JPH0435537B2 - - Google Patents
Info
- Publication number
- JPH0435537B2 JPH0435537B2 JP14077583A JP14077583A JPH0435537B2 JP H0435537 B2 JPH0435537 B2 JP H0435537B2 JP 14077583 A JP14077583 A JP 14077583A JP 14077583 A JP14077583 A JP 14077583A JP H0435537 B2 JPH0435537 B2 JP H0435537B2
- Authority
- JP
- Japan
- Prior art keywords
- chamber
- boiling point
- recovery
- cooling
- inert gas
- 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 - Lifetime
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】
〔技術分野〕
この発明は、合金材の製造において使用される
低沸点成分の回収方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a method for recovering low-boiling components used in the production of alloy materials.
従来、鍍金処理を施すことによつて黄銅材表面
に銅等の良導伝体(良導電体)の伝導層を形成さ
せ、黄銅材の接触抵抗を小さくすることが行われ
ている。処理された黄銅材は、端子基材等として
用いられる。このように、黄銅材表面に伝導層を
形成させることにより、銅材等の良導伝性材料を
そのまま用いるのに比べて原材料コストが低くな
り、しかも接触抵抗が同程度となるといつたよう
な利点が生まれる。しかしながら、前記のような
従来法には、鍍金処理用の装置が大きなものとな
り、生産性が低く加工コストも高いという問題が
あつた。そのうえ、鍍金処理によつて形成された
伝導層は剥離し易いので、フープ材の状態等とな
つた黄銅材を鍍金処理したあと、折曲して部品に
することが非常に困難であるという品質上の問題
もあつた。
BACKGROUND ART Conventionally, a conductive layer of a good conductor such as copper is formed on the surface of a brass material by plating, thereby reducing the contact resistance of the brass material. The treated brass material is used as a terminal base material and the like. In this way, by forming a conductive layer on the surface of the brass material, the raw material cost is lower than when using a highly conductive material such as copper material as is, and the contact resistance is about the same. Benefits arise. However, the conventional method described above requires a large plating apparatus, resulting in low productivity and high processing costs. Furthermore, the conductive layer formed by plating is easily peeled off, so it is extremely difficult to bend the brass material, which has become a hoop material, into parts after plating. I also had the above problem.
鍍金処理のほかに、金属板表面に異種金属を形
成させる技術として、溶射法や金属シート熔接法
等があるが、このような方法を用いて前記のよう
な黄銅材をつくることとしても、やはり、加工コ
ストが高く、得られた黄銅材の品質が劣るといつ
たような問題があつた。 In addition to plating, there are other techniques for forming dissimilar metals on the surface of a metal plate, such as thermal spraying and metal sheet welding. However, there were problems such as high processing costs and poor quality of the brass material obtained.
そこで、減圧下、黄銅材を加熱して表面の亜鉛
を蒸発させることにより、第1図に示されている
ような、銅成分の多い伝導層1aを表面に備えた
黄銅材1をつくることが考え出された。このよう
にして黄銅材をつくるようにすれば、他に金属材
料を用いる必要がなく、鍍金処理を行う場合に比
べ製造装置が小さなものですみ、生産性も高い。
そのうえ、加工コストが低く、得られる黄銅材の
伝導層は剥離する恐れがほとんどない。 Therefore, by heating the brass material under reduced pressure to evaporate the zinc on the surface, it is possible to produce a brass material 1 having a conductive layer 1a with a high copper content on the surface, as shown in FIG. thought out. If the brass material is manufactured in this way, there is no need to use other metal materials, and compared to the case of plating, the manufacturing equipment can be smaller and the productivity is higher.
Moreover, the processing cost is low, and the conductive layer of the resulting brass material has little risk of peeling.
