JP2002088419A - Method for reducing and recovering palladium - Google Patents
Method for reducing and recovering palladiumInfo
- Publication number
- JP2002088419A JP2002088419A JP2000275814A JP2000275814A JP2002088419A JP 2002088419 A JP2002088419 A JP 2002088419A JP 2000275814 A JP2000275814 A JP 2000275814A JP 2000275814 A JP2000275814 A JP 2000275814A JP 2002088419 A JP2002088419 A JP 2002088419A
- Authority
- JP
- Japan
- Prior art keywords
- palladium
- selenium
- reducing
- solution
- hydrochloric 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.)
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Links
Classifications
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- 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
- Catalysts (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、有価物を湿式回収する
方法に関するものであり、更に詳しく述べると有価物で
あるパラジウムを液中から還元回収する方法に関するも
のである。特に自動車廃触媒の浸出液の処理等に有効に
使用される。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for wet recovery of valuable resources, and more particularly, to a method for reducing and recovering valuable palladium from a liquid. In particular, it is effectively used for treating a leachate of an automobile waste catalyst.
【0002】[0002]
【従来の技術】パラジウムは化学的に安定なため、浸出
液として例えば酸化力のある王水や塩酸がよく用いられ
る。これらの液に溶解したパラジウムを水溶液から還元
回収する還元剤として、例えば水素化ホウ素、水素化ホ
ウ素ナトリウム、ヒドラジン等が知られている。しかし
ながら、これらの還元剤は高価であるばかりか、液中の
酸類を同時に消費してしまい経済的に好ましくないこと
が多い。2. Description of the Related Art Since palladium is chemically stable, oxidizing aqua regia or hydrochloric acid is often used as a leachate. As a reducing agent for reducing and recovering palladium dissolved in these liquids from an aqueous solution, for example, borohydride, sodium borohydride, hydrazine and the like are known. However, these reducing agents are not only expensive, but also consume acids in the solution at the same time, and are often economically undesirable.
【0003】一方、酸類を消費しない還元剤として亜硫
酸ガスが挙げられる。この亜硫酸ガスは比較的入手が容
易であり、しかも安価というメリットがある。しかしな
がら、パラジウムを含む塩酸酸性溶液に亜硫酸ガスを通
じてもパラジウムは金属まで還元され難い。これは塩酸
溶液で形成されるパラジウムのクロロ錯体は高酸化状態
にあり、これがクロロ錯体低酸化状態に還元されるのみ
で、金属パラジウムまで還元されないと考えられる。[0003] On the other hand, as a reducing agent which does not consume acids, sulfur dioxide gas can be mentioned. This sulfurous acid gas is relatively easily available and has the advantage of being inexpensive. However, palladium is not easily reduced to metal even by passing sulfurous acid gas through a hydrochloric acid solution containing palladium. This is thought to be because the chloro complex of palladium formed in the hydrochloric acid solution is in a highly oxidized state, and is only reduced to the chloro complex in a low oxidized state, but not reduced to metallic palladium.
【0004】[0004]
【発明が解決しようとする課題】上記問題点を解決す
る、湿式法によるパラジウムの還元回収方法を提供する
ものである。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for reducing and recovering palladium by a wet method, which solves the above problems.
【0005】[0005]
【課題を解決するための手段】本発明者らは、含パラジ
ウム塩酸酸性溶液からのパラジウム回収方法に関して種
々の検討を行った結果、液中からのパラジウム回収方法
として、 (1)パラジウムを含む塩酸酸性溶液に亜硫酸ガスを吹
込むことによりパラジウムを還元回収する方法におい
て、セレン及び又はテルルを液中に共存させることによ
り、パラジウムの還元を効率よく行うことを特徴とする
方法。 (2)共存するセレン、テルルの濃度がそれぞれ、1g
/L以上、0.5g/L以上であることを特徴とする上
記(1)記載の方法。を提供する。 (3)対象処理液が、自動車廃触媒を処理した浸出液で
ある上記(1)及び上記(2)記載のパラジウムの還元
回収方法。Means for Solving the Problems The present inventors have conducted various studies on a method for recovering palladium from a palladium-containing hydrochloric acid-containing acidic solution. A method for reducing and recovering palladium by blowing sulfurous acid gas into an acidic solution, wherein selenium and / or tellurium coexist in a liquid to efficiently reduce palladium. (2) The concentrations of coexisting selenium and tellurium are each 1 g
/ L or more and 0.5 g / L or more. I will provide a. (3) The method for reducing and recovering palladium according to (1) or (2), wherein the target treatment liquid is a leachate obtained by treating an automobile waste catalyst.
