JPH09263847A - Dissolving method of noble metal-containing slime - Google Patents

Dissolving method of noble metal-containing slime

Info

Publication number
JPH09263847A
JPH09263847A JP8076001A JP7600196A JPH09263847A JP H09263847 A JPH09263847 A JP H09263847A JP 8076001 A JP8076001 A JP 8076001A JP 7600196 A JP7600196 A JP 7600196A JP H09263847 A JPH09263847 A JP H09263847A
Authority
JP
Japan
Prior art keywords
slime
hydrogen peroxide
hydrochloric acid
amount
amt
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.)
Withdrawn
Application number
JP8076001A
Other languages
Japanese (ja)
Inventor
Satoshi Okada
智 岡田
Hiromi Mochida
裕美 持田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP8076001A priority Critical patent/JPH09263847A/en
Publication of JPH09263847A publication Critical patent/JPH09263847A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce the treatment time by introducing hydrogen peroxide to a slime containing Au, Pt and Pd in the presence of hydrochloric acid. SOLUTION: By this method, Au, Pt and Pd in a slime are oxidized by hydrogen peroxide and the oxides react with chlorine to produce a chloride complex which can be dissolved. In this method, hydrochloric acid and hydrogen peroxide are required to be present with the noble metals. It is preferable to add the hydrochloric acid in an amt. equal or larger than the required amt. (equiv.) to convent noble metals into chloride complex ion and smaller than twice of the required amt. It is preferable to add hydrogen peroxide in an amt. twice or more as the amt. required to oxidize Au into Au (III), Pt into Pt (IV) and Pd into Pd (IV) and less than four times of the required amt. Thereby, dissolution treatment can be done in several hours, which is shorter compared to a conventional treatment using aqua regia, and since the obtd. soln. is based on hydrochloric acid soln., it can be easily treated in the succeeding process.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、金、白金およびパラジ
ムの白金族元素を含有するスライム(以下、貴金属スラ
イムと云う)の溶解方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for dissolving slime (hereinafter referred to as precious metal slime) containing a platinum group element of gold, platinum and paradium.

【0002】[0002]

【従来の技術】銅やニッケルの精練工程で生じる陽極ス
ライムあるいはニッケルの精練工程で生じる抽出残渣に
は、金、銀、白金、パラジウムおよびその他の貴金属元
素がかなりの量含まれており、これらの貴金属は、銅や
セレンおよびテルル等の親銅元素を回収する諸工程を経
ることにより貴金属濃度が高められ、粗銀として回収さ
れる。
2. Description of the Related Art Anode slime produced in the refining process of copper or nickel or the extraction residue produced in the refining process of nickel contains a considerable amount of gold, silver, platinum, palladium and other precious metal elements. The noble metal is recovered as crude silver by increasing the noble metal concentration through various steps of recovering copper-philic elements such as copper and selenium and tellurium.

【0003】図1に示すように、回収された粗銀は電解
処理され析出銀と陽極スライム(銀スライム)が得られ
る。銀スライムは主として銀と金とを含み、さらに白金
族元素を含有している。銀スライムはまず硝酸により処
理される。これによって金以外の金属が液中に溶解す
る。金は遠心分離等により分離回収される。溶液中には
さらに塩酸が添加され銀の大部分は塩化銀として除かれ
る。残った溶液にヒドラジンのような還元剤を添加する
と、金属成分が微粒子として析出した還元スライムが得
られる。この還元スライム(貴金属スライム)は白金お
よびパラジウムに加え少量の金と銀を含んでいる。
As shown in FIG. 1, the recovered crude silver is subjected to electrolytic treatment to obtain deposited silver and anode slime (silver slime). Silver slime mainly contains silver and gold, and further contains a platinum group element. Silver slime is first treated with nitric acid. This causes metals other than gold to dissolve in the liquid. Gold is separated and collected by centrifugation or the like. Hydrochloric acid is added to the solution to remove most of silver as silver chloride. When a reducing agent such as hydrazine is added to the remaining solution, reduced slime in which metal components are deposited as fine particles is obtained. This reduced slime (precious metal slime) contains a small amount of gold and silver in addition to platinum and palladium.