この黄銅材の製法を具体的に説明する。この黄
銅材の製法は、たとえば第2図に示されているよ
うな製造装置を用いて実施される。図にみるよう
に、この製造装置な巻戻ドラム2および巻取ドラ
ム3を備えており、巻戻ドラム2にはフープ材と
なつた原材料の黄銅材4が巻かれて装着され、巻
取ドラム3には脱亜鉛処理が行われた黄銅材5が
巻き取られるようになつている。巻戻ドラム2と
巻取ドラム3の間には、予熱器6、真空加熱炉
7、および圧延機8が順に設けられており、巻戻
ドラム2から送られてくる黄銅材4がこれらを順
に通過するようになつている。予熱器6は黄銅材
4に付着した油や水分などを取り除いて乾燥させ
るためのものである。真空加熱炉7のまん中には
加熱室9が設けられており、加熱室9の前後には
予備真空室が二つづつ、すなわち、前に予備真空
室10aと10b、後に予備真空室10cと10
dが設けられている。予備真空室10a〜10d
は、加熱室8に向かつて順に真空度(減圧度)を
上げることによつて、加熱室9の真空度を高いも
のとするために設けられたものである。予備真空
室10a,10dにはそれぞれ窒素ガス等の不活
性ガスの入口11が設けられている。窒素ガス等
の不活性ガスは、加熱室9内の酸素を取除いて黄
銅材4の酸化が起こらないようにするために入れ
られる。加熱室9内には加熱装置(加熱部)12
が配置されている。図では省略したが、真空加熱
炉7には真空ポンプ等の減圧装置が配置されてい
る。また、加熱室には、金属板等の、亜鉛を付着
させることにより回収する亜鉛回収手段が配置さ
れるている。 The manufacturing method of this brass material will be specifically explained. This method of manufacturing brass material is carried out using, for example, a manufacturing apparatus as shown in FIG. As shown in the figure, this manufacturing device is equipped with an unwinding drum 2 and a winding drum 3, and the unwinding drum 2 is equipped with a brass material 4, which is a raw material used as a hoop material, wound around the winding drum. A brass material 5 that has been subjected to a dezincing treatment is wound around the wire 3. A preheater 6, a vacuum heating furnace 7, and a rolling mill 8 are provided in order between the unwinding drum 2 and the winding drum 3, and the brass material 4 sent from the unwinding drum 2 is passed through these in order. It's starting to pass. The preheater 6 is for removing oil, moisture, etc. adhering to the brass material 4 and drying it. A heating chamber 9 is provided in the center of the vacuum heating furnace 7, and two preliminary vacuum chambers are provided before and after the heating chamber 9, namely, preliminary vacuum chambers 10a and 10b at the front, and preliminary vacuum chambers 10c and 10 at the rear.
d is provided. Preliminary vacuum chambers 10a to 10d
is provided to increase the degree of vacuum in the heating chamber 9 by increasing the degree of vacuum (degree of reduced pressure) in order toward the heating chamber 8. Each of the preliminary vacuum chambers 10a and 10d is provided with an inlet 11 for inert gas such as nitrogen gas. An inert gas such as nitrogen gas is introduced to remove oxygen from the heating chamber 9 to prevent oxidation of the brass material 4. A heating device (heating section) 12 is provided in the heating chamber 9.
is located. Although not shown in the figure, a pressure reducing device such as a vacuum pump is disposed in the vacuum heating furnace 7. Further, a zinc recovery means, such as a metal plate, for recovering zinc by adhering it thereto is arranged in the heating chamber.
この装置を使用し、つぎのようにして黄銅材を
つくる。巻戻ドラム2に装着された原材料の黄銅
材4を予熱室6に送つて油や水分を取り除くとと
もに乾燥させ、つぎに、加熱室7に送つてここで
減圧下加熱する。たとえば、加熱室内の気圧を
10-2〜10-4Torr程度(10-2Torr程度よりも高真
空)とした場合は、黄銅材を500〜900℃程度に加
熱する。低沸点成分である亜鉛は1気圧では930
℃を沸点として蒸発するが、10-2〜10-4Torr程
度と完全真空に近い状態では500〜900℃程度で蒸
発する。他方、高沸点成分である銅は1気圧では
沸点が2582℃であつて、亜鉛に比べて沸点がかな
り高く、前記のような気圧および温度ではほとん
ど蒸発しない。このような亜鉛および銅の沸点の
差(蒸気圧の差)を利用し、黄銅材4表面の亜鉛
を選択的に蒸発させ除去する。そして、黄銅材表
面に銅成分の多い伝導層を形成させるのである。
蒸発させた亜鉛は亜鉛回収手段に付着させること
により回収する。 Using this device, brass material is produced in the following manner. The raw material brass material 4 mounted on the unwinding drum 2 is sent to a preheating chamber 6 to remove oil and water and dried, and then sent to a heating chamber 7 where it is heated under reduced pressure. For example, the air pressure inside the heating chamber
When the vacuum is about 10 -2 to 10 -4 Torr (higher vacuum than about 10 -2 Torr), the brass material is heated to about 500 to 900°C. Zinc, a low boiling point component, has a temperature of 930 at 1 atm.
