JPH0448024A - Vacuum suction type degassing device - Google Patents
Vacuum suction type degassing deviceInfo
- Publication number
- JPH0448024A JPH0448024A JP15832290A JP15832290A JPH0448024A JP H0448024 A JPH0448024 A JP H0448024A JP 15832290 A JP15832290 A JP 15832290A JP 15832290 A JP15832290 A JP 15832290A JP H0448024 A JPH0448024 A JP H0448024A
- Authority
- JP
- Japan
- Prior art keywords
- melt
- reduced pressure
- gas
- degassing
- 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
Links
Landscapes
- Treatment Of Steel In Its Molten State (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野コ
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、又は回収する真空吸引式脱ガス装置に関する
。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] 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. This invention relates to a vacuum suction type degassing 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、脱ガス処理後の融体中におけるガス生成成分の濃
度の低減が十分ではないという欠点もある。Another drawback is that the concentration of gas-forming components in the melt after degassing is not sufficiently reduced.
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、ランニングコストが
低く、融体中のガス生成成分の濃度を従来に比して低減
することができる真空吸引式脱ガス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:
Gas components in the melt can be easily removed without using large amounts of argon gas, running costs are low, and the concentration of gas-generating components in the melt can be reduced compared to conventional methods. The purpose of the present invention is to provide a vacuum suction type degassing device.
[課題を解決するための手段]
本発明に係る真空吸引式脱ガス装置は、融体を収納した
収納容器と、この収納容器内の前記融体の場面を減圧下
におく減圧手段と、前記収納容器内の前記融体中に不活
性ガスを吹き込む不活性ガス吹き込み手段と、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杖の仕切り部
材と、この仕切り部材の内部を真空下又は減圧下におい
て前記融体中のガス又は前記融体と前記仕切り部材の成
分との反応により生じたガスを吸引する吸引手段とを有
することを特徴とする。[Means for Solving the Problems] A vacuum suction type degassing apparatus according to the present invention includes: a storage container containing a molten material; a depressurizing means for placing the molten material in the storage container under reduced pressure; an inert gas blowing means for blowing an inert gas into the molten material in the storage container; and a porous 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 partition member of a bottomed cylindrical cane, and a suction means for sucking gas in the melt or gas generated by a reaction between the melt and the components of the partition member while the inside of the partition member is under vacuum or reduced pressure. It is characterized by having the following.
[作用コ
本発明においては、減圧手段が収納容器内の融体の場面
を減圧下におく。これは、例えば、融体を収納した収納
容器を減圧容器内に載置し、この減圧容器内を真空又は
減圧雰囲気にすることにより行なう。また、この場面の
減圧と同時に、不活性ガス吹き込み手段により前記収納
容器内の前記融体中に不活性ガスを吹き込む。そうする
と、融体中のガス生成成分はガス化して、不活性ガスの
気泡と共に融体の場面から例えば減圧容器内の雰囲気中
にυ[出される。また、本発明においては、融体中にガ
スを透過するが融体は透過しない多孔質材料で有底筒杖
に成形された仕切り部材が浸漬されている。そして、こ
の仕切り部材の内部は、吸引手段により真空吸引されて
真空又は減圧状態になっている。これにより、融体中の
ガス生成成分は仕切り部材を透過して仕切り部材の内部
に排出される。[Operation] In the present invention, the depressurization means places the scene of the molten material in the storage container under reduced pressure. This is carried out, for example, by placing a storage container containing the melt in a reduced pressure container and creating a vacuum or a reduced pressure atmosphere in the reduced pressure container. Further, at the same time as the pressure is reduced in this scene, an inert gas is blown into the molten material in the storage container by an inert gas blowing means. Then, the gas-generating components in the melt are gasified and ejected from the melt scene, for example, into the atmosphere in a vacuum vessel, together with inert gas bubbles. Further, in the present invention, a partition member formed into a bottomed cylinder made of a porous material that allows gas to pass through the melt but does not allow the melt to pass through is immersed. The inside of this partition member is vacuumed or under reduced pressure by the suction means. As a result, the gas-generating components in the melt pass through the partition member and are discharged into the partition member.
