JP2850064B2 - Processing equipment for used molten salt bath - Google Patents
Processing equipment for used molten salt bathInfo
- Publication number
- JP2850064B2 JP2850064B2 JP21788191A JP21788191A JP2850064B2 JP 2850064 B2 JP2850064 B2 JP 2850064B2 JP 21788191 A JP21788191 A JP 21788191A JP 21788191 A JP21788191 A JP 21788191A JP 2850064 B2 JP2850064 B2 JP 2850064B2
- Authority
- JP
- Japan
- Prior art keywords
- molten salt
- water
- water tank
- temperature
- salt bath
- 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 - Fee Related
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- Electrolytic Production Of Metals (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は、溶融塩浴適用のめっ
き装置や金属電解採取装置から排出される使用済み溶融
塩浴を処理するために、その一部又は全量を水に溶解さ
せる装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for dissolving a part or the whole of a used molten salt bath discharged from a plating apparatus or a metal electrowinning apparatus using a molten salt bath. Things.
【0002】[0002]
【従来技術とその課題】従来、溶融塩を電解浴とするめ
っき装置や金属の電解採取装置等から排出される使用済
み溶融塩浴の処理には、 a) 使用済み溶融塩浴を廃棄用容器に入れて冷却・凝固
させ、これを水で溶解して処理する方法, b) 使用済み溶融塩浴を大容量の水槽に直接流し込んで
溶解し処理する方法,等の手段が採用されている。2. Description of the Related Art Conventionally, the treatment of a used molten salt bath discharged from a plating apparatus using a molten salt as an electrolytic bath, a metal electrowinning apparatus, and the like includes the steps of: a) disposing a used molten salt bath in a waste container; And cooling and coagulation, and dissolving and dissolving this with water. B) A method of directly pouring a used molten salt bath into a large-capacity water tank and dissolving and treating it.
【0003】上記a)法としては、廃棄用容器として容量
の大きいものを用い廃棄対象溶融塩浴の全てを一度に注
入して冷却・凝固させる手法と、廃棄用容器として小容
積のものを使い数回に分けて溶融塩を冷却・凝固させる
手法とが行われており、何れの場合も容器内で溶融塩を
冷却し固形物にしてから水で溶解する処理がなされる
が、使用する装置の規模や周辺設備等の状況に応じて何
れの手法を採用するかが決定される。そして、これらの
方法に従って使用済み溶融塩を水に溶解させる際には、
廃棄用容器内で凝固した溶融塩をそのまま大きな塊の状
態で水槽内へ投入するのが一般的であるが、凝固物を細
かく粉砕して溶解させる場合もある。[0003] As the above-mentioned method a), a large-capacity container is used as a disposal container, and all of the molten salt bath to be disposed is poured at a time to cool and solidify, or a small-volume disposal container is used. The method of cooling and solidifying the molten salt in several times is performed, and in any case, the treatment of cooling the molten salt in a container to a solid substance and then dissolving with water is performed, but the equipment used Which method is to be adopted is determined according to the size of the equipment and the status of peripheral equipment. And when dissolving the used molten salt in water according to these methods,
In general, the molten salt solidified in the waste container is directly introduced into the water tank in a large lump state, but the coagulated material may be finely pulverized and dissolved.
【0004】しかし、このa)法では、処理する溶融塩が
小量であれば格別な問題はないが、大量になると廃棄用
容器中での凝固に時間がかかるので処理に多大な時間を
要するようになる。また、大量の溶融塩浴を処理する場
合、廃棄用容器中に注入した溶融塩が凝固・固形化する
まで容器を放置しておく必要があるため、容器の置き場
所として大きなスペ−スが必要である。In the method a), however, there is no particular problem if the amount of the molten salt to be treated is small, but if the amount is large, it takes a long time for coagulation in a disposal container, so that much time is required for the treatment. Become like Also, when treating a large amount of molten salt bath, it is necessary to leave the container until the molten salt injected into the disposal container solidifies and solidifies. It is.
