JPH059606A - Separation method of gold-silver alloy - Google Patents
Separation method of gold-silver alloyInfo
- Publication number
- JPH059606A JPH059606A JP3189333A JP18933391A JPH059606A JP H059606 A JPH059606 A JP H059606A JP 3189333 A JP3189333 A JP 3189333A JP 18933391 A JP18933391 A JP 18933391A JP H059606 A JPH059606 A JP H059606A
- Authority
- JP
- Japan
- Prior art keywords
- gold
- silver
- silver alloy
- cathode
- nitric acid
- 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.)
- Pending
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)
- Electrolytic Production Of Metals (AREA)
Abstract
(57)【要約】
【目的】 金銀合金の品位調整を行うことなく、硝酸分
金法に伴う窒素酸化物の発生、廃液処理、薬品費などを
低減でき、容易に金銀合金の分離を可能にする方法を提
供すること。
【構成】 金銀合金を金と銀とに分離する方法におい
て、前記金銀合金を陽極となし、沃素化合物電解液中で
電気分解して陰極に析出させ微細な粒子に加工する工程
と前記陰極析出物を酸化性を有する酸で抽出して金と銀
に分離する工程とからなることを特徴としている。(57) [Abstract] [Purpose] It is possible to easily separate gold-silver alloys without adjusting the quality of gold-silver alloys, reducing the generation of nitrogen oxides, waste liquid treatment, chemical costs, etc. associated with nitric acid dispensing To provide a way to do. In the method for separating a gold-silver alloy into gold and silver, the step of forming the gold-silver alloy as an anode, electrolyzing it in an iodine compound electrolyte and depositing it on a cathode to form fine particles, and the cathode deposit. Is extracted with an acid having an oxidizing property to separate into gold and silver.
Description
【0001】[0001]
【産業上の利用分野】本発明は、金銀の分離精製技術に
関するもので、さらに詳しくは、貴金属精錬工程におい
て生じる金銀合金や、宝飾品に代表される金銀を含んだ
屑、電気工業、電子工業等の電気部品に用いられる金銀
合金などより発生する屑などより、金銀を分離する方法
に関わるものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for separating and refining gold and silver. More specifically, the present invention relates to a gold-silver alloy produced in a refining process of precious metals and scraps containing gold and silver represented by jewelry, electrical industry and electronic industry. The present invention relates to a method of separating gold and silver from scraps generated from a gold-silver alloy used for electric parts such as.
【0002】[0002]
【従来の技術とその問題点】金属合金を分離精製する方
法には、ウォールウィル法と硝酸分金法があり、貴金属
精錬や貴金属回収の分野で一般的に用いられている。2. Description of the Related Art The methods for separating and refining metal alloys include the Wall Will method and the nitric acid dispensing method, which are commonly used in the fields of precious metal refining and precious metal recovery.
【0003】ウォールウィル法は、金を含む塩酸電解液
中で銀を含む粗金板を陽極とし、電解により金を溶解
し、次いで陰極に析出させる。銀は塩化銀となり陽極泥
として得られる。しかし陽極上で生じる塩化銀が電解を
妨げるために、精製に用いる粗金板の金の品位は95%以
上、銀は概ね5%以下である必要があり、ウォールウィ
ル法の適用は銀の割合が少ない場合に限定されている。
18金に代表される金銀合金等、銀を5%以上含むものに
ついては硝酸分金法により分離するのが一般的である。In the Wall Will method, a rough gold plate containing silver is used as an anode in a hydrochloric acid electrolyte containing gold, gold is dissolved by electrolysis, and then deposited on the cathode. Silver becomes silver chloride and is obtained as anode mud. However, since silver chloride generated on the anode hinders electrolysis, the gold quality of the rough metal plate used for refining must be 95% or more and silver must be 5% or less. Limited to a few.
It is common to separate those containing 5% or more of silver, such as a gold-silver alloy represented by 18 gold, by the nitric acid separation method.
【0004】硝酸分金法は、金銀合金に銅や銀などの他
の金属を加えて炉中で溶解して、金の品位が20〜25%以
下になるように合金の品位を調整し、次いで硝酸を作用
させると金以外の金属は硝酸に溶かされ、金は硝酸に溶
かされずに残物として得ることにより分離される。硝酸
分金法の欠点は、硝酸を作用させる際に大量の窒素酸化
物が発生することであるが、ここではさらに他の金属を
加えて品位を調整するので最初にあった金属重量の3〜
4倍の量の金属を溶解することになり、窒素酸化物の発
生をより助長することである。また、金銀合金の品位調
整が必要であるなどの手間を要し、廃液処理や薬品費が
かかるなどの問題がある。In the nitric acid dispensing method, other metals such as copper and silver are added to a gold-silver alloy and melted in a furnace to adjust the grade of the alloy so that the grade of gold is 20 to 25% or less. Then, when nitric acid is acted on, metals other than gold are dissolved in nitric acid, and gold is separated without being dissolved in nitric acid to obtain a residue. A drawback of the nitric acid dispensing method is that a large amount of nitrogen oxides are generated when nitric acid acts, but here, since the quality is adjusted by adding another metal, the amount of the metal weight of 3 to 3
This means that four times as much metal is dissolved, which further promotes the generation of nitrogen oxides. Further, there is a problem in that it requires time and effort such as adjustment of the quality of the gold-silver alloy, waste liquid treatment and chemical cost.
【0005】発明者は、金銀合金を微細に加工すること
ができれば、王水や硝酸等の酸に溶解することが出来る
のではと考え、金銀合金をシアン化アルカリ溶液中で電
気分解して得られた電解析出物を王水や硝酸に溶解して
分離する方法を検討した。しかし、第1に有毒なシアン
化合物を用いなければならないこと、第二に電解析出物
の酸溶解に際して有毒なシアン化水素ガスが発生する点
など安全面での問題があり、さらには電解析出物の酸溶
解が十分に行われず溶解残しが多く、さらに金銀合金中
に含まれる金銀以外は貴金属成分の回収が容易でないな
どの欠点があり必ずしも良い方法ではなかった。The inventor believes that if a gold-silver alloy can be finely processed, it can be dissolved in an acid such as aqua regia or nitric acid. Therefore, the gold-silver alloy is obtained by electrolyzing it in an alkali cyanide solution. A method of dissolving the obtained electrolytic precipitate in aqua regia or nitric acid and separating it was examined. However, there are safety-related problems such as the fact that a toxic cyanide compound must be used first, and a toxic hydrogen cyanide gas is generated when the electrolytic precipitate is dissolved in an acid. However, it is not always a good method because it has a drawback that the acid dissolution is not sufficiently performed and a large amount of undissolved residue remains, and that no precious metal components other than gold and silver contained in the gold-silver alloy are not easily recovered.