このようにして、本発明においては、ガス生成成分は融
体がおかれている真空又は減圧雰囲気中に排出されると
共に、融体中に浸漬された仕切り部材を介して融体中か
ら除去される。従って、融体の脱ガス処理を高効率で行
なうことができる。In this way, in the present invention, the gas generating components are discharged into the vacuum or reduced pressure atmosphere in which the melt is placed, and are also removed from the melt through the partition member immersed in the melt. Ru. Therefore, the degassing treatment of the melt can be performed with high efficiency.
第3図は多孔質部材によるガス生成成分の分離の原理を
示す模式図である。仕切り部材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、この仕
切り部材1の一方の面に前記融体2を接触させ、他方の
面を真空又は減圧雰囲気3にした場合に、融体2と接触
した壁面では融体2の静圧に無関係に圧力が低下する。FIG. 3 is a schematic diagram showing the principle of separation of gas generating components using a porous member. The partition 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. When the molten material 2 is brought into contact with one surface of the partition member 1 and the other surface is placed in a vacuum or reduced pressure atmosphere 3, the wall surface in contact with the molten material 2 is independent of the static pressure of the molten material 2. Pressure decreases.
このため、融体2中の不純物成分又は回収する価値があ
る有価成分であって、ガス相を生成するものは、容易に
仕切り部材1の壁面で核生成し、生成したガス4は仕切
り部材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 partition member 1, and the generated gas 4 is transferred to the partition member 1. It is separated from the melt 2 by passing through.
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.
瓦+、N−→Nt ・・・(1)上り
+1L−H2・・・ (2)
℃工+Ω−→CO・・・(3)
1+2Ω−→SO3・・・(4)
また、融体中の不純物が仕切り部材の多孔質材料成分と
反応してガスとなった後、前記仕切り部材を透過して除
去されることもある。Roof +, N-→Nt...(1) Upward+1L-H2... (2) ℃+Ω-→CO...(3) 1+2Ω-→SO3...(4) Also, during melting After the impurities react with the porous material component of the partition member to become a gas, the impurities may permeate through the partition member and be removed.
多孔質材料が酸化物(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 material is an oxide (MXOY), carbon in the melt is removed as a gas according to the reaction formula below.
YfL+Mx O+’ (固体)−+x[+yCO・
・・(5)
また、多孔質材料が炭素で構成されているか、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。YfL+Mx O+' (solid) -+x[+yCO・
(5) In addition, when the porous material is composed of carbon or contains carbon as one component, oxygen in the melt is removed according to the following reaction formula.
U+C(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を価成分をガス化することによ
り行なわれる。U+C (solid)→CO (6) Furthermore, the valuable component (M) having a high vapor pressure in the melt is separated and recovered by gasifying the valuable component according to the following reaction formula.
xM→M、(ガス) ・・・(7)M
Ov→Mow(ガス) ・・・(8)MS、
→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
及び有価成分が融体中から除去され、又は回収される。xM → M, (gas) ... (7) M
Ov → Mow (gas) ... (8) MS,
→MSY (gas) (9) In this way, impurity components and valuable components such as N, H, C, O, and S in the melt are removed or recovered from the melt.
この場合に、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
分と反応する仕切り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仕切り部材中の
成分との反応速度を制御することも可能である。In this case, in the present invention, the concentration of the component in the partition member that reacts with the impurities or valuable components in the target melt is adjusted according to the impurities or valuable components in the melt. It is also possible to control the rate of reaction between impurities or valuable components and components in the partition member.
なお、雰囲気及び収納容器への放熱による融体の温度の
低下、仕切り部材を融体に浸漬することによる融体の温
度の低下及び仕切り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、仕切り部材に通電するか、予め仕切り部材に
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、仕切り部材及
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, the temperature of the molten material decreases due to heat radiation to the atmosphere and the storage container, the temperature of the molten material decreases due to immersion of the partition member in the molten material, and the temperature of the molten material due to an endothermic reaction between the components of the partition member and the molten material. In order to avoid the occurrence of inconveniences caused by a decrease in the temperature, it is necessary to energize the partition member, bury a resistance wire in the partition member in advance and energize the resistance wire, or use external heating (
For example, a heating means capable of heating the partition member and the melt by a method such as plasma heating may be provided.