【0004】従来、この貴金属スライムは王水により処
理されている。王水処理により、白金やパラジウムおよ
び金はそれぞれPtCl6 2-、PdCl4 2-、AuCl4 -
等の塩化物錯イオンとなり溶解する。しかし、貴金属ス
ライムを王水に溶解するには半日ないし一日程度の時間
を要する。また、溶液中に多量の硝酸が含まれるために
後工程の必要上、蒸発乾固・塩酸溶解を繰り返して脱硝
を行なわなければならず、この脱硝工程にさらに2日程
度の処理時間を要するなど、全工程の遂行に長時間を要
するという問題がある。
Conventionally, this precious metal slime has been treated with aqua regia. PtCl 6 2− , PdCl 4 2− , AuCl 4 were added to platinum, palladium and gold by aqua regia treatment.
It becomes a chloride complex ion such as and dissolves. However, it takes half a day or about a day to dissolve the precious metal slime in aqua regia. In addition, since a large amount of nitric acid is contained in the solution, denitration must be performed by repeating evaporation to dryness and dissolution in hydrochloric acid, and this denitration step requires a processing time of about 2 days. However, there is a problem that it takes a long time to perform all the steps.

【0005】そこで、王水溶解に代わる方法として塩素
吹き込み法(特公昭 62-2014号)も提案されている。し
かし、塩素ガスを取り扱うことから作業上の安全確保、
周辺環境への配慮のために特別な設備が必要であり、従
来の処理プラントでは対応が困難であった。
Therefore, a chlorine blowing method (Japanese Patent Publication No. 62-2014) has been proposed as an alternative method to the aqua regia dissolution. However, since chlorine gas is handled, ensuring work safety,
Special equipment was required to consider the surrounding environment, and it was difficult for conventional processing plants to handle this.

【0006】[0006]

【発明の解決課題】本発明は、従来の貴金属スライムの
溶解方法における上記問題を解決したものであって、処
理時間が短く、脱硝などの後処理が不要であり、しかも
有毒で腐食性の強い塩素ガスなどを用いる必要がなく、
安全に低コストで、かつ効率よく貴金属スライムを溶解
する方法を提供する。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems in the conventional method for dissolving noble metal slime, has a short treatment time, does not require post-treatment such as denitration, and is toxic and highly corrosive. There is no need to use chlorine gas,
Provided is a method of safely and inexpensively and efficiently dissolving a precious metal slime.

【0007】[0007]

【課題の解決手段】本発明は、貴金属スライムに塩酸存
在下で過酸化水素を導入することにより、スライム中の
金、白金およびパラジムの含有貴金属を数時間程度で完
全に溶解する方法である。すなわち本発明は、(1)
金、白金およびパラジウムを含有するスライムに、塩酸
存在下で過酸化水素を導入することにより、上記含有貴
金属を塩化物錯体に転化して溶解することを特徴とする
貴金属含有スライムの溶解方法である。
The present invention is a method for completely dissolving a precious metal containing gold, platinum and paradium in slime in about several hours by introducing hydrogen peroxide into the precious metal slime in the presence of hydrochloric acid. That is, the present invention provides (1)
A method for dissolving a noble metal-containing slime, characterized in that, by introducing hydrogen peroxide into a slime containing gold, platinum and palladium in the presence of hydrochloric acid, the contained noble metal is converted into a chloride complex and dissolved. .

【0008】上記溶解方法は(2)塩酸の量が、スライ
ム中の上記含有貴金属を塩化物錯体に転じるに必要な最
低量以上ないしその2倍量以下である上記(1)の溶解方
法、(3)過酸化水素の量が、スライム中の上記含有貴
金属を酸化するのに必要な最低量の2倍量以上ないし4
倍量以下である上記(1)または(2)の溶解方法、(4)6
0〜80℃の温度範囲で溶解を行う上記(1)〜(3)のいず
れかに記載の溶解方法を含む。
The above-mentioned dissolution method is (2) the dissolution method according to (1) above, wherein the amount of hydrochloric acid is at least the minimum amount required to convert the contained noble metal in the slime into a chloride complex or at most twice the amount thereof, ( 3) The amount of hydrogen peroxide is at least twice the minimum amount required to oxidize the precious metal contained in slime or more to 4
Dissolution method according to (1) or (2) above, which is less than or equal to the double amount, (4) 6
The dissolution method according to any one of (1) to (3) above, wherein the dissolution is performed in a temperature range of 0 to 80 ° C.