【0006】[0006]
【発明が解決しようとする課題】本発明は、以上の問題
点に鑑み金銀合金をより容易に分離する方法を提供する
ところにあり、金銀合金の品位調整を不用とし、かつ硝
酸分金法がかかえる窒素酸化物の発生、廃液処理、薬品
費など工程に付帯する問題点を低減することを目的とす
るものである。さらに金銀合金の使用は多岐にわたるた
め、金銀のほかに、有価な白金やパラジウムなどが含ま
れている場合も多く、これらの材料についても適用でき
る方法を提供するものである。SUMMARY OF THE INVENTION In view of the above problems, the present invention provides a method for separating a gold-silver alloy more easily, which makes it unnecessary to adjust the quality of the gold-silver alloy, and the nitric acid dispensing method The purpose is to reduce the problems associated with the process such as generation of nitrogen oxides, waste liquid treatment, and chemical cost. Furthermore, since the use of gold-silver alloys is wide-ranging, valuable platinum and palladium are often contained in addition to gold and silver, and a method applicable to these materials is also provided.
【0007】[0007]
【課題を解決するための手段】本発明は、金銀合金を陽
極としヨウ化物電解液中で電解することにより金銀合金
を再び陰極上に析出させて微細な粒子に加工する工程と
得られた陰極析出物を酸化性を有する酸で処理して金と
銀を分離する工程とからなることを特徴とする貴金属の
分離方法である。According to the present invention, there is provided a step of depositing a gold-silver alloy on a cathode again by electrolyzing in a iodide electrolytic solution using a gold-silver alloy as an anode to process fine particles. A method for separating a noble metal, which comprises a step of treating a precipitate with an acid having an oxidizing property to separate gold and silver.
【0008】[0008]
【作用】本発明方法では、まず金銀合金はヨウ化物電解
液中で電解することにより微細な粒子に加工される。金
銀合金の金品位は、25〜95%の範囲が好ましい。なぜな
らば、25%未満の場合は、前述の硝酸分金法と差がな
く、95%を超える場合にはウォールウィル法による処理
が可能であるからである。しかし本発明方法が適用でき
ないわけではない。また、金銀合金の使用は多岐にわた
るため、金銀のほかに、有価な白金やパラジウムなどが
含まれている場合も多く、これらの材料についても本発
明方法は適用できる。電解液として沃素化合物を用いる
のは、粒子が微細に加工できることと毒性がほとんど無
いことである。沃素化合物としては、ヨウ化カリウムも
しくはヨウ化ナトリウムを使用するのが好ましい。電解
液は、沃素化合物濃度50〜 500g/l、水素イオン濃度
4〜13.0の間に調整する。In the method of the present invention, the gold-silver alloy is first processed into fine particles by electrolysis in the iodide electrolytic solution. The gold grade of the gold-silver alloy is preferably in the range of 25 to 95%. The reason is that if it is less than 25%, there is no difference from the above-mentioned nitric acid fractionation method, and if it exceeds 95%, it can be treated by the Wall Will method. However, the method of the present invention is not inapplicable. In addition, since gold and silver alloys are used in a wide variety of cases, valuable platinum and palladium are often contained in addition to gold and silver, and the method of the present invention can be applied to these materials. The use of an iodine compound as the electrolytic solution means that the particles can be finely processed and that they have almost no toxicity. It is preferable to use potassium iodide or sodium iodide as the iodine compound. The electrolytic solution is adjusted to have an iodine compound concentration of 50 to 500 g / l and a hydrogen ion concentration of 4 to 13.0.
【0009】金銀合金を陽極とするには、二つの方法が
ある。一つは、金銀合金を極板として直接通電する方法
であり、もう一つは、白金めっきしたチタニウム板など
の不溶性電極を極板としてその上に金銀合金を載置など
して接触させて間接的に陽極とする方法である。陰極板
は、ステンレス鋼板などがこのましく、電解液に腐食さ
れにくい材質のものであればよく、前述の不溶性電極で
もよい。電気分解条件としては、概ね2〜10A/dm2 の
電流密度で、常温から70℃ぐらいの範囲で電解を行う。
電気分解により、金銀合金は粒子として陰極に析出して
くるが、金の品位が低くなるに従って茶褐色から除々に
黒くなる、金銀の他に白金やパラジウムなどの貴金属、
銅などの卑金属が陰極に析出してくる。電解液としてシ
アン化カリウムを使用した場合との差は、粒子の状態の
差と白金やパラジウムなどの電析の差である。シアン化
カリウム電解液での、電析粒子は沃素化合物電解液に比
べてやや大きく、析出する金属もデンドライト的析出状
態を示す、しかし沃素化合物電解液での電析粒子は非常
に微細な不定形の析出状態を示している。この差が、つ
ぎなる酸溶解において溶け易さの違いになると言える。
また、シアン化カリウム電解液では、白金とパラジウム
はほとんど析出してこないで電解液中に残ってしまう
が、沃素電解液では、白金とパラジウムも析出してくる
違いがある。シアン化カリウム電解液中からの白金とパ
ラジウムの回収は、非常に難しく金属白金や金属パラジ
ウムとして回収するのが困難であるので、沃素電解液に
よる方法で加工し別の方法で回収したほうがより容易で
ある。つぎなる工程では、陰極析出物は酸化性を有する
酸で処理して金と銀を分離される。この陰極析出物は、
微細な金銀粉でありパラジウムや白金が含まれている。There are two methods for using the gold-silver alloy as the anode. One is a method of directly energizing a gold-silver alloy as an electrode plate, and the other is an indirect electrode by placing an insoluble electrode such as a platinum-plated titanium plate as an electrode plate and placing a gold-silver alloy on it. This is a method of making the anode positive. The cathode plate is preferably made of a stainless steel plate or the like, and may be made of a material that is not easily corroded by the electrolytic solution, and may be the insoluble electrode described above. As electrolysis conditions, a current density of approximately 2 to 10 A / dm 2 and electrolysis at room temperature to about 70 ° C. are performed.