【0005】しかも、前記a)法によると、処理する溶融
塩の温度が高温である場合、廃棄用容器の温度が低いと
急激な熱応力による変形で容器が破壊する恐れがある
上、容器に水分が付着していると水蒸気爆発を起こす危
険性もあるので、処理に当って予め容器を溶融塩温度近
くまで加熱しておく必要が出てくる。In addition, according to the above-mentioned method a), when the temperature of the molten salt to be treated is high, if the temperature of the disposal container is low, the container may be destroyed by deformation due to rapid thermal stress, and If water is attached, there is a risk of causing a steam explosion, so that it is necessary to heat the container to a temperature close to the molten salt temperature in advance in the treatment.
【0006】一方、前記b)法では、輸送管を使えばa)法
と異なって固体状態での搬送工程が省略でき、そのため
連続処理を行うことが容易であったが、反面、次のよう
な問題があった。即ち、溶融塩を水に溶解すると反応熱
により溶融塩溶解用水槽の水温が高くなるが、水温が高
くなると水と溶融塩の反応が爆発的に加速されるのでこ
れを防止するのに大容量の水槽が必要となる。従って、
設備コストが高くなることに加えて処理装置の設置スペ
−スも大きくなる。特に、溶融塩は冷却されると固まっ
て輸送用配管の閉塞を招くため余り遠方への移送は容易
でなく、従って溶融塩装置(めっき装置や電解採取装
置)の近傍に上述した大型(大容量)の処理設備を設置
しなければならず好ましくない。また、こうした大型設
備では溶融塩が水に溶解した時の反応により発生するヒ
ュ−ムの捕捉が困難となり、環境汚染の防止面からも不
利であった。On the other hand, in the above-mentioned method b), unlike the method a), the use of a transport pipe makes it possible to omit the transportation step in a solid state, and thus it is easy to carry out a continuous treatment. There was a problem. That is, when the molten salt is dissolved in water, the heat of reaction increases the temperature of the molten salt dissolving water tank. However, when the water temperature is increased, the reaction between the water and the molten salt is explosively accelerated. Water tank is required. Therefore,
In addition to the increase in equipment cost, the installation space for the processing apparatus also increases. In particular, when the molten salt is cooled, it hardens and consequently clogs the transport piping, so it is not easy to transport the molten salt to a distant place. Therefore, the above-described large (large capacity) It is not preferable to install the processing equipment of (1). Further, in such a large-sized facility, it is difficult to capture fumes generated by a reaction when the molten salt is dissolved in water, which is disadvantageous in terms of preventing environmental pollution.
【0007】このようことから、本発明が目的としたの
は、大規模な設備や処理スペ−スを要することなく使用
済みの溶融塩を迅速かつ的確に処理できる手段を確立す
ることであった。In view of the above, an object of the present invention is to establish a means for quickly and accurately treating a used molten salt without requiring large-scale equipment and processing space. .
【0008】[0008]
【課題を解決するための手段】そこで、本発明者等は上
記目的を達成すべく鋭意研究を重ねた結果、「使用済み
溶融塩の迅速な処理のためには“溶融状態のままで水に
溶解する方法”が断然有利な実用的手段であるが、 この
方法で問題となる“溶融塩を水に溶解する時に発生する
反応熱”は水槽内の水を循環させることによって効果的
に抜去することが可能で、 水の循環にて水槽内の温度上
昇を抑制するようにすれば、 容量の小さい水槽を使用し
た場合でも水と溶融塩の反応を爆走的に進行させること
なく溶解処理を実施できるようになる」との知見を得た
のである。The inventors of the present invention have conducted intensive studies to achieve the above object, and as a result, have found that "for rapid treatment of used molten salt, water is used in a molten state. The "dissolution method" is by far the most advantageous practical means, but the "reaction heat generated when dissolving the molten salt in water", which is a problem in this method, is effectively removed by circulating the water in the water tank. If the temperature rise in the water tank is suppressed by circulating water, the dissolution treatment can be carried out without causing the reaction between the molten salt and water to proceed explosively even if a small water tank is used. Will be able to do it. "
【0009】本発明は、上記知見事項等を基に完成され