【0009】[0009]

【具体的な説明】本発明が適用される貴金属スライムと
は、金、白金およびパラジウムが含有されるスライムで
あり、その代表的なものは、前述したように、銅やニッ
ケルの精練工程で生じる陽極スライムあるいはニッケル
の精練工程で生じる抽出残渣を硝酸処理して金を回収
し、さらに塩酸処理して銀を回収した残液にヒドラジン
などの還元剤を加えて残留する上記貴金属を析出させた
還元スライムである。この還元スライムは、必要に応じ
て水洗し、硝酸などを除いた後に本発明の処理に供す
る。
[Detailed Description] The noble metal slime to which the present invention is applied is a slime containing gold, platinum and palladium, and a typical one thereof is, as described above, produced in the step of refining copper or nickel. Nitrogen treatment of the extraction residue generated in the anode slime or nickel refining process recovers gold, and further hydrochloric acid treatment recovers silver to reduce the residual precious metal by adding a reducing agent such as hydrazine to the residual liquid. It's a slime. This reduced slime is washed with water as necessary, nitric acid and the like are removed, and then subjected to the treatment of the present invention.

【0010】本発明の方法は、(a)塩酸添加工程、(b)過
酸化水素添加工程の2工程を含む。金、白金およびパラ
ジウムは過酸化水素によって酸化され、これに塩素が反
応して塩化物錯体を生じることにより溶解する。すなわ
ち、これら貴金属M(M:Pt,Pd,Au)が過酸化水素H22
との反応により貴金属イオンMx-となり、これと塩素C
-との反応によりMCln(x-n)-が生じて基金属Mが液
中に溶解する。塩酸と過酸化水素は上記貴金属と共に同
時に存在すればよい。塩酸より先に過酸化水素を導入す
ると、塩化物錯体が形成される前に過酸化水素が消費さ
れるので好ましくない。
The method of the present invention includes two steps: (a) hydrochloric acid addition step and (b) hydrogen peroxide addition step. Gold, platinum, and palladium are oxidized by hydrogen peroxide, and chlorine reacts with them to dissolve them by forming a chloride complex. That is, these precious metals M (M: Pt, Pd, Au) are hydrogen peroxide H 2 O 2
Noble metal ion M x- becomes by the reaction with and this and chlorine C
The reaction with l produces MCln (xn) − and the base metal M dissolves in the liquid. Hydrochloric acid and hydrogen peroxide may be present together with the above noble metal. Introducing hydrogen peroxide prior to hydrochloric acid is not preferred because hydrogen peroxide is consumed before chloride complexes are formed.

【0011】(1)塩酸添加工程 塩酸添加量は、スライム中に含まれる金、白金およびパ
ラジウムを塩化物錯イオンに転じるに必要な最低量(当
量)以上であって、その2倍量以下が好ましい。添加量
が当量以下では当然ながらこれらの貴金属を十分に溶解
することができない。また、添加量が当量の2倍を超え
るとコストが高くなる上、スライム中に銀が含有されて
いる場合には、この銀が塩化物錯イオンとなって溶解
し、後工程でのパラジウムあるいは白金の分離の際に混
入する等の問題を生じる。塩酸濃度は8〜12mol/l程
度が好ましい。8mol/l未満では液量が過剰となり後処
理にコストがかかるなどの問題を生じる。なお、上記範
囲より濃度が高いものは市販品では入手困難であり、実
用に適さない。
(1) Hydrochloric Acid Addition Step The amount of hydrochloric acid added is at least the minimum amount (equivalent amount) necessary to convert gold, platinum and palladium contained in slime into chloride complex ions, but not more than twice that amount. preferable. If the amount of addition is less than the equivalent, naturally, these noble metals cannot be sufficiently dissolved. Further, if the addition amount exceeds twice the equivalent amount, the cost becomes high, and when silver is contained in the slime, this silver becomes a chloride complex ion and dissolves, and palladium or This causes problems such as mixing when platinum is separated. The hydrochloric acid concentration is preferably about 8 to 12 mol / l. If it is less than 8 mol / l, the amount of liquid becomes excessive, and there is a problem that post-treatment is costly. It is difficult to obtain a product having a concentration higher than the above range as a commercial product, and it is not suitable for practical use.

