JPH0555575B2 - - Google Patents
Info
- Publication number
- JPH0555575B2 JPH0555575B2 JP61174948A JP17494886A JPH0555575B2 JP H0555575 B2 JPH0555575 B2 JP H0555575B2 JP 61174948 A JP61174948 A JP 61174948A JP 17494886 A JP17494886 A JP 17494886A JP H0555575 B2 JPH0555575 B2 JP H0555575B2
- Authority
- JP
- Japan
- Prior art keywords
- gold
- powder
- refining
- grade
- solution
- 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
Links
- 239000010931 gold Substances 0.000 claims description 41
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 29
- 229910052737 gold Inorganic materials 0.000 claims description 28
- 238000000034 method Methods 0.000 claims description 19
- 238000007670 refining Methods 0.000 claims description 13
- NLKNQRATVPKPDG-UHFFFAOYSA-M potassium iodide Chemical compound [K+].[I-] NLKNQRATVPKPDG-UHFFFAOYSA-M 0.000 claims description 10
- FVAUCKIRQBBSSJ-UHFFFAOYSA-M sodium iodide Chemical compound [Na+].[I-] FVAUCKIRQBBSSJ-UHFFFAOYSA-M 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 3
- 238000005341 cation exchange Methods 0.000 claims description 3
- 239000003792 electrolyte Substances 0.000 claims description 3
- 239000012528 membrane Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 230000003647 oxidation Effects 0.000 claims description 2
- 238000007254 oxidation reaction Methods 0.000 claims description 2
- 235000009518 sodium iodide Nutrition 0.000 claims description 2
- 239000000843 powder Substances 0.000 description 13
- 239000000243 solution Substances 0.000 description 10
- 238000005868 electrolysis reaction Methods 0.000 description 7
- 238000006722 reduction reaction Methods 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 229910052740 iodine Inorganic materials 0.000 description 5
- 239000011630 iodine Substances 0.000 description 5
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000008151 electrolyte solution Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- QZPSXPBJTPJTSZ-UHFFFAOYSA-N aqua regia Chemical compound Cl.O[N+]([O-])=O QZPSXPBJTPJTSZ-UHFFFAOYSA-N 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 150000002496 iodine Chemical class 0.000 description 1
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Description
(産業上の利用分野)
本発明は、金の精製方法の改良に関する。
(従来の技術と問題点)
従来より金の精製方法としては、王水又はHCl
−Cl2水により低品位金を溶解し、ヒドラジン等
の還元剤により金のみを選択還元する方法、HCl
の酸性における低品位金の電解方法が良く知られ
ている。
しかし、前者の方法は排ガス処理に設備と人員
を必要とし、後者の方法は塩酸を電解液に用いる
為陽極でCl2ガスの発生があつて、電解効率が低
いという問題点があつた。
この為、本発明者は塩酸を電解液に用いる代わ
りにハロゲンを用いることを検討し、沃素の電解
方法を試みたが、この沃素の電解方法では金の純
度を上げることができなかつた。
そこで本発明者は、上記の沃素による電解方法
を基礎にして研究を進め、低品位金を効率良く高
品位金に精製することのできる方法を開発したも
のである。
(問題点を解決するための手段)
上記問題点を解決するための本発明による金の
精製方法は、低品位の金を精製するに於いて、沃
化カリウム溶液又は沃化ナトリウム溶液を電解液
とし、陽イオン交換膜を隔膜とした電解槽の陽極
上で直接低品位の金を電解酸化により溶解し、得
られた沃化金酸溶液を反応層中でPH12.5以上にPH
調節して自己還元により金粉のみを析出すること
を特徴とするものである。
(作用)
上記のように本発明による金の精製方法は、隔
膜電解法により陰極上に金を析出させることなく
溶解することができ、これにより得られた沃化金
酸溶液をPH12.5以上にPH調節することにより、自
己還元により金粉として析出する。こうして得ら
れた金は99.4wt%の低品位金の場合99.991wt%以
上の高品位のものである。
(実施例)
本発明による金の精製方法の実施例について説
明する。3M/の沃化カリウム(KI)溶液を電
解液とし、PHを11〜12にPH調整した後、図面に示
す如く陽イオン交換膜2を隔膜とした電解槽1の
陽極室3に入れ、陰極室4には純水を入れた。次
に60A/dで通電し、品位99.4wt%の金陽極を溶
解した後、還元反応タンク7へ送液した。一方陰
極室4内にはKOHアルカリ液が生成されており、
このKOHアルカリ液をポンプ6にて還元反応タ
ンク7へ送液した。次いで還元反応タンク7内
で、陽極室液とKOHアルカリ液を混合撹拌し、
PHを12.5以上にPH調整してAuを自己還元し、Au
粉のみを析出した。この析出したAu粉は溶液と
分離する為、還元反応タンク7内の沈澱したAu
粉を底から排出し、液中に浮遊しているAu粉は、
溶液をポンプ8にて濾過槽9に送液してAu粉を
遠心濾過し、この濾過したAu粉を槽外に排出し
て、さらに還元反応タンク7の底から排出した
Au粉と共に洗浄槽10に入れ、洗浄水にて向流
水洗し、乾燥機11にて乾燥してAu粉を得た。
濾過槽9より排出した液体は、ポンプ12にて電
解槽1に戻される。
こうして得られたAu粉と、従来の沃素の電解
方法によつて品位99.4wt%の金を電析して得た
Au粉の品位を測定した処、下記の表1に示すよ
うな結果を得た。
(Industrial Application Field) The present invention relates to an improvement in a gold refining method. (Conventional techniques and problems) Traditionally, gold purification methods have been using aqua regia or HCl.
