JPH0448021A - Method and device for degassing - Google Patents

Method and device for degassing

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Publication number
JPH0448021A
JPH0448021A JP15832390A JP15832390A JPH0448021A JP H0448021 A JPH0448021 A JP H0448021A JP 15832390 A JP15832390 A JP 15832390A JP 15832390 A JP15832390 A JP 15832390A JP H0448021 A JPH0448021 A JP H0448021A
Authority
JP
Japan
Prior art keywords
melt
gas
molten
components
partition member
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.)
Granted
Application number
JP15832390A
Other languages
Japanese (ja)
Other versions
JPH0753893B2 (en
Inventor
Masamichi Sano
佐野 正道
Nobuo Miyagawa
宮川 信夫
Kimiji Yamamoto
君二 山本
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.)
TYK Corp
Original Assignee
TYK Corp
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Filing date
Publication date
Application filed by TYK Corp filed Critical TYK Corp
Priority to JP15832390A priority Critical patent/JPH0753893B2/en
Publication of JPH0448021A publication Critical patent/JPH0448021A/en
Publication of JPH0753893B2 publication Critical patent/JPH0753893B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Abstract

PURPOSE:To easily remove the gaseous components in a melt with a small amt. of gaseous Ar by dropping the partial pressure of the gaseous components in the melt on the outside partitioned from the melt with a porous member which allows the diffusion of gases but does not allow the infiltration of the melts in an inert gaseous atmosphere. CONSTITUTION:The melt 2 is brought into contact with one surface of the porous member 1 which allows the diffusion of only the gases but does not allow the infiltration of the melts, such as molten metal, molten matte and molten slag. The other surface is formed as the inert gaseous atmosphere 3 of Ar, etc., and the atmosphere 3 is maintained under the pressure lower than the partial pressure of the gaseous components in the melt 2. Then the gaseous components in the melt 2 move from the side of the higher partial pressure thereof to the lower pressure side, i.e., from the inside of the melt 2 into the atmosphere 3. The impurity components in the melt 2 or the valuable components which are of value to be recovered and form the gaseous phase are easily nucleus-formed on the wall surface of the porous member 1. The formed gases 4 diffuse through the porous member 1 and are separated from the melt 2.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、多孔質部材を介して、溶融金属、溶融マット
及び溶融スラグ等の融体からガス相を生成する溶質成分
を除去し、又は回収する脱ガス方法及び装置に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention is a method for removing solute components that generate a gas phase from a melt such as a molten metal, a molten matte, and a molten slag through a porous member; The present invention relates to a degassing method and device for recovery.

[従来の技術] 溶融金属、溶融マット及び溶融スラグ等の融体から、ガ
ス相を生成する溶質成分を除去し、又は回収する技術と
して、従来、RH法及びDH法等の脱ガス法がある。こ
のRH法及びDH法は、真空下又は減圧下において溶湯
中に大量のアルゴンガスを吹き込み、溶湯中のガス成分
の分圧を低下させてこのガス成分を除去している。
[Prior Art] Conventionally, there are degassing methods such as the RH method and the DH method as technologies for removing or recovering solute components that generate a gas phase from melts such as molten metal, molten matte, and molten slag. . In the RH method and the DH method, a large amount of argon gas is blown into the molten metal under vacuum or reduced pressure to lower the partial pressure of the gas component in the molten metal and remove this gas component.

[発明が解決しようとする課題] しかしながら、この従来のRH法及びDH法による脱ガ
ス法は、大量のアルゴンガスを使用するため、ランニン
グコストが高いという欠点がある。
[Problems to be Solved by the Invention] However, the conventional degassing methods using the RH method and the DH method use a large amount of argon gas, and therefore have a drawback of high running costs.

また、大量のアルゴンガスを溶湯中に吹き込むので、溶
湯からスプラッシュが発生し易く、装置の壁面等に地金
が付着し、その除去作業が煩雑である。更に、このスプ
ラッシュが発生するため、装置を大型にせざるを得ず、
装置コストも高い。
In addition, since a large amount of argon gas is blown into the molten metal, splashes are likely to occur from the molten metal, and base metal adheres to the walls of the apparatus, making removal work complicated. Furthermore, because this splash occurs, the equipment has to be made larger.
Equipment costs are also high.