【0012】(2)過酸化水素添加工程 過酸化水素の添加量は、スライム中に含まれるパラジウ
ム(Pd)、白金(Pt)および金(Au)をPd(IV)、Pt(IV)、
Au(III)まで酸化するのに必要な量の2倍以上であっ
て4倍量以下が好ましい。添加量が2当量未満ではこれ
らの貴金属を十分に酸化することができない。また、添
加量が当量の4倍を超えるとコストが高くなる。過酸化
水素濃度は8〜11mol/l程度が好ましい。濃度が8mol
/l未満では液量が過剰となり後処理にコストがかかるな
どの問題を生じる。上記範囲より濃度が高いものは市販
品では入手困難であり、実用に適さない。
(2) Hydrogen Peroxide Adding Step The amount of hydrogen peroxide added is such that palladium (Pd), platinum (Pt) and gold (Au) contained in slime are Pd (IV), Pt (IV),
The amount is preferably 2 times or more and 4 times or less the amount necessary to oxidize up to Au (III). If the added amount is less than 2 equivalents, these noble metals cannot be sufficiently oxidized. On the other hand, if the added amount exceeds four times the equivalent, the cost increases. The concentration of hydrogen peroxide is preferably about 8 to 11 mol / l. Concentration is 8 mol
If it is less than / l, the amount of liquid becomes excessive, which causes problems such as high cost for post-treatment. A product having a concentration higher than the above range is difficult to obtain as a commercial product and is not suitable for practical use.

【0013】過酸化水素の添加は60〜80℃で行なう
ことが好ましい。60℃未満では酸化溶解が進まず効率
が低下する。80℃を超えると添加した過酸化水素がス
ライムの溶解に寄与せずに分解するためやはり効率が低
下する。過酸化水素は必要量を徐々に添加することが好
ましい。当初から過酸化水素の必要量が全量存在する
と、急激に分解反応が進行して激しい発熱を伴う。この
熱によって、過酸化水素の分解が促進され、反応効率が
低下すると共に過酸化水素の分解によって酸素が発生
し、いわゆるフォーミングにより液体積が急激に増加す
るので危険である。添加する速さは、スライムの量や塩
酸、過酸化水素の濃度にもよるが、典型的には上記によ
り決定される添加量の全量を100〜120分程度の時
間をかけて平均して添加することが好ましい。
[0013] The addition of hydrogen peroxide is preferably carried out at 60 to 80 ° C. If the temperature is lower than 60 ° C., oxidative dissolution does not proceed, and the efficiency decreases. If the temperature exceeds 80 ° C, the added hydrogen peroxide decomposes without contributing to the dissolution of slime, and the efficiency also decreases. It is preferable that the required amount of hydrogen peroxide is gradually added. If the required amount of hydrogen peroxide is present from the beginning, the decomposition reaction will proceed rapidly, resulting in intense heat generation. This heat promotes the decomposition of hydrogen peroxide, lowers the reaction efficiency, and generates oxygen by the decomposition of hydrogen peroxide, which is dangerous because the liquid volume is rapidly increased by so-called forming. The speed of addition depends on the amount of slime and the concentrations of hydrochloric acid and hydrogen peroxide, but typically the total amount of addition determined above is added on average over a period of about 100 to 120 minutes. Preferably.

【0014】[0014]

【発明の実施形態】以下、本発明の実施例及び比較例を
示す。なお、これらは例示であり発明の範囲を限定する
ものではない。なお、試料の貴金属スライムは、銀スラ
イムの硝酸溶液から沈殿金を除いた後にヒドラジンを用
いて還元し、洗浄したものであり、5重量%のPt、2
5重量%のPd、2重量%のAuおよび0.3重量%の
Agを含むものを用いた。
Embodiments of the present invention and comparative examples will be described below. In addition, these are illustrations and do not limit the scope of the invention. The noble metal slime of the sample was obtained by removing the precipitated gold from the nitric acid solution of silver slime, reducing it with hydrazine, and washing it.
The one containing 5 wt% Pd, 2 wt% Au and 0.3 wt% Ag was used.