−Cl 2 A method of dissolving low-grade gold in water and selectively reducing only the gold with a reducing agent such as hydrazine, HCl
The method of electrolyzing low-grade gold in acidic conditions is well known. However, the former method requires equipment and personnel for exhaust gas treatment, and the latter method uses hydrochloric acid as the electrolyte, which generates Cl 2 gas at the anode, resulting in low electrolysis efficiency. For this reason, the present inventor considered using a halogen instead of hydrochloric acid as an electrolytic solution and tried an iodine electrolysis method, but this iodine electrolysis method was unable to increase the purity of gold. Therefore, the present inventor conducted research based on the above-mentioned electrolytic method using iodine, and developed a method that can efficiently refine low-grade gold into high-grade gold. (Means for Solving the Problems) In order to solve the above problems, the gold refining method according to the present invention uses a potassium iodide solution or a sodium iodide solution as an electrolytic solution when refining low-grade gold. Then, low-grade gold is directly dissolved by electrolytic oxidation on the anode of an electrolytic cell with a cation exchange membrane as a diaphragm, and the resulting iodoauric acid solution is heated to a pH of 12.5 or higher in the reaction layer.
It is characterized in that only gold powder is precipitated by self-reduction under controlled conditions. (Function) As described above, the method for refining gold according to the present invention can dissolve gold without depositing it on the cathode using the diaphragm electrolysis method, and the iodoauric acid solution obtained thereby can be dissolved at a pH of 12.5 or higher. By adjusting the pH to , it precipitates as gold powder through self-reduction. The gold thus obtained is of high grade of 99.991 wt% or more in the case of low-grade gold of 99.4 wt%. (Example) An example of the gold refining method according to the present invention will be described. After adjusting the pH to 11-12 using a 3M potassium iodide (KI) solution as the electrolyte, it is placed in the anode chamber 3 of the electrolytic cell 1 with the cation exchange membrane 2 as a diaphragm as shown in the drawing, Pure water was placed in chamber 4. Next, electricity was applied at 60 A/d to dissolve the gold anode with a grade of 99.4 wt%, and then the solution was sent to the reduction reaction tank 7. On the other hand, a KOH alkaline solution is generated in the cathode chamber 4.
This KOH alkali solution was sent to the reduction reaction tank 7 using the pump 6. Next, in the reduction reaction tank 7, the anode chamber solution and the KOH alkaline solution are mixed and stirred.
Adjust the pH to 12.5 or higher to self-reduce Au, and
Only powder was precipitated. Since this precipitated Au powder is separated from the solution, the precipitated Au powder in the reduction reaction tank 7
The powder is discharged from the bottom, and the Au powder floating in the liquid is
The solution was sent to the filtration tank 9 by the pump 8, the Au powder was centrifugally filtered, and the filtered Au powder was discharged outside the tank and further discharged from the bottom of the reduction reaction tank 7.
It was placed in a cleaning tank 10 together with Au powder, washed in countercurrent with washing water, and dried in a dryer 11 to obtain Au powder.
The liquid discharged from the filter tank 9 is returned to the electrolytic cell 1 by a pump 12. Gold with a grade of 99.4wt% was deposited on the Au powder obtained in this way using a conventional iodine electrolysis method.
