is as follows. That is, if an attempt is made to close the blow-in outlet valve 13 at the same time as the powder extraction device 12 is stopped, the powder will get caught in the seal between the valve seat and the valve body of the blow-in outlet valve 13, making it impossible to close the valve reliably. This is because not only will it disappear, but it will also cause damage to the sealing part, making it impossible to maintain complete gas-tightness.

ところが切出装置12の停止と吹込出口弁13
の閉鎖に時間的な差が生じることにより、吹込タ
ンク10内に導入されていた均圧用のガスが、均
圧管8及び吹込出口弁13を介して溶融金属16
中へ一気に流れ込んでしまい、その結果溶融金属
16が吹上げ又は吹こぼれ等を生じ人身事故等を
引き起こす原因となつたり、或は製品の歩留りの
低下を引き起こすという問題があつた。すなわち
粉体吹込時には、キヤリアガスの圧力は粉体の圧
送抵抗とバランスを保つているため吹きこぼれ等
を起すことはないが、粉体切出装置12が停止さ
れ吹込ライン14中の粉体量が減少すると、粉体
の圧送抵抗が小さくなつて吹込ライン14内の圧
力が低下し、その結果吹込タンク10側の圧力と
吹込ライ14内の圧力均衡が保たれなくなり、吹
込タンク10側より多量のキヤリアガスがランス
15側へ流れることになるからである。
However, the cutting device 12 stopped and the blow-in outlet valve 13 stopped.
Due to the time difference in closing, the pressure equalizing gas introduced into the blowing tank 10 passes through the pressure equalizing pipe 8 and the blowing outlet valve 13 to the molten metal 16.
The problem is that the molten metal 16 flows into the interior all at once, and as a result, the molten metal 16 blows up or spills over, causing personal injury or the like, or lowering the yield of the product. In other words, when powder is injected, the pressure of the carrier gas is kept in balance with the pumping resistance of the powder, so no boiling over occurs, but the powder cutting device 12 is stopped and the amount of powder in the blowing line 14 is reduced. As a result, the pressure in the blowing line 14 decreases as the resistance to pumping the powder decreases, and as a result, the pressure on the blowing tank 10 side and the pressure inside the blowing line 14 are no longer balanced, and a larger amount of carrier gas flows out from the blowing tank 10 side. This is because the water will flow to the lance 15 side.

そこで本考案者らは溶融金属が飛散しない様な
粉体吹込装置を完成させるべく種々工夫を重ねた
結果、本考案を完成するに至つた。
Therefore, the present inventors made various efforts to complete a powder blowing device that would prevent molten metal from scattering, and as a result, they completed the present invention.

[問題点を解決するための手段] 上記目的を達成し得た本考案粉体吹込装置は、
吹込タンクの下部に粉体切出装置を設け、更にそ
の下流側に吹込出口弁を接続すると共に、上記粉
体切出装置と吹込出口弁の間から前記吹込タンク
の上部空間に連通される均圧管を設け、該均圧管
に加圧回路を接続し、高圧に保持された吹込タン
ク内より前記吹込出口弁を通過した粉体を、前記
加圧回路及び均圧管を介して上記吹込出口弁の上
流側から供給されてくるキヤリアガスにより、粉
体吹込ライン経由で吹込ランスに供給して溶融金
属中に吹込む粉体吹込装置において、前記均圧管
には、加圧回路との接続位置より吹込タンク上部
空間側に、上記粉体切出装置の停止と同時に閉鎖
される遮断弁を配設してなることを要旨とするも
のである。
[Means for solving the problems] The powder blowing device of the present invention, which has achieved the above objectives, has the following features:
A powder cutting device is provided at the lower part of the blowing tank, and a blowing outlet valve is further connected to the downstream side thereof, and an equalizer is connected to the upper space of the blowing tank from between the powder cutting device and the blowing outlet valve. A pressure pipe is provided, a pressure circuit is connected to the pressure equalization pipe, and the powder that has passed through the blow outlet valve from inside the blow tank maintained at high pressure is passed through the pressure circuit and the pressure equalization pipe to the blow outlet valve. In a powder blowing device in which a carrier gas supplied from the upstream side is supplied to a blowing lance via a powder blowing line and blown into molten metal, the pressure equalizing pipe is connected to a blowing tank from a connection position with a pressurizing circuit. The gist is that a shutoff valve is disposed on the upper space side and is closed simultaneously when the powder cutting device is stopped.