本発明はかかる問題点に鑑みてなされたものであって、
融体中のガス成分を大量のアルゴンガスを使用すること
なく、容易に除去することができ、融体の脱ガスを簡素
な装置で低コストで実施することができる脱ガス方法及
び装置を提供することを目的とする。
The present invention has been made in view of such problems, and includes:
Provided is a degassing method and device that can easily remove gas components in a melt without using a large amount of argon gas, and can degas the melt with a simple device at low cost. The purpose is to

[課題を解決するための手段] 本発明に係る脱ガス方法は、ガスを透過するが融体は透
過しない多孔質部材により融体と外界とを仕切り、前記
外界側を不活性ガス雰囲気において、前記融体中のガス
成分の分圧を低下させることにより、前記ガス成分を除
去することを特徴とする。
[Means for Solving the Problems] The degassing method according to the present invention partitions the melt from the outside world with a porous member that allows gas to pass through but not the melt, and places the outside world side in an inert gas atmosphere. The method is characterized in that the gas component is removed by lowering the partial pressure of the gas component in the melt.

また、本発明に係る脱ガス装置は、融体を収納した収納
容器と、ガスを透過するが融体は透過しない多孔質材料
で成形され前記収納容器内の前記融体中に浸漬された有
底筒状の仕切り部材と、この仕切り部材の内部に不活性
ガスを送給してこの内部における前記融体中のガス成分
の分圧を低下させる不活性ガス送給手段と、前記融体中
のガス又は前記融体と前記仕切り部材との反応により生
じたガスを前記仕切り部材の内部から排出する排出手段
とを有することを特徴とする。
Further, the degassing device according to the present invention includes a storage container containing a molten material, and a material formed of a porous material that permeates gas but not the molten material and is immersed in the molten material in the storage container. a bottom cylindrical partition member; an inert gas feeding means for feeding an inert gas into the partition member to reduce the partial pressure of the gas component in the melt inside the partition member; or a gas generated by a reaction between the molten material and the partition member, the apparatus further comprises a discharge means for discharging the gas produced by the reaction between the melt and the partition member from inside the partition member.

[作用] 第1図は本発明の原理を示す模式図である。多孔質部材
1は、ガスのみを透過し、溶融金属、溶融マット及び溶
融スラグ等の融体は透過しない多孔質材料からなる部材
である。そして、この多孔質部材1の一方の面に前記融
体2を接触させ、他方の面をAr又はN2等の不活性ガ
ス雰囲気3にしてこの他方の面側の雰囲気3を融体2中
のガス成分の分圧より低い状態にする。そうすると、融
体2中のガス成分はその分圧の高いほうから低いほうへ
、即ち、融体2中から不活性ガス雰囲気3中に移動する
。
[Operation] FIG. 1 is a schematic diagram showing the principle of the present invention. The porous member 1 is a member made of a porous material that allows only gas to pass therethrough and does not allow melts such as molten metal, molten matte, and molten slag to pass therethrough. Then, the molten material 2 is brought into contact with one surface of the porous member 1, and the other surface is made into an inert gas atmosphere 3 such as Ar or N2, and the atmosphere 3 on the other surface side is changed to the atmosphere 3 in the molten material 2. Make the partial pressure lower than the partial pressure of the gas component. Then, the gas components in the melt 2 move from the higher partial pressure to the lower partial pressure, that is, from the melt 2 to the inert gas atmosphere 3.

このため、融体2中の不純物成分又は回収する価値があ
る仔価成分であって、ガス相を生成するものは、容易に
多孔質部材1の壁面で核生成し、生成したガス4は多孔
質部材1を透過して融体2から分離される。
Therefore, impurity components in the melt 2 or valuable components worth recovering that generate a gas phase easily nucleate on the wall surface of the porous member 1, and the generated gas 4 It passes through the mass member 1 and is separated from the melt 2.