【0006】[0006]
【作用】以下本発明の構成を詳しく説明する。なお構成
は例を挙げて説明しているが、本発明はこの例に制限さ
れるものではない。The structure of the present invention will be described below in detail. Although the configuration has been described using an example, the present invention is not limited to this example.
【0007】パラジウムは化学的に安定なため、浸出液
として例えば酸化力のある王水や塩酸がよく用いられ
る。これらの液に溶解したパラジウムを水溶液から回収
する還元剤として、例えば水素化ホウ素、水素化ホウ素
ナトリウム、ヒドラジン等が知られている。しかしなが
ら、これらの還元剤は高価であるばかりか、液中の酸類
を同時に消費してしまい経済的に好ましくないことが多
い。Since palladium is chemically stable, for example, oxidizing aqua regia or hydrochloric acid is often used as a leachate. As a reducing agent for recovering palladium dissolved in these liquids from an aqueous solution, for example, borohydride, sodium borohydride, hydrazine and the like are known. However, these reducing agents are not only expensive, but also consume acids in the solution at the same time, and are often economically undesirable.
【0008】一方、酸類を消費しない還元剤として亜硫
酸ガスが挙げられる。しかしながら、パラジウムを含む
塩酸酸性溶液に亜硫酸ガスを通じてもパラジウムは還元
されない。On the other hand, as a reducing agent that does not consume acids, sulfurous acid gas can be mentioned. However, palladium is not reduced even when sulfurous acid gas is passed through a hydrochloric acid solution containing palladium.
【0009】本発明者らは、塩酸酸性溶液からのパラジ
ウム還元回収の種々の検討を行った結果、パラジウムの
他にセレン及び又はテルル(以下セレン等と称す。)を
液中に単独或いは、共存させることにより、亜硫酸ガス
によるパラジウムの還元が容易に行えることを見出し
た。The present inventors have conducted various studies on the reduction and recovery of palladium from an acidic hydrochloric acid solution. By doing so, it has been found that palladium can be easily reduced with sulfurous acid gas.
【0010】パラジウムのみを溶解した塩酸酸性溶液に
亜硫酸ガスを吹込むと酸化還元電位は、吹込む前の80
0〜1,000mV(vs.Ag/AgCl)から40
0mV付近まで低下し平衡に達する。しかしながら、パ
ラジウムは還元されないまま、液中に溶解している。When sulfur dioxide is blown into a hydrochloric acid solution in which only palladium is dissolved, the oxidation-reduction potential becomes 80
0 to 1,000 mV (vs. Ag / AgCl) to 40
It drops to around 0 mV and reaches equilibrium. However, palladium is dissolved in the liquid without being reduced.
【0011】パラジウム含む塩酸酸性溶液として、例え
ば自動車廃触媒を浸出したものがある。この浸出液の組
成は、例えばPd=0.5〜10g/L、HCl=20
〜200g/Lであり、セレン、テルルは廃触媒に含ま
れていないため、液中に存在しない。この液にセレン等
を加えた後、亜硫酸ガスを吹込むと酸化還元電位は、吹
込む前の800〜1,000mV(vs.Ag/AgC
l)から400mV付近まで低下し平衡に達する。この
とき液中のパラジウム濃度は、徐々に低下し400mV
でほぼゼロに近くなる。セレン等の共存成分もほぼ同様
の挙動を示す。この反応は共沈等によるものと考えてい
る。なおセレン、テルル以外の金属、例えば鉄等を共存
させても、パラジウムの還元回収はできない。液温は7
0℃以上が好ましい。これより温度が低いと還元された
セレンがゴム状となるため、その後の取扱いが困難とな
る。また酸濃度は亜硫酸ガス吹込み前後でほぼ変わらな
い値を示す。したがって、セレン等を共存させた場合、
酸を消費せず塩酸酸性溶液中のパラジウムを還元回収で
きることを見出した。As a hydrochloric acid solution containing palladium, for example, there is a solution obtained by leaching a waste catalyst for automobiles. The composition of this leachate is, for example, Pd = 0.5 to 10 g / L, HCl = 20
200200 g / L, and selenium and tellurium are not contained in the liquid because they are not contained in the spent catalyst. After selenium or the like is added to this solution, when a sulfurous acid gas is blown, the oxidation-reduction potential becomes 800 to 1,000 mV (vs. Ag / AgC
from 1) to around 400 mV and reach equilibrium. At this time, the palladium concentration in the liquid gradually decreased to 400 mV
And it becomes almost zero. Coexisting components such as selenium also show almost the same behavior. This reaction is thought to be due to coprecipitation and the like. Note that even if a metal other than selenium and tellurium, for example, iron and the like coexist, palladium cannot be reduced and recovered. Liquid temperature is 7
0 ° C. or higher is preferred. If the temperature is lower than this, the reduced selenium becomes rubbery, which makes subsequent handling difficult. Further, the acid concentration shows a value that does not substantially change before and after the introduction of the sulfurous acid gas. Therefore, when selenium and the like coexist,
It has been found that palladium in hydrochloric acid solution can be reduced and recovered without consuming acid.
