JPS60131933A - Refining device for gold - Google Patents
Refining device for goldInfo
- Publication number
- JPS60131933A JPS60131933A JP24004383A JP24004383A JPS60131933A JP S60131933 A JPS60131933 A JP S60131933A JP 24004383 A JP24004383 A JP 24004383A JP 24004383 A JP24004383 A JP 24004383A JP S60131933 A JPS60131933 A JP S60131933A
- Authority
- JP
- Japan
- Prior art keywords
- gold
- gas
- molten
- crucible
- refining
- 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
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は金の精製装置、詳しくは溶解ルツボ内の溶融金
表面にガス吹込管を通して精製ガス(塩素ガス又は塩素
と酸素との一合ガス)を吹付けて金を精製する装置の改
良に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gold refining apparatus, specifically, a gold refining device that sprays refining gas (chlorine gas or a combined gas of chlorine and oxygen) onto the surface of molten gold in a melting crucible through a gas blowing pipe. This invention relates to improvements in purification equipment.
従来装置においてはガス吹込み手段に何らの考慮がはら
れれておらず、単にガス吹込管より溶解ルツボ内に精製
ガスを吹付けるものであっlこ 。In the conventional apparatus, no consideration was given to the gas blowing means, and purified gas was simply blown into the melting crucible from the gas blowing pipe.
しかるに−回の精製に長時間を要して作業性に劣るばか
りでなく、純度が高くとも99.5〜99.6%程度の
ものしか得られないとともに精製ガスの吹込み世が多い
ために金の揮発量が多い欠点がある。However, not only does it take a long time to purify the process, resulting in poor workability, but also the purity is only about 99.5 to 99.6%, and the purified gas is often blown into the process. The disadvantage is that the amount of gold volatilization is large.
又、従来装置は開放型であるため、揮発する金及び塩化
物の回収が困難であるとともに毒性、腐食性のある塩素
ガスが飛散するため環境衛生を悪化させる等の不具合が
ある。Further, since the conventional apparatus is an open type, it is difficult to recover volatilized gold and chloride, and toxic and corrosive chlorine gas is scattered, resulting in deterioration of environmental hygiene.
本発明は斯る従来事情に鑑み、所要時間を短縮し少いガ
ス供給量でもって反応効果を大ならしめる装置に改良し
、高純度金(99,999%)を作業性よく提供せんと
することを目的とし、他の目的とする処は揮発する金、
塩化物の回収を容易ならしめるとともに塩素ガスの処理
を確実にし環境衛生を確保せんとすることにある。In view of such conventional circumstances, the present invention aims to provide high-purity gold (99,999%) with good workability by improving the apparatus to shorten the required time and increase the reaction effect with a small gas supply amount. Where the purpose is to do something, and where it is for other purposes, it is volatile money,
The objective is to facilitate the recovery of chlorides, ensure the treatment of chlorine gas, and ensure environmental hygiene.
断る本発明は、ガス吹込管の先端に逆漏斗形の吹込口を
設け、該吹込口より溶融金の表面に精製ガスを均一分布
に吹付けさせることを第1発明とし、前記第1発明の構
成とともに溶解ルツボ上を排気ダクトへ通じる冷却筒に
より包覆せしめたことを第2発明とする。A first aspect of the present invention is to provide an inverted funnel-shaped inlet at the tip of a gas blowing pipe, and to spray purified gas uniformly onto the surface of molten metal from the inlet, In addition to the structure, the second invention is that the top of the melting crucible is covered by a cooling cylinder that communicates with the exhaust duct.
本発明を図面により説明ずれば、第1図において、(1
)は電気炉であって、(2)が加熱ヒーター、(3)が
溶解ルツボであり、(4)はガス吹込管、(5)は冷却
筒、(6)は排気ダクトである。To explain the present invention with reference to the drawings, in FIG.
) is an electric furnace, (2) is a heating heater, (3) is a melting crucible, (4) is a gas blowing pipe, (5) is a cooling cylinder, and (6) is an exhaust duct.
溶解ルツボ(3)は加熱ヒーター(2)により加熱され
て金塊を溶解せしめ、溶融金(A)を得る。The melting crucible (3) is heated by the heating heater (2) to melt the gold ingot and obtain molten gold (A).