本願発明者等はこのような原理に基づいて融体中からガ
ス成分を除去できることに想到し、本発明を完成させる
に至ったものである。
The inventors of the present invention have come up with the idea that gas components can be removed from a molten material based on such a principle, and have completed the present invention.

而して、融体中に溶解しているガス生成成分は下記の反
応式により、ガスとなって除去される。
Thus, the gas-generating components dissolved in the melt are removed in the form of gas according to the reaction formula below.

止十瓦→N2          ・・・(1)比+比
→H2・・・(2) U+Ω−→CO・・・(3) 名ヨ+2.0−→SO2・・・ (4)また、融体中の
不純物が多孔質部材の成分と反応してガスとなった後、
前記多孔質部材を透過して除去されることもある。
Tojugawara → N2 ... (1) Ratio + ratio → H2 ... (2) U + Ω- → CO ... (3) Name +2.0- → SO2 ... (4) Also, molten material After the impurities inside react with the components of the porous member and become gas,
It may also be removed by passing through the porous member.

多孔質部材が酸化物(MXOY)の場合には、融体中の
炭素は下記反応式によりガスとなって除去される。
When the porous member is an oxide (MXOY), carbon in the melt is removed as a gas according to the following reaction formula.

yL+Mx Oy  (固体)+x、li+3’c。yL+Mx Oy (solid) +x, li+3'c.

・・・(5) また、多孔質部材が炭素で構成されているが、又は炭素
を1成分として含有している場合には、下記反応式によ
り融体中の酸素が除去される。
(5) Furthermore, when the porous member is made of carbon or contains carbon as one component, oxygen in the melt is removed according to the following reaction formula.

1十〇(固体)→CO・・・(6) 更に、融体中の蒸気圧が高い有価成分(M)の分離回収
は下記反応式により前記有価成分をガス化することによ
り行なわれる。
100 (solid) → CO (6) Furthermore, the separation and recovery of the valuable component (M) with a high vapor pressure in the melt is carried out by gasifying the valuable component according to the following reaction formula.

xM−+Mx  (ガス)        ・・・(7
)MOY→MoV (ガス)      ・・・(8)
M S v→MSY (ガス)      ・・・(9
)このようにして、融体中のN、H,C,O及びS等の
不純物成分及び仔価成分が融体中がら除去され、又は回
収される。
xM-+Mx (gas)...(7
) MOY → MoV (gas) ... (8)
M S v → MSY (gas) ... (9
) In this way, impurity components such as N, H, C, O, and S in the melt and the free components are removed or recovered from the melt.

多孔質部材を介して融体側と他方の側とのガス成分の分
圧の差によりガスを融体がら分離するためには、前記他
方の側を真空又は減圧雰囲気にすることも考えられる。
In order to separate the gas from the melt by the difference in partial pressure of gas components between the melt side and the other side via the porous member, it is conceivable to create a vacuum or reduced pressure atmosphere on the other side.

しかし、前記他方の側の圧力を極端に低減すると、融体
が多孔質部材中に浸透し、多孔質部材の多孔内で凝固し
て孔を閉塞してしまう虞れがある。そうすると、ガス分
離効率が低減してしまう。そこで、本発明においては、
多孔質部材の融体に接触する面に対応する他方の面を不
活性ガス雰囲気にする。これにより、前記他方の側には
前記ガス成分の分圧が低い雰囲気が得られ、他方の側の
圧力を極端に低下させなくても、前記多孔質部材の両側
にはガス成分の分圧の差が発生し、ガス成分を融体から
分離することができる。
However, if the pressure on the other side is extremely reduced, there is a risk that the melt will penetrate into the porous member, solidify within the pores of the porous member, and block the pores. In this case, the gas separation efficiency will be reduced. Therefore, in the present invention,
The other surface of the porous member corresponding to the surface that contacts the melt is placed in an inert gas atmosphere. As a result, an atmosphere in which the partial pressure of the gas component is low is obtained on the other side, and even if the pressure on the other side is not extremely reduced, the gas component is in a low partial pressure on both sides of the porous member. A difference is generated and the gas components can be separated from the melt.

