JP2001107157A - Method for recovering platinum of high purity - Google Patents
Method for recovering platinum of high purityInfo
- Publication number
- JP2001107157A JP2001107157A JP27889299A JP27889299A JP2001107157A JP 2001107157 A JP2001107157 A JP 2001107157A JP 27889299 A JP27889299 A JP 27889299A JP 27889299 A JP27889299 A JP 27889299A JP 2001107157 A JP2001107157 A JP 2001107157A
- Authority
- JP
- Japan
- Prior art keywords
- palladium
- platinum
- added
- aqueous solution
- dmg
- 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.)
- Granted
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
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、高純度の白金を得
る方法に関する。詳細には、パラジウムと白金とを含有
する水溶液から、パラジウムを分離し、高純度の白金を
得る方法に関する。さらには、製錬工程で得られた白金
を含有する抽出液からパラジウムを分離し、高純度の白
金を得る方法に関する。[0001] The present invention relates to a method for obtaining high-purity platinum. More specifically, the present invention relates to a method for separating palladium from an aqueous solution containing palladium and platinum to obtain high-purity platinum. Further, the present invention relates to a method for obtaining high-purity platinum by separating palladium from an extract containing platinum obtained in a smelting process.
【0002】[0002]
【従来の技術】製錬工程で得られる白金には、テルル、
パラジウム、鉄等の不純物が含まれ、そこから得られる
スポンジ白金には、従来、規格を満足できないものもあ
った。とりわけ、パラジウムは、白金とその化学的特性
が近似しているために、白金からパラジウムを分離する
のは、困難である。2. Description of the Related Art Platinum obtained in a smelting process includes tellurium,
Conventionally, sponge platinum containing impurities such as palladium and iron could not satisfy the standards. In particular, palladium is difficult to separate from platinum because of its similar chemical properties to platinum.
【0003】白金及びパラジウムを分離する方法とし
て、溶媒抽出法が知られている(特開平3−25352
4号公報、特開平11−229052号 公報参照)。
特開平3−253524号公報には、ジアルキルエタン
を抽出剤として用いる溶媒抽出方法が記載されている。
この方法においては、塩酸濃度と抽出時間とを調整する
ことで、パラジウムと白金とを分離できる可能性が示唆
されてはいるが、通常は、パラジウムと白金とが同時に
抽出回収される。特開平11−229052号公報に
は、白金とパラジウムとを含有する硝酸酸性溶液から、
ヒドロオキシム系溶媒でパラジウムを抽出し、次いでオ
クチルアミン系溶媒に接触させて白金を抽出するとい
う、パラジウムと白金とを分離する方法が記載される
が、2段階の抽出を要するものである。[0003] As a method for separating platinum and palladium, a solvent extraction method is known (JP-A-3-25352).
No. 4, JP-A-11-229052).
JP-A-3-253524 describes a solvent extraction method using a dialkylethane as an extractant.
In this method, it is suggested that palladium and platinum can be separated by adjusting the hydrochloric acid concentration and the extraction time, but usually, palladium and platinum are simultaneously extracted and recovered. JP-A-11-229052 discloses a nitric acid solution containing platinum and palladium,
A method for separating palladium from platinum, which involves extracting palladium with a hydroxime-based solvent and then contacting it with an octylamine-based solvent to extract platinum, which requires two-stage extraction.
【0004】また、白金とパラジウムの混合塩酸酸性溶
液にアリルアルコールを加え、パラジウムを金属状に還
元し、濾過洗浄後の濾液を水酸化ナトリウムでアルカリ
性にし、蟻酸を加えて加熱し、白金を金属状に還元し、
濾別することからなる白金とパラジウムの分離方法も提
供されている(特開平6−287654号公報)が、工程
が煩雑である。[0004] Also, allyl alcohol is added to a mixed hydrochloric acid solution of platinum and palladium to reduce palladium to a metal form, the filtrate after washing by filtration is made alkaline with sodium hydroxide, and formic acid is added to heat the platinum to remove the platinum. In the form of
A method for separating platinum and palladium by filtration is also provided (JP-A-6-287654), but the process is complicated.
【0005】このように、現状では、パラジウムを含む
白金含有水溶液からパラジウムを効率よく簡便に分離で
きる満足な方法は、提供されていない。As described above, at present, there is no satisfactory method capable of efficiently and simply separating palladium from a platinum-containing aqueous solution containing palladium.