たものであり、「使用済み溶融塩浴の処理装置を、 少な
くとも1箇所に流量制御バルブが介挿された溶融塩輸送
管で連結される使用済み溶融塩の貯蔵タンクと溶融塩溶
解用の水槽とを有し、 かつ前記溶融塩溶解用水槽に水の
補給・循環装置を備えしめて成る構成とすることによっ
て、 溶融塩処理設備の小型化を実現すると同時に迅速か
つ的確な処理を可能とした点」に大きな特徴を有してい
る。The present invention has been completed on the basis of the above findings and the like. "The treatment apparatus for a used molten salt bath is connected by a molten salt transport pipe having at least one flow control valve inserted therein. A storage tank for the used molten salt to be used and a water tank for dissolving the molten salt, and a system for replenishing and circulating water in the molten salt dissolving water tank. In that it enables miniaturization and at the same time enables quick and accurate processing. "
【0010】以下、実施例に基づき、本発明に係わる溶
融塩浴の処理装置を具体的に説明する。図1は、本発明
溶融塩浴処理装置の一実施例に係わる概要図であり、溶
融塩浴を用いるめっき装置や金属電解採取装置から排出
される溶融塩1を収容しておく貯蔵タンク2と溶融塩を
溶解するための水槽3とを有し、この貯蔵タンク2と水
槽3とが“2箇所に流量制御バルブ4,4 が介挿された溶
融塩輸送管"5で連結されると共に、水槽3には水の補給
・循環用配管6が設置されたものを示している。Hereinafter, a treatment apparatus for a molten salt bath according to the present invention will be specifically described based on examples. FIG. 1 is a schematic diagram relating to one embodiment of a molten salt bath treatment apparatus of the present invention, and includes a storage tank 2 for storing a molten salt 1 discharged from a plating apparatus using a molten salt bath or a metal electrowinning apparatus. A water tank 3 for dissolving the molten salt, the storage tank 2 and the water tank 3 being connected by a "molten salt transport pipe 5 having flow control valves 4, 4 inserted at two locations", The water tank 3 is provided with a water supply / circulation pipe 6.
【0011】なお、図1で示した実施例装置は、適宜に
配設される付属設備であるところの“溶融塩が水に溶解
した際の反応で生じるヒュ−ム”を排気するための排気
用配管7と、測温素子8と温度測定装置9から成る水槽
内の水温を測定する装置と、温度測定装置9からの信号
を受けて溶融塩輸送管5に取付けられた流量制御バルブ
4,4 に開度調節信号を送るバルブ開度制御装置10とが設
けられたものである。ここで、符号11はファン、12はポ
ンプ、13はオ−バ−フロ−用配管、そして14は水をそれ
ぞれ示している。The apparatus of the embodiment shown in FIG. 1 is an exhaust system for exhausting "a fume generated by a reaction when a molten salt is dissolved in water", which is an auxiliary equipment appropriately provided. Pipe 7, a device for measuring the water temperature in the water tank comprising a temperature measuring element 8 and a temperature measuring device 9, and a flow control valve attached to the molten salt transport pipe 5 in response to a signal from the temperature measuring device 9.
4, 4 are provided with a valve opening control device 10 for sending an opening adjustment signal. Here, reference numeral 11 denotes a fan, 12 denotes a pump, 13 denotes an overflow pipe, and 14 denotes water.
【0012】[0012]
【作用】さて、上記装置によって溶融塩の処理を行う場
合、まず流量制御バルブ4,4 を開いて貯蔵タンク2内の
溶融塩1を水槽3へ連続的に流し込む。この際、処理す
る溶融塩が高温のときは溶融塩輸送管5を予め溶融塩温
度まで加熱しておくのが良い。これは、溶融塩が輸送管
内で凝固して配管詰まりを起こすのを防止するためであ
る。溶融塩1が水槽3内の水14と接触し反応した時に発
生するヒュ−ムは、排気用配管7で吸引され、ファン11
にて装置外へ送られる。When the molten salt is to be treated by the above apparatus, the flow control valves 4, 4 are first opened, and the molten salt 1 in the storage tank 2 is continuously poured into the water tank 3. At this time, when the molten salt to be treated is at a high temperature, the molten salt transport pipe 5 is preferably heated to the molten salt temperature in advance. This is to prevent the molten salt from solidifying in the transport pipe and causing clogging of the pipe. The fumes generated when the molten salt 1 comes into contact with and reacts with the water 14 in the water tank 3 are sucked by the exhaust pipe 7 and
Is sent out of the device.
