JPS6289888A - Method for electrodepositing high purity manganese from manganese amalgam - Google Patents

Method for electrodepositing high purity manganese from manganese amalgam

Info

Publication number
JPS6289888A
JPS6289888A JP22890385A JP22890385A JPS6289888A JP S6289888 A JPS6289888 A JP S6289888A JP 22890385 A JP22890385 A JP 22890385A JP 22890385 A JP22890385 A JP 22890385A JP S6289888 A JPS6289888 A JP S6289888A
Authority
JP
Japan
Prior art keywords
manganese
amalgam
cathode
anode
high purity
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
JP22890385A
Other languages
Japanese (ja)
Inventor
Akira Nakamura
彰 中村
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP22890385A priority Critical patent/JPS6289888A/en
Publication of JPS6289888A publication Critical patent/JPS6289888A/en
Pending legal-status Critical Current

Links

Landscapes

  • Electrolytic Production Of Metals (AREA)

Abstract

PURPOSE:To electrodeposit high purity metallic manganese on the cathode and to collect it efficiently by carrying out electrolysis with manganese amalgam as the anode and stainless steel plates as the cathode. CONSTITUTION:Discoid amalgam raising plates 12 and semicircular stainless steel plates 14 as the cathode are arranged opposite to one another in a vessel 10, an electrolytic soln. 16 is filled into the upper part of the vessel 10 and a pool of manganese amalgam 18 as the anode is formed at the lower part. When the raising plates 12 are rotated, they are wetted with the manganese amalgam 18 to raise vertically the manganese amalgam 18 and to form specular anode surfaces. At the same time, the manganese amalgam 18 is agitated. Electrolysis is then carried out. High purity metallic manganese is electrodeposited on the cathode with about 55-65% current efficiency. The electrodeposited manganese is stripped, washed, dried and reutilized.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、マンガンアマルガムを陽極として利用して高
純度の金属マンガンを電着する方法に関する。一般に金
属の電解採取は、陽極をカーボン極又は船種にして行な
われているが、本発明ではマンガンアマルガムを陽極と
した点に特徴を有する。本発明のように、マンガンアマ
ルガムを陽極としステンレス板等を陰極として電解し、
陰極に高純度金属マンガンを電着する方法は、従来見当
たらない。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for electrodepositing high purity manganese metal using manganese amalgam as an anode. Generally, electrolytic winning of metals is carried out using a carbon electrode or ship type as an anode, but the present invention is characterized in that a manganese amalgam is used as an anode. As in the present invention, electrolysis is performed using manganese amalgam as an anode and a stainless steel plate as a cathode,
Conventionally, no method has been found to electrodeposit high-purity metal manganese on the cathode.

従来の技術 金属を製錬する工程からの中間産物である各種ダスt−
tiや排液あるいはいったん市場に出てから廃棄される
各種含金属物質の中には、金属資源として再利用可能な
ものが多(含まれている。最近問題となっている使用済
み乾電池の処理に当たっては、微量水銀の処理のみなら
ず大量に含まれているマンガンの処理方法についても検
討の余地があるが、これまでのところマンガンの再資源
化についての有効な方法は見出されていなかった。
Various types of dust, which are intermediate products from the process of smelting conventional technology metals,
Ti, waste liquid, and various metal-containing substances that are discarded once on the market include many that can be reused as metal resources. In this regard, there is room to consider not only how to treat trace amounts of mercury but also how to treat large amounts of manganese, but so far no effective method for recycling manganese has been found. .

本発明者は特に使用済み乾電池を大量に収集してマンガ
ンを再資源化するのに好適な方法として本発明を想到す
るに至ったものである。
The present inventor came up with the present invention as a particularly suitable method for collecting used dry batteries in large quantities and recycling manganese.

発明が解決しようとする問題点 本発明の目的は、金属二次資源から高純度の金属マンガ
ンを効率良く採取するための方法を提供することにある
Problems to be Solved by the Invention An object of the present invention is to provide a method for efficiently extracting high-purity metallic manganese from secondary metal resources.

問題点を解決するための手段とその作用本発明の前述し
た目的は、マンガンアマルガムを陽極とし、ステンレス
板等を陰極として電解し、陰極に高純度金属マンガンを
電着させることを特徴とするマンガンアマルガムから高
純度金属マンガンを電着する方法によって達成される。
Means for Solving the Problems and Their Effects The above-mentioned object of the present invention is to produce a manganese solution, which is characterized by electrolyzing a manganese amalgam as an anode and a stainless steel plate as a cathode, and electrodepositing high-purity metallic manganese on the cathode. This is accomplished by electrodepositing high-purity metal manganese from amalgam.