また、本発明においては、対象とする融体中の不純物又
は有価成分に応じて、これらの不純物又は有価成分と反
応する多孔質部材中の成分の濃度を調整することにより
、融体中の不純物又は有価成分と多孔質部材中の成分と
の反応速度を制御することも可能である。
Furthermore, in the present invention, impurities in the melt can be reduced by adjusting the concentration of components in the porous member that react with impurities or valuable components in the target melt. Alternatively, it is also possible to control the reaction rate between the valuable component and the component in the porous member.

なお、多孔質部材の周囲の融体中における物質移動を促
進するために、例えば融体中に不活性ガスを吹き込むか
、又は多孔質部材の回転若しくは揺動等の方法により融
体を攪拌する攪拌手段を設けることが好ましい。また、
雰囲気及び収納容器への放熱による融体の温度の低下、
多孔質部材を融体に浸漬することによる融体の温度の低
下及び多孔質部材の成分と融体との吸熱反応による融体
の温度の低下等に起因する不都合の発生を回避するため
に、多孔質部材に通電するか、予め多孔質部材に抵抗線
を埋設しこの抵抗線に通電するか又は外部加熱(例えば
、プラズマ加熱)等の方法により、多孔質部材及び融体
を加熱することができる加熱手段を設けておいてもよい
。
In addition, in order to promote mass transfer in the molten material around the porous member, the molten material is stirred by, for example, blowing an inert gas into the molten material, or by rotating or rocking the porous member. Preferably, a stirring means is provided. Also,
Decreasing the temperature of the melt due to heat radiation to the atmosphere and storage container,
In order to avoid the occurrence of inconveniences caused by a decrease in the temperature of the melt due to immersion of the porous member in the melt and a decrease in the temperature of the melt due to an endothermic reaction between the components of the porous member and the melt, The porous member and the melt can be heated by applying electricity to the porous member, by embedding a resistance wire in the porous member in advance and applying electricity to the resistance wire, or by external heating (for example, plasma heating). A heating means that can be used may be provided.

多孔質部材としては、A I 203 、M g O。As the porous member, AI 203, MgO.

Cabs S ioa 、Fe20a % F e* 
04、Cra O3、BNN S i3N4並びにSi
C及びC等の金属酸化物、金属非酸化物及び炭素並びに
これらの混合物等、種々のものを使用することができる
が、融体の主成分と反応しないものが好ましい。このよ
うに、主成分と反応しないことにより、融体と接触する
多孔質部材の溶損が防止される。
Cabs Sioa, Fe20a% Fe*
04, Cra O3, BNN S i3N4 and Si
Various materials can be used, such as metal oxides such as C and C, metal non-oxides, carbon, and mixtures thereof, but materials that do not react with the main component of the melt are preferred. In this way, by not reacting with the main component, erosion of the porous member that comes into contact with the melt is prevented.

また、ガスのみを透過させ、融体は透過させないように
するため、融体に濡れにくい多孔質材料の仕切り部材を
使用する。更に、多孔質の仕切り部材の気孔率は、40
%以下にすることが好ましい。
Furthermore, in order to allow only the gas to pass through and not the molten material, a partition member made of a porous material that is difficult to get wet with the molten material is used. Furthermore, the porosity of the porous partition member is 40
% or less.

更にまた、仕切り部材の融体への濡れ性によっても異な
るが、仕切り部材の気孔径は約200μm以下とするこ
とが好ましい。
Furthermore, although it varies depending on the wettability of the partition member to the melt, it is preferable that the pore diameter of the partition member is about 200 μm or less.

