JPH11302626A - Reducing agent for metal recovery - Google Patents

Reducing agent for metal recovery

Info

Publication number
JPH11302626A
JPH11302626A JP12414398A JP12414398A JPH11302626A JP H11302626 A JPH11302626 A JP H11302626A JP 12414398 A JP12414398 A JP 12414398A JP 12414398 A JP12414398 A JP 12414398A JP H11302626 A JPH11302626 A JP H11302626A
Authority
JP
Japan
Prior art keywords
metals
reducing agent
metal
desirably
present
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
Application number
JP12414398A
Other languages
Japanese (ja)
Inventor
Yoshihisa Tomotaki
善久 友滝
Takashi Kitajima
孝志 北島
Keiichiro Ishikawa
圭一郎 石川
Akihiro Nabeshima
亮浩 鍋島
Tomohiro Furuichi
智広 古市
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.)
Otsuka Chemical Co Ltd
Original Assignee
Otsuka Chemical Co Ltd
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 Otsuka Chemical Co Ltd filed Critical Otsuka Chemical Co Ltd
Priority to JP12414398A priority Critical patent/JPH11302626A/en
Publication of JPH11302626A publication Critical patent/JPH11302626A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a reducing agent usable to efficiently recover metals including noble metals and not problematic in the deposition of metals, etc., on e.g. the inside wall of a reactor by using a 1-aminopyrrolidine (salt) as the effective component. SOLUTION: This agent contains 1-aminopyrrolidine or a hydrochloride, sulfate, phosphate, or like salt thereof as the effective component. Metals can be recovered in the following way. Scraps of noble metal ornaments are dissolved in aqua regia, concentrated sulfuric acid is added to the solution, and the nitric acid contained in aqua regia is perfectly removed. At least 1.5 mol, desirably, 3-7 mol of the reducing agent is added per mol of the metals to be recovered, and optionally, an alkali agent is added to adjust the system to a pH of 3-13, desirably 5-10.5. The resulting mixture is heated to 20-120 deg.C, desirably, 50-85 deg.C under or without agitation and left standing for at least 10 min, desirably, 30 min to 1 hr to deposit metals containing noble metals. The alkali agent is exemplified by potassium hydroxide or sodium hydroxide.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、新規な金属回収用
還元剤に関する。本発明の金属回収用還元剤は、溶液中
から金属、好ましくは貴金属を還元回収するのに有効で
ある。
[0001] The present invention relates to a novel reducing agent for recovering metals. The metal recovery reducing agent of the present invention is effective for reducing and recovering a metal, preferably a noble metal, from a solution.

【0002】[0002]

【従来の技術】近年、電気・電子分野、有機合成分野等
を始めとする各種分野において、工業技術のめざましい
発展に伴い、金、銀、パラジウム、白金、ロジウム、イ
リジウム、オスミウム、レニウム等の貴金属は、装飾品
だけではなく、例えば半導体、回路基板、ブラウン管等
の電子工業材料や有機化学反応の触媒等として広く使用
されている。一方、貴金属の産出量が他の金属に比べて
非常に少ないことは周知の事実であり、そのため、貴金
属を効率良く回収、再利用することが大きな課題となっ
ている。
2. Description of the Related Art In recent years, in various fields such as an electric / electronic field and an organic synthesis field, with the remarkable development of industrial technology, precious metals such as gold, silver, palladium, platinum, rhodium, iridium, osmium, rhenium, etc. Are widely used not only as decorative articles but also as electronic industrial materials such as semiconductors, circuit boards, cathode ray tubes, etc., and catalysts for organic chemical reactions. On the other hand, it is a well-known fact that the amount of production of precious metals is very small as compared with other metals, and therefore, it is a major issue to efficiently recover and reuse precious metals.

【0003】貴金属の回収は、貴金属装飾品のスクラッ
プ、貴金属や貴金属イオンを含む廃液やメッキ廃液等
に、酸による溶解、電気分解、金属錯体形成、金属化合
物吸着剤、溶媒抽出、塩析、イオンクロマトグラフィー
等の分離精製手段を施して貴金属化合物を得、この貴金
属化合物を還元することにより実施され、その回収率は
95%にも達している。
[0003] Recovery of precious metals involves dissolving with acid, electrolysis, metal complex formation, metal compound adsorbents, solvent extraction, salting out, ionization into scraps of precious metal decorations, waste liquids containing noble metals and noble metal ions, and plating waste liquids. A noble metal compound is obtained by performing separation and purification means such as chromatography, and the noble metal compound is reduced. The recovery is as high as 95%.