マンガンアマルガムは、塩化マンガン水溶液等から、イ
オン化傾向の特性を利用した公知の方法で銅、鉛、カド
ミウム、亜鉛等を除いた塩化マンガン水溶液等から隔膜
電解により生成することが出来る。乾電池に含まれる二
酸化マンガンは容易に塩化マンガン水溶液等に変化させ
ることが出来る。
Manganese amalgam can be produced by diaphragm electrolysis from a manganese chloride aqueous solution, etc., from which copper, lead, cadmium, zinc, etc. have been removed by a known method that takes advantage of its ionization tendency. Manganese dioxide contained in dry batteries can be easily converted into manganese chloride aqueous solution and the like.

つぎに実施例を示す。Next, examples will be shown.

実施例 塩化マンガン水溶液を、PH1〜2、マンガン濃度5〜
10g/It、電流密度0.5 A /dva” 、電
解温度25℃(常温)に保ち、カーボンを陽極、水銀を
陰極、素焼きの円筒を隔膜にして、隔膜電解法によりマ
ンガン濃度0.1%、0.5%、1%の3種類の濃度の
マンガンアマルガムを作った。
Example A manganese chloride aqueous solution was prepared with a pH of 1 to 2 and a manganese concentration of 5 to 2.
10 g/It, current density 0.5 A/dva", electrolysis temperature kept at 25°C (room temperature), carbon as an anode, mercury as a cathode, unglazed cylinder as a diaphragm, manganese concentration 0.1% by diaphragm electrolysis method. Three concentrations of manganese amalgam were prepared: , 0.5%, and 1%.

続いて第1図、第2図の装置内に3種類の濃度のマンガ
ンアマルガムを注入して電解を行なった。
Subsequently, three different concentrations of manganese amalgam were injected into the apparatus shown in FIGS. 1 and 2, and electrolysis was performed.

図において、容器10内に円板形のアマルガム持上げ板
12と半円形をした陰極側ステンレス板14とが対向配
置され、上部に電解液16、下部にマンガンアマルガム
プール18が収容されている。容器10の底部には、水
銀の使用量を少なくするために図のような上げ底形状の
ブロック20が配置されている(工業用大量生産の際に
はこのブロックは取外してもよい)。マンガンアマルガ
ム持上げ板12の中心軸22にはモーター24が連結さ
れ回転可能となっている。持上げ板12が回転すること
により、陽極マンガンアマルガム18が持ち上げ板12
上に鏡面のように濡れて、マンガンアマルガムを陽極面
として垂直に立ち上がらせることになる。同時にマンガ
ンアマルガムを撹拌する作用も行なわれる。銅線26の
下端はマンガンアマルガム18の中に浸されている。
In the figure, a disc-shaped amalgam lifting plate 12 and a semicircular cathode-side stainless steel plate 14 are arranged facing each other in a container 10, and an electrolytic solution 16 is housed in the upper part and a manganese amalgam pool 18 is housed in the lower part. At the bottom of the container 10, a raised-bottom block 20 as shown in the figure is arranged in order to reduce the amount of mercury used (this block may be removed during industrial mass production). A motor 24 is connected to the central shaft 22 of the manganese amalgam lifting plate 12 so that it can rotate. By rotating the lifting plate 12, the anode manganese amalgam 18 is lifted up by the lifting plate 12.
The surface will be wetted like a mirror, and the manganese amalgam will stand up vertically as an anode surface. At the same time, the action of stirring the manganese amalgam is also performed. The lower end of the copper wire 26 is immersed in the manganese amalgam 18.

この装置を用いて、マンガン濃度0.1%、0.5%、
1%のマンガンアマルガムを各々、電解液の組成 Mn
  10〜18g/j!、(NH4)tsO4120〜
140g/iPH8,1〜8.4、温度34〜37℃、
電圧約0.2 V、電流密度3.0〜4.5A/dII
l!、陽極マンガンアマルガム、持上げ板の回転速度1
分間に1回転、陰極ステンレス板の電解条件で電解した
ところ、電流効率55〜65%で陰極に高純度金属マン
ガンが電着された状態で得られた。この際電解液の酸化
を防止するためにごくわずかのHt S Osの溶液を
添加した。
Using this device, manganese concentrations of 0.1%, 0.5%,
1% manganese amalgam respectively, electrolyte composition Mn
10-18g/j! , (NH4)tsO4120~
140g/iPH8.1~8.4, temperature 34~37℃,
Voltage approximately 0.2 V, current density 3.0-4.5 A/dII
l! , anode manganese amalgam, lifting plate rotation speed 1
When electrolysis was performed using the cathode stainless steel plate at one revolution per minute, high-purity metal manganese was electrodeposited on the cathode with a current efficiency of 55 to 65%. At this time, a very small amount of HtSOs solution was added to prevent oxidation of the electrolyte.

さらに、持上げ板の回転速度を1分間に〃回転及び2回
転にして電解を行なったところ、同様の結果が得られた
Furthermore, similar results were obtained when electrolysis was carried out by changing the rotational speed of the lifting plate to 1 and 2 rotations per minute.