【0015】実施例1 温度制御装置および撹拌機を取り付けた200mlの反応
容器にヒドラジン還元した貴金属スライム50gを入
れ、36%濃度塩酸70ml(当量の 1.4倍)を加えた後、
液温をおよそ65℃に保ち撹拌しながら31%過酸化水
素水30ml(当量の3倍)を0.3ml/minの割合で添加し
た。添加終了後も前記温度を維持して撹拌を続けたとこ
ろ4時間でスライムは全量溶解した。反応終了後、液を
濾過したが残渣はほとんど認められなかった。濾液をI
PC分析により分析したところ、スライム中のPtおよ
びPdについては95%以上が溶液中に浸出されている
ことが確認された。なお、濾液中にはAg、Auも含ま
れていたが、2倍量の水で希釈することによりAgは塩
化銀として沈殿し、シュウ酸を添加することにより金属
Auを回収除去することができた。
Example 1 50 g of noble metal slime reduced with hydrazine was placed in a 200 ml reaction vessel equipped with a temperature control device and a stirrer, and 70 ml of 36% concentration hydrochloric acid (1.4 times the equivalent amount) was added thereto.
While maintaining the liquid temperature at about 65 ° C., 30 ml of 31% hydrogen peroxide solution (3 times the equivalent amount) was added at a rate of 0.3 ml / min while stirring. When the stirring was continued while maintaining the above temperature after the addition was completed, the slime was completely dissolved in 4 hours. After the reaction was completed, the liquid was filtered, but almost no residue was observed. The filtrate is I
Analysis by PC analysis confirmed that 95% or more of Pt and Pd in slime were leached into the solution. The filtrate also contained Ag and Au, but Ag was precipitated as silver chloride by diluting it with twice the amount of water, and metallic Au could be recovered and removed by adding oxalic acid. It was

【0016】実施例2 塩酸の添加量を60ml(当量の 1.2倍)に減らし、浸出温
度を70〜80℃にした以外は実施例1と同様にしてス
ライムの処理を行なった。4時間でスライムの全量が溶
解した。濾液をIPC分析したところ、スライム中のP
tおよびPdの95%以上が溶液中に溶解していること
が確認された。
Example 2 The slime treatment was carried out in the same manner as in Example 1 except that the addition amount of hydrochloric acid was reduced to 60 ml (1.2 times the equivalent amount) and the leaching temperature was changed to 70 to 80 ° C. The total amount of slime was dissolved in 4 hours. IPC analysis of the filtrate revealed that P in slime
It was confirmed that 95% or more of t and Pd were dissolved in the solution.

【0017】比較例1 塩酸の添加量を40ml(当量の 0.8倍)に減らした他は実
施例2と同様にしてスライムの処理を行なった。この処
理液を濾過したところ、少量の黒い滓が認められた。処
理液のPd浸出率は95%以上であったが、Pt浸出率
は61.2%であった。
Comparative Example 1 Slime was treated in the same manner as in Example 2 except that the amount of hydrochloric acid added was reduced to 40 ml (0.8 times the equivalent amount). When this treatment liquid was filtered, a small amount of black slag was observed. The Pd leaching rate of the treatment liquid was 95% or more, but the Pt leaching rate was 61.2%.

【0018】比較例2 塩酸の添加量を200ml(当量の4倍)とする一方、過酸
化水素水の添加量を15ml(当量の1.5倍)に減らした他
は実施例2と同様にしてスライムの処理を行なった。液
を濾過したところ、少量の黒い滓が認められ、Pd浸出
率は79.2%であり、Pt浸出率は29.3%と低かっ
た。
Comparative Example 2 A slime was prepared in the same manner as in Example 2 except that the amount of hydrochloric acid added was 200 ml (4 times the equivalent amount) and the amount of hydrogen peroxide solution was reduced to 15 ml (1.5 times the equivalent amount). Was processed. When the liquid was filtered, a small amount of black slag was observed, the Pd leaching rate was 79.2%, and the Pt leaching rate was as low as 29.3%.

【0019】比較例3 塩酸の添加量を50ml(当量の1倍)とし、液温を45℃
とした他は実施例1と同様にしてスライムの処理を行な
った。処理液を濾過したところ、少量の黒い滓が認めら
れた。Pd浸出率は74.9%以上であったが、Pt浸
出率は56.6%にとどまった。
Comparative Example 3 Hydrochloric acid was added in an amount of 50 ml (one equivalent) and the liquid temperature was 45 ° C.
The slime treatment was performed in the same manner as in Example 1 except for the above. When the treatment liquid was filtered, a small amount of black slag was observed. The Pd leaching rate was 74.9% or more, but the Pt leaching rate remained at 56.6%.