更にまた、多孔質浸漬管へ融体が侵入しても、真空系へ
融体が入るのを防止するため、圧力損失が小さいフィル
タを多孔質浸漬管上部に設置し、侵入した融体をこのフ
ィルタで凝固させ、トラップするようにすることが好ま
しい。
Furthermore, in order to prevent molten material from entering the vacuum system even if it enters the porous immersion tube, a filter with low pressure loss is installed at the top of the porous immersion tube to prevent the molten material from entering the porous immersion tube. It is preferable to coagulate and trap it in a filter.

次に、本発明を融体からのガス生成成分の除去回収に適
用した用途例について説明する。
Next, an application example in which the present invention is applied to the removal and recovery of gas generating components from a melt will be described.

■ 先ず、本発明を、溶鉄から炭素、窒素又は水素を除
去する脱炭素、脱窒素及び脱水素の工程に使用すること
ができる。
(1) First, the present invention can be used in decarbonization, denitrification, and dehydrogenation processes for removing carbon, nitrogen, or hydrogen from molten iron.

溶鉄中の炭素の除去に不法を使用する場合、前記仕切り
部材の主成分はAl2O3又はMgO等とし、溶鉄中の
炭素の主酸化剤としてF e 2031Fe3041 
MnO,S io2等を配合する。これらの主酸化剤の
配合割合を高くすることにより、溶鉄中の酸素の除去速
度を増加させることができる。しかし、主酸化剤の配合
割合をあまり高くすると、仕切り部材の融点の低下又は
機械的強度の低下等を招き、また特に溶鉄中の炭素濃度
が低い場合には溶鉄中の酸素濃度が増加するため、目的
に応じて主酸化剤の配合割合を既に確立されている状態
図を参考にして決定する。
When illegally removing carbon from molten iron, the main component of the partition member is Al2O3 or MgO, and Fe 2031Fe3041 is used as the main oxidizing agent for carbon in molten iron.
Blend MnO, Sio2, etc. By increasing the blending ratio of these main oxidizing agents, the rate of oxygen removal from molten iron can be increased. However, if the blending ratio of the main oxidizing agent is too high, it will lower the melting point or mechanical strength of the partition member, and especially if the carbon concentration in the molten iron is low, the oxygen concentration in the molten iron will increase. Depending on the purpose, the blending ratio of the main oxidizing agent is determined with reference to the already established phase diagram.

一方、溶鉄中の窒素の除去に不法を使用する場合、前記
仕切り部材には、安定な酸化物、例えばCab、Ar1
03.MgO等を使用する。
On the other hand, if illegal methods are used to remove nitrogen from molten iron, the partition member may contain stable oxides such as Cab, Ar1, etc.
03. MgO etc. are used.

また、溶鉄中の炭素及び窒素を同時に除去するために不
法を使用する場合、溶鉄中の炭素及び窒素の目標潤度に
応じて前記主酸化剤の配合割合を変化させる。
Further, when using an illegal method to simultaneously remove carbon and nitrogen from molten iron, the blending ratio of the main oxidizing agent is changed depending on the target moisture content of carbon and nitrogen in molten iron.

■ また、本発明を、溶鋼中から酸素を除去する脱酸工
程にも適用することができる。
(2) The present invention can also be applied to a deoxidation process for removing oxygen from molten steel.

■ 更に、本発明は溶融アルミニウム中から水素を除去
する脱水素工程にも適用することができる。
(2) Furthermore, the present invention can also be applied to a dehydrogenation process for removing hydrogen from molten aluminum.

■ 更にまた、本発明を、溶融シリコンの脱炭素、脱窒
素及び脱水素に適用することができる。
(2) Furthermore, the present invention can be applied to decarbonization, denitrification, and dehydrogenation of molten silicon.

■ 一方、本発明により、溶融船中の亜鉛を回収するこ
とができる。
(2) On the other hand, according to the present invention, zinc in the melting vessel can be recovered.

■ 溶融銅マットから硫黄及び酸素を除去する脱硫黄・
脱酸素の工程に本発明を適用することもできる。
■ Desulfurization and removal of sulfur and oxygen from molten copper matte
The present invention can also be applied to the process of deoxidizing.