[作用] 粉体切出装置12の停止操作と吹込出口弁13
の閉鎖操作の時間的ずれは、該弁13のシール部
の保護と完全な気密確保のため不可避の工程操作
手順であり、省略又は変更することはできない。
従つて吹込タンク10内のガスが粉体吹込ライン
14側へ一気に流出しない様にするには、均圧管
8の一部に遮断弁を設け、粉体切出装置12の停
止と同時に該遮断弁を閉鎖すれば良いとの結論を
得るに至つた。但し遮断弁の閉鎖によつてキヤリ
アガス供給源からのガス供給が同時に停止されて
しまうので、吹込出口弁13の粉体除去ができな
くなつてしまう恐れがあるので、加圧回路7と均
圧管が接続される位置よりも吹込タンク側に遮断
弁を配設することが必要である。
[Operation] Stopping operation of powder cutting device 12 and blowing outlet valve 13
The time lag in the closing operation is an unavoidable process operation procedure for protecting the seal portion of the valve 13 and ensuring complete airtightness, and cannot be omitted or changed.
Therefore, in order to prevent the gas in the blowing tank 10 from flowing out all at once to the powder blowing line 14 side, a cutoff valve is provided in a part of the pressure equalizing pipe 8, and the cutoff valve is closed at the same time as the powder cutting device 12 is stopped. We came to the conclusion that it would be best to close it down. However, when the shutoff valve is closed, the gas supply from the carrier gas supply source will be stopped at the same time, and there is a risk that powder removal at the blow-in outlet valve 13 will become impossible. It is necessary to install a shutoff valve closer to the blow tank than the location where it is connected.

遮断弁の閉鎖によつて吹込タンク内に閉じ込め
られた加圧キヤリアガスは、吹込タンクに別の放
圧弁を配設して大気中に廃棄しても良いし、或は
配管ブロー用ガスとして徐々に吹込ラインから放
出することもできる。
The pressurized carrier gas trapped in the blow tank by closing the shutoff valve can be disposed of into the atmosphere by providing a separate pressure relief valve in the blow tank, or it can be gradually released as pipe blowing gas. It can also be discharged from the blow line.

[実施例] 第1図は本考案の代表的な実施例を示す説明図
である。第2図に示した従来例と構造面で相違す
る箇所は、均圧管8に遮断弁9を設けた点であ
る。そして遮断弁9は加圧回路7と均圧管8の接
合位置よりも吹込タンク10の上部空間側に配設
される。
[Embodiment] FIG. 1 is an explanatory diagram showing a typical embodiment of the present invention. The difference in structure from the conventional example shown in FIG. 2 is that a cutoff valve 9 is provided in the pressure equalizing pipe 8. The cutoff valve 9 is disposed closer to the upper space of the blow tank 10 than the joining position of the pressure circuit 7 and the pressure equalization pipe 8.