【0013】ところで、前述したように、溶融塩1が水
槽3内の水14に溶解した時に発生する反応熱は水温を上
昇し、爆発的な反応の加速を誘因する原因となりがちで
あるが、本発明装置では水槽3に水の補給・循環装置が
設置されており、水温の上昇を「水槽3内への新水の補
給」或いは「水槽3内での水14の循環」によって抑える
ことができるので、上記弊害は効果的に防止される。By the way, as described above, the reaction heat generated when the molten salt 1 is dissolved in the water 14 in the water tank 3 tends to raise the water temperature and induce explosive acceleration of the reaction. In the apparatus of the present invention, a water replenishing / circulating device is installed in the water tank 3, and the rise in water temperature can be suppressed by "replenishing new water into the water tank 3" or "circulating water 14 in the water tank 3". As a result, the above adverse effects are effectively prevented.
【0014】即ち、図1に例示した装置では、溶融塩1
を水槽3内へ流し込み、水槽3内の水温上昇に応じてポ
ンプ12により水槽3内へ水を補給する。従って、水槽3
内の水14は増加して水温上昇を抑えつつ水位を上げ、所
定量以上になるとオ−バ−フロ−用配管13から水槽外へ
オ−バ−フロ−する。なお、ポンプ12で水槽3内へ送る
水は新水を使っても良いが、オ−バ−フロ−用配管13を
通ってオ−バ−フロ−した水を循環させても良い。た
だ、オ−バ−フロ−水を使う場合には、水温が上昇して
いるので熱交換器等を使って冷却させた後に循環させる
のが好ましい。また、オ−バ−フロ−させた水を使用す
る場合、オ−バ−フロ−水を一旦貯蔵しておく槽を別に
設けても良い。勿論、場合によっては水槽3内の水14を
循環させるだけでも水温が所望値以下に保たれることも
ある。That is, in the apparatus illustrated in FIG.
Is poured into the water tank 3, and water is replenished into the water tank 3 by the pump 12 according to a rise in the water temperature in the water tank 3. Therefore, the water tank 3
The internal water 14 increases to raise the water level while suppressing a rise in water temperature. When the water level exceeds a predetermined amount, the water overflows from the overflow pipe 13 to the outside of the water tank. The water to be sent into the water tank 3 by the pump 12 may be fresh water, or the overflowed water may be circulated through the overflow pipe 13. However, when using overflow water, it is preferable to circulate after cooling using a heat exchanger or the like since the water temperature is rising. When using the overflowed water, a tank for temporarily storing the overflowed water may be provided separately. Of course, in some cases, merely circulating the water 14 in the water tank 3 may keep the water temperature below a desired value.
【0015】更に、水槽3への水の補給・循環を行って
も水温の上昇傾向が止まらない場合には、流量制御バル
ブ4の開度調整を行って溶融塩1が水槽3内へ流れ込む
量を調節する。これによって水温の上昇は更に確実に抑
えられる。図1に例示した装置は、この操作もより的確
に行うことができる。即ち、該装置では水槽3に測温素
子8を備えた温度測定装置9が配置され、水槽内水温に
関する温度信号をバルブ開度制御装置10に送るように構
成されているが、バルブ開度制御装置10では温度測定装
置9からの温度信号に基づいて水温が予め定められた目
標温度となるような溶融塩の流入量を算出し、これに基
づく信号を流量制御バルブ4に送りその開度をコントロ
−ルする。従って、水槽内水温の調整、即ち溶融塩と水
との反応の高度な制御を容易に実施することが可能とな
る。Further, if the increase in water temperature does not stop even after replenishing and circulating water into the water tank 3, the opening of the flow control valve 4 is adjusted to adjust the amount of molten salt 1 flowing into the water tank 3. Adjust As a result, a rise in water temperature can be more reliably suppressed. The apparatus illustrated in FIG. 1 can perform this operation more accurately. That is, in this device, a temperature measuring device 9 having a temperature measuring element 8 is arranged in the water tank 3 and configured to send a temperature signal relating to the water temperature in the water tank to the valve opening control device 10. The device 10 calculates the inflow amount of the molten salt such that the water temperature becomes a predetermined target temperature based on the temperature signal from the temperature measuring device 9, and sends a signal based on the calculated amount to the flow control valve 4 to determine the opening degree. Control. Therefore, adjustment of the water temperature in the water tank, that is, advanced control of the reaction between the molten salt and water can be easily performed.