It evaporates at a boiling point of 10 -2 to 10 -4 Torr, which is close to a complete vacuum, at a temperature of 500 to 900°C. On the other hand, copper, which is a high boiling point component, has a boiling point of 2582° C. at 1 atmosphere, which is considerably higher than that of zinc, and hardly evaporates at the above pressure and temperature. Utilizing such a difference in boiling point (difference in vapor pressure) between zinc and copper, zinc on the surface of the brass material 4 is selectively evaporated and removed. Then, a conductive layer containing a large amount of copper is formed on the surface of the brass material.
The evaporated zinc is recovered by attaching it to a zinc recovery means.
脱亜鉛処理を行つたあと、黄銅材4を圧延機8
に送り、ここで所定の厚みに圧延する。処理直後
の黄銅材4は高温加熱によつて電気的特性が向上
てしている反面、亜鉛が蒸発して孔ができる等し
て機械的特性、つまり強度が下がり、表面が粗面
となつている。しかし、この圧延により強度が向
上するとともに表面が平面となる。圧延されて得
られる黄銅材5は巻取ドラム3に巻取られる。こ
うして第1図に示されているような黄銅材が得ら
れる。 After dezincing treatment, the brass material 4 is transferred to a rolling mill 8.
It is then rolled to a predetermined thickness. Immediately after the treatment, the brass material 4 has improved electrical properties due to high-temperature heating, but on the other hand, the mechanical properties, that is, the strength, have decreased due to evaporation of zinc and the formation of pores, and the surface has become rough. There is. However, this rolling improves the strength and makes the surface flat. The brass material 5 obtained by rolling is wound around a winding drum 3. In this way, a brass material as shown in FIG. 1 is obtained.
しかしながら、この黄銅材の製法では、加熱室
中に設けた亜鉛回収手段に付着させることにより
亜鉛を回収するようにしているため、一旦、亜鉛
回収手段に付着しても、温度が高いので運動エネ
ルギーが大きいといつたような理由で、亜鉛が再
び蒸発する恐れが多い。そのため、亜鉛の回収率
が低下したり、亜鉛が再び黄銅に付着する恐れが
多くなるといつた問題が発生していた。 However, in this method of manufacturing brass materials, zinc is recovered by adhering it to the zinc recovery means installed in the heating chamber, so even if the zinc adheres to the zinc recovery means, the temperature is high enough to generate kinetic energy. For the reasons mentioned above, there is a high risk that the zinc will evaporate again. This has caused problems such as a decrease in the zinc recovery rate and an increased risk of zinc re-adhering to the brass.