【0004】[0004]

【発明が解決しようとする課題】ここで貴金属化合物を
還元する方法としては、装置や使用する薬品が安価であ
り且つ操作も容易であることから、還元剤を使用する方
法が一般的である。該還元剤としては、例えば、ヒドラ
ジンヒドラート、硫酸ヒドラジン、塩酸ヒドラジン、亜
硫酸、亜硫酸ナトリウム、ホルマリン、蟻酸等を挙げる
ことができる。しかしながら、これらの還元剤を使用す
ると、還元反応により生成する貴金属や副生物が反応容
器の内壁等に付着し易く、貴金属の回収率が低下すると
いう問題が生じる。上記した95%という回収率を達成
するためには、反応容器の内壁等に付着した貴金属をも
回収しなければならないが、それには、現状では、繁雑
な工程が多数必要になる。本発明の課題は貴金属を含む
金属を効率良く回収でき、しかも反応容器の内壁等に金
属等が付着することのない金属回収用還元剤を提供する
ことにある。
As a method for reducing a noble metal compound, a method using a reducing agent is generally used because the equipment and chemicals used are inexpensive and the operation is easy. Examples of the reducing agent include hydrazine hydrate, hydrazine sulfate, hydrazine hydrochloride, sulfurous acid, sodium sulfite, formalin, formic acid and the like. However, when these reducing agents are used, there is a problem that noble metals and by-products generated by the reduction reaction easily adhere to the inner wall of the reaction vessel and the like, and the recovery rate of the noble metals decreases. In order to achieve the above-mentioned 95% recovery rate, it is necessary to recover also the noble metal adhered to the inner wall and the like of the reaction vessel. However, at present, many complicated steps are required. An object of the present invention is to provide a reducing agent for metal recovery that can efficiently recover a metal containing a noble metal and that does not adhere to an inner wall or the like of a reaction vessel.

【0005】[0005]

【課題を解決するための手段】本発明は、1−アミノピ
ロリジン及びその塩から選ばれる少なくとも1種を有効
成分とする金属回収用還元剤に係る。本発明の金属回収
用還元剤によれば、貴金属を含む金属を反応容器内壁に
付着させることなく、析出させることができ、回収率の
向上及び回収工程の簡略化が達成される。従って、本発
明の金属回収用還元剤は、金属の溶液から金属を回収す
るのに特に有用である。更に、本発明の金属回収用還元
剤は、非常に低毒性であり、自然環境の保全や作業場に
おける従業者の安全性が特に重視される現状において
は、非常に有用である。
Means for Solving the Problems The present invention relates to a reducing agent for recovering metals containing at least one selected from 1-aminopyrrolidine and a salt thereof as an active ingredient. ADVANTAGE OF THE INVENTION According to the reducing agent for metal collection | recovery of this invention, a metal containing a noble metal can be precipitated, without adhering to the inner wall of a reaction container, and improvement of a collection rate and simplification of a collection | recovery process are achieved. Therefore, the metal recovery reducing agent of the present invention is particularly useful for recovering a metal from a solution of the metal. Furthermore, the reducing agent for recovering metals of the present invention has very low toxicity, and is very useful in the present situation where the preservation of the natural environment and the safety of employees in workplaces are particularly important.

【0006】[0006]

【発明の実施の形態】本発明の金属回収用還元剤は、1
−アミノピロリジン及びその塩から選ばれる少なくとも
1種を有効成分とする。1−アミノピロリジンは公知化
合物であり、例えば、医薬品や農薬の製造用中間体とし
て使用されている。また、1−アミノピロリジンの塩と
しては、例えば、塩酸塩、硫酸塩、リン酸塩等を挙げる
ことができる。これらの中でも、1−アミノピロリジン
そのものを好ましく使用できる。
BEST MODE FOR CARRYING OUT THE INVENTION The reducing agent for recovering metals according to the present invention comprises:
-At least one selected from aminopyrrolidine and salts thereof is used as an active ingredient. 1-Aminopyrrolidine is a known compound and is used, for example, as an intermediate for the production of pharmaceuticals and agricultural chemicals. Examples of the salt of 1-aminopyrrolidine include, for example, hydrochloride, sulfate, phosphate and the like. Among these, 1-aminopyrrolidine itself can be preferably used.