By electrolysis, gold-silver alloys are deposited on the cathode as particles, but as the quality of gold decreases, it gradually turns dark brown to black.In addition to gold and silver, precious metals such as platinum and palladium,
Base metal such as copper is deposited on the cathode. The difference from the case of using potassium cyanide as the electrolytic solution is the difference in the state of particles and the difference in the electrodeposition of platinum, palladium and the like. Electrodeposited particles in the potassium cyanide electrolytic solution are slightly larger than those in the iodine compound electrolytic solution, and the deposited metal shows a dendrite-like deposition state, but the electrodeposited particles in the iodine compound electrolytic solution are extremely fine and amorphous. It shows the state. It can be said that this difference is the difference in the solubility in the next acid dissolution.
Further, in the potassium cyanide electrolytic solution, platinum and palladium are hardly deposited and remain in the electrolytic solution, but in the iodine electrolytic solution, platinum and palladium are also deposited. Recovery of platinum and palladium from potassium cyanide electrolyte is very difficult and difficult to recover as metallic platinum or metal palladium, so it is easier to process by iodine electrolyte and recover by another method. . In the next step, the cathode deposit is treated with an oxidizing acid to separate gold and silver. This cathode deposit is
It is a fine gold-silver powder that contains palladium and platinum.
【0010】処理には、二法あり、ひとつは硝酸で処理
を行い銀を抽出して金を残物として得る方法で、金の品
位が低く銀の品位が高い場合に好ましい方法である。も
う一つの方法は、金を王水、塩酸への塩素吹き込み、硫
酸−食塩−硝酸などのように、金を溶かすことのできる
酸で金を溶解し、銀は塩化銀として残物とする方法で、
金の品位が高く、銀の品位が低い場合に好ましい方法で
ある。There are two methods of treatment, one is a method of treating with nitric acid to extract silver to obtain gold as a residue, which is a preferable method when the grade of gold is low and the grade of silver is high. Another method is to blow gold with aqua regia, chlorine blown into hydrochloric acid, sulfuric acid-salt-nitric acid, etc. to dissolve gold with an acid capable of dissolving gold and leave silver as silver chloride as a residue. so,
This is a preferable method when the quality of gold is high and the quality of silver is low.
【0011】硝酸による方法では、おおむね5規定から
15規定程度の濃度の硝酸で処理をおこなう。陰極析出
物は、微細に加工されているため通常であれば溶解しに
くい金銀合金中の銀は、容易に溶解して硝酸銀溶液とし
て得られる。残物の金は、95%以上の純度まで濃縮され
ウォールウィル法等により精製することができる。また
銀は、食塩を加えて塩化銀とし、苛性ソーダとホウ砂を
加えてるつぼ中で強熱し、金属銀とし、メービウス法な
どにより精製する。白金とパラジウムが含まれる場合に
は、白金とパラジウムの大部分は、硝酸抽出液中に抽出
されるから、塩化銀を得たのちの液は、中和し、さらに
水素化ホウ素ナトリウムなどの還元剤により金属白金、
金属パラジウムとして容易に回収することができる。硝
酸を用いる方法の特徴は、金の品位が低く銀の品位が高
い場合により効果的であるので、金品位が80%を下廻る
場合にも95〜98%位の金を得ることができ、かつ銀の抽
出比率が高くなるからである。しかし、金の品位を98%
以上にするには、複数回の抽出を行う必要がある。In the method using nitric acid, the treatment is performed with nitric acid having a concentration of about 5 to 15 N. Since the cathode precipitate is finely processed, silver in the gold-silver alloy, which is usually difficult to dissolve, is easily dissolved to obtain a silver nitrate solution. The remaining gold can be purified to a purity of 95% or higher by the Wallwil method or the like. Also, silver is made into silver chloride by adding salt, ignited in a crucible containing caustic soda and borax, made into metallic silver, and purified by the Mobius method or the like. When platinum and palladium are contained, most of platinum and palladium are extracted in the nitric acid extract, so the solution after obtaining silver chloride is neutralized and further reduced with sodium borohydride or the like. Depending on the agent, metallic platinum,
It can be easily recovered as metallic palladium. The characteristic of the method using nitric acid is that it is more effective when the grade of gold is low and the grade of silver is high, so even when the grade of gold is below 80%, it is possible to obtain 95 to 98% of gold, Moreover, the extraction ratio of silver becomes high. However, gold grade 98%
To do so, it is necessary to perform extraction multiple times.
【0012】金を溶かすことのできる酸で溶解する方法
では、王水による方法がもっとも簡便であるので王水を
用いた際の作用に基づいて説明する。この作用は、塩酸
に塩素を吹き込んだ場合や、硫酸−食塩−硝酸などその
他の金を溶かすことができる酸でもほぼ同じである。金
銀合金中の金は通常であれば溶解しにくいが、この方法
で得られた陰極析出物は、微細に加工されているため容
易に王水中に溶解する。残物には、塩化銀が得られ金と
銀を分離することがでる。王水中の金は、二塩酸ヒドラ
ジン、シュウ酸などの還元剤により金属金となり、また
塩化銀も苛性ソーダとホウ砂を加えてるつぼ中で強熱し
金属銀となる。白金とパラジウムが含まれる場合には、
白金とパラジウムは王水液中に抽出されるから、金を得
たのちの液は、中和しさらに水素化ホウ素ナトリウムな
どの還元剤により金属白金、金属パラジウムとして容易
に回収することができる。王水を用いる方法の特徴は、
金の品位が高く銀の品位が低い場合により効果的で、特
に金品位が70%を上廻る場合に好ましい。それは、王水
溶解の際に発生する塩化銀量が少なければろ過が容易で
あり、より短い時間で処理できるという理由による。Of the methods of dissolving gold with an acid capable of dissolving gold, the method using aqua regia is the simplest, so the explanation will be based on the action when aqua regia is used. This action is almost the same when chlorine is blown into hydrochloric acid, or when an acid capable of dissolving gold such as sulfuric acid-salt-nitric acid is dissolved. Gold in the gold-silver alloy is usually difficult to dissolve, but the cathode precipitate obtained by this method is easily processed in aqua regia because it is finely processed. In the residue, silver chloride is obtained and gold and silver can be separated. Gold in aqua regia is made into metallic gold by a reducing agent such as hydrazine dihydrochloride and oxalic acid, and silver chloride is also ignited in a crucible containing caustic soda and borax to become metallic silver. If platinum and palladium are included,
Since platinum and palladium are extracted into the aqua regia solution, the solution after obtaining gold can be neutralized and further easily recovered as metallic platinum or metallic palladium with a reducing agent such as sodium borohydride. The characteristics of the method using aqua regia are:
It is more effective when the gold grade is high and the silver grade is low, and is particularly preferable when the gold grade exceeds 70%. The reason is that if the amount of silver chloride generated during aqua regia dissolution is small, the filtration is easy and the treatment can be performed in a shorter time.