多孔質材料としては、At20+ 、MgO1CaO1
S io。、Fent O* 、Fea 04、Cr2
0z 、BNlS i3N、並びにSiC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、融体と接触する仕切り部材の溶
損が防止される。Porous materials include At20+, MgO1CaO1
Sio. , Fent O*, Fea 04, Cr2
Various materials can be used, such as 0z, BNlS i3N, metal oxides such as SiC and C, metal non-oxides and carbon, and mixtures thereof, but those that do not react with the main component of the melt are preferred. In this manner, by not reacting with the main component, the partition member that comes into contact with the melt is prevented from being melted and damaged.
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、仕切り部材の気孔率は、40%以下に
することが好ましい。更にまた、仕切り部材の融体への
濡れ性によって異なるが、仕切り部材の気孔径は約20
0μm以下と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 partition member is preferably 40% or less. Furthermore, although it varies depending on the wettability of the partition member to the melt, the pore diameter of the partition member is about 20
The thickness is preferably 0 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Al2O2又はMgO等とし、溶鉄中の
炭素の主酸化剤としてFe 203 +Fe304 +
MnO,S i 02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 Al2O2 or MgO, and Fe 203 +Fe304 + is used as the main oxidizing agent for carbon in molten iron.
Blend MnO, S i 02, 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Ca O* A
120 a + M g O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 CaO*A.
120 a + M g O 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濃度に
応じて前記主酸化剤の配合割合を変化させる。Furthermore, when using an illegal method to simultaneously remove carbon and nitrogen from molten iron, the blending ratio of the main oxidizer is changed depending on the target concentration 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舎
脱酸素の工程に本発明を適用することもできる。(2) The present invention can also be applied to the deoxidation process in a desulfurization chamber to remove sulfur and oxygen from molten copper matte.
■ そして、溶融鋼マット又はニッケルマット中の有価
金属(As、Sb+ B t、Se、Te。(2) Valuable metals (As, Sb+Bt, Se, Te) in the molten steel matte or nickel matte.
Pb、Cd等)の回収にも本発明を適用することができ
る。The present invention can also be applied to the recovery of Pb, Cd, etc.).
■ 更に、溶融スラグ中から有価金属(A s +S
b + B s + S e + T e + P b
、Cd + Z n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 metals (A s + S
b + B s + S e + T e + P b
, Cd + Z n, 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1図は本発明の第1の実施例装置を示す模式的断面図
である。FIG. 1 is a schematic cross-sectional view showing a first 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
は減圧容器10内に載置されている。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
られており、この気泡発生器9には配管8bを介してA
rガス等の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
is placed inside the vacuum container 10. A bubble generator 9 made of bottom-blown porous brick is provided at the bottom of the storage container 5, and a bubble generator 9 is connected to A via a pipe 8b.
Inert gas such as r gas is supplied.
また、減圧容器10は真空吸引ポンプ(図示せず)に接
続されており、減圧容器10内を減圧雰囲気にすること
ができるようになっている。Further, the reduced pressure container 10 is connected to a vacuum suction pump (not shown), so that a reduced pressure atmosphere can be created inside the reduced pressure container 10.
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
の多孔質材料で成形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、更に適宜
の真空ポンプ(図示せず)に連結された配管8aがこの
連結部材7に、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 b, and a pipe 8a connected to a suitable vacuum pump (not shown) is connected to this connecting member 7 so as to communicate with the degassing member 6. ing.
このように構成された真空吸引式脱ガス装置においては
、真空吸引ポンプにより減圧容Ws 10内を減圧雰囲
気にすると共に、気泡発生器9にArガス等を供給して
、融体2中に気泡を発生させる。In the vacuum suction type degassing apparatus configured in this way, the vacuum suction pump creates a reduced pressure atmosphere in the reduced pressure volume Ws 10, and Ar gas or the like is supplied to the bubble generator 9 to generate air bubbles in the melt 2. to occur.
また、真空ポンプにより、配管8aを介して脱ガス部材
6の内部を吸引し、脱ガス部材6の内部を真空又は減圧
状態にする。Further, the inside of the degassing member 6 is sucked through the piping 8a by a vacuum pump, and the inside of the degassing member 6 is brought into a vacuum or reduced pressure state.