【0012】還元滓にはパラジウムとセレンが含まれる
が、例えばこの還元滓を加熱することによりセレンが昇
華するため、パラジウムとセレンの分離は容易に行え
る。また昇華したセレンは二酸化セレンとして回収し、
工程内へ繰返すことが可能である。The reduced slag contains palladium and selenium. For example, selenium sublimates by heating the reduced slag, so that palladium and selenium can be easily separated. The sublimated selenium is recovered as selenium dioxide,
It is possible to repeat into the process.
【0013】以上説明したように、塩酸酸性溶液からの
パラジウム回収方法を確立した。As described above, a method for recovering palladium from hydrochloric acid acidic solution has been established.
【0014】以下本発明の実施例を説明する。なお本発
明は実施例に限定されるものではない。An embodiment of the present invention will be described below. Note that the present invention is not limited to the embodiments.
【実施例1】Embodiment 1
【0015】自動車廃触媒を塩酸で浸出した液を想定し
た。廃触媒中には、セレン、テルルが含まれないため、
浸出液中にもセレン、テルルは存在しない。3M/L塩
酸0.5Lに、塩化パラジウムを溶解し、パラジウム濃
度を1g/Lに調整し供試液とした。[0015] A liquid obtained by leaching a waste automobile catalyst with hydrochloric acid was assumed. Since selenium and tellurium are not contained in the spent catalyst,
Neither selenium nor tellurium is present in the leaching solution. Palladium chloride was dissolved in 0.5 L of 3 M / L hydrochloric acid, and the palladium concentration was adjusted to 1 g / L to prepare a test solution.
【0016】この供試液に亜セレン酸を溶解してセレン
濃度5g/Lに調整し、80℃に昇温後亜硫酸ガスを
0.1L/minで吹込んだ。その結果、酸化還元電位
は430mVで平衡に達した。この時の結果を表1に示
す。パラジウム、セレンの100%近くが還元され、塩
酸は消費されなかった。Selenic acid was dissolved in this test solution to adjust the selenium concentration to 5 g / L. After the temperature was raised to 80 ° C., sulfuric acid gas was blown at 0.1 L / min. As a result, the redox potential reached equilibrium at 430 mV. Table 1 shows the results at this time. Nearly 100% of palladium and selenium were reduced, and no hydrochloric acid was consumed.
【0017】[0017]
【表1】 [Table 1]
【実施例2】Embodiment 2
【0018】実施例1の供試液に亜セレン酸を溶解しセ
レン濃度を表2に示すように調整した。セレン濃度を調
整した液を80℃に加温後、亜硫酸ガスを0.1L/m
inで吹込み、酸化還元電位が平衡になるまで還元を継
続した。その結果、酸化還元電位はいずれも400〜4
50mVで平衡となった。この時の結果を表2に示す。Selenous acid was dissolved in the test solution of Example 1 and the selenium concentration was adjusted as shown in Table 2. After the selenium concentration-adjusted solution was heated to 80 ° C., sulfurous acid gas was added at 0.1 L / m.
In was blown in, and reduction was continued until the oxidation-reduction potential became equilibrium. As a result, the oxidation-reduction potential was 400 to 4
Equilibrium was reached at 50 mV. Table 2 shows the results at this time.
【0019】[0019]
【表2】 表2から把握できるように、初期のセレン濃度が1.0
g/L以上でパラジウムの還元が効率的に行われた。[Table 2] As can be seen from Table 2, the initial selenium concentration was 1.0
The reduction of palladium was efficiently performed at g / L or more.
【実施例3】Embodiment 3
【0020】実施例1の供試液に二酸化テルルを溶解
し、表3に示すようにテルル濃度を調整した。この液を
80℃に加温後、亜硫酸ガスを実施例1と同様に吹込ん
だ。Tellurium dioxide was dissolved in the test solution of Example 1 and the tellurium concentration was adjusted as shown in Table 3. After the solution was heated to 80 ° C., sulfurous acid gas was blown in in the same manner as in Example 1.