この発明は、このような事情に鑑みなされたも
ので、亜鉛等の低沸点成分の回収率が低下した
り、低沸点成分が再び黄銅材等の合金材に付着す
る恐れが少ない、低沸点成分の回収方法を提供す
ることを目的としている。
This invention was made in view of the above circumstances, and it is possible to reduce the possibility that the recovery rate of low boiling point components such as zinc will decrease or that the low boiling point components will adhere to alloy materials such as brass materials again. The purpose is to provide a collection method for
発明者らは、前記のような問題を解決するため
研究を重ねた。その結果、内部の圧力が不活性ガ
スによりほぼ大気圧に保たれている放冷室を加熱
室の出口に接続して設けるとともに、冷却装置を
備えた回収室を放冷室に接続して設け、黄銅材を
加熱したあと放冷室に通し、蒸発する亜鉛を不活
性ガスとともに回収室に送り、回収室でこの混合
気体を冷却することにより亜鉛を回収することと
すればよいというこうを見い出した。また、沸点
の異なる成分からなる黄銅材以外の合金材を処理
する場合でも、同様にして低沸点成分を回収する
こととすれば同様の効果が得られるということを
見い出し、ここにこの発明を完成した。
The inventors have conducted repeated research to solve the above problems. As a result, a cooling chamber, whose internal pressure is maintained at almost atmospheric pressure using inert gas, is connected to the outlet of the heating chamber, and a recovery chamber equipped with a cooling device is connected to the cooling chamber. They found that the zinc can be recovered by heating the brass material, passing it through a cooling chamber, sending the evaporated zinc together with an inert gas to a recovery chamber, and cooling this gas mixture in the recovery chamber. Ta. In addition, we discovered that even when processing alloy materials other than brass materials, which consist of components with different boiling points, the same effect can be obtained by recovering the low boiling point components in the same way, and we have hereby completed this invention. did.
したがつて、この発明は、加熱室中において、
沸点の異なる成分からなる合金材を加熱し、表面
の低沸点成分を蒸発させて高沸点成分の多い層を
表面に備えた合金材をつくるにあたり、内部の圧
力が不活性ガスによりほぼ大気圧に保たれている
放冷室を加熱室の出口に接続して設けるととも
に、冷却装置を備えた回収室を放冷室に接続して
設け、合金材を加熱したあと放冷室に通して、蒸
発する低沸点成分を不活性ガスとともに放冷室か
ら回収室に送り込み、回収室でこの混合気体を冷
却することにより低沸点成分を回収するようにす
ることを特徴とする低沸点成分回収方法をその要
旨としている。以下、この発明を詳しく説明す
る。 Therefore, the present invention provides the following advantages: In the heating chamber,
When an alloy material consisting of components with different boiling points is heated to evaporate the low boiling point components on the surface to create an alloy material with a layer containing many high boiling point components on the surface, the internal pressure is brought to almost atmospheric pressure by an inert gas. A cooling chamber is connected to the outlet of the heating chamber, and a recovery chamber equipped with a cooling device is connected to the cooling chamber. After the alloy material is heated, it is passed through the cooling chamber and evaporated. A low boiling point component recovery method is provided, which is characterized in that the low boiling point components are sent together with an inert gas from a cooling chamber to a recovery chamber, and the low boiling point components are recovered by cooling this mixed gas in the recovery chamber. This is the summary. This invention will be explained in detail below.
第3図は、加熱室と、この発明にかかる低沸点
成分回収方法で使用する放冷室および回収室の配
置状態をあらわす。図にみるように、加熱室13
の出口13aに放冷室14が接続され、放冷室1
4には回収室15が配管16,17により接続さ
れている。配管17には循環ポンプ18が配置さ
れている。加熱室13には加熱装置13bが配置
され、加熱室13の入口13cおよび出口13a
近傍には真空ポンプ19,19がそれぞれ接続さ
れている。放冷室14には真空ポンプ19と、不
活性ガスボンベ20等の不活性ガス供給手段が接
続されている。回収室15の内部には、第5図に
示されているように、内部に冷却水等の冷媒が通
る通路21aを備えた板状の熱交換器(冷却装
置)21…が配置されている。ここでは、熱交換
器21…が、回収室15の左右の壁から交互に突
出し、図面において左側の壁からはその先端が斜
め上を向き、右側の壁からはその先端が斜め下を
向くように配置されている。そして、これらの熱
交換器21…により通路22がつくられている。 FIG. 3 shows the arrangement of the heating chamber, the cooling chamber and the recovery chamber used in the method for recovering low boiling point components according to the present invention. As shown in the figure, heating chamber 13
A cooling chamber 14 is connected to the outlet 13a of the cooling chamber 1.
4 is connected to a recovery chamber 15 by pipes 16 and 17. A circulation pump 18 is arranged in the piping 17 . A heating device 13b is arranged in the heating chamber 13, and an inlet 13c and an outlet 13a of the heating chamber 13 are arranged.