これにより、融体2中の脱ガス成分は不活性ガスの気泡
と共に減圧容器10内の減圧雰囲気中に排出されると共
に、脱ガス部材6の仕切り部材6aを透過して脱ガス部
材6の内部に排出され、配管8aを介して除去される。As a result, the degassed components in the melt 2 are discharged together with the inert gas bubbles into the reduced pressure atmosphere in the decompression container 10, and are also transmitted through the partition member 6a of the degassing member 6 into the interior of the degassing member 6. and is removed via piping 8a.
このように、本実施例装置においては、融体2中の脱ガ
ス成分を減圧容器10内の減圧雰囲気中に排出させると
共に、多孔質材料からなる仕切り部材6aを介して融体
2中から除去するため、融体2の脱ガス処理速度が速い
と共に、融体中の脱ガス成分の濃度を極めて低くするこ
とができる。In this way, in the apparatus of this embodiment, the degassed components in the melt 2 are discharged into the reduced pressure atmosphere in the reduced pressure container 10, and are also removed from the melt 2 through the partition member 6a made of a porous material. Therefore, the degassing process speed of the melt 2 is high, and the concentration of the degassed components in the melt can be made extremely low.
また、不活性ガスは融体2を撹拌する程度に少量供給す
ればよいため、ランニングコストが低い。Moreover, since the inert gas only needs to be supplied in a small amount to the extent that the melt 2 is stirred, running costs are low.
第2図は本発明の第2の実施例装置を示す模式的断面図
である。FIG. 2 is a schematic cross-sectional view showing a second embodiment of the present invention.
本実施例が第1の実施例と異なる点は脱ガス部材の形状
が異なることにあり、その他の構成は基本的には第1の
実施例と同様であるので、第2図において第1図と同一
物には同一符号を付してその詳しい説明は省略する。This embodiment differs from the first embodiment in that the shape of the degassing member is different, and the other configurations are basically the same as the first embodiment. Components that are the same as those shown in FIG.
脱ガス部材12は、多孔質材料からなる複数個(図では
3個)の有底円筒状の仕切り部材12a及びこれらの仕
切り部材12aに連結したハウジング12bにより構成
されている。そして、この脱ガス部材12は真空ポンプ
(図示せず)に接続されており、この真空ポンプにより
内部が真空又は減圧状態に吸引されるようになっている
。The degassing member 12 includes a plurality of (three in the figure) bottomed cylindrical partition members 12a made of a porous material and a housing 12b connected to these partition members 12a. This degassing member 12 is connected to a vacuum pump (not shown), and the inside is sucked into a vacuum or reduced pressure state by this vacuum pump.
本実施例においては、多孔質材料からなる仕切り部材1
2aと融体2との接触面積が大きいため、第1の実施例
に比して、融体2からのガス生成成分の除去効率が高い
という長所を有している。In this embodiment, the partition member 1 made of porous material
Since the contact area between 2a and the melt 2 is large, this embodiment has the advantage that the removal efficiency of gas generating components from the melt 2 is higher than in the first embodiment.
[発明の効果]
以上説明したように本発明によれば、収納容器内に収納
した融体の湯面を減圧下におき、不活性ガス吹き込み手
段により融体中に不活性ガスを吹き込んで融体中の脱ガ
ス成分を前記減圧雰囲気中に排出させると共に、ガスを
透過するが融体は透過しない多孔質材料により有底筒状
に成形された仕切り部材を前記融体に浸漬させ、この仕
切り部材の内部を真空下又は減圧下において前記融体と
前記多孔質材料との反応により生じたガスを吸上するか
ら、融体中のガス生成成分の分離を極めて高効率で行な
うことができ、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 surface of the molten material stored in the storage container is placed under reduced pressure, and the inert gas is blown into the molten material by the inert gas blowing means. The degassing components in the body are discharged into the reduced pressure atmosphere, and a partition member formed into a bottomed cylindrical shape made of a porous material that allows gas to pass through but not the melt is immersed in the melt, and the partition member is immersed in the melt. Since the interior of the member is vacuumed or under reduced pressure to suck up the gas generated by the reaction between the melt and the porous material, the gas-generating components in the melt can be separated with extremely high efficiency; The concentration of solute components in the melt can be reduced to extremely low concentrations.