When the quality of the Au powder was measured, the results shown in Table 1 below were obtained.
【表】
また本発明の前述の方法と従来の沃素の電解方
法とにより90.5wt%Auを精製して得たAu粉の品
位を測定した処、下記の表−2に示すような結果
を得た。[Table] In addition, when we measured the quality of Au powder obtained by refining 90.5wt% Au using the method described above of the present invention and the conventional iodine electrolysis method, we obtained the results shown in Table 2 below. Ta.
【表】
さらに本発明の前述の方法と従来の沃素の電解
方法とにより75wt%Auを精製して得たAu粉の品
位を測定した処、下記の表−3に示すような結果
を得た。[Table] Furthermore, when we measured the quality of Au powder obtained by refining 75wt% Au using the method described above of the present invention and the conventional iodine electrolysis method, we obtained the results shown in Table 3 below. .
【表】
上記の表−1、2、3で明らかなように実施例
の方法は従来例の方法に比し著しくAuの純度を
上げることができて、精製効率が高いことが判
る。
(発明の効果)
以上詳記した通り本発明の金の精製方法によれ
ば、低品位の金を、純度の高い金に効率に良く精
製できるという効果があつて、従来の精製方法に
とつて代わることのできる画期的な方法と言え
る。[Table] As is clear from Tables 1, 2, and 3 above, the method of the example can significantly increase the purity of Au compared to the conventional method, indicating that the purification efficiency is high. (Effects of the Invention) As detailed above, the gold refining method of the present invention has the effect of efficiently refining low-grade gold into high-purity gold, which is superior to conventional refining methods. It can be said to be an innovative method that can be replaced.
図は本発明の金の精製方法を実施する手段を示
す図である。
The figure is a diagram showing means for carrying out the gold refining method of the present invention.
Claims (1)
ム溶液又は沃化ナトリウム溶液を電解液とし、陽
イオン交換膜を隔膜とした電解槽の陽極上で直接
低品位の金を電解酸化により溶解し、得られた沃
化金酸溶液を反応槽中でPH12.5以上にPH調節して
自己還元により金粉のみを析出することを特徴と
する金の精製方法。1. When refining low-grade gold, low-grade gold is dissolved by electrolytic oxidation directly on the anode of an electrolytic cell with a cation exchange membrane as a diaphragm using a potassium iodide solution or a sodium iodide solution as an electrolyte. A method for refining gold, which comprises adjusting the pH of the obtained iodized gold acid solution to 12.5 or higher in a reaction tank to precipitate only gold powder by self-reduction.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61174948A JPS6333528A (en) | 1986-07-25 | 1986-07-25 | Refining of gold |
EP87830273A EP0253783B1 (en) | 1986-07-16 | 1987-07-15 | Process for refining gold and apparatus employed therefor |
DE8787830273T DE3775645D1 (en) | 1986-07-16 | 1987-07-15 | METHOD AND DEVICE FOR CLEANING GOLD. |
US07/073,509 US4859293A (en) | 1986-07-16 | 1987-07-15 | Process for refining gold and apparatus employed therefor |
AU75670/87A AU607921B2 (en) | 1986-07-16 | 1987-07-15 | Process for refining gold and apparatus employed therefor |
CA000542230A CA1322855C (en) | 1986-07-16 | 1987-07-15 | Process for refining gold and apparatus employed therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61174948A JPS6333528A (en) | 1986-07-25 | 1986-07-25 | Refining of gold |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6333528A JPS6333528A (en) | 1988-02-13 |
JPH0555575B2 true JPH0555575B2 (en) | 1993-08-17 |
Family
ID=15987530
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61174948A Granted JPS6333528A (en) | 1986-07-16 | 1986-07-25 | Refining of gold |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6333528A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6350489A (en) * | 1986-08-21 | 1988-03-03 | Tanaka Kikinzoku Kogyo Kk | Method for dissolving gold |
JPH01242730A (en) * | 1988-03-23 | 1989-09-27 | Tanaka Kikinzoku Kogyo Kk | Method for recovering noble metal |
JP2928040B2 (en) * | 1993-02-26 | 1999-07-28 | ワイケイケイ株式会社 | Slider for slide fastener with automatic stop device |
-
1986
- 1986-07-25 JP JP61174948A patent/JPS6333528A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6333528A (en) | 1988-02-13 |
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