JPS58210129A - Production of high-purity gold - Google Patents
Production of high-purity goldInfo
- Publication number
- JPS58210129A JPS58210129A JP57092404A JP9240482A JPS58210129A JP S58210129 A JPS58210129 A JP S58210129A JP 57092404 A JP57092404 A JP 57092404A JP 9240482 A JP9240482 A JP 9240482A JP S58210129 A JPS58210129 A JP S58210129A
- Authority
- JP
- Japan
- Prior art keywords
- gold
- purity
- soln
- impurities
- impure
- 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
Classifications
-
- 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)
Abstract
Description
【発明の詳細な説明】
本発明は高純度金の製造方法に関するもので、特にシア
ン化金酸溶液から純度の高い金を効率よく製造する方法
であり、銀、銅、ニッケル、鉄。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing high-purity gold, and in particular a method for efficiently producing high-purity gold from a cyanauric acid solution, including silver, copper, nickel, and iron.
白金、パラジウム等々金以外の元素を含む溶液から純度
99.99%以上の高純度の金を製造する方法である。This is a method for producing high-purity gold with a purity of 99.99% or more from a solution containing elements other than gold, such as platinum and palladium.
一般的に純度99.99%以上の高純度の金はウオール
ウィル法として知られる電解精製法が用いられているが
、この電解精製法は通常40〜80g(1)
/eの金を含有する電解液や高純度の陰極用金板が必要
であり、また電解液中の不純物等液管理も必要で高純度
の金を製造する5Fで効率的に欠点が′ある。他方、金
のシアン化金酸の溶液を還元剤で還元する方法としては
、亜鉛、コノゲル。アルミニウム等の金属を用いて還九
場る方法が知られている。しかしながら、還元剤で’1
A7cする方法は金の還2cと同時に他の不純物も還元
されるため純度99.99%以上の高純度金を製造する
ことができなかった。Generally, high-purity gold with a purity of 99.99% or higher is produced using an electrolytic refining method known as the wall will method, but this electrolytic refining method usually contains 40 to 80 g(1)/e of gold. It requires an electrolytic solution and a high-purity gold plate for the cathode, and also requires liquid management such as impurities in the electrolytic solution, which is a disadvantage in terms of efficiency in producing high-purity gold at 5F. On the other hand, as a method for reducing a solution of gold cyanide and auric acid using a reducing agent, zinc and conogel are used. A method is known that uses a metal such as aluminum. However, with reducing agent '1
In method A7c, other impurities are also reduced at the same time as gold is reduced, so it was not possible to produce high purity gold with a purity of 99.99% or higher.
本発明材は、上記欠点に鑑み鋭意攻究の結果、効率的に
高純度の金を製造する方法を見出したものである。The material of the present invention was created as a result of intensive research in view of the above-mentioned drawbacks and the discovery of a method for efficiently producing high-purity gold.
本発明は、不純物を含有するシアン化金酸溶液から高純
度金を製造する方法に才、いて、・大部分の金を還元剤
で還元ろ別した後残りの金を不純物とともに還元して不
純金とし、その後その不純金をシアン化金酸として溶解
して次のジrン化金酸溶液に混入することを特徴とする
高純度金の製造方法である。The present invention provides a method for producing high-purity gold from a cyanauric acid solution containing impurities. After most of the gold is reduced and filtered out using a reducing agent, the remaining gold is reduced together with the impurities to make it impure. This is a method for producing high-purity gold, which is characterized in that the impure gold is made into pure gold, and then the impure gold is dissolved as cyanauric acid and mixed into the subsequent cyanauric acid solution.
(2)
本発明は、還元剤で還元するときシアン化金酸溶液中で
はまず金が先に還元しその後不純物が急激に還元される
ことにもとづくものである。4′なわち、第1図におい
て金の還元曲線lはほぼ還元剤の添加量に比例し゛C還
元されるが、不純物の還元曲線2は金の還元量が95%
を越えると急激に立ちあがる。したがって、純度99.