【0013】本発明方法を実施した場合、金銀合金の品
位調整が不用となり、品位調整に加えた金属を溶かす必
要が無くなるので、その分の薬品量が少なくなり、また
窒素酸化物の発生量も低減される。例えば、金75%、銀
25%の18金合金を1kg処理した場合、従来の硝酸分金法
では、2kgの銅を加えて金25%、銀 8.3%、銅66.7%の
金銀銅合金3kgに調整した後硝酸で処理をおこなうが、
本発明方法では、1kgを処理すれば良いからである。ま
た、沃素化合物電解液は、再利用することができるの
で、操業に伴う僅かな減少分を補えば良いという特徴が
ある。さらに、金銀の分離能が高く、次なる金の精製、
銀の精製設備へ供給が可能な原料を作り出すことが可能
であるという特徴がある。以下、本発明の実施について
示す。When the method of the present invention is carried out, it is not necessary to adjust the quality of the gold-silver alloy, and it is not necessary to dissolve the metal added for the quality adjustment, so the amount of chemicals is reduced and the amount of nitrogen oxides generated is also reduced. Will be reduced. For example, 75% gold, silver
When 1 kg of 25% 18-gold alloy is treated, in the conventional nitric acid dispensing method, 2 kg of copper is added to adjust to 3 kg of gold-silver-copper alloy of 25% gold, 8.3% silver and 66.7% copper, and then treated with nitric acid. I will do it,
This is because the method of the present invention only needs to process 1 kg. Further, since the iodine compound electrolyte can be reused, there is a feature that it is sufficient to compensate for a slight decrease due to the operation. Furthermore, the separation ability of gold and silver is high, and the next gold purification,
It has the feature that it can produce raw materials that can be supplied to silver refining equipment. Hereinafter, the implementation of the present invention will be described.
【0014】[0014]
【実施例1】金74.8%、銀25.0%を含む金銀合金 1.0kg
を幅5cm、長さ10cmの板状に加工したものを陽極とし、
陰極には同寸のステンレス鋼板(JISSUS304
品)を用い、ヨウ化カリウム200g/lを含む電解液中
で、8Aの直流電流を印加して電解をおこなった。電解
開始後始めの、30分間は陰極より水素発生がみられた
が、電解液色が透明から黒褐色になるに従い水素発生が
おさまり陰極上に黒褐色の電析物が析出し始めた。得ら
れた電析物は、微細な粒子よりなり分析の結果、水分31
%、金51.2%、銀16.5%の組成であり、金銀合金である
陽極が電解により溶解し、再び陰極に析出したにほかな
らないものである。得られた陰極析出物を乾燥の後、 1
00gをとり、純水 100mlと塩酸 150mlを加えてビーカー
中で加熱しさらに硝酸40mlを滴下して王水溶解をおこな
い、王水溶解後約 500mlにまで希釈し、ろ別により沈殿
物(塩化銀)と液(金溶液)に分離した。液中には、金
74.2g、銀0.05gが含まれ、沈殿物には銀23.7gと金0.
02gが含まれていた。液中の金は、二塩酸ヒドラジンに
より還元したところ品位99.8%の金属金が得られ、また
沈殿物中の銀はるつぼ中で苛性ソーダとホウ砂を加えて
強加熱して品位99.5%の金属銀を得ることができた。以
上の操作により金銀合金を金と銀に分離することができ
た。Example 1 1.0 kg of gold-silver alloy containing 74.8% gold and 25.0% silver
A plate with a width of 5 cm and a length of 10 cm was used as the anode,
For the cathode, stainless steel plate of the same size (JISSUS304
Electrolysis was performed by applying a direct current of 8 A in an electrolytic solution containing 200 g / l of potassium iodide. Hydrogen generation was observed from the cathode for the first 30 minutes after the start of electrolysis, but as the color of the electrolyte changed from transparent to black brown, hydrogen generation subsided and a black brown electrodeposit started to deposit on the cathode. The obtained electrodeposit was composed of fine particles, and as a result of analysis, water content 31
%, Gold 51.2%, silver 16.5%, and the anode, which is a gold-silver alloy, was dissolved by electrolysis and deposited again on the cathode. After drying the obtained cathode deposit, 1
Take 00 g, add 100 ml of pure water and 150 ml of hydrochloric acid, heat in a beaker, add 40 ml of nitric acid to dissolve aqua regia, dissolve in aqua regia, dilute to about 500 ml, and precipitate by filtration (silver chloride). ) And liquid (gold solution). Gold in the liquid
It contains 74.2g and 0.05g silver, and the precipitate contains 23.7g silver and 0.
It contained 02g. The gold in the liquid was reduced with hydrazine dihydrochloride to obtain 99.8% metallic gold, and the silver in the precipitate was caustic soda and borax in a crucible and heated strongly to give 99.5% metallic silver. I was able to get By the above operation, the gold-silver alloy could be separated into gold and silver.
【0015】[0015]
【従来例1】金74.8%、銀25.0%を含む金銀合金 100g
と銅 300gを坩堝中で溶解し金の品位を4分の1(約19
%)に下げた合金を得た、硝酸に溶かしやすくするため
にこれを圧延機で薄板(厚さ約 0.5mm)に加工しさらに
金切り鋏で数cm角の小片にした。ビーカー中にこの小片
をいれ純水 200mlを入れて加熱しながら硝酸 400mlを少
しずつ滴下しながら溶解した。硝酸溶解終了後、濾別に
より残物と液に分離したところ、液中には、銀23.5gが
含まれ、残物には銀 1.4gと金74.3gが含まれていた。
銀を含む液は、食塩を加えて塩化銀として析出させた。
ついで塩化銀は坩堝中で苛性ソーダとホウ砂を加えて強
加熱して品位99.8%の金属銀とすることができた。残物
も坩堝中で溶解後、分析したところ金の品位は96.2%で
あり、銀の他に銅が多く含まれていた。[Prior art example 1] 100g of gold-silver alloy containing 74.8% gold and 25.0% silver
And 300 g of copper are melted in a crucible to reduce the quality of gold to 1/4 (about 19
%) To obtain a thin alloy (thickness: about 0.5 mm) using a rolling machine to make it easy to dissolve in nitric acid. This small piece was put in a beaker, 200 ml of pure water was added, and 400 ml of nitric acid was gradually added dropwise while heating and dissolved. After the dissolution of nitric acid, the residue and the liquid were separated by filtration. The liquid contained 23.5 g of silver, and the residue contained 1.4 g of silver and 74.3 g of gold.