■ そして、溶融銅マット又はニッケルマット中の有価
金属(As+  Sb、B i、Set Te+Pb、
Cd等)の回収にも本発明を適用することができる。
■ Valuable metals in the molten copper matte or nickel matte (As+Sb, Bi, Set Te+Pb,
The present invention can also be applied to the recovery of Cd, etc.).

■ 更に、溶融スラグ中から有価金n (A s +S
b+ Bit Se、Te、pb、cd、Zn等)を回
収する場合にも、本発明を適用することができる。
■ Furthermore, valuable gold n (A s + S
The present invention can also be applied to the case of recovering (b+ Bit Se, Te, pb, cd, Zn, etc.).

[実施例コ 次に、本発明の実施例について添付の図面を参照して説
明する。
[Embodiments] Next, embodiments of the present invention will be described with reference to the accompanying drawings.

第2図は本発明の実施例に係る脱ガス装置を示す模式的
断面図である。
FIG. 2 is a schematic cross-sectional view showing a degassing device according to an embodiment of the present invention.

融体2は収納容器5に収納されており、この収納容器5
の底部には底吹きポーラスレンガからなる気泡発生器9
が設けられている。この気泡発生器9には、配管8Cを
介して不活性ガスが供給されるようになっている。
The molten material 2 is stored in a storage container 5, and this storage container 5
A bubble generator 9 made of bottom-blown porous brick is installed at the bottom of the
is provided. Inert gas is supplied to this bubble generator 9 via a pipe 8C.

融体2には脱ガス部材6の下半部が浸漬されている。こ
の脱ガス部材6は下端が閉塞した円筒状をなし、融体2
内に浸漬される下半部は、ガスは透過するが、溶融金属
、溶融スラグ及び溶融マット等の融体2は侵入できない
ような細孔を有していて、この融体2は透過しない多孔
質の材料で成形されている。この脱ガス部材6の下半部
の多孔質材料で形成された部分が仕切り部材6aである
。
The lower half of the degassing member 6 is immersed in the melt 2 . This degassing member 6 has a cylindrical shape with a closed lower end, and the molten material 2
The lower half that is immersed in the interior has pores that allow gas to pass through but prevent molten material 2 such as molten metal, molten slag, and molten matte from penetrating. Molded from quality materials. A portion formed of a porous material in the lower half of this degassing member 6 is a partition member 6a.

また、脱ガス部材6の上半部はガスを透過しない緻密質
の部材6bにより形成されている。この仕切り部材6a
と緻密質部材6bとは夫々別個に作成した後、両者を接
合して一体化してもよいし、多孔質材料で脱ガス部材6
の全体を作成した後、緻密質部材6bの部分にガスを透
過しない緻密質材料をコーティングする等の方法により
、この部分をガス非透過性にしてもよい。
Further, the upper half of the degassing member 6 is formed of a dense member 6b that does not allow gas to pass through. This partition member 6a
The degassing member 6b and the dense member 6b may be created separately and then joined together to integrate them, or the degassing member 6b may be made of a porous material.
After creating the entire dense member 6b, this portion may be made gas-impermeable by coating the portion with a gas-impermeable dense material.

この融体2の上に露出するガス非透過性の緻密質部材6
bの上端部には連結部材7が固定されており、更にAr
又はN2等の不活性ガス供給源(図示せず)に接続され
た配管8a及び融体2から分離した脱ガス成分を脱ガス
部材6から排出するための配管8bが、脱ガス部材6と
連通ずるようにして連結されている。
A gas-impermeable dense member 6 exposed above the melt 2
A connecting member 7 is fixed to the upper end of the
Alternatively, a pipe 8a connected to an inert gas supply source (not shown) such as N2 and a pipe 8b for discharging the degas components separated from the melt 2 from the degas member 6 are connected to the degas member 6. They are connected so that they can communicate.