次に遮断弁9を配設した粉体吹込装置を使つて
粉体吹込の停止操作を行なう手順を説明する。ま
ず最初に粉体切出装置12の停止と遮断弁9の閉
鎖をほぼ同時に行ない、極く短時間キヤリアガス
だけを流した後で吹込出口弁13を閉鎖する。そ
してブロー回路4から減圧されたキヤリアガスを
通して粉体吹込ライン14内の残留粉体を除去す
るか、或は吹込出口弁13を開けて遮断弁9を小
開し、吹込タンク10内の加圧ガスを徐々に粉体
吹込ライン14へ導いて配管ブローを行なう。吹
込タンク10内のキヤリアガスを配管ブロー用と
して利用すればキヤリアガスの節約がはかれる。
Next, a procedure for stopping powder injection using a powder injection device equipped with a shutoff valve 9 will be described. First, the powder cutting device 12 is stopped and the cutoff valve 9 is closed almost simultaneously, and after only the carrier gas is allowed to flow for a very short time, the blowing outlet valve 13 is closed. Then, the residual powder in the powder blowing line 14 is removed by passing the carrier gas reduced in pressure from the blow circuit 4, or the pressurized gas in the blowing tank 10 is removed by opening the blowing outlet valve 13 and slightly opening the shutoff valve 9. is gradually introduced into the powder blowing line 14 to perform piping blowing. If the carrier gas in the blowing tank 10 is used for piping blowing, the carrier gas can be saved.

第3図は本考案の他の実施例を示す説明図であ
り、該実施例では遮断弁9の他に吹込タンク10
上部に排気用弁19を設け、更に粉体吹込ライン
14と吹込タンク10の間に差圧計18を設けた
ものである。粉体吹込終了時の操作は前述の第1
図の例と同様な手順に従つて行ない、吹込タンク
内に残存する加圧キヤリアガスは排気用弁19の
開放によつて放出し、配管ブロー用として送られ
てくる減圧されたキヤリアガスとの圧力差を差圧
計18によつて読み取り、該差圧計18の表示が
0.5Kg/cm2以下になつたときに排気用弁19を閉
鎖し、その後遮断弁9を開放して吹込タンク10
内の残存キヤリアガスは配管ブロー用ガスとして
利用する。
FIG. 3 is an explanatory diagram showing another embodiment of the present invention, and in this embodiment, in addition to the cutoff valve 9, a blow tank 10 is
An exhaust valve 19 is provided at the top, and a differential pressure gauge 18 is further provided between the powder blowing line 14 and the blowing tank 10. The operation at the end of powder injection is as described in step 1 above.
The pressurized carrier gas remaining in the blowing tank is released by opening the exhaust valve 19, and the pressure difference between the pressurized carrier gas and the depressurized carrier gas sent for piping blowing is carried out in accordance with the same procedure as in the example shown in the figure. is read by the differential pressure gauge 18, and the display of the differential pressure gauge 18 is
When the temperature falls below 0.5Kg/cm 2 , the exhaust valve 19 is closed, and the cutoff valve 9 is then opened to open the blow tank 10.
The remaining carrier gas will be used as pipe blowing gas.

[考案の効果] 均圧管の遮断弁を設けて吹込終了時に該弁を閉
鎖することにより、吹込タンク均圧用に用いられ
た加圧キヤリアガスが吹込ランスから溶融金属中
に一気に流出されることがなくなり、溶融金属の
飛散が防止され、製品歩留りの低下及び人身事故
発生の危険性が回避される。
[Effect of the invention] By providing a cutoff valve for the pressure equalization pipe and closing the valve at the end of blowing, the pressurized carrier gas used for equalizing the pressure in the blowing tank is prevented from flowing out from the blowing lance into the molten metal all at once. , molten metal is prevented from scattering, and a reduction in product yield and the risk of personal injury are avoided.