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、本発明はアルゴンガスを融体を攪拌する程度
に少量供給すれば足り、ランニングコストを著しく低減
することができる。Unlike the conventional degassing method in which a large amount of argon gas is blown into the melt, the present invention only needs to supply a small amount of argon gas to the extent that the melt is stirred, and running costs can be significantly reduced.
第1図は本発明の第1の実施例装置を示す模式的断面図
、第2図は本発明の第2の実施例装置を示す模式的断面
図、第3図は多孔質材料を利用した脱ガスの原理を示す
模式図である。
1.6a、12a;仕切り部材、2;融体、3;真空又
は減圧雰囲気、4;ガス、5;収納容器、6.12;脱
ガス部材、6b、12b;緻密質部材、7;連結部材、
8a、8b;配管、9;気泡発生器、10;減圧容器FIG. 1 is a schematic sectional view showing a first embodiment of the device of the present invention, FIG. 2 is a schematic sectional view of a second embodiment of the device of the present invention, and FIG. 3 is a schematic sectional view of a device using a porous material. FIG. 2 is a schematic diagram showing the principle of degassing. 1.6a, 12a; partition member, 2; melt, 3; vacuum or reduced pressure atmosphere, 4; gas, 5; storage container, 6.12; degassing member, 6b, 12b; dense member, 7; connecting member ,
8a, 8b; Piping, 9; Bubble generator, 10; Decompression container
Claims (2)
記融体の湯面を減圧下におく減圧手段と、前記収納容器
内の前記融体中に不活性ガスを吹き込む不活性ガス吹き
込み手段と、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を真
空下又は減圧下において前記融体中のガス又は前記融体
と前記仕切り部材の成分との反応により生じたガスを吸
引する吸引手段とを有することを特徴とする真空吸引式
脱ガス装置。(1) A storage container containing a molten material, a pressure reducing means for reducing the surface of the molten material in the storage container, and an inert gas for blowing an inert gas into the molten material in the storage container. a blowing means, a bottomed cylindrical partition member formed of a porous material that permeates gas but not permeates the melt and is immersed in the melt in the storage container, and the interior of the partition member is placed under vacuum. Alternatively, a vacuum suction type degassing device characterized by having a suction means for suctioning the gas in the melt or the gas generated by the reaction between the melt and the components of the partition member under reduced pressure.
することを特徴とする請求項1に記載の真空吸引式脱ガ
ス装置。(2) The vacuum suction type degassing device according to claim 1, further comprising a heating means for electrically heating the partition member.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2158322A JPH0830226B2 (en) | 1990-06-16 | 1990-06-16 | Vacuum suction type degasser |
| EP91109887A EP0462536A1 (en) | 1990-06-16 | 1991-06-17 | Vacuum-suction degassing method and an apparatus therefor |
| CA002044724A CA2044724C (en) | 1990-06-16 | 1991-06-17 | A vacuum-suction degassing method and an apparatus therefor |
| US08/058,792 US5306472A (en) | 1990-06-16 | 1993-05-10 | Vacuum-suction degassing method and an apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2158322A JPH0830226B2 (en) | 1990-06-16 | 1990-06-16 | Vacuum suction type degasser |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0448024A true JPH0448024A (en) | 1992-02-18 |
| JPH0830226B2 JPH0830226B2 (en) | 1996-03-27 |
Family
ID=15669108
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2158322A Expired - Lifetime JPH0830226B2 (en) | 1990-06-16 | 1990-06-16 | Vacuum suction type degasser |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0830226B2 (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5278602A (en) * | 1975-12-25 | 1977-07-02 | Toyota Motor Corp | Vacuum degassing of molten metal |
| JPS6156257A (en) * | 1984-08-25 | 1986-03-20 | Japan Metals & Chem Co Ltd | Method for degassing molten metal |
-
1990
- 1990-06-16 JP JP2158322A patent/JPH0830226B2/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5278602A (en) * | 1975-12-25 | 1977-07-02 | Toyota Motor Corp | Vacuum degassing of molten metal |
| JPS6156257A (en) * | 1984-08-25 | 1986-03-20 | Japan Metals & Chem Co Ltd | Method for degassing molten metal |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0830226B2 (en) | 1996-03-27 |
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