Vacuum pumps 19, 19 are connected nearby. A vacuum pump 19 and inert gas supply means such as an inert gas cylinder 20 are connected to the cooling chamber 14 . As shown in FIG. 5, inside the recovery chamber 15, a plate-shaped heat exchanger (cooling device) 21 is disposed, which is provided with a passage 21a through which a refrigerant such as cooling water passes. . Here, the heat exchangers 21... protrude alternately from the left and right walls of the recovery chamber 15, with their tips pointing diagonally upward from the left wall in the drawing, and their tips pointing diagonally downward from the right wall. It is located in A passage 22 is created by these heat exchangers 21.
前記のように配置した冷却室14および回収室
15を使用し、たとえば、つぎのようにして、こ
の発明にかかる低沸点成分回収方法を実施する。 Using the cooling chamber 14 and recovery chamber 15 arranged as described above, the low boiling point component recovery method according to the present invention is carried out, for example, in the following manner.
まず、加熱室13および放冷室14内を真空ポ
ンプ19…により減圧し、放冷室14内の圧力を
不活性ガスによりほぼ大気圧程度とする。加熱室
13の出口(放冷室2の入口)13aは、フープ
材となつた合金材23の断面よりほんのわずかだ
け大きいので、放冷室14から加熱室13へは不
活性ガスがほとんど通らず、そのため、加熱室1
3内の真空度が保持されるようになつている。そ
して、ポンプ18により、放冷室14と回収室1
5間で不活性ガスを循環させておく。つぎに、加
熱装置13bで加熱室13内の所定の温度とす
る。合金材23の予熱等を行つたあと、加熱室1
3で合金材23を加熱し、つぎに、合金材23を
放冷室14に送る。放冷室14では、不活性ガス
の対流効果等を利用して合金材23を室温程度ま
で放冷する。室内のガスが不活性ガスであるか
ら、合金材23はここで酸化されることなく冷え
る。他方、放冷室14では、室内の気圧がほぼ大
気圧となつているので、合金材23から蒸発した
低沸点成分は平均自由行程が小さくなり、散乱す
る。そのため、低沸点成分は放冷室14の内壁面
にほとんど付着することなく、不活性ガスととも
に回収室15に送り込まれる。第5図に示されて
いるように、低沸点成分24と不活性ガス25か
らなる混合気体は、配管16から回収室15内の
通路22へと送られる。通路22を通る間に低沸
点成分24は冷却されて熱交換器21に付着し、
不活性ガス25だけが配管17から、再び放冷室
14に送られる。このあと、合金材23は従来と
同様にして処理される。たとえば、圧延処理等が
行われて、製品の合金材となるのである。 First, the pressure inside the heating chamber 13 and the cooling chamber 14 is reduced by the vacuum pumps 19, and the pressure inside the cooling chamber 14 is brought to approximately atmospheric pressure using an inert gas. Since the outlet 13a of the heating chamber 13 (inlet of the cooling chamber 2) is only slightly larger than the cross section of the alloy material 23 that has become the hoop material, almost no inert gas passes from the cooling chamber 14 to the heating chamber 13. , Therefore, heating chamber 1
The degree of vacuum within the chamber is maintained. Then, the pump 18 operates the cooling chamber 14 and the recovery chamber 1.
Circulate inert gas for 5 minutes. Next, the temperature inside the heating chamber 13 is set to a predetermined temperature using the heating device 13b. After preheating the alloy material 23, the heating chamber 1
3, the alloy material 23 is heated, and then the alloy material 23 is sent to the cooling chamber 14. In the cooling chamber 14, the alloy material 23 is left to cool down to about room temperature using the convection effect of inert gas. Since the gas in the room is an inert gas, the alloy material 23 cools without being oxidized. On the other hand, in the cooling chamber 14, since the indoor pressure is approximately atmospheric pressure, the low boiling point components evaporated from the alloy material 23 have a small mean free path and are scattered. Therefore, the low boiling point components are sent into the recovery chamber 15 together with the inert gas without substantially adhering to the inner wall surface of the cooling chamber 14. As shown in FIG. 5, a gas mixture consisting of a low boiling point component 24 and an inert gas 25 is sent from a pipe 16 to a passage 22 in the recovery chamber 15. While passing through the passage 22, the low boiling point component 24 is cooled and adheres to the heat exchanger 21,
Only the inert gas 25 is sent from the pipe 17 to the cooling chamber 14 again. Thereafter, the alloy material 23 is processed in the same manner as in the prior art. For example, it is subjected to rolling treatment and the like to become an alloy material for products.