【0006】[0006]
【発明が解決しようとする課題】本発明は、パラジウム
と白金とを含有する水溶液から、効率よくパラジウムを
分離し、高純度の白金を回収することを技術課題とす
る。また、製錬工程から得られたパラジウムを含む白金
抽出液からパラジウムを分離し、高純度の白金を回収す
る方法を提供することも課題とする。SUMMARY OF THE INVENTION An object of the present invention is to efficiently separate palladium from an aqueous solution containing palladium and platinum and to recover high-purity platinum. Another object is to provide a method for separating palladium from a palladium-containing platinum extract obtained from a smelting process and recovering high-purity platinum.
【0007】[0007]
【課題を解決するための手段】一方、本出願人は、ジメ
チルグリオキシムがパラジウムの定量分析方法に用いら
れていることに注目し、パラジウムを含有する金電解液
にジメチルグリオキシムを添加して、パラジウム錯体を
生成沈殿させてパラジウムを分離する金電解液の精製方
法を提供した(特開平11−12778号公報)。本発
明者らは、白金の製錬工程において、パラジウムを分離
するために、このジメチルグリオキシムによる沈殿方法
を用いることができることに着目し、鋭意研究した結
果、特定の条件でジメチルグリオキシムを添加すること
によって、高い除去率でパラジウムを分離することがで
きることを見出して本発明に至った。Means for Solving the Problems On the other hand, the present applicant has noticed that dimethylglyoxime is used in a method for quantitative analysis of palladium, and added dimethylglyoxime to a gold electrolyte containing palladium. And a method for purifying a gold electrolyte for separating a palladium by forming and precipitating a palladium complex (JP-A-11-12778). The present inventors have focused on the fact that this precipitation method using dimethylglyoxime can be used to separate palladium in the smelting process of platinum, and as a result of intensive research, added dimethylglyoxime under specific conditions. As a result, the present inventors have found that palladium can be separated at a high removal rate, thereby leading to the present invention.
【0008】すなわち、本発明は、白金とパラジウムと
を含有する水溶液を8を超えるpHに調整した後、ジメ
チルグリオキシムを添加することによって、白金とパラ
ジウムとを含有する水溶液からパラジウムを高い除 去
率で効率よく分離除去できることを見出した。さらに、
ジメチルグリオキシムの添加量が、液中のパラジウム量
に対するモル比で2以上であるときには、パラジウムを
さらに高い除去率で除去できることも見出した。また、
白金とパラジウムとを含有する水溶液が、製錬工程にお
ける白金抽出工程から得られた水溶液であるときに、本
発明は、一層有用である。さらに、本発明では、このよ
うにしてパラジウムを除去した白金水溶液を用いて、高
純度の白金を回収する方法も提供する。That is, the present invention provides a method for removing palladium from an aqueous solution containing platinum and palladium by adjusting the pH of an aqueous solution containing platinum and palladium to a pH exceeding 8, and then adding dimethylglyoxime. It has been found that separation and removal can be performed efficiently at a high rate. further,
It was also found that when the amount of dimethylglyoxime added was 2 or more in molar ratio to the amount of palladium in the liquid, palladium could be removed at a higher removal rate. Also,
The present invention is more useful when the aqueous solution containing platinum and palladium is an aqueous solution obtained from a platinum extraction step in a smelting step. Furthermore, the present invention also provides a method for recovering high-purity platinum using the aqueous platinum solution from which palladium has been removed in this way.
【0009】[0009]
【発明の実施の形態】以下、本発明を、図1、及び図2
に示すフローチャートに沿って説明する。図1は、銅製
錬工程などから得られるパラジウム、白金などを含む抽
出液から、白金を回収する工程(Pt工程)を示すフロ
ーチャートである。図2は、Pt工程の中の、トリブチ
ルホスフェート(TBP)逆抽出後液(以下、塩化白金
酸溶液という)からPtを晶析するまでの工程を、脱パ
ラジウム工程(脱Pd工程)として示す。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described with reference to FIGS.
This will be described along the flowchart shown in FIG. FIG. 1 is a flowchart showing a step (Pt step) of recovering platinum from an extract containing palladium, platinum and the like obtained from a copper smelting step and the like. FIG. 2 shows a process from back-extraction of tributyl phosphate (TBP) (hereinafter referred to as chloroplatinic acid solution) to crystallization of Pt in the Pt process as a palladium removal process (Pd removal process).
【0010】脱パラジウム工程の概略は、最初に、塩化
白金酸溶液のpHを調整して中和し、中和工程で鉄等を
沈殿させて、次いで、ジメチルグリオキシム(DMG)
を添加してパラジウムを除去するものである。[0010] The outline of the palladium removal step is as follows. First, the pH of the chloroplatinic acid solution is adjusted to neutralize the solution, iron and the like are precipitated in the neutralization step, and then dimethylglyoxime (DMG)
Is added to remove palladium.
