JP2010222625A - Electrolytic method (2) for lead - Google Patents
Electrolytic method (2) for lead Download PDFInfo
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- JP2010222625A JP2010222625A JP2009069945A JP2009069945A JP2010222625A JP 2010222625 A JP2010222625 A JP 2010222625A JP 2009069945 A JP2009069945 A JP 2009069945A JP 2009069945 A JP2009069945 A JP 2009069945A JP 2010222625 A JP2010222625 A JP 2010222625A
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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
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Abstract
Description
本発明は、非鉄製錬、基盤や電子部品などリサイクル原料の溶融炉、及び産業廃棄物を溶融処理する乾式炉より発生する乾式煙灰中に含まれているPbを回収する方法に関する。 The present invention relates to a method for recovering Pb contained in non-ferrous smelting, melting furnaces for recycled materials such as bases and electronic components, and dry smoke ash generated from a dry furnace for melting industrial waste.
非鉄製錬、基盤や電子部品などリサイクル原料の溶融炉、及び産業廃棄物を溶融処理する乾式炉より非鉄製錬の乾式煙灰中に含まれているPbを回収するため、煙灰を硫酸浸出し、硫酸鉛にした後、電気炉で溶融還元を行う。溶融還元により分離されたメタルをソーダ処理し、その後、メタルをアノード鋳造した後、特許文献1においては、スルファミン酸浴中にて電解精製することでPbを回収している。 In order to recover Pb contained in non-ferrous smelting dry ash from non-ferrous smelting, melting furnaces for recycling raw materials such as foundations and electronic parts, and dry furnaces for melting industrial waste, fumes are leached with sulfuric acid, After changing to lead sulfate, smelting reduction is performed in an electric furnace. In the patent document 1, Pb is recovered by electrolytic purification in a sulfamic acid bath after the metal separated by smelting reduction is soda-treated and then the metal is subjected to anode casting.
特許文献1において、原料中のBi品位が高い原料を処理した場合、電気鉛中のBi品位が高くなる。そのため、再度、Bi品位が高い電気鉛をアノードとして鋳造後、電解精製によりBiを除去する必要がある。
従来の技術に対して、高Bi品位のアノードに対しても高純度の鉛を回収することができる鉛の電解方法を提供することを目的とする。 An object of the present invention is to provide a lead electrolysis method capable of recovering high-purity lead even for a high-Bi grade anode with respect to the prior art.
本発明者等は、上記の課題を解決するため以下の発明を成した。
(1)Bi品位5から30mass%の高不純物アノードを用いた、スルファミン酸浴での電解精製において、電流密度を50A/m2以下にすることにより高純度の鉛を回収する特徴とする鉛の電解方法。
The present inventors made the following invention in order to solve the above-mentioned problems.
(1) Lead electrolysis, characterized by the recovery of high-purity lead by reducing the current density to 50 A / m2 or less in electrolytic refining in a sulfamic acid bath using a high impurity anode of Bi grade 5 to 30 mass% Method.
本発明によれば、
(1)高Bi品位の鉛アノードから効率よく、Bi品位が、5massppm以下の極めて低い高純度の鉛を回収することができることを特徴とする鉛の電解方法を見出した。
According to the present invention,
(1) A lead electrolysis method characterized by being able to efficiently recover highly pure lead having a Bi grade of 5 massppm or less from a high Bi grade lead anode has been found.
(2)電着面が、平滑な電着が容易に得られる。 (2) Smooth electrodeposition of the electrodeposition surface can be easily obtained.
以下に本発明をさらに詳細に説明する。
原料は、本発明の鉛含有物は、鉛 70〜99mass%、錫 0.04mass%、ビスマス5〜30mass%含有する。ビスマスが、アノード中に5から30mass%と高くなると電着した電気鉛中のビスマスの汚染が多くなるためである。
例えば、上記鉛含有物を、アノード鋳造をし、そのアノードを用いて電解精製を行う。アノードのサイズとしては、カソードのサイズに比べ小さくすることで、エッジ効果を防ぐことができ、平滑で良好な電着鉛を回収することができる。
The present invention is described in further detail below.
The raw material contains 70 to 99 mass% lead, 0.04 mass% tin, and 5 to 30 mass% bismuth in the lead-containing material of the present invention. This is because when bismuth is increased to 5 to 30 mass% in the anode, the contamination of bismuth in the electrodeposited electrode lead increases.
For example, the lead-containing material is subjected to anode casting, and electrolytic purification is performed using the anode. By making the anode size smaller than the cathode size, the edge effect can be prevented, and smooth and good electrodeposited lead can be recovered.