【0007】本発明の金属回収用還元剤は、還元により
回収し得る種々の金属の回収に使用できるが、金、銀、
パラジウム、白金、ロジウム、イリジウム、オスミウ
ム、レニウム等の貴金属の回収に使用するのが好まし
く、それらの中でも金、パラジウム、白金等の回収に使
用するのが特に好ましい。本発明の金属回収用還元剤
は、金属を含む有機溶媒溶液又は水溶液、好ましくは水
溶液から金属を回収するのに使用される。本発明におい
て金属を回収するに際しては、従来の還元剤に代えて本
発明の還元剤を用いる以外は、従来の方法と同様に実施
できる。但し、後記する様に、還元剤の使用量、反応系
のpH、反応温度、反応時間等は適宜変更することがで
きる。
The reducing agent for recovering metals of the present invention can be used for recovering various metals recoverable by reduction.
It is preferably used for recovering precious metals such as palladium, platinum, rhodium, iridium, osmium, rhenium and the like, and particularly preferably used for recovering gold, palladium, platinum and the like. The metal recovery reducing agent of the present invention is used for recovering a metal from an organic solvent solution or an aqueous solution containing a metal, preferably from an aqueous solution. In recovering the metal in the present invention, the method can be carried out in the same manner as in the conventional method, except that the reducing agent of the present invention is used instead of the conventional reducing agent. However, as described later, the amount of the reducing agent used, the pH of the reaction system, the reaction temperature, the reaction time, and the like can be appropriately changed.

【0008】本発明における金属回収の具体的な一例を
挙げると、金属のスクラップ(例えば、貴金属装飾品の
スクラップ)を王水に溶解し、これに濃塩酸を加えて王
水に含まれる硝酸を完全に除去した後、本発明の還元剤
を添加する方法、金属精製後の廃液やメッキ廃液に本発
明の還元剤を添加する方法、有機化合物の合成において
使用した触媒(例えば、貴金属触媒)を酸に溶解させ、
これをイオン交換樹脂に通して触媒由来の金属のみを吸
着させ、この金属を酸で溶出させ、本発明の還元剤を添
加する方法等を挙げることができる。本発明還元剤の使
用量は、用いる還元剤や回収しようとする金属の種類、
系内のpH値や反応温度等に応じて広い範囲から適宜選
択できるが、通常回収しようとする金属1モルに対し
て、1.5モル以上、好ましくは3〜7モルとすればよ
い。
As a specific example of the metal recovery in the present invention, a scrap of metal (for example, a scrap of a precious metal ornament) is dissolved in aqua regia and concentrated hydrochloric acid is added thereto to remove nitric acid contained in the aqua regia. After completely removing, the method of adding the reducing agent of the present invention, the method of adding the reducing agent of the present invention to the waste liquid after metal purification or the plating waste liquid, and the catalyst used in the synthesis of the organic compound (for example, a noble metal catalyst) Dissolved in acid,
This can be passed through an ion exchange resin to adsorb only the metal derived from the catalyst, elute this metal with an acid, and add the reducing agent of the present invention. The amount of the reducing agent of the present invention depends on the type of the reducing agent used and the metal to be recovered,
It can be appropriately selected from a wide range according to the pH value, reaction temperature and the like in the system, but is usually 1.5 mol or more, preferably 3 to 7 mol, per 1 mol of the metal to be recovered.

【0009】本発明において、還元剤の使用量を減らす
ために、系内にアルカリ剤を添加することができる。回
収の対象となる、金属を含む溶液のpHがアルカリ性で
あれば、そのまま回収を実施してもよく、必要に応じて
更にアルカリ剤を添加した後に回収を実施してもよい。
一方、金属を含む溶液のpHが酸性である場合は、その
まま回収を実施してもよいが、好ましくはアルカリ剤を
適量添加した後回収を実施するのがよい。ここで、アル
カリ剤としては特に制限されず、公知のものが使用で
き、例えば、水酸化カリウム、水酸化ナトリウム等のア
ルカリ金属の水酸化物、炭酸カリウム、炭酸ナトリウム
等のアルカリ金属の炭酸塩、アンモニア、炭酸アンモニ
ウム等を挙げることができる。これらの中でも、アルカ
リ金属の水酸化物を好ましく使用できる。アルカリ剤は
1種を単独で使用でき、又は2種以上を併用できる。ア
ルカリ剤の添加量は、回収の対象となる溶液のpHや該
溶液中に含まれる金属及びその他の成分等に応じて広い
範囲から適宜選択できるが、通常系内のpHが3〜13
程度、好ましくは5〜10.5となるようにアルカリ剤
が添加される。
In the present invention, an alkali agent can be added to the system in order to reduce the amount of the reducing agent used. If the pH of the solution containing the metal to be recovered is alkaline, the recovery may be performed as it is, or the recovery may be performed after further adding an alkali agent as needed.
On the other hand, when the pH of the solution containing the metal is acidic, the recovery may be carried out as it is, but it is preferable to carry out the recovery after adding an appropriate amount of an alkali agent. Here, the alkali agent is not particularly limited, and known agents can be used. For example, potassium hydroxide, hydroxides of alkali metals such as sodium hydroxide, potassium carbonate, carbonates of alkali metals such as sodium carbonate, Ammonia, ammonium carbonate and the like can be mentioned. Among these, an alkali metal hydroxide can be preferably used. One alkali agent can be used alone, or two or more alkali agents can be used in combination. The amount of the alkaline agent to be added can be appropriately selected from a wide range according to the pH of the solution to be recovered and the metals and other components contained in the solution.
The alkali agent is added to a degree, preferably 5 to 10.5.