加熱源には前記加熱ヒーター(2)に代えて高周波コイ
ル(2′)を用いることもよい(第2図)。A high frequency coil (2') may be used as the heat source instead of the heater (2) (FIG. 2).
上記溶解ルツボ(3)には底面下に昇降杆(7)を上下
動自在に係着し、この昇降杆(7〉によってルツボ(3
)を昇降動させるようにする。An elevating rod (7) is attached to the melting crucible (3) below the bottom so that it can move up and down, and the elevating rod (7)
) to move up and down.
溶解ルツボ(3)は塩素又は塩化物に対し反応しないア
ルミナルツボ等を用いる。As the dissolution crucible (3), an alumina crucible or the like which does not react with chlorine or chloride is used.
ガス吹込管(4)は石英製にし、冷却筒(5)の側壁を
貫通して前記ルツボ(3)内に垂下せしめ、その下端に
吹込口(4′)を一体に形成してなる。The gas blowing pipe (4) is made of quartz, passes through the side wall of the cooling cylinder (5), hangs down into the crucible (3), and has a blowing port (4') integrally formed at its lower end.
吹込口(4′)は下方が拡開ゼる逆漏斗状に形成し、そ
の下端の最大径をルツボ(3)の内径より所定最小さな
径とする。The inlet (4') is formed in the shape of an inverted funnel that widens at the bottom, and the maximum diameter at its lower end is a predetermined minimum diameter smaller than the inner diameter of the crucible (3).
上記吹込口(4′)は溶融金(A)との間隙(]1)を
1〜10mmの範囲に設定する。The gap (]1) between the blowing port (4') and the molten metal (A) is set in the range of 1 to 10 mm.
ガス吹込管(4)は精製ガス(塩素ガス又は塩素と酸素
との混合ガス)を収容せるタンク(図示せず)に接続し
て、該ガス(b)を吹込口(4′)よりルツボ(3)内
の溶融金(A)表面に吹イ」ける。The gas blowing pipe (4) is connected to a tank (not shown) containing purified gas (chlorine gas or a mixed gas of chlorine and oxygen), and the gas (b) is injected into the crucible ( 3) Blow the surface of the molten gold (A) inside.
上記間隙(h)は、吹込口(4′)及びルツボ(3)の
内径や、ガス吹込量に応じて前記範囲中の最適値に選択
するとともに選択された間隙(11)を精製作業中一定
に保持するために、溶融金(A)表面の下降に応じてル
ツボ(3)を昇降杆(7)により微量宛上動させる作業
を行なう。The above-mentioned gap (h) is selected to be the optimum value within the above range according to the inner diameter of the injection port (4') and the crucible (3), and the gas injection amount, and the selected gap (11) is kept constant during the refining operation. In order to maintain the temperature, the crucible (3) is moved up by a minute amount using the lifting rod (7) in accordance with the descent of the surface of the molten metal (A).
冷却筒(5)は電気炉(1)上に起設して前記ルツボ(
3)上を包覆せしめるもので、側壁には水などの冷媒を
流通せしめる流路(8)を形成し、該流路(8)の下端
に流入管(9)を、上端に吐出管(9′)を連結する。The cooling cylinder (5) is installed on the electric furnace (1) and the crucible (
3) The upper part is covered, and a channel (8) through which a refrigerant such as water flows is formed on the side wall, an inflow pipe (9) is provided at the lower end of the channel (8), and a discharge pipe (9) is provided at the upper end of the channel (8). 9') are connected.
冷却筒(5)は前記流路(8)に冷媒を循環させること
によって筒壁を冷却される。The cylinder wall of the cooling cylinder (5) is cooled by circulating a refrigerant through the flow path (8).
冷却筒(5)の上端には排気ダクト(6)を連結せしめ
、該ダクト(6)を介して冷却筒(5)内を適度に吸引
するようにする。An exhaust duct (6) is connected to the upper end of the cooling cylinder (5), and the inside of the cooling cylinder (5) is appropriately suctioned through the duct (6).