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

第1図は本考案の代表的な実施例を示す説明
図、第2図は従来の粉体吹込装置の例を示す説明
図、第3図は本考案の他の実施例を示す説明図で
ある。 1……キヤリアガス供給源、2……ブロー用減
圧弁、3……ブロー元弁、4……ブロー回路、5
……吹込元弁、6……加圧元弁、7……加圧回
路、8……均圧管、10……吹込タンク、11…
…粉体、12……粉体切出装置、13…吹込出口
弁、14……粉体吹込ライン、15……吹込ラン
ス、16……溶融金属、17……取鍋、18……
差圧計、19……排気用弁、20a,20b……
逆止弁。
Fig. 1 is an explanatory diagram showing a typical embodiment of the present invention, Fig. 2 is an explanatory diagram showing an example of a conventional powder blowing device, and Fig. 3 is an explanatory diagram showing another embodiment of the present invention. be. 1...Carrier gas supply source, 2...Blow pressure reducing valve, 3...Blow source valve, 4...Blow circuit, 5
...Blowing source valve, 6... Pressurizing source valve, 7... Pressurizing circuit, 8... Pressure equalizing pipe, 10... Blowing tank, 11...
... powder, 12 ... powder cutting device, 13 ... blowing outlet valve, 14 ... powder blowing line, 15 ... blowing lance, 16 ... molten metal, 17 ... ladle, 18 ...
Differential pressure gauge, 19...exhaust valve, 20a, 20b...
non-return valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 吹込タンクの下部に粉体切出装置を設け、更に
その下流側に吹込出口弁を接続すると共に、上記
粉体切出装置と吹込出口弁の間から前記吹込タン
クの上部空間へ連通される均圧管を設け、該均圧
管に加圧回路を接続し、高圧に保持された吹込タ
ンク内より前記吹込出口弁を通過した粉体を、前
記加圧回路及び均圧管を介して上記吹込出口弁の
上流側から供給されてくるキヤリアガスにより、
粉体吹込ライン経由で吹込ランスに供給して溶融
金属中に吹込む粉体吹込装置において、前記均圧
管には、前記加圧回路との接続位置より吹込タン
ク上部空間側に、上記粉体切出装置の停止と同時
に閉鎖される遮断弁を配設してなることを特徴と
する粉体吹込装置。
A powder cutting device is provided at the lower part of the blowing tank, and a blowing outlet valve is further connected to the downstream side of the blowing tank. A pressure pipe is provided, and a pressurizing circuit is connected to the pressure equalizing pipe, and the powder that has passed through the blowing outlet valve from inside the blowing tank maintained at high pressure is transferred to the blowing outlet valve through the pressurizing circuit and the pressure equalizing pipe. Carrier gas supplied from the upstream side allows
In a powder blowing device that supplies powder to a blowing lance via a powder blowing line and blows it into molten metal, the pressure equalizing pipe has the powder cutter connected to the upper space side of the blowing tank from the connection position with the pressurizing circuit. A powder blowing device characterized in that it is equipped with a shutoff valve that is closed at the same time as the pumping device is stopped.
JP1985164604U 1985-10-25 1985-10-25 Expired JPH037383Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1985164604U JPH037383Y2 (en) 1985-10-25 1985-10-25

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1985164604U JPH037383Y2 (en) 1985-10-25 1985-10-25

Publications (2)

Publication Number Publication Date
JPS6275059U JPS6275059U (en) 1987-05-14
JPH037383Y2 true JPH037383Y2 (en) 1991-02-25

Family

ID=31093873

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1985164604U Expired JPH037383Y2 (en) 1985-10-25 1985-10-25

Country Status (1)

Country Link
JP (1) JPH037383Y2 (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53114706A (en) * 1977-03-09 1978-10-06 Kobe Steel Ltd Treating equipment for molten iron
JPS60121213A (en) * 1983-12-06 1985-06-28 Mitsubishi Heavy Ind Ltd Method for desulfurizing molten cr-mo cast steel

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54120505U (en) * 1978-02-10 1979-08-23
JPS5721032Y2 (en) * 1978-06-10 1982-05-07

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53114706A (en) * 1977-03-09 1978-10-06 Kobe Steel Ltd Treating equipment for molten iron
JPS60121213A (en) * 1983-12-06 1985-06-28 Mitsubishi Heavy Ind Ltd Method for desulfurizing molten cr-mo cast steel

Also Published As

Publication number Publication date
JPS6275059U (en) 1987-05-14

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