【0010】本発明還元剤による金属の回収は、通常2
0〜120℃程度、好ましくは50〜85℃の温度で行
われる。本発明の還元剤による金属回収は、撹拌下又は
無撹拌下に行われる。本発明においては、回収しようと
する金属を含む溶液に本発明の還元剤を添加すると同時
に該金属がほぼ100%に近い回収率で析出するが、更
に必要に応じて、撹拌下又は無撹拌下に通常10分以
上、好ましくは30分〜1時間程度放置し、反応を完全
に進行させてもよい。本発明においては、本発明還元剤
の好ましい効果が損なわれない範囲で、ヒドラジンヒド
ラート、硫酸ヒドラジン、塩酸ヒドラジン、亜硫酸、亜
硫酸ナトリウム、ホルマリン、蟻酸等の従来の還元剤を
併用することもできる。本発明の還元剤により反応系内
に析出する金属は、従来法と同様に、ろ過等の簡易な分
離精製手段により、容易に回収できる。
The recovery of metal by the reducing agent of the present invention is usually carried out in two steps.
The reaction is performed at a temperature of about 0 to 120 ° C, preferably 50 to 85 ° C. The metal recovery by the reducing agent of the present invention is performed with or without stirring. In the present invention, the reducing agent of the present invention is added to a solution containing the metal to be recovered, and at the same time, the metal precipitates at a recovery rate close to 100%. The reaction may be allowed to proceed usually for at least 10 minutes, preferably for about 30 minutes to 1 hour. In the present invention, conventional reducing agents such as hydrazine hydrate, hydrazine sulfate, hydrazine hydrochloride, sulfurous acid, sodium sulfite, formalin and formic acid can be used in combination as long as the preferable effects of the reducing agent of the present invention are not impaired. The metal precipitated in the reaction system by the reducing agent of the present invention can be easily recovered by a simple separation and purification means such as filtration as in the conventional method.

【0011】[0011]

【実施例】以下に実施例及び比較例を挙げ、本発明をよ
り具体的に説明する。 実施例1 白金を1.3×10-3モル/リットルの濃度で含有する
王水(pH=5)1リットルを反応容器に入れ、水酸化
ナトリウムの10重量%水溶液を滴下してpHを10に
調整した。この溶液を80℃に加熱しながら、撹拌下に
1−アミノピロリジンの60重量%水溶液を1.95g
(1.3×10-2モル)添加したところ、白金は反応容
器の内壁に付着することなく析出した。析出した白金を
ろ過により回収した。白金の回収率は99.8%であっ
た。
The present invention will be described more specifically with reference to examples and comparative examples. Example 1 1 liter of aqua regia (pH = 5) containing platinum at a concentration of 1.3 × 10 −3 mol / l was placed in a reaction vessel, and a 10% by weight aqueous solution of sodium hydroxide was added dropwise to adjust the pH to 10%. Was adjusted. While heating this solution to 80 ° C., 1.95 g of a 60% by weight aqueous solution of 1-aminopyrrolidine was stirred.
(1.3 × 10 −2 mol), platinum was deposited without adhering to the inner wall of the reaction vessel. The precipitated platinum was recovered by filtration. The recovery of platinum was 99.8%.

【0012】比較例1 1−アミノピロリジンの60重量%水溶液に代えて、ヒ
ドラジンヒドラートの80重量%水溶液0.81g(1.
3×10-2モル)を使用する以外は、実施例1と同様に
して、白金の回収操作を実施したところ、反応溶液の内
壁に白金が一部付着した。ろ過による白金の回収率は8
6%にとどまった。
Comparative Example 1 Instead of a 60% by weight aqueous solution of 1-aminopyrrolidine, 0.81 g of an 80% by weight aqueous solution of hydrazine hydrate (1.
When platinum was recovered in the same manner as in Example 1 except that 3 × 10 -2 mol) was used, platinum was partially adhered to the inner wall of the reaction solution. Recovery rate of platinum by filtration is 8
Only 6%.