電解液として、スルファミン酸の濃度は、20〜100g/L、鉛濃度は、20〜100g/Lが最適である。
更に平滑剤としては、ノイゲン BN-1390及び又はノイゲン BN-2560を1〜10mg/Lにすることで、平滑で良好な電着鉛を回収することができる。
As the electrolytic solution, the sulfamic acid concentration is optimally 20 to 100 g / L, and the lead concentration is optimally 20 to 100 g / L.
Furthermore, smooth and good electrodeposited lead can be recovered by setting Neugen BN-1390 and / or Neugen BN-2560 to 1 to 10 mg / L as the smoothing agent.
次に電流密度とカソード中のBi品位の関係を確認した結果、図1に示す通り、電流密度50A/m2以下であればBi品位が、5massppm以下の低Bi品位であると共に平滑な電着鉛を回収することができる。 Next, as a result of confirming the relationship between the current density and the Bi quality in the cathode, as shown in FIG. 1, if the current density is 50 A / m 2 or less, the Bi quality is a low Bi quality of 5 massppm or less and smooth electrodeposition. Lead can be recovered.
(実施例1) 低Bi品位の電着鉛を回収する方法
電解液の組成として、鉛濃度:80g/L、スルファミン酸濃度:20g/Lに調整した溶液に平滑剤としてノイゲンBN-1390を10mg/Lを添加する。
高Bi品位の鉛アノードと鉛の種板または、ステンレス板をカソードとして、交互に電槽に装入する。
カソードの大きさは、アノードに対して、20〜30mm程度大きくした方が、エッジ部への電流集中を緩和することができ、最適である。
電極装入後、電槽内に電解液を補充し、電解液の電槽内滞留時間が1時間程度になるように給液することで、電槽内の濃度分布を均等にする。
電解液の液温を、20〜30℃に調整後、電流密度50A/m2で通電することで、Bi品位が、5mass ppm以下の低Bi品位の電着鉛を回収することができる。
(Example 1) Method for recovering low-Bi-grade electrodeposited lead As a composition of the electrolytic solution, 10 mg of Neugen BN-1390 as a smoothing agent was added to a solution adjusted to lead concentration: 80 g / L and sulfamic acid concentration: 20 g / L. Add / L.
The high-Bi grade lead anode and lead seed plate or stainless steel plate is used as the cathode, and the battery is inserted alternately.
It is optimal that the size of the cathode be about 20 to 30 mm larger than the anode because the current concentration on the edge portion can be reduced.
After the electrode is charged, the electrolytic solution is replenished in the battery case, and the concentration distribution in the battery case is made uniform by supplying the electrolyte solution so that the residence time of the electrolytic solution in the battery case is about 1 hour.
By adjusting the electrolyte temperature to 20 to 30 ° C. and then energizing it at a current density of 50 A / m 2, it is possible to recover low Bi quality electrodeposited lead with a Bi quality of 5 mass ppm or less.
Claims (1)
Electrolysis of lead characterized in that high purity lead is recovered by reducing the current density to 50 A / m2 or less in electrolytic purification in a sulfamic acid bath using a high impurity anode of Bi grade 5 to 30 mass% .
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JP2009069945A JP2010222625A (en) | 2009-03-23 | 2009-03-23 | Electrolytic method (2) for lead |
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JP2009069945A JP2010222625A (en) | 2009-03-23 | 2009-03-23 | Electrolytic method (2) for lead |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105887138A (en) * | 2016-06-16 | 2016-08-24 | 郴州市金贵银业股份有限公司 | Method for treating lead bullion through electrorefining |
CN110284155A (en) * | 2019-07-29 | 2019-09-27 | 富民薪冶工贸有限公司 | A kind of lead electrolytic method containing high bismuth |
CN113046787A (en) * | 2021-03-12 | 2021-06-29 | 赵坤 | Electrolyte, system and method for wet lead recovery of waste lead storage battery lead plaster ternary system |
-
2009
- 2009-03-23 JP JP2009069945A patent/JP2010222625A/en not_active Withdrawn
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105887138A (en) * | 2016-06-16 | 2016-08-24 | 郴州市金贵银业股份有限公司 | Method for treating lead bullion through electrorefining |
CN110284155A (en) * | 2019-07-29 | 2019-09-27 | 富民薪冶工贸有限公司 | A kind of lead electrolytic method containing high bismuth |
CN113046787A (en) * | 2021-03-12 | 2021-06-29 | 赵坤 | Electrolyte, system and method for wet lead recovery of waste lead storage battery lead plaster ternary system |
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