【0021】[0021]
【表3】 表3から把握できるように、初期のテルル濃度が0.5
g/L以上でパラジウムの還元が効率的に行われた。[Table 3] As can be seen from Table 3, the initial tellurium concentration was 0.5
The reduction of palladium was efficiently performed at g / L or more.
【実施例4】Embodiment 4
【0022】実施例1の供試液に亜セレン酸と二酸化テ
ルルを溶解し、表4に示すようにセレン及びテルル濃度
を調整した。この液を80℃に加温後、亜硫酸ガスを実
施例1と同様に吹込んだ。Selenous acid and tellurium dioxide were dissolved in the test solution of Example 1, and the concentrations of selenium and tellurium were adjusted as shown in Table 4. After the solution was heated to 80 ° C., sulfurous acid gas was blown in in the same manner as in Example 1.
【0023】[0023]
【表4】 表4から把握できるように、セレンとテルルが同時に液
中に存在した場合でもパラジウムの還元が効率的に行わ
れた。[Table 4] As can be seen from Table 4, even when selenium and tellurium were present in the solution at the same time, palladium was reduced efficiently.
【0024】[0024]
【比較例1】実施例1の液(パラジウム濃度1g/L)
を80℃に加温後、亜硫酸ガスを実施例1と同様に吹込
んだ。Comparative Example 1 Liquid of Example 1 (palladium concentration 1 g / L)
After heating to 80 ° C., sulfurous acid gas was blown in in the same manner as in Example 1.
【0025】[0025]
【表5】 表1の結果と比較すると表5の結果は、パラジウムが亜
硫酸ガス吹き込み後であっても還元されていないため、
液中にほとんど残存していることが把握できる。[Table 5] Compared to the results in Table 1, the results in Table 5 show that palladium was not reduced even after sulfur dioxide gas was blown,
It can be understood that almost all of the liquid remains.
【0026】[0026]
【発明の効果】以上説明したように、本発明のセレン及
び又は、テルルを共存させることにより塩酸酸性溶液中
のパラジウムを亜硫酸ガスによって、簡便かつ容易に回
収することが可能となった。As described above, the coexistence of selenium and / or tellurium of the present invention makes it possible to easily and easily recover palladium in a hydrochloric acid acidic solution by using sulfurous acid gas.
【図1】本発明の処理フロー一態様を示す。FIG. 1 shows one embodiment of a processing flow of the present invention.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C22B 7/00 C22B 11/04 3/00 T ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C22B 7/00 C22B 11/04 3/00 T
Claims (3)
スを吹込むことによりパラジウムを還元回収する方法に
おいて、セレン及び又はテルルを液中に共存させること
により、パラジウムの還元を効率よく行うことを特徴と
するパラジウムの還元回収方法。1. A method for reducing and recovering palladium by blowing sulfurous acid gas into a hydrochloric acid solution containing palladium, wherein selenium and / or tellurium coexist in the liquid to efficiently reduce palladium. Method for reducing and recovering palladium.
れ、1g/L以上、0.5g/L以上であることを特徴
とする請求項1に記載の方法。2. The method according to claim 1, wherein the coexisting concentrations of selenium and tellurium are 1 g / L or more and 0.5 g / L or more, respectively.
出液であることを特徴とする請求項1及び請求項2のパ
ラジウムの還元回収方法。3. The method for reducing and recovering palladium according to claim 1, wherein the target treatment liquid is a leachate obtained by treating an automobile waste catalyst.
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JP2000275814A JP3679985B2 (en) | 2000-09-12 | 2000-09-12 | Palladium reduction recovery method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP2000275814A JP3679985B2 (en) | 2000-09-12 | 2000-09-12 | Palladium reduction recovery method |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008533293A (en) * | 2005-03-22 | 2008-08-21 | アングロ オペレーションズ リミティッド | Leaching method in the presence of hydrochloric acid to recover valuable metals from ora |
JP2021031728A (en) * | 2019-08-23 | 2021-03-01 | 国立大学法人東京工業大学 | Noble metal recovery method |
-
2000
- 2000-09-12 JP JP2000275814A patent/JP3679985B2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008533293A (en) * | 2005-03-22 | 2008-08-21 | アングロ オペレーションズ リミティッド | Leaching method in the presence of hydrochloric acid to recover valuable metals from ora |
JP2021031728A (en) * | 2019-08-23 | 2021-03-01 | 国立大学法人東京工業大学 | Noble metal recovery method |
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