The liquid containing silver was added as salt to precipitate as silver chloride.
Then, silver chloride could be made into 99.8% metallic silver by adding caustic soda and borax in a crucible and heating it strongly. When the residue was also dissolved in the crucible and analyzed, the quality of gold was 96.2%, which contained a large amount of copper in addition to silver.
【0016】[0016]
【従来例2】金74.8%、銀25.0%を含む金銀合金 100g
を圧延機で薄板(厚さ約1mm)に加工しさらに金切り鋏
で数cm角の小片にした。ビーカー中にこの小片をいれ純
水 100mlと塩酸 150mlを加えてビーカー中で加熱しさら
に硝酸40mlを滴下して王水溶解をおこなったが、金属表
面に白色の皮が被ったようになり溶解することはできな
かった。[Prior art example 2] 100g of gold-silver alloy containing 74.8% gold and 25.0% silver
Was processed into a thin plate (thickness: about 1 mm) with a rolling mill, and further cut into small pieces of several cm square with scissors. Put this small piece in a beaker, add 100 ml of pure water and 150 ml of hydrochloric acid, heat in a beaker and add 40 ml of nitric acid to dissolve aqua regia, but the metal surface appears to be covered with white skin and dissolves. I couldn't do that.
【0017】[0017]
【従来例3】金74.8%、銀25.0%を含む金銀合金 100g
を圧延機で薄板(厚さ約1mm)に加工しさらに金切り鋏
で数cm角の小片にした。ビーカー中にこの小片をいれ純
水 100mlと硝酸 150mlを加えてビーカー中で加熱し硝酸
溶解をおこなったが、金属光沢がすこし光沢を失った
が、その他は変化はみられず溶解することはできなかっ
た。同じ重量の金銀合金を処理するために実施例1で
は、 100gの金属を処理すればよいが、実施例2では、
約4倍の金属を溶解しなければならない。また薬品の使
用量、窒素酸化物の発生、廃液の発生量もそれに伴い数
倍になってしまう。さらに、本発明方法のほうがより高
品位の金を得ることができた。[Prior art example 3] 100g of gold-silver alloy containing 74.8% gold and 25.0% silver
Was processed into a thin plate (thickness: about 1 mm) with a rolling mill, and further cut into small pieces of several cm square with scissors. The small pieces were placed in a beaker, 100 ml of pure water and 150 ml of nitric acid were added, and the mixture was heated in a beaker to dissolve nitric acid.The metallic luster slightly lost its luster, but the others did not change and could not be dissolved. There wasn't. To treat the same weight of gold-silver alloy in Example 1, 100 g of metal may be treated, but in Example 2,
About four times as much metal must be dissolved. Also, the amount of chemicals used, the amount of nitrogen oxides generated, and the amount of waste liquid generated will increase several times. Furthermore, the method of the present invention was able to obtain higher quality gold.
【0018】[0018]
【実施例2】金50.3%、銀41.0%、パラジウム 5.5%、
白金 1.0%を含む金銀合金 1.0kgを幅5cm、長さ10cmの
板状に加工したものを陽極とし、陰極には同寸のステン
レス鋼板(JISSUS304品)を用い、ヨウ化カリ
ウム 500g/lを含む電解液中で、8Aの直流電流を印
加して電解をおこなった。電解開始後始めの、30分間は
陰極より水素発生がみられたが、電解液色が透明から黒
褐色になるに従い水素発生がおさまり陰極上に黒褐色の
電析物が析出し始めた。得られた電析物は、微細な粒子
よりなり分析の結果、水分28%、金32.2%、銀29.5%、
パラジウム 3.0%、白金 0.6%の組成であり、金銀合金
である陽極が電解により溶解し、再び陰極に析出したに
ほかならないものである。得られた陰極析出物を乾燥の
後、 100gをとり、純水 100mlと塩酸 250mlを加えてビ
ーカー中で加熱しさらに硝酸40mlを滴下して王水溶解を
おこない、王水溶解後約 500mlにまで希釈し、濾別によ
り、沈殿物(塩化銀)と液に分離した。濾別の際には、
沈殿物量がややおおく濾過がやや困難であった。液中に
は、金49.5g、銀0.10g、パラジウム 5.4g、白金 1.2
gが含まれ、沈殿物には銀39.5gと金0.95gが含まれて
いた。液中の金は、二塩酸ヒドラジンにより還元析出
後、濾別分離して品位99.8%の金属金をえることができ
た。濾液は中和処理し水素化ホウ素ナトリウム5%溶液
を作用させてさらに還元して白金とパラジウムを析出さ
せた。また沈殿物中の銀は坩堝中で苛性ソーダとホウ砂
を加えて強加熱して品位97.0%の金属銀を得ることがで
きた。以上の操作により金銀合金を金と銀に分離するこ
とができた。Example 2 Gold 50.3%, Silver 41.0%, Palladium 5.5%,
A 1.0 kg gold-silver alloy containing 1.0% platinum was processed into a plate with a width of 5 cm and a length of 10 cm, which was used as the anode. A stainless steel plate of the same size (JISSUS304) was used as the cathode, containing 500 g / l of potassium iodide. Electrolysis was performed by applying a direct current of 8 A in the electrolytic solution. Hydrogen generation was observed from the cathode for 30 minutes after the start of electrolysis, but as the electrolyte color changed from transparent to black-brown, hydrogen generation subsided and a black-brown electrodeposit began to deposit on the cathode. The obtained electrodeposit was composed of fine particles, and as a result of analysis, moisture was 28%, gold was 32.2%, silver was 29.5%,
It has a composition of 3.0% palladium and 0.6% platinum, and the anode, which is a gold-silver alloy, is dissolved by electrolysis and deposited again on the cathode. After drying the obtained cathode deposit, 100 g of it is taken, 100 ml of pure water and 250 ml of hydrochloric acid are added, heated in a beaker, and 40 ml of nitric acid is added dropwise to dissolve aqua regia. It was diluted and separated by filtration into a precipitate (silver chloride) and a liquid. When filtering,
Filtration was a little difficult and filtration was a little difficult. In the liquid, gold 49.5g, silver 0.10g, palladium 5.4g, platinum 1.2
g, and the precipitate contained 39.5 g of silver and 0.95 g of gold. The gold in the liquid was reduced and precipitated with hydrazine dihydrochloride and then separated by filtration to obtain 99.8% metallic gold. The filtrate was neutralized and treated with a 5% sodium borohydride solution to further reduce the platinum and palladium. The silver in the precipitate was caustic soda and borax in a crucible and heated strongly to obtain 97.0% metallic silver. By the above operation, the gold-silver alloy could be separated into gold and silver.