99%以上の高純度金を製造するには不純物許容量がO
,O1%思1・と極めて少ないため立ちあがる直前でや
める必要がある。本発明において大部分の金を還元ろ別
し。(2) The present invention is based on the fact that when reducing with a reducing agent, gold is reduced first in a cyanauric acid solution, and then impurities are rapidly reduced. 4' In other words, in Figure 1, the gold reduction curve 1 shows that the amount of gold reduced is approximately proportional to the amount of reducing agent added, but the impurity reduction curve 2 shows that the amount of gold reduced is 95%.
When it exceeds , it rises rapidly. Therefore, the purity is 99.
To produce high purity gold of 99% or higher, the impurity tolerance is O.
, 1%, which is extremely low, so it is necessary to stop just before standing up. In the present invention, most of the gold is separated by reduction filtration.
てまず高純度金をうる。そして、濃度′の躊くなった溶
液から金をすべて還元し゛(不純金をうる。その後不純
金を再溶解してシアン化金酸溶液を得、これを久のシア
ン化金酸溶液に混入する。不純物の還元曲線2は不純物
の種類や濃度等により定まるが、金の還元曲線lがほは
直線のためあらか(7め還元剤の添加量を想定すること
により還元される不純物の量を限ることができる。した
がって、連続して本発明のM遣方法を実施しても、不純
物の濃度が蓄積して増加することもない。First, obtain high-purity gold. Then, all the gold is reduced from the solution whose concentration has decreased (to obtain impure gold. After that, the impure gold is redissolved to obtain a cyanide-auric acid solution, and this is mixed into the cyanide-auric acid solution. The reduction curve 2 of impurities is determined by the type and concentration of impurities, but since the reduction curve 1 of gold is almost a straight line, the amount of impurities reduced can be calculated by assuming the amount of reducing agent added. Therefore, even if the method for applying M according to the present invention is carried out continuously, the concentration of impurities will not accumulate and increase.
(3) 以ト、実施例と従来例につい(説明する。(3) Examples and conventional examples will be explained below.
〔実施例1〕
金を75%含冑する装飾品のくず5 kgをシアン化カ
リウム溶液に溶解しIf!の金含自溶液をえた。この溶
液にアルミニウム336 gを添加し大部分の金を還元
した。このときの1澄液を分析したところ金の濃度は3
.1g/j!であった。また、還元した金をろ別洗浄乾
燥したところ、3673.41!の金粉をえた。この金
粉の純度を分析したところ99.996%の純度であっ
た。一方、U:Ki液をさらにアルミニウム8gで還元
したところ、73.4[の金粉をえた。これを分析した
ところ99.70%であった。以上のごとく、本発明の
製造方法によれば99.996%の高純度の金が98%
の収率で製造することができた。[Example 1] 5 kg of ornamental scraps containing 75% gold were dissolved in a potassium cyanide solution and the If! A gold-containing solution was obtained. 336 g of aluminum was added to this solution to reduce most of the gold. When one clear liquid was analyzed, the gold concentration was 3.
.. 1g/j! Met. In addition, when the reduced gold was filtered, washed and dried, it turned out to be 3673.41! I got gold powder. When the purity of this gold powder was analyzed, it was found to be 99.996% pure. On the other hand, when the U:Ki solution was further reduced with 8 g of aluminum, 73.4 gold powder was obtained. When this was analyzed, it was 99.70%. As described above, according to the manufacturing method of the present invention, gold with a high purity of 99.996% can be produced with a purity of 98%.
could be produced with a yield of .
〔従来例1〕
実施例1と同様な溶液にアルミニウム344gを加え金
を完全に還元析出さセた。ごの還元した金をろ別洗浄乾
燥したところ3747.4gの金粉i!また。[Conventional Example 1] 344 g of aluminum was added to the same solution as in Example 1 to completely reduce and precipitate gold. When the reduced gold was filtered, washed and dried, it yielded 3747.4g of gold powder. Also.
この金粉を分析したところ純度は99.97%であっ(
4)
た。このときの金の回収率は99.9V6であった。When this gold powder was analyzed, the purity was 99.97% (
4) Ta. The gold recovery rate at this time was 99.9V6.