【0016】なお、溶融塩輸送管5に設置する流量制御
用バルブ4は1箇所に取付けるだけでも良いが、出来れ
ば2箇所以上に取付けるのが好ましい。なぜなら、使用
済み溶融塩の貯蔵タンク2から水槽3までの輸送管の長
さが長い場合には、1つのバルブで流量制御を行おうと
してもバルブ位置から水槽まで溶融塩が流れる時間が長
いので、制御に応答遅れが生じる危険性があるためであ
る。勿論、輸送管の長さが応答遅れを生じない程度に短
い場合には、流量制御用バルブの取付けを1箇所だけと
して良いことは言うまでもない。The flow control valve 4 installed in the molten salt transport pipe 5 may be installed at only one place, but preferably installed at two or more places if possible. This is because, when the length of the transport pipe from the storage tank 2 for the used molten salt to the water tank 3 is long, even if the flow rate is controlled by one valve, the time required for the molten salt to flow from the valve position to the water tank is long. This is because there is a risk that response delay may occur in control. Of course, when the length of the transport pipe is short enough not to cause a response delay, it goes without saying that the flow control valve may be attached to only one place.
【0017】次に、前記図1に示した溶融塩浴の処理装
置(水槽の容量:400リットル)を用いて200℃の塩化
アルミ系溶融塩浴を処理した際の実績を示す。なお、塩
化アルミ系溶融塩の処理では単位時間当りの溶融塩処理
量に対して5倍以上の循環水量が必要で、水槽中の目標
水温は80℃以下、好ましくは50℃以下である。これ
らの条件を踏まえて、処理に際しては処理対象溶融塩浴
が200℃であることから溶融塩輸送管5も200℃に
予熱しておき、また水槽3への補給水として新水を用
い、補給量は1分間に80リットルとした。Next, the results of processing an aluminum chloride-based molten salt bath at 200 ° C. using the molten salt bath processing apparatus (water tank capacity: 400 liters) shown in FIG. 1 will be described. In the treatment of the aluminum chloride-based molten salt, the amount of circulating water is required to be at least 5 times the amount of molten salt processed per unit time, and the target water temperature in the water tank is 80 ° C or lower, preferably 50 ° C or lower. Based on these conditions, the molten salt transport pipe 5 is also preheated to 200 ° C. since the molten salt bath to be treated is 200 ° C. during the treatment, and fresh water is supplied to the water tank 3 using fresh water. The volume was 80 liters per minute.
【0018】この条件で約700kgの廃棄塩化アルミ系
溶融塩の連続水溶解処理を実施したところ、処理中の水
槽への溶融塩流入量は1分間当り約7kgに調整され、水
槽内水温:50℃以下が維持されつつ約1時間で処理が
終了した。Under these conditions, a continuous water dissolution treatment of about 700 kg of waste aluminum chloride-based molten salt was carried out. As a result, the amount of molten salt flowing into the water tank during the treatment was adjusted to about 7 kg per minute, and the water temperature in the water tank: 50 The process was completed in about one hour while maintaining the temperature at or below ° C.
【0019】[0019]
【効果の総括】以上に説明した如く、この発明によれ
ば、使用済みの廃棄溶融塩を迅速に処理できるコンパク
トな装置を提供することができ、めっきや電解精錬等の
操業性向上に大きく寄与し得るなど、産業上有用な効果
がもたらされる。As described above, according to the present invention, it is possible to provide a compact apparatus capable of rapidly processing used waste molten salt, which greatly contributes to improving the operability of plating and electrolytic refining. And industrially useful effects.
【図1】本発明に係わる溶融塩浴処理装置例の概要説明
図である。FIG. 1 is a schematic explanatory view of an example of a molten salt bath treatment apparatus according to the present invention.