【0019】[0019]
【実施例3】金81.0%、銀17.0%、パラジウム 1.5%、
白金 0.3%を含む金銀合金 1.0kgを幅5cm、長さ10cmの
板状に加工したものを陽極とし、陰極には同寸のステン
レス鋼板(JISSUS304品)を用い、ヨウ化カリ
ウム 150g/lを含む電解液中で、8Aの直流電流を印
加して電解をおこない、金77.9%、銀16.8%、パラジウ
ム1.49%、白金0.26%の陰極析出物を得た。この陰極析
出物 500gを蒸発皿にとり、硝酸 250mlと純水 250mlを
加えて、銀、白金、パラジウムを加熱抽出した。この操
作を2回繰り返したところ、陰極析出物中に含まれてい
た金以外の貴金属のうち、銀、白金、パラジウムが抽出
された。また硝酸抽出後の残物中には、金97.4%、銀2.
04%、白金0.05%、パラジウムが0.38%含まれており、
金以外の不純物の90%が除かれ、金の品位が95%以上あ
るため、ウォールウィル法により十分精製可能な純度の
ものであった。実施例3においては、本発明方法によ
り、従来硝酸抽出が難しかった品位のものでも、本発明
方法により硝酸抽出操作が可能になることを示してい
る。Example 3 Gold 81.0%, Silver 17.0%, Palladium 1.5%,
A 1.0 kg gold-silver alloy containing 0.3% platinum was processed into a plate shape with a width of 5 cm and a length of 10 cm, which was used as the anode. A stainless steel plate of the same size (JISSUS304) was used as the cathode, containing 150 g / l of potassium iodide. Electrolysis was carried out by applying a direct current of 8 A in the electrolytic solution to obtain a cathode deposit of 77.9% gold, 16.8% silver, 1.49% palladium, and 0.26% platinum. 500 g of this cathode precipitate was placed in an evaporation dish, 250 ml of nitric acid and 250 ml of pure water were added, and silver, platinum and palladium were extracted by heating. When this operation was repeated twice, silver, platinum, and palladium were extracted from the noble metals other than gold contained in the cathode deposit. In the residue after nitric acid extraction, gold 97.4%, silver 2.
04%, platinum 0.05%, palladium 0.38%,
90% of impurities other than gold were removed, and the quality of gold was 95% or more, so the purity was sufficient for purification by the Wall-Will method. Example 3 shows that the method of the present invention enables the nitric acid extraction operation to be performed by the method of the present invention even if the quality of the nitric acid was conventionally difficult to extract.
【0020】[0020]
【実施例4】実施例3と同様にして金81.0%、銀17.0
%、パラジウム 1.5%、白金 0.3%を含む金銀合金 1.0
kgを幅5cm、長さ10cmの板状に加工したものを陽極と
し、陰極には同寸のステンレス鋼板(JISSUS30
4品)を用い、ヨウ化カリウム150g/lを含む電解溶
液中で、8Aの直流電流を印加して電解をおこない、金
77.9%、銀16.8%、パラジウム1.49%、白金0.26%の陰
極析出物を得た。この陰極析出物50gを蒸発皿にとり、
塩酸 100mlと純水50mlを加えて、さらに加熱しつつ硝酸
を25ml滴下して王水溶解をおこなった。銀を除く金属成
分は、王水液中に抽出されて、分析をしたところ金38.9
g、白金0.11g、パラジウム0.81gが含まれていた。こ
の液を、二塩酸ヒドラジンで還元して金粉を得たのち、
中和してさらに水素化ホウ素ナトリウム溶液で還元して
白金とパラジウムの混合粉末を得た。王水溶解の際の残
物の殆んどは塩化銀であり、シアン化カリウム溶液中に
溶かして電気分解により金属銀 8.5gを得ることができ
た。Example 4 Similar to Example 3, 81.0% gold, 17.0 silver
%, Palladium 1.5%, platinum 0.3%, gold-silver alloy 1.0
A plate processed to have a width of 5 cm and a length of 10 cm was used as an anode, and the cathode was made of a stainless steel plate of the same size (JISSUS30).
4 products) in an electrolytic solution containing 150 g / l potassium iodide and applying a direct current of 8 A to electrolyze,
A cathode deposit containing 77.9%, silver 16.8%, palladium 1.49%, and platinum 0.26% was obtained. 50 g of this cathode deposit is placed in an evaporation dish,
100 ml of hydrochloric acid and 50 ml of pure water were added, and 25 ml of nitric acid was added dropwise with further heating to dissolve aqua regia. Metal components except silver were extracted into aqua regia and analyzed to find that gold 38.9
g, 0.11 g of platinum, and 0.81 g of palladium. After reducing this solution with hydrazine dihydrochloride to obtain gold powder,
The mixture was neutralized and further reduced with a sodium borohydride solution to obtain a mixed powder of platinum and palladium. Most of the residue when the aqua regia was dissolved was silver chloride, and 8.5 g of metallic silver could be obtained by electrolysis after dissolving in a potassium cyanide solution.