〔実施例2〕
金99.62%、銅0.34%、紐0,03%その他微
量の鉄やパラジウムなどを含有する粗金5 kgをン゛
J′ン化ナトリウム水溶液に溶解し18Rの熔坂をえた
。[Example 2] 5 kg of crude gold containing 99.62% gold, 0.34% copper, 0.03% string and other trace amounts of iron and palladium was dissolved in an aqueous solution of sodium chloride. I got a hotspot.
この液を9Eづつ分割した後一方の液に助船823gを
添加したところ2477.2gの金粉をえた。この金粉
の純度を分析したところ99.992%の純度であった
。This liquid was divided into 9E portions, and 823g of auxiliary ship was added to one of the liquids, yielding 2477.2g of gold powder. When the purity of this gold powder was analyzed, it was found to be 99.992% pure.
〔従来例2〕
他方の91!の液に亜鉛832gを添加したところ25
00.6gの金粉をえた。この金粉を分析したところ9
9.94%の純度であった。[Conventional Example 2] The other 91! When 832g of zinc was added to the solution, 25
Obtained 00.6g of gold powder. When this gold powder was analyzed, 9
The purity was 9.94%.
以上のごとく、本発明の製造方法によれば99.992
%の純度の金が99%の収率で製造4ることができた。As described above, according to the manufacturing method of the present invention, 99.992
Gold with a purity of 4% could be produced with a yield of 99%.
以上詳述したように本発明の製造方法に、Lれば純度9
9.99%以上の高純度の金を不純物のLI4度によら
ず効率よく製造でき、しかもくり返し実施し。As detailed above, in the production method of the present invention, if L is 9.
High-purity gold of 9.99% or higher can be efficiently produced regardless of the LI4 degree of impurities, and it can be repeatedly produced.
でも不純物の濃度が艙積されていかないといつj(5) ぐれた〃J果がある。However, if the concentration of impurities does not accumulate, then There is a stray J result.
弟1図は還元剤の添加量に対する金と不純物の含有量を
示す図である。
l −金の還元曲線、2− 不純物の還ノし曲線出願人
ul中貴金属工業株式会社
(6)Figure 1 is a diagram showing the content of gold and impurities relative to the amount of reducing agent added. l - Reduction curve of gold, 2 - Reduction curve of impurities Applicant: UL Naka Kikinzoku Kogyo Co., Ltd. (6)
Claims (1)
する方法において、大部分の還元剤で還元ろ別した後残
りの金を不純物とともに還元して不純金とし、その後そ
の不純金をシアン化金酸として溶解して次のシアン化金
酸溶液に混入することを特徴とする高純度金の製造方法
。In a method for producing high-purity gold from a cyanide-auric acid solution containing impurities, most of the gold is reduced and filtered using a reducing agent, the remaining gold is reduced together with impurities to make impure gold, and then the impure gold is cyanated. A method for producing high-purity gold, characterized by dissolving it as gold acid and mixing it into a subsequent cyanide-auric acid solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57092404A JPS58210129A (en) | 1982-05-31 | 1982-05-31 | Production of high-purity gold |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57092404A JPS58210129A (en) | 1982-05-31 | 1982-05-31 | Production of high-purity gold |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58210129A true JPS58210129A (en) | 1983-12-07 |
JPH0133538B2 JPH0133538B2 (en) | 1989-07-13 |
Family
ID=14053473
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57092404A Granted JPS58210129A (en) | 1982-05-31 | 1982-05-31 | Production of high-purity gold |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58210129A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015151582A (en) * | 2014-02-14 | 2015-08-24 | 田中貴金属工業株式会社 | Method for recovering gold or silver from gold or silver-containing cyanogen-based waste fluid |
-
1982
- 1982-05-31 JP JP57092404A patent/JPS58210129A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015151582A (en) * | 2014-02-14 | 2015-08-24 | 田中貴金属工業株式会社 | Method for recovering gold or silver from gold or silver-containing cyanogen-based waste fluid |
Also Published As
Publication number | Publication date |
---|---|
JPH0133538B2 (en) | 1989-07-13 |
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