1 溶融塩 2 貯蔵タンク 3 水槽 4 流量制御バルブ 5 溶融塩輸送管 6 水の補給・循環用配管 7 排気用配管 8 測温素子 9 温度測定装置 10 バルブ開度制御装置 11 ファン 12 ポンプ 13 オ−バ−フロ−用配管 14 水 Reference Signs List 1 molten salt 2 storage tank 3 water tank 4 flow control valve 5 molten salt transport pipe 6 water supply / circulation pipe 7 exhaust pipe 8 temperature measuring element 9 temperature measuring device 10 valve opening control device 11 fan 12 pump 13 o Bar flow piping 14 Water
フロントページの続き (72)発明者 山本 康博 大阪府大阪市中央区北浜4丁目5番33号 住友金属工業株式会社内 (72)発明者 内田 淳一 大阪府大阪市中央区北浜4丁目5番33号 住友金属工業株式会社内 (72)発明者 阿部 賢 大阪府大阪市中央区北浜4丁目5番33号 住友金属工業株式会社内 (72)発明者 福井 国博 大阪府大阪市中央区北浜4丁目5番33号 住友金属工業株式会社内 (72)発明者 米田 順吉 広島県広島市西区観音新町4丁目6番22 番 三菱重工業株式会社広島製作所内 (72)発明者 橋本 律男 広島県広島市西区観音新町4丁目6番22 番 三菱重工業株式会社広島製作所内 (72)発明者 田口 俊夫 広島県広島市西区観音新町4丁目6番22 番 三菱重工業株式会社広島製作所内 (58)調査した分野(Int.Cl.6,DB名) C25D 21/16 - 21/18,3/66 F27D 15/00 - 15/02Continued on the front page (72) Inventor Yasuhiro Yamamoto 4-5-33 Kitahama, Chuo-ku, Osaka-shi, Osaka Inside Sumitomo Metal Industries, Ltd. (72) Inventor Junichi Uchida 4-5-33 Kitahama, Chuo-ku, Osaka-shi, Osaka Within Sumitomo Metal Industries, Ltd. (72) Inventor Ken Abe 4-5-33 Kitahama, Chuo-ku, Osaka-shi, Osaka Prefecture Inside Sumitomo Metal Industries, Ltd. (72) Kunihiro Fukui 4-5-Kitahama, Chuo-ku, Osaka, Osaka No. 33 Sumitomo Metal Industries, Ltd. (72) Inventor Junkichi Yoneda 4-6-22 Kannonshinmachi, Nishi-ku, Hiroshima, Hiroshima Prefecture Mitsubishi Heavy Industries, Ltd.Hiroshima Works (72) Inventor Norio Hashimoto 4 Kannonshinmachi, Nishi-ku, Hiroshima, Hiroshima 6-22, Mitsubishi Heavy Industries, Ltd.Hiroshima Works (72) Inventor Toshio Taguchi 4-6-2-2 Kanon Shinmachi, Nishi-ku, Hiroshima-shi, Hiroshima Mitsubishi Heavy Industries, Ltd.Hiroshima Works (58) Field surveyed (Int.Cl. 6 , DB name) C25D 21/16-21 / 18,3 / 66 F27D 15/00-15/02
Claims (1)
挿された溶融塩輸送管で連結される使用済み溶融塩の貯
蔵タンクと溶融塩溶解用の水槽とを有し、かつ前記溶融
塩溶解用水槽に水の補給・循環装置を備えしめて成るこ
とを特徴とする、使用済み溶融塩浴の処理装置。1. A method for dissolving a molten salt, comprising a storage tank for a used molten salt and a water tank for dissolving the molten salt, the storage tank being connected to a molten salt transport pipe having a flow control valve interposed at at least one place. An apparatus for treating a used molten salt bath, comprising a water tank provided with a water replenishing / circulating device.
Priority Applications (1)
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JP21788191A JP2850064B2 (en) | 1991-08-03 | 1991-08-03 | Processing equipment for used molten salt bath |
Applications Claiming Priority (1)
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JP21788191A JP2850064B2 (en) | 1991-08-03 | 1991-08-03 | Processing equipment for used molten salt bath |
Publications (2)
Publication Number | Publication Date |
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JPH0539598A JPH0539598A (en) | 1993-02-19 |
JP2850064B2 true JP2850064B2 (en) | 1999-01-27 |
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JP21788191A Expired - Fee Related JP2850064B2 (en) | 1991-08-03 | 1991-08-03 | Processing equipment for used molten salt bath |
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