すなわち、本発明の方法によればマンガンアマルガムを
陽極として利用し、高純度金属マンガンを陰極側の極板
上に析出させることが出来た。極板上の高純度金属マン
ガンを剥離し水洗乾燥して集積すれば新たな資源として
再利用することが出来る。
That is, according to the method of the present invention, manganese amalgam was used as an anode, and high purity metallic manganese could be deposited on the electrode plate on the cathode side. If the high-purity metal manganese on the electrode plate is peeled off, washed with water, dried, and accumulated, it can be reused as a new resource.

発明の詳細 な説明した如く、本発明によれば金属二次資源から高純
度の金属マンガンが効率良く、採取できることになり、
使用済み乾電池の有効な利用方法が見出される等、その
作用効果には極めて顕著なものがある。
As described in detail, according to the present invention, high-purity metallic manganese can be efficiently extracted from secondary metal resources.
Its effects are extremely remarkable, such as the discovery of effective ways to utilize used dry batteries.

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

第1図は本発明の方法を実施するための電解装置の縦断
面図、第2図は第1図の線A−Aに沿う側断面図である
。 10・・・容器 12・・・アマルガム持上げ板 14・・・ステンレス板 16・・・電解液 18・・・マンガンアマルガム
FIG. 1 is a longitudinal sectional view of an electrolytic apparatus for carrying out the method of the present invention, and FIG. 2 is a side sectional view taken along line A--A in FIG. 10... Container 12... Amalgam lifting plate 14... Stainless steel plate 16... Electrolyte 18... Manganese amalgam

Claims (1)

【特許請求の範囲】[Claims] マンガンアマルガムを陽極とし、ステンレス板等を陰極
として電解し、陰極に高純度金属マンガンを電着させる
ことを特徴とするマンガンアマルガムから高純度金属マ
ンガンを電着する方法。
A method for electrodepositing high-purity metallic manganese from manganese amalgam, characterized by electrolyzing manganese amalgam as an anode and a stainless steel plate as a cathode, and electrodepositing high-purity metallic manganese on the cathode.
JP22890385A 1985-10-16 1985-10-16 Method for electrodepositing high purity manganese from manganese amalgam Pending JPS6289888A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22890385A JPS6289888A (en) 1985-10-16 1985-10-16 Method for electrodepositing high purity manganese from manganese amalgam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22890385A JPS6289888A (en) 1985-10-16 1985-10-16 Method for electrodepositing high purity manganese from manganese amalgam

Publications (1)

Publication Number Publication Date
JPS6289888A true JPS6289888A (en) 1987-04-24

Family

ID=16883664

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22890385A Pending JPS6289888A (en) 1985-10-16 1985-10-16 Method for electrodepositing high purity manganese from manganese amalgam

Country Status (1)

Country Link
JP (1) JPS6289888A (en)

Similar Documents

Publication Publication Date Title
JPS6289888A (en) Method for electrodepositing high purity manganese from manganese amalgam
US1942208A (en) Means for obtaining lead in metallic condition
EP0096662A1 (en) Method for the electrolytic production of lead
US5372683A (en) Method and apparatus for the electrolytic extraction of metals from a solution containing metal ions
US5250166A (en) Method of recovering palladium by electrolysis and apparatus therefor
US1511967A (en) Treatment of tin-plate scrap
US4273640A (en) Zinc extraction apparatus
JPH1018073A (en) Electrolysis with addition of ultrasonic vibration
JP2003171788A (en) Equipment for fractional recovery of metallic base material from object to be plated and method for fractional recovery of the same
SU550461A1 (en) The method of cleaning the lead-silver electrode from manganese sludge
JPS5693887A (en) Pecovery of tallium from lead electrolyte
RU2000105358A (en) METHOD FOR GOLD EXTRACTION FROM GOLD-CONTAINING POLYMETALLIC MATERIALS
RU2000123379A (en) METHOD FOR EXTRACTION OF NOBLE METALS
EP0598642A1 (en) Production of compact zinc deposits from alkaline electrolyte
RU2657063C1 (en) Equipment and method of anode synthesis of thermal-expanding compounds of graphite
SU1654378A1 (en) Method for electrochemical depositing of antimony from depleted solutions
RU2048612C1 (en) Gold bearing alloy processing method
US2225904A (en) Lead oxide and electrolytic process of forming the same
JPS53141125A (en) Process for removing tin from tinned copper material
JPS6070196A (en) Method and device for electrolytic refining of gold
Bush et al. Recovery of silver from laboratory wastes
CA1051820A (en) Zinc extraction method and apparatus
CN115595440A (en) Preparation method for efficiently leaching refined lead of electrode from waste lead paste
RU1786193C (en) Method of recovering noble metals
RU2144962C1 (en) Method of copper recovery from solutions