【0021】[0021]
【比較例1】金81.0%、銀17.0%、パラジウム 1.5%、
白金 0.3%を含む金銀合金 1.0kgを幅5cm、長さ10cmの
板状に加工したものを陽極とし、陰極には同寸のステン
レス鋼板(JISSUS304品)を用い、シアン化カ
リウム 150g/lを含む電解液中で、8Aの直流電流を
印加して電解をおこない、金79.5%、銀18.8%、パラジ
ウム0.02%、白金0.01%の陰極析出物を得た。この陰極
析出物50gを蒸発皿にとり、塩酸 100mlと純水50mlを加
えて、さらに加熱しつつ硝酸を25ml滴下して王水溶解を
おこなった。銀を除く金属成分は、王水液中に抽出され
て、分析をしたところ金35.2gが含まれていたが、白金
とパラジウムは殆んど含まれていなかった。また王水溶
解に際して、有毒なシアン化水素ガスが発生した。この
液からは二塩酸ヒドラジンで還元して金粉を得ることが
できた。王水溶解の際の残物の殆んどは塩化銀であるの
で、シアン化カリウム溶液中に溶かしたところ、シアン
化カリウム溶液に溶けないものが 1.3g含まれていた。
この不溶物を分析したところ、金と銀が検出された。塩
化銀を溶かしたシアン化カリウム溶液からは、容易に金
属銀を回収することができた。パラジウムと白金は、前
述のシアン化カリウムを含む電解液中に蓄積されるが、
陰極には析出してこないため、陽極を白金めったしたチ
タニウム板に切り換えて電気分解をおこなったが、長い
時間をかけても析出してこなかった。Comparative Example 1 Gold 81.0%, Silver 17.0%, Palladium 1.5%,
A 1.0 kg gold-silver alloy containing 0.3% platinum was processed into a plate with a width of 5 cm and a length of 10 cm, which was used as the anode. A stainless steel plate of the same size (JISSUS304) was used as the cathode, and an electrolytic solution containing 150 g / l of potassium cyanide. Then, a direct current of 8 A was applied to carry out electrolysis to obtain a cathode deposit of 79.5% gold, 18.8% silver, 0.02% palladium, and 0.01% platinum. 50 g of this cathode precipitate was placed in an evaporation dish, 100 ml of hydrochloric acid and 50 ml of pure water were added, and 25 ml of nitric acid was added dropwise while heating to dissolve aqua regia. Metal components other than silver were extracted into aqua regia and analyzed, and as a result, 35.2 g of gold was contained, but platinum and palladium were hardly contained. Also, toxic hydrogen cyanide gas was generated when the aqua regia was dissolved. Gold powder could be obtained from this solution by reduction with hydrazine dihydrochloride. Almost all of the residue when dissolved in aqua regia was silver chloride, so when dissolved in a potassium cyanide solution, 1.3 g of what was insoluble in the potassium cyanide solution was contained.
When this insoluble material was analyzed, gold and silver were detected. The metallic silver could be easily recovered from the potassium cyanide solution in which silver chloride was dissolved. Palladium and platinum are accumulated in the electrolytic solution containing potassium cyanide described above,
Since it did not deposit on the cathode, the anode was switched to a platinum-plated titanium plate for electrolysis, but it did not deposit even after a long time.
【0022】[0022]
【比較例2】金50.3%、銀41.0%、パラジウム 5.5%、
白金 1.0%を含む金銀合金 1.0kgを幅5cm、長さ10cmの
板状に加工したものを陽極とし、陰極には同寸のステン
レス鋼板(JISSUS304品)を用い、シアン化カ
リウム 150g/lを含む電解液中で、8Aの直流電流を
印加して電解をおこない、金53.1%、銀45.5%、パラジ
ウム0.01%、白金0.01%の陰極析出物を得た。この陰極
析出物50gを蒸発皿にとり、塩酸 100mlと純水50mlを加
えて、さらに加熱しつつ硝酸を25ml滴下して王水溶解を
おこなった。銀を除く金属成分は、王水液中に抽出され
て、分析をしたところ金16.4gが含まれていたが、白金
とパラジウムは殆んど含まれていなかった。また王水溶
解に際して、有毒なシアン化水素ガスが発生した。この
液からは二塩酸ヒドラジンで還元して金粉を得ることが
できた。王水溶解の際の残物を、シアン化カリウム溶液
中に溶かしたところ、シアン化カリウム溶液に溶けない
ものが13.5g含まれていた。この不溶物を分析したとこ
ろ、金が62.3%、銀が36.9%含まれていた。パラジウム
と白金は、前述のシアン化カリウムを含む電解液中に蓄
積されるが、陰極には析出してこなかったため、陽極を
白金めっきしたチタニウム板に切り換えて電気分解をお
こなったが、長い時間をかけても析出してこなかった。[Comparative Example 2] 50.3% gold, 41.0% silver, 5.5% palladium,
A 1.0 kg gold-silver alloy containing 1.0% platinum was processed into a plate with a width of 5 cm and a length of 10 cm, which was used as the anode. A stainless steel plate of the same size (JISSUS304) was used as the cathode, and an electrolyte containing potassium cyanide 150 g / l. Then, electrolysis was performed by applying a direct current of 8 A to obtain a cathode deposit of 53.1% gold, 45.5% silver, 0.01% palladium, and 0.01% platinum. 50 g of this cathode precipitate was placed in an evaporation dish, 100 ml of hydrochloric acid and 50 ml of pure water were added, and 25 ml of nitric acid was added dropwise while heating to dissolve aqua regia. Metal components other than silver were extracted into aqua regia and analyzed to find that 16.4 g of gold was contained, but platinum and palladium were scarcely contained. Also, toxic hydrogen cyanide gas was generated when the aqua regia was dissolved. Gold powder could be obtained from this solution by reduction with hydrazine dihydrochloride. When the residue obtained by dissolving aqua regia was dissolved in a potassium cyanide solution, 13.5 g of a substance that was insoluble in the potassium cyanide solution was contained. Analysis of this insoluble material revealed that it contained 62.3% gold and 36.9% silver. Palladium and platinum were accumulated in the above-mentioned electrolytic solution containing potassium cyanide, but because they did not deposit on the cathode, the anode was switched to a platinum-plated titanium plate for electrolysis, but it took a long time. Also did not precipitate.
【0023】比較例1および比較例2は、金銀合金を電
気分解する際の電解液にシアン化カリウムを用いている
が、次なる王水溶解の際に有害なシアン化水素が発生し
たり、また陰極析出物中の金を全て溶解することが難し
いことを示しており、特に金銀合金中の銀が増えるに従
って溶けにくくなることがわかる。また白金やパラジウ
ムの回収も実施例に比べて難しくなる。In Comparative Examples 1 and 2, potassium cyanide is used as an electrolytic solution for electrolyzing a gold-silver alloy, but harmful hydrogen cyanide is generated when the aqua regia is dissolved next time, and a cathode precipitate is also generated. It shows that it is difficult to dissolve all the gold in it, and in particular, it can be seen that it becomes difficult to dissolve as the amount of silver in the gold-silver alloy increases. Also, recovery of platinum and palladium becomes more difficult than in the examples.