合金材として黄銅材を使用する場合は、加熱室
および放冷室の温度と圧力の分布が第4図に示さ
れているような状態となるように調整するとよ
い。図中、実線が温度、一点鎖線が気圧を示して
いる。すなわち、図にみるように、加熱室の温度
が500〜900℃で圧力が10-2〜10-4Torr、放冷室
の温度が、不活性ガスの流量を調整する等して出
口ほど低くなるようにし、圧力がほぼ大気圧程度
となるようにするとよい。 When a brass material is used as the alloy material, it is preferable to adjust the temperature and pressure distribution in the heating chamber and the cooling chamber so that they are as shown in FIG. 4. In the figure, the solid line indicates temperature, and the dashed line indicates atmospheric pressure. In other words, as shown in the figure, the temperature in the heating chamber is 500 to 900℃ and the pressure is 10 -2 to 10 -4 Torr, and the temperature in the cooling chamber is lower at the outlet by adjusting the flow rate of inert gas. It is recommended that the pressure be approximately atmospheric pressure.
この発明にかかる低沸点成分回収方法では、加
熱室の出口に接続して設けられた放冷室におい
て、大気圧の不活性ガス雰囲気中で低沸点成分を
散乱させたのち、この低沸点成分を加熱室から独
立した回収室に送り、ここで回収を行うようにす
るのて、一旦、回収した低沸点成分が再び蒸発す
る恐れがほとんどなく、低沸点成分の回収率が高
くなる。また、低沸点成分が再び合金材に付着す
る恐れも非常に少ないので、得られる合金材の品
質が高いものとなる。 In the low boiling point component recovery method according to the present invention, the low boiling point components are scattered in an inert gas atmosphere at atmospheric pressure in a cooling chamber connected to the outlet of the heating chamber, and then the low boiling point components are removed. By sending the low boiling point components from the heating chamber to a separate recovery chamber and recovering them there, there is almost no risk that the recovered low boiling point components will evaporate again, and the recovery rate of the low boiling point components will be high. Furthermore, since there is very little possibility that the low boiling point components will adhere to the alloy material again, the quality of the obtained alloy material will be high.
なお、前記実施例のように放冷室と回収室の間
で、必ずしも不活性ガスを循環させるようにする
必要はない。 Note that it is not necessary to circulate the inert gas between the cooling chamber and the recovery chamber as in the above embodiment.
この発明にかかる低沸点成分回収方法では、加
熱室中において、沸点の異なる成分からなる合金
材を加熱し、表面の低沸点成分を蒸発させて高沸
点成分の多い層を表面に備えた合金材をつくるに
あたり、内部の圧力が不活性ガスによりほぼ大気
圧に保たれている放冷室を加熱室の出口に接続し
て設けるとともに、冷却装置を備えた回収室を放
冷室に接続して設け、合金材を加熱したあと放冷
室に通して、蒸発する低沸点成分を不活性ガスと
ともに放冷室から回収室に送り込み、回収室でこ
の混合気体を冷却することにより低沸点成分を回
収するようにするので、低沸点成分の回収率が高
くなる。また、低沸点成分が再び合金材に付着す
る恐れが非常に少なくなつて、得られる合金材の
品質が高いものとなる。
In the low boiling point component recovery method according to the present invention, an alloy material consisting of components with different boiling points is heated in a heating chamber, and the low boiling point components on the surface are evaporated, so that the alloy material has a layer containing many high boiling point components on the surface. When making a heating chamber, a cooling chamber whose internal pressure is maintained at almost atmospheric pressure with an inert gas is connected to the outlet of the heating chamber, and a recovery chamber equipped with a cooling device is connected to the cooling chamber. After heating the alloy material, it is passed through a cooling chamber, and the low-boiling point components that evaporate are sent together with an inert gas from the cooling chamber to the recovery chamber.The low-boiling point components are recovered by cooling this mixed gas in the recovery chamber. As a result, the recovery rate of low boiling point components is increased. Furthermore, the possibility that the low-boiling point components will adhere to the alloy material again is extremely reduced, and the quality of the obtained alloy material will be high.