而して、ルツボ(3)内で金塊を溶解し、溶融金(A)
を製造した後に吹込管(4)の吹込口(4′)より精製
ガス(b)を溶融金(A>表面に所定時間吹付けて溶融
金(A)を精製する。Then, the gold ingot is melted in the crucible (3), and the molten gold (A)
After producing the molten gold (A), the purified gas (b) is blown onto the surface of the molten gold (A) for a predetermined period of time from the inlet (4') of the blowing pipe (4) to purify the molten gold (A).
精製ガス(b)は吹込口(4′)によって溶融金(A)
表面に均等分布状に吹込まれ効率よく置換反応を起す。The purified gas (b) is passed through the inlet (4') to the molten gold (A).
It is blown into the surface evenly and efficiently causes a substitution reaction.
精製作業中に、ルツボ(3)内より金中の不要不純物及
び一部少量の金が塩化物としてガス化し揮発するが、そ
れらの塩化物は冷却筒(5)内を上昇する問に冷却によ
り凝結し、冷却筒(5)の内壁に結晶(a )となって
付着する。During refining work, unnecessary impurities in the gold and a small amount of gold are gasified and volatilized as chlorides from inside the crucible (3), but these chlorides are cooled while rising inside the cooling cylinder (5). It condenses and adheres to the inner wall of the cooling cylinder (5) as crystals (a).
精製作業後、冷却筒(5)を水洗いし、結晶(a )中
の塩化金溶液より金を回収覆る。After the refining work, the cooling cylinder (5) is washed with water, and the gold is recovered from the gold chloride solution in the crystal (a) and covered.
尚、冷却筒(5)内に付着しなかった塩化物を排気ダク
ト(6)内で回収することも自由であり、また揮発する
塩化物中の塩化ガス成分は排気ダクト(6)を経た後、
又は排気ダクト内でカセイソーダによる洗浄処理をする
。Note that the chloride that has not adhered to the inside of the cooling cylinder (5) can be freely collected in the exhaust duct (6), and the chloride gas component in the volatilized chloride can be recovered after passing through the exhaust duct (6). ,
Or clean the exhaust duct with caustic soda.
次に実施例を示す。Next, examples will be shown.
ルツボ(3)の大きさを内径9QlIlIiφ、高さ2
00 mm、冷却筒(5)を800mmとした装置を使
用し、金塊10KCIを高周波コイルによって約120
0℃に加熱して溶融金(A)を製造し lこ 。The crucible (3) has an inner diameter of 9QlIlIiφ and a height of 2
00 mm, and the cooling tube (5) is 800 mm, 10 KCI of gold ingots are heated to about 120 KCI by a high frequency coil.
Molten gold (A) is produced by heating to 0°C.
次いで吹込口(4′)と溶融金(A)表面との間隙を3
mmに設定し、精製ガス(塩素:酸素=1=1の混合ガ
ス)を吹込口(4′)より約20分間吹込んで精製した
。Next, the gap between the injection port (4') and the surface of the molten metal (A) is set to 3.
mm, and purified gas (mixed gas of chlorine:oxygen=1=1) was blown into the tank from the blowing port (4') for about 20 minutes for purification.
その結果、純度99.5%の金が99.998%の純度
となった。As a result, gold with a purity of 99.5% became 99.998% pure.
さらに10分間精製した後において、純度99.999
%の金が得られた。After further purification for 10 minutes, purity 99.999
% of gold was obtained.
精製作業後、冷却筒(5)を水洗いし、約30gの金を
回収した。After the refining work, the cooling cylinder (5) was washed with water and about 30 g of gold was recovered.
本発明は叙上第1発明の如く、ガス吹込管の先端に逆漏
斗形の吹込口を設け、溶融金表面に間隙を介し対向せし
めるので、吹込口より精製ガスを溶融金表面全体にわた
って均等分布状に排気ダクトである。In the present invention, as in the first invention described above, an inverted funnel-shaped inlet is provided at the tip of the gas blowing pipe and is opposed to the surface of the molten metal with a gap therebetween, so that purified gas is uniformly distributed from the inlet to the entire surface of the molten metal. This is an exhaust duct.
吹付けることができる。Can be sprayed.