【0011】この中和工程のpHがDMG添加による脱
Pd率に影響を及ぼすことが、今回、本発明者らによっ
て明らかになった。中和工程のpHが8以下であると、
Pdの除去効果が悪く、pHが8を超えると、Pdの除
去効果は顕著に増大する。また、本発明者らは、DMG
添加工程において、DMGの添加量が、脱Pdに影響を
及ぼすことも見出した。すなわち、液中のPd量に対し
てモル比で2以上のDMGを添加するとき、Pd除去率
はさらに増大する。The present inventors have now found that the pH of the neutralization step affects the Pd removal rate due to the addition of DMG. When the pH of the neutralization step is 8 or less,
The effect of removing Pd is poor, and if the pH exceeds 8, the effect of removing Pd is significantly increased. In addition, the present inventors have proposed that DMG
It has also been found that in the addition step, the amount of DMG added affects the removal of Pd. That is, when 2 or more of DMG is added in a molar ratio to the amount of Pd in the solution, the Pd removal rate further increases.
【0012】以下、実施例1及び2により、中和工程の
pH、及びDMGの添加量がPd除去率に及ぼす影響を
詳細に説明する。Hereinafter, the effects of the pH in the neutralization step and the amount of DMG added on the Pd removal rate will be described in detail with reference to Examples 1 and 2.
【実施例1】塩化白金酸溶液をNaOH溶液にてpH1
に調整した後、5Cの濾紙にて濾過し、濾液の一部を分
析用試料とした。この濾液を300mlずつ採取し、NaO
H溶液にて各中和pH(5〜10)にした後、直ちに1
μのメンブランフィルターにて濾過した。この濾液を25
0ml採取し、モル比(DMG/pH調整後液中のPd)=
2になるようにDMGを添加して1時間攪拌した後、再
度1μのメンブランフィルターにて濾過して、濾液量及
び残渣量を測定した後、分析用試料とした。Example 1 A chloroplatinic acid solution was adjusted to pH 1 with a NaOH solution.
Then, the mixture was filtered with a 5C filter paper, and a part of the filtrate was used as an analysis sample. The filtrate was collected in 300 ml portions and NaO
After each neutralization pH (5-10) with H solution, 1
The solution was filtered through a μ membrane filter. 25 of this filtrate
0 ml was collected and the molar ratio (DMG / Pd in the solution after pH adjustment) =
After adding DMG to 2 and stirring for 1 hour, the mixture was again filtered through a 1 μm membrane filter, and the amount of filtrate and the amount of residue were measured.
【0013】各中和pHにて処理した後液中と、その
後、DMGを添加した後の後液中の各成分濃度を表1に
示す。Table 1 shows the concentration of each component in the solution after the treatment at each neutralization pH and after the addition of DMG.
【表1】 中和後液中及びDMG添加後液中濃度 [Table 1] Concentrations in solution after neutralization and after addition of DMG
【0014】さらに、中和pHと、中和後液中及びDM
G添加後液中のPd及びPt濃度との関係を図3に示
す。Further, the neutralization pH, the concentration in the solution after neutralization and the DM
FIG. 3 shows the relationship between the Pd and Pt concentrations in the solution after the addition of G.
【0015】表1及び図3より、Pd濃度は、8を超え
るpHで中和した後、DMGを添加すれば、55〜12
5mg/Lから数mg/Lまで低下するのが分かる。それに対し
てpH8より低い領域においてDGMを添加したときに
は、Pd濃度は21mg/L程度までしか低下していない。As shown in Table 1 and FIG. 3, the Pd concentration was 55 to 12 when neutralized at a pH exceeding 8 and DMG was added.
It can be seen that it decreases from 5 mg / L to several mg / L. On the other hand, when DGM is added in a region lower than pH 8, the Pd concentration is reduced only to about 21 mg / L.
【0016】[0016]
【実施例2】DMG添加量の影響を試験するために、p
Hを8.5に設定し、DMGの添加モル比(DMG/p
H調整後液中のPd)を変化させた以外は実施例1と同
じ方法を繰り返し、分析した。結果を表2及び図4に示
す。Example 2 In order to test the effect of the amount of DMG added, p
H was set to 8.5, and the addition molar ratio of DMG (DMG / p
The same method as in Example 1 was repeated and analyzed except that Pd) in the solution after H adjustment was changed. The results are shown in Table 2 and FIG.
【表2】DMG添加量とPd濃度 表2及び図4は、8を超えるpHに調整した後、DMG
を、モル比(DMG/pH調整後液中のPd)2以上に
なるように添加すると、Pdの除去率が一層増加するこ
とを示す。[Table 2] DMG addition amount and Pd concentration Table 2 and FIG. 4 show that after adjusting the pH to above 8, DMG
Is added so that the molar ratio (Pd in the DMG / pH adjusted solution) is 2 or more, the removal rate of Pd is further increased.