【0013】実施例2 本発明還元剤の使用量と白金の回収率の関係を調べた。
試料としては、実施例1と同様に、白金を1.3×10
-3モル/リットルの濃度で含有する王水(pH=5)1
リットルに水酸化ナトリウムの10重量%水溶液を滴下
してpHを10にしたものを用いた。還元剤としては1
−アミノピロリジンを用いた。反応温度を80〜85℃
の範囲に制御しながら、還元剤の添加量を変化させて白
金の回収率を調べた。結果を図1に示す。図1から、白
金濃度/還元剤濃度(モル比)3以上で、99%以上の
回収率が達成されることが判る。
Example 2 The relationship between the amount of the reducing agent of the present invention and the recovery of platinum was examined.
As a sample, as in Example 1, 1.3 × 10
Aqua regia (pH = 5) 1 containing -3 mol / L
A 10 wt% aqueous solution of sodium hydroxide was added dropwise to the liter to adjust the pH to 10. 1 as a reducing agent
-Aminopyrrolidine was used. Reaction temperature 80-85 ° C
The recovery rate of platinum was examined by changing the amount of the reducing agent while controlling the amount of platinum. The results are shown in FIG. From FIG. 1, it can be seen that at a platinum concentration / reducing agent concentration (molar ratio) of 3 or more, a recovery of 99% or more is achieved.

【0014】[0014]

【発明の効果】本発明によれば、貴金属を含む金属を効
率良く回収でき、しかも反応容器の内壁等に金属等が付
着することのない金属回収用還元剤を得ることができ
る。更に、本発明の金属回収用還元剤は、非常に低毒性
であり、自然環境の保全や作業場における従業者の安全
性が特に重視される現状においては、非常に有用であ
る。
According to the present invention, it is possible to obtain a metal-reducing reducing agent which can efficiently recover metals including noble metals and which does not adhere to the inner walls of the reaction vessel. Furthermore, the reducing agent for recovering metals of the present invention has very low toxicity, and is very useful in the present situation where the preservation of the natural environment and the safety of employees in workplaces are particularly important.

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

【図1】 還元剤(1−アミノピロリジン)の添加量
(濃度)と白金の回収率との関係を示すグラフである。
FIG. 1 is a graph showing the relationship between the addition amount (concentration) of a reducing agent (1-aminopyrrolidine) and the recovery rate of platinum.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 鍋島 亮浩 徳島県徳島市川内町加賀須野463 大塚化 学株式会社徳島工場内 (72)発明者 古市 智広 徳島県徳島市川内町加賀須野463 大塚化 学株式会社徳島工場内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Akihiro Nabeshima 463 Kagasuno, Kawauchi-machi, Tokushima City, Tokushima Prefecture Inside the Otsuka Chemical Co., Ltd. Inside Tokushima Factory

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 1−アミノピロリジン及びその塩から選
ばれる少なくとも1種を有効成分とする金属回収用還元
剤。
1. A reducing agent for recovering a metal, comprising as an active ingredient at least one selected from 1-aminopyrrolidine and a salt thereof.
【請求項2】 金属が貴金属である請求項1に記載の金
属回収用還元剤。
2. The reducing agent according to claim 1, wherein the metal is a noble metal.
JP12414398A 1998-04-16 1998-04-16 Reducing agent for metal recovery Pending JPH11302626A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12414398A JPH11302626A (en) 1998-04-16 1998-04-16 Reducing agent for metal recovery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12414398A JPH11302626A (en) 1998-04-16 1998-04-16 Reducing agent for metal recovery

Publications (1)

Publication Number Publication Date
JPH11302626A true JPH11302626A (en) 1999-11-02

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ID=14878003

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JP12414398A Pending JPH11302626A (en) 1998-04-16 1998-04-16 Reducing agent for metal recovery

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JP (1) JPH11302626A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11136681B2 (en) 2015-06-24 2021-10-05 Greene Lyon Group, Inc. Selective removal of noble metals using acidic fluids, including fluids containing nitrate ions
US11193214B2 (en) 2013-12-20 2021-12-07 Greene Lyon Group, Inc. Method and apparatus for recovery of noble metals, including recovery of noble metals from plated and/or filled scrap

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11193214B2 (en) 2013-12-20 2021-12-07 Greene Lyon Group, Inc. Method and apparatus for recovery of noble metals, including recovery of noble metals from plated and/or filled scrap
US11136681B2 (en) 2015-06-24 2021-10-05 Greene Lyon Group, Inc. Selective removal of noble metals using acidic fluids, including fluids containing nitrate ions

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