第1図は銅成分の多い層を表面に備えた黄銅材
の一部を切り欠いてあらわした斜視図、第2図は
黄銅材の製造に使用される製造装置の概略説明
図、第3図は放冷室および回収室の配置説明図、
第4図は加熱室と放冷室の温度と圧力の分布をあ
らわすグラフ、第5図は回収室の縦断面図であ
る。
13……加熱室、13a……加熱室の出口、1
4……放冷室、15……回収室、21……熱交換
器(冷却装置)、23……合金材、24……低沸
点成分、25……不活性ガス。
Figure 1 is a partially cutaway perspective view of a brass material with a layer with a high copper content on its surface, Figure 2 is a schematic explanatory diagram of the manufacturing equipment used to manufacture the brass material, and Figure 3 is an explanatory diagram of the layout of the cooling room and recovery room,
FIG. 4 is a graph showing the distribution of temperature and pressure in the heating chamber and the cooling chamber, and FIG. 5 is a longitudinal sectional view of the recovery chamber. 13...Heating chamber, 13a...Heating chamber outlet, 1
4... Cooling chamber, 15... Recovery chamber, 21... Heat exchanger (cooling device), 23... Alloy material, 24... Low boiling point component, 25... Inert gas.
Claims (1)
る合金材を加熱し、表面の低沸点成分を蒸発さ
せ、高沸点成分の多い層を表面に備えた合金材を
つくるにあたり、内部の圧力が不活性ガスにより
ほぼ大気圧に保たれている放冷室を加熱室の出口
に接続して設けるとともに、冷却装置を備えた回
収室を放冷室に接続して設け、合金材を加熱した
あと放冷室に通して、蒸発する低沸点成分を不活
性ガスとともに放冷室から回収室に送り込み、回
収室でこの混合気体を冷却することにより低沸点
成分を回収するようにすることを特徴とする低沸
点成分回収方法。 2 放冷室と回収室の間で不活性ガスを循環させ
る特許請求の範囲第1項記載の低沸点成分回収方
法。[Scope of Claims] 1. In a heating chamber, an alloy material consisting of components with different boiling points is heated to evaporate the low boiling point components on the surface to produce an alloy material with a layer containing many high boiling point components on the surface, A cooling chamber whose internal pressure is maintained at almost atmospheric pressure with inert gas is connected to the outlet of the heating chamber, and a recovery chamber equipped with a cooling device is connected to the cooling chamber. After heating, the gas is passed through a cooling chamber, and the low-boiling components that evaporate are sent together with an inert gas from the cooling chamber to the recovery chamber, and the low-boiling components are recovered by cooling this gas mixture in the recovery chamber. A method for recovering low boiling point components. 2. The low boiling point component recovery method according to claim 1, wherein an inert gas is circulated between the cooling chamber and the recovery chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58140775A JPS6033323A (en) | 1983-07-31 | 1983-07-31 | Recovery of low-boiling point component |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58140775A JPS6033323A (en) | 1983-07-31 | 1983-07-31 | Recovery of low-boiling point component |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6033323A JPS6033323A (en) | 1985-02-20 |
| JPH0435537B2 true JPH0435537B2 (en) | 1992-06-11 |
Family
ID=15276457
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58140775A Granted JPS6033323A (en) | 1983-07-31 | 1983-07-31 | Recovery of low-boiling point component |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6033323A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007089748A (en) * | 2005-09-28 | 2007-04-12 | Scope:Kk | Goggle |
-
1983
- 1983-07-31 JP JP58140775A patent/JPS6033323A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6033323A (en) | 1985-02-20 |
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