【0020】[0020]

【発明の効果】従来の白金族スライムの処理法では、王
水溶解に半日ないし一日程度の時間を要し、さらに硝酸
を除去するために2日余り脱硝処理が必要であるが、本
発明の方法によれば全体でも数時間程度の時間でスライ
ムを溶解することができる。また、得られた溶解液は塩
酸性溶液であるため後工程処理が容易である。さらに、
スライムに含有される貴金属の溶解率も高い。また、本
発明のプロセスは従来の王水溶解法で用いられている設
備をそのまま転用できるため、追加的な設備投資をほと
んど要することなくプロセスの改善が可能である。
According to the conventional method for treating platinum group slime, it takes about half a day to about one day to dissolve aqua regia, and denitrification treatment is required for more than 2 days to remove nitric acid. According to the above method, slime can be dissolved in a time of about several hours as a whole. Further, since the obtained solution is a hydrochloric acid solution, the post-process treatment is easy. further,
The dissolution rate of precious metals contained in slime is also high. Further, since the process of the present invention can directly use the facility used in the conventional aqua regia dissolution method, the process can be improved with almost no additional capital investment.

【図面の簡単な説明】[Brief description of drawings]

【図1】 従来の貴金属含有スライムの処理プロセス
図。
FIG. 1 is a process diagram of a conventional precious metal-containing slime.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 金、白金およびパラジウムを含有するス
ライムに、塩酸存在下で過酸化水素を導入することによ
り、上記含有貴金属を塩化物錯体に転化して溶解するこ
とを特徴とする貴金属含有スライムの溶解方法。
1. A noble metal-containing slime, characterized in that, by introducing hydrogen peroxide into a slime containing gold, platinum and palladium in the presence of hydrochloric acid, the contained noble metal is converted into a chloride complex and dissolved. Dissolution method.
【請求項2】 塩酸の量が、スライム中の上記含有貴金
属を塩化物錯体に転じるに必要な最低量以上ないしその
2倍量以下である請求項1の溶解方法。
2. The method according to claim 1, wherein the amount of hydrochloric acid is at least the minimum amount required to convert the precious metal contained in the slime into a chloride complex or at most twice the amount thereof.
【請求項3】 過酸化水素の量が、スライム中の上記含
有貴金属を酸化するのに必要な最低量の2倍量以上ない
しその4倍量以下である請求項1または2の溶解方法。
3. The method according to claim 1, wherein the amount of hydrogen peroxide is at least twice the minimum amount required to oxidize the precious metal contained in the slime and at most four times the minimum amount.
【請求項4】 60〜80℃の温度範囲で溶解を行う請
求項1〜3のいずれかに記載の溶解方法。
4. The melting method according to claim 1, wherein the melting is performed in a temperature range of 60 to 80 ° C.
JP8076001A 1996-03-29 1996-03-29 Dissolving method of noble metal-containing slime Withdrawn JPH09263847A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8076001A JPH09263847A (en) 1996-03-29 1996-03-29 Dissolving method of noble metal-containing slime

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8076001A JPH09263847A (en) 1996-03-29 1996-03-29 Dissolving method of noble metal-containing slime

Publications (1)

Publication Number Publication Date
JPH09263847A true JPH09263847A (en) 1997-10-07

Family

ID=13592576

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8076001A Withdrawn JPH09263847A (en) 1996-03-29 1996-03-29 Dissolving method of noble metal-containing slime

Country Status (1)

Country Link
JP (1) JPH09263847A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011021259A (en) * 2009-07-17 2011-02-03 Dowa Eco-System Co Ltd Solution for separating platinum, and method for separating and recovering platinum
JP2013508566A (en) * 2010-07-23 2013-03-07 メタルス リカバリー テクノロジー インコーポレイテッド Precious metal recovery method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011021259A (en) * 2009-07-17 2011-02-03 Dowa Eco-System Co Ltd Solution for separating platinum, and method for separating and recovering platinum
JP2013508566A (en) * 2010-07-23 2013-03-07 メタルス リカバリー テクノロジー インコーポレイテッド Precious metal recovery method

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