従って、溶融金を精製ガスによって効率よく精製反応を
起ごさせることができ、従来に較べて精製時間を著しく
短縮し且つガス吸込緒を少なくする結果、金の揮発量を
激減するとともに高純麿の金(99,999%)を得る
ことができた。Therefore, the refining reaction of molten gold can be efficiently caused by the refining gas, and as a result, the refining time is significantly shortened and the amount of gas sucked is reduced compared to the conventional method.As a result, the amount of gold volatilization is drastically reduced, and high-purity gold is produced. of gold (99,999%).
又、第2発明の如く、溶解ルツボ上を排気ダクトへ通じ
る冷却筒により包覆せしめたので、精製作業中に揮発J
る金を塩化金として冷却筒内壁に付着させ回収させるこ
とができ経済的であるとともに揮発するガス成分が作業
場内で飛散するおそれがなく環境衛生上好ましい。In addition, as in the second invention, since the top of the melting crucible is covered with a cooling cylinder leading to the exhaust duct, the volatilized J during refining work is prevented.
The gold can be deposited as gold chloride on the inner wall of the cooling cylinder and recovered, which is economical, and there is no risk of the volatile gas components scattering in the workplace, which is preferable in terms of environmental hygiene.
依って所期の目的を達成し得る。Therefore, the intended purpose can be achieved.
第1図は本発明装置の断面図、第2図は加熱源の変形例
を示す断面図である。
図中、(3)は溶解ルツボ、(4)はガス吹込管、(4
′)は吹込口、(A)は溶融金、(b)は精製ガス、(
5)は冷却筒、(6)は特許出願人 田中電子工業株式
会社FIG. 1 is a sectional view of the apparatus of the present invention, and FIG. 2 is a sectional view showing a modification of the heating source. In the figure, (3) is a melting crucible, (4) is a gas blowing pipe, and (4) is a melting crucible.
') is the inlet, (A) is the molten gold, (b) is the purified gas, (
5) is a cooling cylinder, and (6) is patent applicant Tanaka Electronics Co., Ltd.
Claims (3)
精製ガスを吹付けて金を精製する装置において、上記ガ
ス吹込管の先端に逆漏斗形の吹込口を設け、溶融金表面
に間隙を介し対向せしめたことを特徴とする金の精製装
置。(1) In a device that purifies gold by blowing purified gas onto the surface of molten gold in a melting crucible through a gas blowing tube, an inverted funnel-shaped blowing port is provided at the tip of the gas blowing tube to create a gap on the surface of the molten gold. A gold refining device characterized in that the gold refining devices are arranged opposite to each other.
る特許請求の範囲第1項記載の精製装置。(2) The refining device according to claim 1, wherein the gap between the inlet and the surface of the molten metal is adjustable.
精製ガスを吹付けて金を精製する装置において、上記ガ
ス吹込管の免端に逆漏斗形の吹込口を設け、溶融金表面
に間隙を介し対向せしめるとともに溶解ルツボ上を排気
ダクトへ通じる冷却筒により包覆せしめたことを特徴と
する金の精製装置。(3) In an apparatus for purifying gold by spraying purified gas through a gas blowing pipe onto the surface of molten gold in a melting crucible, an inverted funnel-shaped blowing port is provided at the end of the gas blowing pipe, and a gap is formed on the surface of the molten gold. A gold refining apparatus characterized in that the melting crucible is opposed to the melting crucible through a cooling cylinder which is connected to an exhaust duct.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24004383A JPS60131933A (en) | 1983-12-19 | 1983-12-19 | Refining device for gold |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24004383A JPS60131933A (en) | 1983-12-19 | 1983-12-19 | Refining device for gold |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60131933A true JPS60131933A (en) | 1985-07-13 |
JPH0459372B2 JPH0459372B2 (en) | 1992-09-22 |
Family
ID=17053619
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24004383A Granted JPS60131933A (en) | 1983-12-19 | 1983-12-19 | Refining device for gold |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60131933A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101025985B1 (en) | 2009-01-22 | 2011-03-30 | 김일두 | Combustion apparatus of filter for gilding solution |
-
1983
- 1983-12-19 JP JP24004383A patent/JPS60131933A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101025985B1 (en) | 2009-01-22 | 2011-03-30 | 김일두 | Combustion apparatus of filter for gilding solution |
Also Published As
Publication number | Publication date |
---|---|
JPH0459372B2 (en) | 1992-09-22 |
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