【0017】次に、本発明の方法によって、塩化白金酸
溶液からPtを回収する実施例を実施例2として示す。Next, an example of recovering Pt from a chloroplatinic acid solution by the method of the present invention will be described as Example 2.
【実施例3】実施例1の方法により、Pdが除去された
高純度Pt含有溶液を得る。このとき、DGMを添加す
る際のpHは、8.5に調整した。得られた高純度Pt
含有溶液460Lに濃塩酸46Lを添加して、1M塩酸溶液
とする。200g/L塩化アンモニウム水溶液を添加して、P
tを塩化白金酸アンモンとして晶析する。この塩化白金
酸アンモンを焼成して得られた白金スポンジの純度は9
9.95%以上であった。Example 3 A high-purity Pt-containing solution from which Pd was removed was obtained by the method of Example 1. At this time, the pH at the time of adding DGM was adjusted to 8.5. High purity Pt obtained
46 L of concentrated hydrochloric acid is added to 460 L of the containing solution to make a 1 M hydrochloric acid solution. Add 200g / L ammonium chloride aqueous solution and add P
Crystallize t as ammonium chloroplatinate. The purity of the platinum sponge obtained by firing this ammonium chloroplatinate is 9
9.95% or more.
【0018】[0018]
【発明の効果】以上のとおり、本発明においては、白金
とパラジウムとを含有する水溶液を8を超えるpHに調
整した後、ジメチルグリオキシムを添加することによっ
て、Pt水溶液中からPdを高い除去率で分離すること
が出来た。また、DMGの添加量を、モル比(DMG/
pH調整後液中のPd )で2以上にすることによっ
て、さらにPdを高い除去率で分離できるという効果を
奏することができた。このPd分離方法は、製錬工程に
よって得られるPdを含有するPt水溶液から、Pdを
分離するのに特に効果を奏する。また、本発明の方法に
よって、Pdを分離したPt水溶液からPtを晶析する
ことで、高純度のPtを得ることが出来る。As described above, in the present invention, the aqueous solution containing platinum and palladium is adjusted to a pH of more than 8, and then dimethylglyoxime is added to thereby remove Pd from the aqueous Pt solution at a high rate. Was able to be separated. Further, the amount of DMG to be added was adjusted in a molar ratio (DMG /
By setting Pd 2 in the solution after pH adjustment to 2 or more, the effect of separating Pd at a higher removal rate could be obtained. This Pd separation method is particularly effective for separating Pd from a Pd-containing aqueous Pt solution obtained by a smelting process. Further, high-purity Pt can be obtained by crystallizing Pt from the aqueous solution of Pt from which Pd has been separated by the method of the present invention.
【図1】製錬工程において白金を回収する工程(Pt工
程)を示すフローチャートである。FIG. 1 is a flowchart showing a step of recovering platinum (Pt step) in a smelting step.
【図2】本発明の脱パラジウム工程(脱Pd工程)を示
すフローチャートである。FIG. 2 is a flowchart showing a palladium removal step (Pd removal step) of the present invention.
【図3】脱Pdに及ぼす中和pHの影響を示す図であ
る。FIG. 3 is a graph showing the effect of neutralization pH on Pd removal.
【図4】脱Pdに及ぼすDMG添加量の影響を示す図で
ある。FIG. 4 is a graph showing the effect of the amount of DMG added on Pd removal.
Claims (4)
8を超えるpHに調整した後、ジメチルグリオキシムを
添加してパラジウムを分離することを特徴とする、白金
とパラジウムとを含有する水溶液からパラジウムを分離
する方法。An aqueous solution containing platinum and palladium is adjusted to a pH of more than 8, and then dimethylglyoxime is added to separate the palladium. How to separate.
のパラジウムに対するモル比で2以上である請求項1に記
載の方法。2. The method according to claim 1, wherein the amount of dimethylglyoxime added is 2 or more in molar ratio to palladium in the liquid.
製錬工程において白金抽出工程から得られた水溶液であ
る請求項1又は請求項2に記載の方法。3. The method according to claim 1, wherein the aqueous solution containing platinum and palladium is an aqueous solution obtained from a platinum extraction step in a smelting step.
でパラジウムを分離した後、白金を含有する水溶液から
高純度の白金を回収する方法。4. A method for recovering high-purity platinum from an aqueous solution containing platinum after separating palladium by the method according to claim 1.
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Cited By (1)
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JP2003027154A (en) * | 2001-07-18 | 2003-01-29 | Nikko Materials Co Ltd | Method of recovering high-purity platinum and palladium |
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1999
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