このように構成された脱ガス装置においては、配管8C
を介してArガス又はN2ガス等の不活性ガスを気泡発
生器9に供給して、融体2中に気泡を発生させて、融体
2を攪拌する。また、配管8aを介して、不活性ガス供
給源から脱ガス部材6の内部にArガス又はN2ガス等
の不活性ガスを供給し、脱ガス部材6の内部を不活性ガ
ス雰囲気にする。そうすると、融体2中の脱ガス成分は
、その分圧の差により仕切り部材6aを透過して脱ガス
部材6の内側に移動する。そして、配管8bを介して脱
ガス部材6の外部に排出される。このようにして、本実
施例装置により融体2の脱ガス処理を行なうことができ
る。
In the degassing device configured in this way, the pipe 8C
An inert gas such as Ar gas or N2 gas is supplied to the bubble generator 9 through the bubble generator 9 to generate bubbles in the melt 2 and stir the melt 2. Further, an inert gas such as Ar gas or N2 gas is supplied from an inert gas supply source to the inside of the degassing member 6 via the piping 8a to create an inert gas atmosphere inside the degassing member 6. Then, the degas components in the melt 2 pass through the partition member 6a and move inside the degas member 6 due to the difference in partial pressure. Then, it is discharged to the outside of the degassing member 6 via the pipe 8b. In this manner, the molten material 2 can be degassed by the apparatus of this embodiment.

なお、上述の実施例においては、融体攪拌手段として、
底吹きポーラスレンガからなる気泡発生器9を介して融
体2中に不活性ガスを吹き込む場合について説明したが
、例えば収納容器5の上方にランスパイプを設置し、こ
のランスパイプの下端を収納容器5内の融体2中に浸漬
することにより、このランスパイプを介して融体2中に
不活性ガスを吹き込んでもよい。また、脱ガス部材6を
融体2中で移動させ、これにより融体2を攪拌してもよ
い。
In addition, in the above-mentioned embodiment, as the melt stirring means,
The case has been described in which inert gas is blown into the melt 2 through the bubble generator 9 made of bottom-blown porous bricks. For example, a lance pipe is installed above the storage container 5, and the lower end of this lance pipe is connected to the storage container. By dipping into the melt 2 in the lance pipe 5, an inert gas may be blown into the melt 2 through this lance pipe. Alternatively, the degassing member 6 may be moved within the melt 2, thereby stirring the melt 2.

[発明の効果コ 以上説明したように本発明によれば、ガスを透過するが
融体は透過しない多孔質部材により融体と外界とを仕切
り、前記外界側を不活性ガス雰囲気において前記融体中
のガス成分の分圧を低下させることによりこのガス成分
を前記融体から除去するから、脱ガス成分をその分圧の
差により前記外界に移動させることができる。また、本
発明装置においては、多孔質部材の融体と接触する面積
を任意に大きく設定することができるので、融体中の溶
質成分の濃度を極めて低い濃度にまで低下させることが
できる。
[Effects of the Invention] As explained above, according to the present invention, the molten material and the outside world are partitioned by a porous member that allows gas to pass through but not the molten material, and the outside world side is separated from the molten material in an inert gas atmosphere. Since this gas component is removed from the melt by lowering the partial pressure of the gas component therein, the degassed component can be transferred to the outside world due to the difference in the partial pressure. Furthermore, in the apparatus of the present invention, since the area of the porous member in contact with the melt can be set arbitrarily large, the concentration of solute components in the melt can be reduced to an extremely low concentration.

そして、大量のアルゴンガスを吹き込む従来の脱ガス法
と異なり、本発明は不活性ガスを仕切り部材内側の脱ガ
ス成分の分圧が低下する程度に少量供給すれば足り、ア
ルゴンガスの使用原単位を著しく低減することができる
。また、アルゴンガスの使用量が極めて少ないことから
、スプラッシュの発生が抑制され、装置の壁面への地金
の付着を低減することができる。従って、本発明により
、装置の小型化による装置コストの低減、更に装置のラ
ンニングコストの著しい低減を実現することができる。
Unlike the conventional degassing method that blows in a large amount of argon gas, the present invention only needs to supply a small amount of inert gas to the extent that the partial pressure of the degassed component inside the partition member decreases, and the unit consumption rate of argon gas is can be significantly reduced. Furthermore, since the amount of argon gas used is extremely small, the occurrence of splash can be suppressed, and the adhesion of metal to the wall surface of the apparatus can be reduced. Therefore, according to the present invention, it is possible to reduce the cost of the device by downsizing the device, and also to significantly reduce the running cost of the device.