【0024】[0024]
【実施例5】金50.3%、銀41.0%、パラジウム 5.5%、
白金 1.0%を含む金銀合金 1.0kgを幅5cm、長さ10cmの
板状に加工したものを陽極とし、陰極には同寸のステン
レス鋼板(JISSUS304品)を用い、ヨウ化カリ
ウム 500g/lを含む電解液中で、8Aの直流電流を印
加して電解をおこなった。電解開始後始めの、30分間は
陰極より水素発生がみられたが、電解液色が透明から黒
褐色になるに従い水素発生がおさまり陰極上に黒褐色の
電析物が析出し始めた。得られた電析物は、微細な粒子
よりなり分析の結果、水分28%、金35.0%、銀27.5%、
パラジウム 3.0%、白金 0.6%の組成であり、金銀合金
である陽極が電解により溶解し、再び陰極に析出したに
ほかならないものである。得られた陰極析出物を乾燥の
後、 100gをとり、純水 100mlと硝酸 250mlを加えてビ
ーカー中で加熱し硝酸抽出をおこなった後、濾別によ
り、沈殿物(金)と液に分離した。沈殿物である金を分
析したところ、品位は96.2%のものであった。金銀合金
中の金は、濃縮されウォールウィル法に直接投入可能な
品位のものであり、実質的に金と銀は分離された。Example 5 Gold 50.3%, Silver 41.0%, Palladium 5.5%,
A 1.0 kg gold-silver alloy containing 1.0% platinum was processed into a plate with a width of 5 cm and a length of 10 cm, which was used as the anode. A stainless steel plate (JISSUS304) of the same size was used as the cathode, containing 500 g / l of potassium iodide. Electrolysis was performed by applying a direct current of 8 A in the electrolytic solution. Hydrogen generation was observed from the cathode for the first 30 minutes after the start of electrolysis, but as the color of the electrolyte changed from transparent to black brown, hydrogen generation subsided and a black brown electrodeposit started to deposit on the cathode. The obtained electrodeposit was composed of fine particles, and as a result of analysis, water content was 28%, gold was 35.0%, silver was 27.5%,
It has a composition of 3.0% palladium and 0.6% platinum, and the anode, which is a gold-silver alloy, is dissolved by electrolysis and deposited again on the cathode. After drying the obtained cathode deposit, 100 g of it was taken, 100 ml of pure water and 250 ml of nitric acid were added, and the mixture was heated in a beaker to perform nitric acid extraction, and then separated by filtration to obtain a precipitate (gold) and a liquid. . Analysis of the gold deposit revealed that the quality was 96.2%. The gold in the gold-silver alloy was of a grade that could be concentrated and directly input into the Wallwil method, and the gold and silver were substantially separated.
【0025】[0025]
【発明の効果】本発明は、金銀合金の品位調整を不用と
し、かつ硝酸分金法に伴う窒素酸化物の発生、廃液処
理、薬品費など低減でき、容易に金銀合金を分離するこ
とができる。INDUSTRIAL APPLICABILITY The present invention makes it unnecessary to adjust the quality of a gold-silver alloy, and can reduce the generation of nitrogen oxides associated with the nitric acid dispensing method, waste liquid treatment, chemical costs, etc., and easily separate the gold-silver alloy. .
Claims (4)
て、前記金銀合金を陽極となし沃素化合物電解液中で電
気分解して陰極に析出させ微細な粒子に加工する工程と
前記陰極析出物を酸化性を有する酸で抽出して金と銀に
分離する工程とからなる金銀合金の分離方法。1. A method for separating a gold-silver alloy into gold and silver, a step of electrolyzing the gold-silver alloy in an iodine compound electrolyte solution serving as an anode and depositing it on a cathode to process it into fine particles, and the cathode deposit. A method for separating a gold-silver alloy, which comprises a step of extracting the slag with an acid having an oxidizing property to separate into gold and silver.
金銀合金が金品位80%以下であることを特徴とする請求
項1記載の金銀合金の分離方法。2. The method of separating a gold-silver alloy according to claim 1, wherein the oxidizing acid is nitric acid and the gold-silver alloy has a gold quality of 80% or less.
塩素吹き込み水、硫酸−食塩−硝酸のいずれかでかつ前
記金銀合金が金品位70%以上であることを特徴とする請
求項1記載の金銀合金の分離方法。3. The oxidative acid is any of aqua regia, chlorine-blown water into hydrochloric acid, and sulfuric acid-salt-nitric acid, and the gold-silver alloy has a gold grade of 70% or more. 1. The method for separating a gold-silver alloy according to 1.
していることを特徴とする請求項1記載の金銀合金の分
離方法。4. The method for separating a gold-silver alloy according to claim 1, wherein the gold-silver alloy contains platinum and palladium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3189333A JPH059606A (en) | 1991-07-03 | 1991-07-03 | Separation method of gold-silver alloy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3189333A JPH059606A (en) | 1991-07-03 | 1991-07-03 | Separation method of gold-silver alloy |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH059606A true JPH059606A (en) | 1993-01-19 |
Family
ID=16239590
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3189333A Pending JPH059606A (en) | 1991-07-03 | 1991-07-03 | Separation method of gold-silver alloy |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH059606A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110274598A1 (en) * | 2008-04-14 | 2011-11-10 | Akridge James R | Sustainable recovery of metal compounds |
| JP2017110301A (en) * | 2010-08-20 | 2017-06-22 | インテグリス・インコーポレーテッド | Sustainable process for reclaiming precious metal and base metal from waste of electric/electronic equipment |
-
1991
- 1991-07-03 JP JP3189333A patent/JPH059606A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110274598A1 (en) * | 2008-04-14 | 2011-11-10 | Akridge James R | Sustainable recovery of metal compounds |
| JP2017110301A (en) * | 2010-08-20 | 2017-06-22 | インテグリス・インコーポレーテッド | Sustainable process for reclaiming precious metal and base metal from waste of electric/electronic equipment |
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