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

第1図は本発明の原理を示す模式図、第2図は本発明の
実施例に係る脱ガス装置を示す模式的断面図である。 1;多孔質部材、 囲気、4;ガス、5 6a;仕切り部材、 部材、8a、8b。 2;融体、3;不活性ガス雰 ;収納容器、6;脱ガス部材、 6b;緻密質部材、7;連結 8b;配管、9;気泡発生器
FIG. 1 is a schematic diagram showing the principle of the present invention, and FIG. 2 is a schematic sectional view showing a degassing device according to an embodiment of the present invention. 1; porous member, surrounding air, 4; gas, 5 6a; partition member, member, 8a, 8b. 2; Melt, 3; Inert gas atmosphere; Storage container, 6; Degassing member, 6b; Dense member, 7; Connection 8b; Piping, 9; Bubble generator

Claims (4)

【特許請求の範囲】[Claims] (1)ガスを透過するが融体は透過しない多孔質部材に
より融体と外界とを仕切り、前記外界側を不活性ガス雰
囲気において、前記融体中のガス成分の分圧を低下させ
ることにより、前記ガス成分を除去することを特徴とす
る脱ガス方法。
(1) By partitioning the melt from the outside world with a porous member that allows gas to pass through but not the melt, and by lowering the partial pressure of the gas components in the melt by placing the outside world in an inert gas atmosphere. , a degassing method characterized by removing the gas component.
(2)融体を収納した収納容器と、ガスを透過するが融
体は透過しない多孔質材料で成形され前記収納容器内の
前記融体中に浸漬された有底筒状の仕切り部材と、この
仕切り部材の内部に不活性ガスを送給してこの内部にお
ける前記融体中のガス成分の分圧を低下させる不活性ガ
ス送給手段と、前記融体中のガス又は前記融体と前記仕
切り部材との反応により生じたガスを前記仕切り部材の
内部から排出する排出手段とを有することを特徴とする
脱ガス装置。
(2) a storage container that stores a molten material; a bottomed cylindrical partition member formed of a porous material that allows gas to pass through but not the molten material and is immersed in the molten material in the storage container; an inert gas feeding means for feeding an inert gas into the interior of the partition member to reduce the partial pressure of the gas component in the melt inside the partition member; 1. A degassing device comprising: a discharge means for discharging gas generated by reaction with the partition member from inside the partition member.
(3)前記融体を攪拌する攪拌手段を有することを特徴
とする請求項2に記載の脱ガス装置。
(3) The degassing device according to claim 2, further comprising a stirring means for stirring the melt.
(4)前記仕切り部材を電気的に加熱する加熱手段を有
することを特徴とする請求項2又は3に記載の脱ガス装
置。
(4) The degassing device according to claim 2 or 3, further comprising a heating means for electrically heating the partition member.
JP15832390A 1990-06-16 1990-06-16 Degassing method and device Expired - Lifetime JPH0753893B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15832390A JPH0753893B2 (en) 1990-06-16 1990-06-16 Degassing method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15832390A JPH0753893B2 (en) 1990-06-16 1990-06-16 Degassing method and device

Publications (2)

Publication Number Publication Date
JPH0448021A true JPH0448021A (en) 1992-02-18
JPH0753893B2 JPH0753893B2 (en) 1995-06-07

Family

ID=15669131

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15832390A Expired - Lifetime JPH0753893B2 (en) 1990-06-16 1990-06-16 Degassing method and device

Country Status (1)

Country Link
JP (1) JPH0753893B2 (en)

Also Published As

Publication number Publication date
JPH0753893B2 (en) 1995-06-07

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